JAERI-M—93-160 JP9312111 JAERI-M 93-160 PROCEEDINGS OF THE WORKSHOPS ON THE UTILIZATION OF ELECTRON BEAMS July 9 and 13, 1992, Bangkok and Jakarta September 1993 (Ed.) Shoichi SATO B * R ^ * W * M Japan Atomic Energy Research Institute JAERI-M 93-160 PROCEEDINGSOFTHEWORKSHOPSON THEUTI Ll ZATIONOFELECTRONBEAMS July9 and 13. 1992.BangkokandJakarta September 1993 (E d.)ShoichiSA TO 日本原子力研究所 Japan Atomic Energy Research Institute JP9312111
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JAERI-M—93-160
JP9312111
J A E R I - M 93-160
PROCEEDINGS OF THE WORKSHOPS ON
THE UTILIZATION OF ELECTRON BEAMS
July 9 and 13, 1992, Bangkok and Jakarta
September 1993
(Ed.) Shoichi SATO
B * R ^ * W * M Japan Atomic Energy Research Institute
JAERI-M
93-160
PROCEEDINGS OF THE WORKSHOPS ON
THE UTILlZATION OF ELECTRON BEAMS
July 9 and 13. 1992. Bangkok and Jakarta
September 1993
(Ed.) Shoichi SA TO
日本原子力研 究所
Japan Atomic Energy Research Institute
JAERI-~1-93-160
JP9312111
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Department of Technical Information, Japan Atomic Hnergy Research Institute. Tckai-mura. Naka-gun. Ibaraki-ken 319-1 1, Japan.
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JAERI-M 93-160
Proceedings of the Workshops on the Utilization of Electron Beams July 9 and 13, 1992, Bangkok and Jakarta
(Ed.) Shoichi SATO
Takasaki Radiation Chemistry Research Establishment Japan Atomic Energy Research Institute Watanuki-cho, Takasaki-shi, Gunma-ken
(Received July 20, 1993)
Workshops organized by JAERI in cooperation with OAEP, BATAN and JAIF on the utilization of electron beam (EB) were held in Bangkok and Jakarta on 9 and 13 July 1992, respectively. The proceedings contain 13 papers presented at the Workshops. Welcome remarks, opening address and closing remarks are also recorded. At the first part of the Workshops, general view on the application of electron accelerators and introduction of electron accelerators v<=re made. Potential applications of electron accelerators to polymer processing, sterilization of medical products, flue gas purification, treatment of wastewater and sewage sludge and bio-resources were introduced from Japanese participants. Potential application of electron accelerators to polymer processing and food irradiation in Thailand and Indonesia were also discussed.
Keywords: Electron Accelerator, Electron Beam, Industrial Application, Polymer, Curing, Economical Aspects, Food Irradiation, Flue Gas, Wastewater, Sludge, Bioresources, Sterilization
JAERI-M 93-160
Proceedings of the Workshops on the Utilization of Electron Beams
July 9 and 13, 1992, B~ngkok and Jakarta
(Ed.) Shoichi SATO
Takasaki Radiation Chemistry Research Establishment
Japan Atomic Energy Research Institute
Watanuki-cho, Takasaki-shi, Gunma-ken
(Received July 20, 1993)
Workshops organized by JAERI in cooperation with OAEP, BATAN and
JAIF on the utilization of electron beam (EB) were held in Bangkok and
Jakarta on 9 and 13 July 1992, respectively. The proceedings contain 13
papers presented at the Workshops. Welcome remarks. opening address and
closing remarks are also recorded. At the first part of the Workshops,
general view on the application of electron accelerators and introduction
of electron accelerators '"・~re made. Potential applications of electron
accelerators to polymer processing. sterilization of medical products,
flue gas purification, treatment of wastewater and sewage sludge and bio-
resources were introduced from Japanese participants. Potential applica-
tion of electron accelerators to polymer processing and food irradiation
in Thai1and and lndonesia were a1so discussed.
Keywords: Electron Accelerator, Electron Beam, Industrial Application,
Shoichi Sato Japan Atomic Energy Research Institute
Editors
Jindarom Chvajarernpun Of f i ce of Atomic Energy f o r Peace ,
Tha i land
Mirzan T. Razzak N a t i o n a l Atomic Energy Agency,
I ndones i a
Shoji Hashimoto Japan Atomic Energy Research
I n s t i t u t e
Tamikazu Kume Japan Atomic Energy Research
I n s t i t u t e
«/|V
]AERI-M 93ー160
EDITORS
Chief Editor
Shoichi Sato Japan Atomic Energy Research
Insti七ute
Editors
Jindarom Chvajarernpun Office of A七omicEnergy for Peace,
Thailand
Mirzan T. Razzak National Atomic Energy Agency,
工ndonesia
Shoji Hashimoto Japan Atomic Energy Research
工nsti七ute
Tamikazu Kume Japan Atomic Energy Research
工ns七i七ute
JUV
Jffrz
JAERI-M 93-160
PREFACE
The Workshops on the utilization of electron beam (EB), organized by JAERI in cooperation with OAEP, SATAN and JAIF, were held in Thailand and Indonesia on 9 and 13 July 1992, respectively following to the First Workshops in 1990.
Dr. S Sato, Dr. W. Kawakami, Dr. K. Makuuchi, Dr. S. Hashimoto and Dr. T. Kume of JAERI, Mr. S. Takahashi of JAIF, Mr. K. Tomita and Dr. M. Takehisa of Radia Ind. Co. Ltd., Dr. Y. Sasaki of Yazaki Co., Mr. A. Kuroyanagi of Nisshin Electric Co. Ltd., Mr. M. Suzuki of Nisshin-High Voltage Co. Ltd. and Mr. T. Doi of NKK Corporation participated from Japan.
The Workshop in Thailand entitled "Workshop on Industrial Utilization of Electron Accelerators" was held in the Central Plaza Hotel, Bangkok. About 140 persons participated from OAEP and other government offices, universities and companies. It was mentioned from Mr. Suchat Mongkolpantha that the information exchange through the cooperation between Thailand and Japan is very meaningful to promote research and development in Thailand and potential for the application of electron accelerators in Thailand were discussed.
The Workshop in Indonesia entitled "Second Workshop on Industrial Utilization of Electron Accelerators" was held in the
V
JAERI-M 93-160
PREFACE
The Workshops on the u七三lizationof electron beam (EB),
organized by JAER工 in cooperation with OAEP, BATAN and JAIF,
were held in Thailand and Indonesia on 9 and 13 July 1992,
Dr. S Sato, Dr. W. KawaKami, Dr. K. Makuuchi, Dr. S.
Hashimoto and Dr. T. Kume of JAERI, Mr. S. Takahashi of JAIF, Mr.
K. Tomita and Dr. M. Takehisa of Radia Ind. Co. Ltd., Dr. Y.
Sasaki of Yazaki Co., Mr. A. Kuroyanagi of Nisshin Electric Co.
L七d.,Mr. M. Suzuki of Nisshin-High Voltage Co. Ltd. and Mr. T.
Doi of NKK Corporation par七icipa七edfrom Japan.
The Workshop in Thailand entitled "Workshop on Industrial
U七ilizationof Electron Accelerators" was held in the Central
P1aza Ho七e工, Bangkok. Abou七 140persons participated from OAEP
and other governmen七 offices,universities and companies. 1七
was men七ioned from Mr. Sucha七 Mongkolpan七ha七ha七七heinformation
exchange through the coopera七ionbetween Thailand and Japan is
very meaningful to promote research and deve10pment in Thailand
and poten七ial for七heapp1ica七ionof electron acce1erators in
Thailand were discussed.
The Workshop in 工ndonesiaentitled "Second Workshop on
工ndus七rialU七ilizationof Elec七ronAccelerators" was he1d in the
V
JAERI-M 93-160
Hotel Indonesia, Jakarta. About 90 persons participated from BATAN and other government offices, universities and companies. It was mentioned from Dr. Nazir Abdulla that National Atomic Energy Agency concerns very much with the radiation technology into industrial line in Indonesia and BATAN going to built an EB machine with a medium energy of 2 MeV. A low energy electron accelerator was already installed in Indonesia and strong interest was shown from many participants. Many questions and discussions were made about the possibility of the utilization of electron accelerators in Indonesia.
S. Sato Editor in Chief
Takasaki Radiation Chemistry Research Establishment JAERI
VI
]AERI-M 93-160
Hote1 工ndonesia,Jakarta. About 90 persons participated from
BATAN and other government offices, universities and companies.
工七 was mentioned from Dr. Nazir Abdu11a that Na七iona1 Atomic
Energy Agency concerns very much with the radiation technology
into industria1 1ine in Indonesia and BATAN going to built an EB
machine wi七h a medium energy of 2 MeV. A low energy electron
acce1erator was a1ready ins七a11ed in 工ndonesia and s七rong
interes七 wasshown from many participants. Many questions and
discussions were made abou七 thepossibi1i七Yof the u七ilizationof
Secretary-General Office of Atomic Energy for Peace, Thailand
Dr. Sato, Dr. Sasaki, Honored Guests, Ladies and Gentlemen,
The Government of Thailand has indeed good reason to welcome the holding of this Workshop on Industrial Utilization of Electron Accelerators. Before I go any further, please let me extend a warm welcome to those who come a long way to join us here, the distinguished group of experts and scientists as well as decision makers from the governmental institutes and private sectors from Japan. I also wish to welcome all of distinguished participants, who are present here to assess and exchange views on electron accelerator utilization and its future direction.
As for Thailand has given high priority to industrial development. Emphasis is placed on study and research of modern and advance technologies to achieve considerably impressive industrial growth. The utilization of electron accelerators.
- 3 -
]AERI-M 93-160
1.1. Welcome Remarks
SuchatA1ongkolphantha
Secretary-General
Office of A七omicEnergy for Peace, Thailand
Dr. Sato,
Dr. Sasaki,
Honored Guests,
Ladies and Gentlemen,
The Government of Thailand has indeed good reason七owelcome
the holding of 七his Workshop on Indus七rial Utiliza七ion of
E工ec七ronAccelerators. Before 1 go any further, p工easelet me
extend a warm welcome to those who come a long way七o join us
here,七hedis七inguishedgroup of exper七s and scien七istsas well
as decision makers from the governmental institutes and private
sectors from Japan. 工 a工sowish to welcome all of distinguished
par七icipants,who are present here to assess and exchange views
on electron accelerator utilization and i七s fu七uredirec七ion.
As for Thailand has given high priori七y 七o industrial
developmen七 Emphasisis placed on study and research of modern
and advance 七echnologies to achieve considerably impressive
industrial growth. The u七ilizationof elec七ronaccelera七ors,
。d
JAERI-M 93-160
which has been developed and proven beneficial in the developed countries, has been introduced into Thailand and generally accepted for its importance to the development in a wide range of industries, namely plastic products, radiation curing of surface coating, radiation cross-linking of wires and cables, sterilization of medical products, vulcanization of natural rubber, food irradiation, flue gas purification, and radiation treatment of wastewater and sewage sludge.
Considering that industry and technology have become inseparably related, and considering also that we live in a time of such rapid technological changes, the Office of Atomic Energy for Peace (OAEP), in cooperation with the Japan Atomic Energy Research Institute (JAERI) and Japan Atomic Industrial Forum (JAIF), organizing this workshop to welcome the proven awareness and demonstration of electron accelerator advantages. This is also to promote the transfer of the technology encouraging maximum benefits from its utilization in the future.
Ladies and Gentlemen, Bilateral cooperations are playing increasingly significant
roles. Apart from the Implementing Arrangement between OAEP and JAERI on the research cooperation in the field of radiation processing which has made significant progress satisfactorily, this workshop is a good case in point. With a network of information and experience, Japan has the capabilities to assist neighboring countries in numerous areas and range of
- 4 -
]AERI-M 93-160
which has been developed and proven beneficial in the developed
countries, has been in七roduced into Thailand and generally
accepted for its importance to the deve10pment in a wide range of
industries, namely plastic products, radiation curing of surface
coating, radiation cross-1inking of wires and cab1es,
sterilization of medical produc七s,vu1canization of na七ura1
rubber, food irradiation, f1ue gas purification, and radiation
treatment of wastewa七erand sewage sludge.
Considering that industry and techno1ogy have become
inseparab1y re1ated, and considering a1so that we live in a time
of such rapid七echno1ogicalchanges,七heOffice of Atomic Energy
for Peace (OAEP), in cooperation with the Japan A七omicEnergy
Research Institute (JAERI) and Japan Atomic Industrial Forum
(JAIF), organizing this workshop to welcome the proven awareness
and demonstration of e1ectron accelerator advantages. This is
a1so to promo七e 七he 七ransferof 七hetechnology encouraging
maximum benefits from its utiliza七ionin the future.
Ladies and Gentlemen,
Bi1ateral cooperations are playing increasingly significant
ro1es. Apar七 fromthe Implemen七ingArrangemen七 betweenOAEP and
JAERI on the research cつopera七ionin the field of radiation
processing which has made significan七 progress satisfac七ori1y,
this workshop is a good case in point. Wi七h a network of
informa七iOlland experience, Japan has七hecapabili七ies七o assist
neighboring countries in numerous areas and range of
-4一
JAERI-M 93-160
circumstances and Thailand is not as exception.
On this auspicious occasion, I would like to compliment the Government of Japan, JAERI and JAIF who have contributed their time, resources and energies to make the workshop a reality. I wish you a very pleasant and fruitful stay in Thailand. And I wish all of you a great success.
Thank you.
- 5 -
jAERI-M 93-160
circumstances and Thailand is not as exception.
On七hisauspicious occasion, 1 would like to compliment the
Government of Japan, JAER工 andJAIF who have contributed their
七ime,. resources and energies to make the workshop a reali七y. 1
wish you a very pleasant and fruitful stay in Thailand. And 1
wish all of you a great success.
Thank you.
- 5一
JAERI-M 93-160
1.2. Welcome Remarks
Nazir Abdullah
Acting Director General National Atomic Energy Agency, Indonesia
Dr. Sato, Mr. Takahashi, Ladies and gentlemen,
I was very happy today to have all of you in this conference room. This is the second joint Workshop BATAN/JAERI/JAIF on the Industrial Utilization of Electron Accelerators. Since the first workshop two years ago, there are many progress had been achieved.
First of all, I would like to inform you that Indonesian government has paid a great attention on the development of radiation technology in Indonesia. At present. National Atomic Energy Agency has two pilot scale gamma rays irradiators with total power of 225 kCi Cobalt-60 gamma ray source and one pilot scale Electron Beam Machine of 300 keV.
The gamma rays irradiators were used mainly for research and development of sterilization technique and for food preservation
- 6 -
JAERI-M 93-160
1.2. Welcome Remarks
Nazir Abdullah
Acting Direc七orGenera1
Nationa1 Atomic Energy Agency,工ndonesia
Dr. Sato,
Mr. Takahashi,
Ladies and gen七1emen,
1 was very happy today七o have a11 of you in this conference
room. This is the second joint Workshop BATANjJAER工jJAIFon the
工ndus七ria1 U七i1iza七ion of E1ectron Acce1erators. Since 七he
first workshop七woyears ago, there are many progress had been
achieved.
First of a11,工 wou1d1ike to inform you that Indonesian
government has paid a grea七 attentionon 七he deve10pmen七 of
radiation七echno1ogyin Indonesia. At present, Nationa1 Atomic
Energy Agency has two pi10七 sca1egamma rays irradiators with
七0七a1power of 225 kCi Coba1t-60 gamma ray source and one pi10七
sca1e E1ectron Beam Machine of 300 keV.
The gamma rays irradiators were used main1y for research and
deve10pmen七 of steri1iza七iontechnique and for food preservation
-6 -
JAERI-M 93-160
as well as for modification of natural rubber latex.
We have known that the radiation sterilization technique is very helpful for our medical and pharmaceutical industries. One private company, INDOGAMA, has operated a new gamma ray irradiator at Bekasi area and ready tried to take over the former BATAN's service actively in the field of radiation sterilization. The new gamma ray irradiation facilities with an initial of power 400 kCi Cobalt-60 gamma ray source have been commissioned last month and its ready to be operated commercially.
An electron accelerator is another type of irradiation source which is very important for the production of polymer cross-linked products such as wire and cable insulation, heat shrinkable film and tube, polyethylene foam and rubber tire.
The electron accelerators or in more familiar we called electron beam machine is also useful for flue gas and sludge treatment. The two application are very important to demonstrate the contribution of radiation technology in environmental pollution control program.
I believe, this workshop will be capable to open our interest and even create a new idea about the application of EB machine as a new tools in our industrial line. A mutual interaction among the participants and of course the useful discussion between participants and speakers will make everything
- 7 -
JAERI-M 93-160
as well as for modification of natural rubber latex.
We have known that the radia七ionsterilization technique is
very he1pfu1 for our medica1 and pharmaceu七ica1industries. One
private company, INDOGAMA, has opera七ed a new gamma ray
irradiator at Bekasi area and ready tried to take over the former
BATAN's service ac七ive工y in七hefield of radia七ions七eri1ization.
The new gamma ray irradiation faci1ities with an ini七ialof power
400 kCi Coba1t-60 gamma ray source have been commissioned 1ast
month and i七sready七obe opera七edcommercial1y.
An e1ec七ron accelerator is another type of irradiation
source which is very important for 七he produc七ion of po1ymer
cross-1inked produc七s such as wire and cable insula七ion,heat
shrinkab1e film and七ube,polye七hy1enefoam and rubber七ire.
The electron acce1era七orsor in more fami1iar we ca1工ed
e1ectron beam machine is a1so usefu1 for f1ue gas and sludge
七reatmen七. The two application are very importan七七0
demons七rate the contribution of radiation techno1ogy in
environmen七a1po11u七ioncontro1 program.
工 be1ieve, this workshop wi11 be capab1e to open our
in七eres七 andeven create a new idea about the app1ication of EB
machine as a new too1s in our industrial 1ine. A mutua1
in七eraction among the participants and of course the usefu1
discussion between participants and speakers will make everything
- 7一
JAERI-M 93-160
understandable and be more benefit each other.
Today we have our friends from Japan and China who will energize your idea about radiation technology. In addition, the speakers from BATAN will also give you some information about their activities in this field. BATAN is ready to cooperate with all of you to gain a benefit of the irradiation technology.
I would like to convince you that BATAN is not only made effort to introduce the application of Nuclear Power Plant in Indonesia as an alternative to overcome the shortage in electrical energy, but also made effort to introduce appropriate radiation technology in our modern industrial sector.
National Atomic Energy Agency concerns very much with the radiation technology into industrial line in Indonesia. In order to accelerate the technology transfer in appropriate manner, we are going to built an EB machine with a medium energy of 2 MeV later this year. The EB machine will be located at the Center for the Application of Isotopes and Radiation, Psar Jumat, Jakarta.
The EB machine is purchased from China and it is planned to be used as the research & development as well as a demonstration plant and to produce heat resistant cross-linked wire & cable insulation, sterilization, heat shrinkable film for packing material etc. man power training facility. In this opportunity.
- 8 -
JAERI-M 93-160
understandab1e and be more benefit each other.
Today we have our friends from Japan and China who wi11
energize your idea about radiation techno1ogy. 工n addition,七he
speakers from BATAN wi11 a1so give you some information about
七heiractivi七iesin七his field. BATAN is ready to cooperate
with a11 of you to gain a benefit of the irradiation techno1ogy.
工 wou1d1ike to convince you that BATAN is not on1y made
effor七七o introduce七heapp1ication of Nuc1ear Power P1ant in
工ndonesia as an a1ternative 七o overcome the shor七age in
e1ec七rica1energy, but a1so made effor七七o in七roduceappropria七e
radiation七echnologyin our modern industrial sec七or.
National Atomic Energy Agency concerns very much wi七h 七he
radia七ion七echno1ogy into indus七rial 1ine in Indonesia. 工n
order to acce1erate七he七echno1ogy七ransferin appropriate
manner, we are going to built an EB machine with a medium energy
of 2 MeV 1ater七hisyear. The EB machine wi11 be 10ca七eda七
七heCenter for the Application of Isotopes and Radiation, Psar
Juma七, Jakar七a.
The EB machine is purchased from China and it is p1anned七o
be used as the research & deve10pmen七 aswe1l as a demons七ra七ion
p1ant and to produce heat resistan七 cross-linkedwire & cable
insu1ation, S七eri1iza七ion,hea七 shrinkab1e fi1m for packing
ma七eriale七c. man power training facility ・ Inthis oppor七unity,
- 8 -
JAERI-M 93-160
I would like to invite all of you, scientists, engineers, entrepreneur to joint us in the development of radiation technology in Indonesia and therefore makes significant profit for our country.
Ladies and Gentlemen,
I appreciate very much for a nice cooperation of our colleagues from Japan to jointly organize this workshop and I do hope the workshop will be useful and radiation technology will be developed in our industrial line in the near future.
Also, I appreciate for China's delegation to participate in this workshop. I hope during your brief stay here in Indonesia, all of our colleagues from Japan and China will be a pleasant, enjoyable and fruitful one.
I now have much pleasure in declaring open the BATAN/JAERI/JAIF Second Workshop on the industrial utilization of electron accelerator and wish you all every success.
Thank you.
- 9 -
jAERI-M 93-160
工 would like to invite all of you, scientis七s, engineers,
entrepreneur to joint us in the development 0王 radiation
technology in 工ndonesia and therefore makes significant profiで
for our coun七ry.
Ladies and Gentlemen,
工 apprecia七e very much for a nice cooperation of our
colleagues from Japan to join七lyorganize this workshop and 工 do
hope七heworkshop will be useful and radia七iontechnology will be
developed in our industrial line in the near fu七ure.
Also, 1 appreciate for China's delegation じo participa七e in
七hisworkshop. 工 hopeduring your brief stay here in Indonesia,
all of our colleagues from Japan and China will be a pleasant,
enjoyable and fruitful one.
1 now have much pleasure in declaring open the
BATAN/JAERI/JAIF Second Workshop on七heindus七rialutilization of
elec七ronaccelera七orand wish you all every success.
Thank you.
- 9一
JAERI-M 93-160
1.3. Opening Address
S. Sato
Director General Takasaki Radiation Chemistry Research Establishment
Japan Atomic Energy Research Institute
Mr. Suchat Mongkolpantha, Secretary-General of OAEP, Distinguished Guests, Ladies and Gentlemen,
On behalf of JAERI, JAIF and members of Japanese delegation, I would like to express our gratitude to OAEP for their excellent preparation and hosting of this Workshop on Industrial Utilization of Electron Accelerators. This Workshop was organized jointly by OAEP, JAIF and JAERI to exchange information on the status of research and development in the field of industrial application of radiation, mainly from electron accelerators. By the combined presentations from industries and research institutes, as is realized in the program of this workshop, I believe the mutual understanding in both countries will be promoted further, to the progress of radiation chemical industry.
As we observe the situation in manj countries, the use of
-10-
JAERI-M 93-160
1.3. Opening Address
S. Sato
Direc七orGeneral
Takasaki Radia七ionChemistry Research Establishment
Japan Atomic Energy Research工nstitute
Mr. Suchat Mongkolpan七ha,Secre七ary-Generalof OAEP,
Dis七inguishedGuests,
Ladies and Gentlemen,
On behalf of JAER工, JAIF and members of Japanese delega七ion,
工 wouldlike to express our grati七udeto OAEP for七heirexcellent
prepara七ion and hos七ing of 七his Workshop on 工ndustrial
Utilization of Elec七ron Accelera七ors. This Workshop was
organized join七lyby OAEP, JA工F and JAER工七oexchange information
on 七he sta七us of research and development in the field of
industrial application of radia七ion,mainly from elec七ron
accelera七ors. By七hecombined presen七a七ionsfrom industries and
research institutes, as is realized in the program of 七his
workshop,工 believethe mu七ual unders七anding in both countries
will be promo七edfurther,七o 七heprogress of radiation chemical
indus七ry.
As we observe the situa七ionin ma!q countries, the use of
-10一
JAERI-M 93-160
r a d i a t i o n a s an impor tan t and very c h a r a c t e r i s t i c energy form i n
i n d u s t r i e s h a s been i n c r e a s i n g . In J apan , t h e r e a r e a b o u t 200
e l e c t r o n a c c e l e r a t o r s f o r u s e i n c o m m e r c i a l p r o c e s s i n g and
r e s e a r c h .
We r e c o g n i z e t h a t t h e a p p l i c a t i o n of a t o m i c e n e r g y i n
g e n e r a l c a n be p r o m o t e d e f f i c i e n t l y , o n l y by i n t e r n a t i o n a l
c o o p e r a t i o n . Today, t h e p r o g r e s s of n u c l e a r i n d u s t r y i n one
c o u n t r y i s s t r o n g l y l i n k e d w i t h t h e d e v e l o p m e n t i n o t h e r
c o u n t r i e s . I t ' s a l s o t h e p o l i c y of t h e Atomic Energy Commission
of J a p a n a n d o u r i n s t i t u t e t o p r o m o t e t h e i n t e r n a t i o n a l
c o o p e r a t i o n wi th Asian c o u n t r i e s . The c o o p e r a t i o n between OAEP
and JAERI i n t h e f i e l d of r a d i a t i o n p r o c e s s i n g i n t h e sewage
s l u d g e t r e a t m e n t t e c h n o l o g y w i l l be r e p o r t e d i n t h i s m e e t i n g ,
r e s u l t i n g from t h e OAEP-JAERI c o o p e r a t i o n . And i t i s our common
u n d e r s t a n d i n g t h a t JAIF has been c o n t r i b u t i n g v e r y much t o t h e
exchange of i n fo rma t ion from t h e i n d u s t r i a l s t a n d p o i n t , i n c l u d i n g
o r g a n i z a t i o n of t h i s workshop.
I am conv inced t h a t t h e s i g n i f i c a n c e of t h i s workshop w i l l
b e u n d e r s t o o d by a l l t h e p a r t i c i p a n t s , a s an e f f e c t i v e and
meaningful o p p o r t u n i t y f o r t h e advancement of t echno logy t r a n s f e r
t o i n d u s t r y .
Thank you very much f o r your a t t e n t i o n .
- 11 -
JAERI-M 93-160
radia七ionas an important and very characteristic energy form in
indus七rieshas been increasing. 工n Japan, there are about 200
e1ectron acce1era七ors for use in commercial processing and
research.
We recognize that the app1ication of atomic energy in
genera工 canbe promoted efficien七1y,on1y by internationa1
coopera七ion. Today, the progress of nuc1ear indus七ryin one
coun七ry is strong1y linked with 七he deve10pment in other
of Japan and our institute to promo七e the interna七iona1
coopera七ionwi七hAsian coun七ries. The coopera七ionbetween OAEP
and JAER工 in the fie1d of radiation processing in 七he sewage
sludge treatment 七echnologywi11 be repor七ed in this meeting,
resu1七ingfrom七heOAEP-JAER工 coopera七ion. And i七 isour common
understanding 七hat JAIF has been contributing very much七o the
exchange of information from the industria1 standpoint, inc1uding
organization of this workshop.
1 am convinced七ha七七hesignific己nceof this workshop wi11
be understood by a11 七hepar七icipants,as an effective and
meaningful opportunity for the advancemen七 of七echno10gytransfer
to indus七ry.
Thank you very much for your attention.
'・a-唱
'za
JAERI-M 93-160
1.4. Opening Remark
M. Takehisa
Executive Director, Radia Ind. Co- Ltd.
Dr. Nazir Abudllah, Acting Director General of BATAN, Distinguished Guests, Ladies and Gentlemen,
It is a great honor and pleasure for me to deliver a brief opening remark on behalf of JAIF mission to the second workshop on industrial utilization of electron accelerators.
Firstly, I would like to refer a recommendation adopted at the panel discussion chaired by Mrs. Nazly Hilmy held in the first electron beam workshop in 1990.
There are 4 items, among which "there is a need to establish and maintain cooperation between Japanese industrial society and Indonesian industrial society" and "needs of workshop at regular intervals" were taken note for me, in addition to BATAN industry interaction and public education of atomic energy. I fully agree the recommendation for effective evolution of the radiation technology in industry.
- 12 -
]AERI-M 93-160
1.4. Opening Remark
M. Takehisa
Executive Direc七or,Radia工nd. Co. Ltd.
Dr. Nazir Abudllah, Acting Director General of BATAN,
Distinguished Guests,
Ladies and Gentlemen,
工七 is a great honor and pleasure for me 七o deliver a brief
opening remark on behalf of JAIF mission to the second workshop
on industrial utilization of electron accelerators.
Firs七ly,1 would like to refer a recommendation adopted at
the pane工 discussion chaired by Mrs. Nazly Hilmy held in 七he
firs七 elec七ronbeam workshop in 1990.
There are 4 items, among which "七hereis a need七oes七ablish
and main七aincooperation between Japanese industrial society and
Indonesian industrial society" and "needs of workshop at regular
in七ervals" were七akennote for me, in addi七ion七o BATAN industry
interaction and public education of atomic energy. 工 fully
agree七herecommenda七ionfor effec七iveevoluセionof the radiation
七echnologyin industry.
q'u
'EA
JAERI-M 93-160
I found that many attendants from Indonesian industries are in this second workshop on a series of electron beam application based on the recommendation. I appreciate efforts of BATAN and JAERI people who are committing to realize the 2nd workshop.
The one of significance of this workshop is that Japanese mission consists of both governmental, JAERI, and industrial, JAIF, sectors. For Indonesian side, I appreciate BATAN's effort for excellent preparation publicize the potential application of electron beams in various fields to industries which resulted in many attendants from the sector.
I would like to point out that there are some differences for information evaluation in governmental and in industrial sectors. I myself spent a long time in the former sector, now I am in the latter sector for almost 4 years. I am planning to talk electron beam sterilization not only from technical points but also from broad view points based on my experience in industry, and I expect all JAIF member will present a talk with industrial sense.
I really expect that the BATAN/JAERI/JAIF organized workshop will be useful for profitable evolution of industrial electron beam utilization in Indonesia. I also expect more commitment of Indonesian industrial sector to the workshop in the future.
- 13 -
jAERI-M 93-160
1 found that many attendants from lndonesian industries are
in this second workshop on a series of e1ectron beam app1ication
based on the recommendation. 工 appreciateefforts of BATAN and
JAER工 peop1ewho are committing to rea1ize the 2nd workshop.
The one of significance of this workshop is七hatJapanese
mission consists of both governmenta1, JAER工 andindus七ria1,
will be useful for profitab1e evolution of industrial electron
beam u七ilizationin工ndonesia. 1 a1so expect more commitmen七
of Indonesian industria工 sec七orto the workshop in the future.
- 13-
JAERI-M 93-160
Ladies and Gentlemen,
I hope this workshop would be not only effective means for long lasting cooperation in radiation application between both countries but also this workshop is effective for strength a mutual understanding and friendship for both countries.
Thank you very much for your attention.
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JAERl-M 93-160
Ladies and Gent1emen,
工 hopethis workshop wou1d be no七 on1yeffective means for
long lasting cooperation in radiation application between both
countries but a1so this workshop is effective for strength a
mutual understanding and friendship for both coun七ries.
Thank you very much for your atten七ion.
-14一
JAERI-M 93-160
1.5. Organization Committee Report
Mirzan T. Razzak
Head, Radiation Processing Division Centre for Application of Isotopes and Radiation
National Atomic Energy Agency, Indonesia
Yang terhormat Dr. Nazir Abdullah, Acting Director general BATAN
Dr. Shoichi Sato, Director General Takasaki Radiation Chemistry Research Establishment, JAERI
Dr. Takehisa, JAIF Mr. Takahashi, Manager International Nuclear Cooperation Centre, JAIF
Honorable Deputy D i r e c t o r General.BATAN
D i s t i n g u i s h e d g u e s t s .
Lad ies and Gentlemen, Good Morning,
As chai rman of Organ iz ing Committee of t h i s f u n c t i o n , i t i s
my p l e a s a n t d u t y t o welcome a l l of you t o t h i s s e c o n d j o i n t
BATAN/JAERI/JAIF workshop on i n d u s t r i a l a p p l i c a t i o n of e l e c t r o n
a c c e l e r a t o r .
- 15 -
且ERI-M93-1印
1.5. Organization Committee Report
Mirzan T. Razzak
Head, Radiation Processing Division
Centre for Application of工sotopesand Radia七ion
National Atomic Energy Agency, Indonesia
Yang七erhorma七 Dr. Nazir Abdullah, Acting Director general BATAN
Mr. Takahashi, Manager Internationa1 Nuc1ear Cooperation Centre,
JA工F
Honorab1e Deputy Director Genera1.BATAN
Dis七inguishedguests,
Ladies and Gent1emen, Good Morning,
As chairman of Organizing Committee of this func七ion,it is
my p1easant du七Y to we1come a11 of you to this second joint
BATAN/JAER工/JA工Fworkshop on indus七ria1application of e1ectron
accelerator.
Ea --A
JAERI-M 93-160
First of all, let me report about the composition of the participants:
1. 16 Participant from Japan, 2. 30 Participant from Indonesian Companies, 3. 16 Participant from Research Institute, Universities and
government officials, 4. 43 Participant from BATAN
Total becomes 105 p a r t i c i p a n t s .
Todays workshop w i l l have 10 speakers i . e . 7 speakers from Japan
and 3 speakers from Indonesia.
I t i s d i v i d e d i n t o 3 s e s s i o n . In s e s s i o n 1, we have 3
s p e a k e r s from J a p a n who w i l l t a l k a b o u t g e n e r a l v iew and
economical aspect of i n d u s t r i a l a c c e l e r a t o r . In s e s s ion 2, we
have one speaker from Japan and 2 speakers from Indonesia. They
w i l l t a l k a b o u t t h e p o t e n t i a l and t h e r e a l i n d u s t r i a l
a p p l i c a t i o n s of EB p rocess ing . In sess ion 3 , we a r e going t o
have two speakers from Japan and one speaker from Indonesia. In
t h i s s e s s i o n we may have i n f o r m a t i o n a b o u t t h e e m e r g i n g
app l ica t ion or the most promising appl ica t ion of EB a c c e l e r a t o r .
I do hope, a l l p a r t i c i p a n t s could g e t some idea about t h e
f u t u r e a p p l i c a t i o n of EB a c c e l e r a t o r in Indones ia and I would
- 1 6 -
JAERI-M 93-160
First of a11, 1et me report about七hecomposition of the
par七icipan七s:
1. 16 Par七icipantfrom Japan,
2. 30 Participant from 1ndonesian Companies,
3. 16 Participan七 fromResearch 1nstitute, Universities and
government officials,
4. 43 Participant from BATAN
Total becomes 105 participan七s.
Todays workshop will have 10 speakers i.e. 7 speakers from Japan
and 3 speakers from 1ndonesia.
工七 is divided into 3 session. 1n session 1, we have 3
speakers from Japan who wi11 ta1k about genera1 view and
economica1 aspec七 ofindus七ria1acce1erator. 1n session 2, we
have one speaker from Japan and 2 speakers from 1ndonesia. They
wi1工七a1k about 七he poten七ia1 and the rea1 indus七ria1
app1ications of EB processing. 1n session 3, we are going 七0
have七wospeakers from Japan and one speaker from 1ndonesia. 1n
七his session we may have informa七ion abou七 the emerging
app1ication or七hemost promising app1ication of EB acce1era七or.
工 dohope, a11 par七icipantscou1d get some idea abou七七he
fu七ureapplication of EB accelerator in工ndonesiaand 1 would
po --A
JAERI-M 93-160
like to invite all of you to be active in discussions.
It is my duty to acknowledge the support given by the JAIF, JAERI, CAIR-BATAN and several other to realize this workshop. Since the Honorable Director General BATAN, Mr. Djali Ahimsa is still in Vienna, it is also my duty to express my appreciation to the Honorable Acting Director General BATAN, Dr. Nazir Abdullah to take time off to officially open the function and give us the benefit of his advice.
Thank you and have a nice workshop.
-17-
]AERI-M 93-}伺
1ike七o invite a11 of you七o be active in discussions.
工t is my duty to acknow1edge the support given by the JAIF,
JAER工, CAIR-BATAN and severa1 other to rea1ize七hisworkshop.
Since the Honorab1e Director Genera1 BATAN, Mr. Dja1i Ahimsa is
sti11 in Vienna, it is a1so my duty to express my apprecia七ionto
the Honorable Acting Director General BATAN, Dr. Nazir Abdullah
七o take七imeoff to 0~ficia11y open七hefunc七ionand give us the
benefi七 ofhis advice.
Thank you and have a nice workshop.
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JAERI-M 93-160
1.6. Progress and Development of EB-irradiation in Japan
Y. Sasaki
Advisor, Yazaki Co., JAIF Representative
Mr. Chairman, Ladies and Gentlemen,
Thank you very much for your kind greet ing and warm welcome.
I t i s a p l e a s u r e t o be h e r e t o have t h e workshop on t h e
U t i l i z a t i o n of E l e c t r o n Beams. On b e h a l f of Japan Atomic
I n d u s t r i a l Forum, I would l i k e to speak some remarks.
Allow me, I would like to introduce myself in short.
I am a member of Yazaki Corporation, a commercial company in Japan, which mainly manufactures automobile parts such as electric wires and also meters for that.
I feel good familiarity with you and your country, because now our corporation has five factories in around of Bangkok since establishment of the first factory in 1962 and about 7,500 Thai peoples are working with us there, and also they contribute your country by exporting some of their products.
- 18 -
]AERI-Mヨ3-160
1.6. Progress and Development of EB-irradiation in Japan
Y. Sasaki
Advisor, Yazaki Co., JAIF Represen七a七ive
Mr. Chairman,
Ladies and Gentlemen,
Thank you very much for your kind greeting and warm welcome.
工t is a pleasure to be here 七o have 七he workshop on the
Utiliza七ionof Electron Beams. On behalf of Japan A七omic
工ndustrialForum, 1 would like七o speak some remarks.
Allow me, 1 would like七o introduce myself in short.
工 ama member of Yazaki Corporation, a commercial company in
Japan, which mainly manufac七ures automobile parts such as
elec七ricwires and also meters for七hat.
工 feelgood familiari七Y wi七hyou and your country, because
now our corporation has five factories in around of Bangkok since
estab1ishment of七hefirst factory in 1962 and about 7,500 Thai
peoples are working wi七h us七here,and also七heycontribute your
country by exporting some of七heirproduc七s.
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JAERI-M 93-160
Since the famous finding of cross-linking reaction of polyethylene by Professor A. Charlesby in 1950, wide research works in this field have been deployed in the world ambitiously. These researches have given us much important information on the progress of radiation utilization in science and industries.
In Japan, the study-group in this field was organized in 1955 and development researches were initiated in 1957. Since then, various research works have been deployed looking for many kinds of the application year by year steadily.
Since the first EB-machine used in Japanese industry, it has passed about 30 years. So far, many researchers and engineers have grappled to overcome with the many difficulties and troubles encountered in the development process.
Nowadays, the total number of EB-machine for radiation processing including researches and developments in Japan are estimated over 180 sets.
Meanwhile, along with the progress or the development of fundamental and industrial researches, EB-machine and irradiation facilities have been improved very much year by year through mutual collaboration among researchers and engineers and we can now have the excellent EB-machine and irradiation facilities.
Nowadays, we can enjoy new high quality materials such as
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JAERI-M 93-160
Since七hefamous finding of cross-1inking reac七ionof po1y-
ethylene by Professor A. Charlesby in 1950, wide research works
in七his field have been deployed in the wor1d ambitious1y.
These researches have given us "much importan七 informationon七he
progress of radiation u七i1iza七ionin science and industries.
In Japan, the study-group in this field was organized in
1955 and deve10pment researches were initiated in 1957. Since
七hen,various research works have been dep10yed 100king for many
kinds of the app1ica七ionyear by year steadily.
Since七hefirs七 EB-machineused in Japanese industry, it has
passed about 30 years. So far, many researchers and engineers
have grapp1ed to overcome wi七h 七hemany difficu1ties and troub1es
encoun七eredin七hedeve10pment process.
Nowadays, the to七a1 number of EB-machine for radiation
processing inc1uding researches and deve10pmen七s in Japan are
estima七edover 180 sets.
Meanwhile, a10ng wi七h the progress or the development of
fundamen七a1and industria1 researches, EB-machine and irradia七ion
faci1ities have been improved very much year by year through
mu七ua1co11abora七ionamong researchers and engineers and we can
now have七heexce11en七 EB-machineand irradiation faci1ities.
Nowadays, we can enjoy new high qua1ity materia1s such as
-19 --
JAERI-M 93-160
cross-linked urethane and fluoro elastmer produced by a high technology as a radiation irradiation in every day life. In future, EB-machines will be more and more necessitated according to the excellent performance of cross-linked products and for many potential applications.
I believe that these accumulated knowledge and techniques will explode into the big leading industry someday in future.
I hope these our accumulated knowledge, experiences and
technologies will be transferred to your country successfully
through this workshop and benefit each other.
It is our pleasure to have this kind of meeting.
Thank you.
- 20 -
]AERI-M 93-160
cross-linked ure七hane and fluoro elastmer produced by a high
七echnologyas a radiation irradiation in every day life. 工n
fu七ure, EB-machines will be more and more necessitated according
to the excellent performance of cross-linked products and for
many potential applications.
工 believe七ha七七heseaccumulated knowledge and techniques
will explode in七0 七hebig leading industry someday in future.
工 hopethese our accumulated knowledge, experiences and
七echnologieswill be transferred七o your coun七rysuccessfully
七hどoughthis workshop and benefi七 eachother.
工七 is our pleasure 七ohave 七hiskind of mee七ing.
Thank you.
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JAERI-M 93-160
2. PRESENTED PAPERS
-\tu
JAERI -M 93-160
2. PRESENTED PAPERS
-21-μ
JAERI-M 93-160
2.1. General View of Electron Accelerator Utilization
S. Sato
Takasaki R a d i a t i o n Chemist ry Research Es t ab l i shmen t Japan Atomic Energy Research I n s t i t u t e
As radiation sources, electron accelerators have become widely used for processing of polymer products and other materials, along with cobalt-60 gamma sources which are used mainly for sterilization of medical products. With increasing reliability and availability of the electron accelerators (EB machines), their merits over gamma sources are recognized: variable energy ranges, high energy utilization efficiency, high outputs and no generation of radiation when switched off.
EB machines are used industrially for manufacturing of heat-resistant wires and cables, foamed polyolefins, heat-shrinkable tubes and sheets, for pre-vulcanization of tire rubber components, and also for a few kinds of surface curing (hardening of surface coatings). It is noted that the major chemical reactions involved are all crosslinking reactions of polymers. There are of course other radiation chemical reactions applied: polymerization, grafting reaction, and decomposition of polymers.
By absorption of radiation energy, active species are formed in materials. Selective reactions of these active species can be applied practically for a number of processes. The removal of sulfur and nitrogen oxides in flue gases from coal-burners, heavy oil-burners and municipal garbage incinerators have been under process development recently in Japan and some other countries. Sterilization or pasteurization of medical products and other organic materials may also be considered decomposition or modification of biological polymers such as DNA, protein or enzyme.
New radiation chemical products are in the process of industrial application, including radiation vulcanization and grafting of natural rubber latex, production of selective adsorbent materials for uranium in sea water, and those for deodorant use, and battery separator membrane by grafting technique, and several others.
Development of efficient X-ray conversion techniques of high energy electrons will further stimulate wider uses of the EB machines.
- 23 -
JAERI-M 93-160
2.1. General View of Electron Accelerator Utilization
S. Sato
Takasaki Radia七ionChemistry Research Establishmen七Japan Atomic Energy Research Institu七e
As radiation sources, electron accelerators have become widely used for processing of polymer products and other materials, along with cobalt-60 gamma sources which are used mainly for sterilization of medical products. With increasing reliability and availability of the elec-tron accelerators (EB machines), their merits over gamma sources are recognized: variable energy ranges, high energy utilization efficiency‘
high outputs and no generation of radiation when switched off.
EB machines are used industrially for manufacturing of heat-resis-tant wires and cables, foamed polyolefins, heat-shrinkable tubes and sheets, for pre-vulcanization of tIre rubber components, and also for a few kinds of surface curing (hardening of surface coatings). It is noted that the major chemical reactions involved are all crossli此 ingreactions of polymers. There are of course other radiation chemical reactions ap-plied: polymerization, grafting reaction, and decomposition of polymers.
By absorption of radiation energy, active species are formed in materials. Selective reactions of these active species can be applied prac-ticaIly for a number of processes. The removal of sulfur and nitrogen oxides in flue gases from coaJ-bumers, heavy oiJ-bumers and municipaJ garbage incinerators have been under process development recently in J apan and some other countries. Sterilization or pasteurization of medical products and other organic materiaJs may aJso be considered decomposi-tion or modification of biological polymers such as DNA, protein or en-zyme.
New radiation chemical products are in the process of industrial application, including radiation vulcanization and grafting of natural rub-ber latex, production of selective adsorbent materials for uranium in sea water, and those for deodorant use, and battery separator membrane by grafting technique, and several others.
Development of efficient X-ray conversion techniques of high en-ergy electrons will further stimulate wider UseS of the EB machines.
。dn'u
JAERI-M 93-160
2.2. Introduction to Industrial Electron Acceleratrors M. Suzuki
N i s s i n - H i g h V o l t a g e C o . , L t d .
I.INTRODUCTION
I t was in 1960's tha t radiation was industr ial ly i r radiated to improve materials. For twenty and several yea r s from then till now, an electron accelerator (hereinafter refer red to as "EB system") which is a principal radiation source has been making rapid p rog re s s as principal pa r t of large scale industr ia l installations capable of economically and stably producing a large quant i ty of products . Nissin-High Voltage Co., Ltd. (NHV) is a worldwide collective manufacturer of EB sys tems covering all energy regions rang ing from low energy to high energy in indust r ia l u ses . Hereinafter, both c u r r e n t s t a t u s of utilization of EB's in the world and tha t of EB systems of NHV are in t roduced .
II. UTILIZATION OF ELECTRON BEAM 1. Utilization of low-energy electron beam
Fields utilizing low-energy EB systems for production or for research and development a re as shown in Fig. l . Low-energy electron beam has a e n e r g y of 150 to 300 keV in general . As a resul t , the utilization there-of is centralized to processing, i.e., what is called conver t ing on the surface of thin layers , such as improvements of films and surface of shee t s and cur ing of liquid re s ins on base materials, e.g., films, pape r s , metallic pla tes , e tc .
In part icular , it is fields of p roduc ts obtained by utilizing cur ing of so-called liquid res ins such as top coats produced for the purpose of obtaining gloss and protection on the surface of base materials, pr int ing inks , adhesives for lamination and b inders for magnetic media, and fields of p roduc ts obtained by utilizing graft polymerization techniques such as supe r absorben t non-woven fabrics and flame r e t a r d a n t cloths tha t have made rapid p rog res s in r ecen t years .
- 24 -
JAERI-M 93-160
2.2. Introduction to Industrial Electron Acceleratrors
M.Suzuki
Nissin-High Voltage Co., L七d.
1 . 1NTRODUCTION
It was in 1960's that radiation was industrially irradiated to improve materials.
For twenty and several years from then till now, an electron accelerator
(hereinafter referred to as "EB system") which is a principal radiation source
has been making rapid progress as principal part of large sca1e industrial
installations capable of economically and stably producing a large quantity of
products. Nissin-High Voltage Co., Ltd. (NHV) is a worldwide collective
manufacturer of EB systems covering a11 energy regions ranging from low
energy to high energy in industrial uses. Hereinafter, both current status of
utilization of EB's in the world and that of EB systems of NHV are introduced.
II. UT1L1ZATION OF ELECTRON BEAM
1. Utilization of low-energy electron beam
Fields utilizing low-energy EB systems for production or for research and
development are as shown in Fig.l. Low-energy electron beam has a energy of
150 to 300 keV in general. As a result, the utilization there-of is centralized to processing, i.e., what is called converting on the surface of thin layers, such as improvements of films and surface of sheets and curing of liquid resins on base
materials, e.g., films, papers, meta11ic plates, etc.
1n particular, it is fields of products obtained by utilizing curing of so-ca11ed
liquid resins such as top coats produced for the purpose of obtaining gloss and
protection on the surface of base materials, printing inks, adhesives for lamination and binders for magnetic media, and fields of products obtained by
utilizing graft polymerization techniques such as super absorbent non-woven
fabrics and flame retardant cloths that have made rapid progress in recent
years.
-24一
JAERI-M 93-160
2. Utilization of medium-and h igh-energy electron beams Medium and h igh-energy electron beams (350 to 5,000 keV herein) a re utilized
on a large scale as means indispensable to crossl inking of thin wire insulating materials, foamed polyethylene, hea t -shr inkable tubings , r ubbe r for t i res , and the like. On the o ther hand, as means for sterilization of foods, medical supplies , packaging materials, and the like they a re beginning to counteract gamma rays from cobalt 60 which is unstable in view of supply and pr ice. Fur thermore, in the field of desulfurization and denitrification of exhaust gases cont r ibutory to protection of global environment which has often been proposed in recent years , researches and developments for realization of EB process are being performed extensively in Japan, U.S.A., Europe, e tc .
As is apparen t from Fig. l , approximately 580 EB systems in all belonging to the above energy region have already been supplied to markets covering Japan, North America and Europe since 1960. And in case that EB process on a full scale is realized in the fields of the above descr ibed sterilization, desulfurization and denitrification of exhaust gases , and in view of effective utilization of resources , sterilization and conversion to fertil izer of sewage s ludges , decomposition and conversion to alcohol of biomass resources such as s ta rch and cellulose, and the like, the re can be fu r ther expected substant ia l r ise in demands for EB systems.
III. RELATIONS AMONG ACCELERATION VOLTAGE, DEPTH-DOSE AND APPLICATION FIELDS OF EB
Fig.2 shows the Depth-dose curves for accelerated electrons. The energy of accelerated electrons diminishes after they pene t ra te a certain depth of the i r radiated material. In o rde r to p resen t a penetra t ion capability of electrons, Depth-dose cu rves a re widely used. These determine the relationship between the penetrat ion depth in a material of uni t specific gravi ty and the relat ive dose given to the material. Regarding the maximum thickness of a t reated material, in many cases a th ickness which cor responds to 60% of the relat ive dose on a Depth-dose cu rve is chosen. In the case of cur ing, 80% is selected. When the material has a densi ty of p , measurement in the horizontal axis of the Depth-dose curve should be devided by p .
- 25 -
]AERI-M 93-160
2. Utilization of medium-and high-energy electron beams
Medium and high-energy electron beams (350 to 5,000 keV herein) are utilized
on a large scale as means indispensable lo crosslinking of thin wire insulating
materials, foamed polyethylene, heat-shrinkable tubings, 1'ubber fo1' tires, and
the like. On the other hand, as means for sterilization of foods, medical
supplies, packaging materials, and the like they are beginning to counteract
gamma rays from cobalt 60 which is unstable in view of supply and price.
Furthermore, in the field of desulfurization and denitrification of exhaust gases
contributory to protection of global environment which has often been
proposed in recent years, researches and developments for realization of EB
process are being performed extensively in Japan, U.S.A., Europe, etc.
As is apparent from Fig.l, approximately 580 EB systems in all belonging t.o the
above energy region have already been supplied to markets covering Japan,
North America and Europe since 1960. And in case that EB process 011 a full
scale is realized in the fields of the above described sterilization,
desulfurization and denit1'ificat.ion of exhaust gases, and in view of effective
utilizatiol1 of resources, sterilizatiol1 and cOl1version to fertilizer of sewage
sludges, decomposition and conversion to alcohol of biomass resources such as
starch and cellulose, and the like, there can be further expected substantial
rise in demands for EB systems.
111. RELATIONS AMONG ACCELERATION VOLTAGE, DEPTH-DOSE AND APPLICATION
F1ELDS OF EB
Fig.2 shows the Depth-dose curves for accelerated electrons. The energy of
accelerated electrons diminishes after they penetrate a ce1'tain depth of the
irradiated material. 1n order to present a penetration capability of electrons,
Depth-dose curves are widely used. These determine the relationship between
the penetration depth in a material of unit specific gravity and the relative
dose given to the material. Regarding the maximum thickness of a treated
material, in many cases a thickness which corresponds to 60% of the relative
dose on a Depth-dose curve is chosen. 1n the case of curing, 80% is selected.
When the material has a density of p, measurement in t.he horizontal axis of the
Depth-dose curve should be devided by ρ.
-25-
JAERI-M 93-160
Fig.3 shows the optimum thickness for double bombardment (both s ides irradiation) . Thicker materials can be t rea ted by lower acceleration voltage irradiation from both s ides . Fig.4 shows the relation between acceleration voltage and application, and the
relation between dose and application.
IV. EB SYSTEMS 1. Low-energy EB system
The low-energy EB system(commercial name of NHV : Area beam type EB system "CURETRON") is a processing system tha t accelerates thermal electrons which a r e emitted from an electron gun having a filament a r rangement of t he length appropr ia te for the width of i r radiated art icles by applying a high DC voltage and then i r rad ia tes a flat electron beam taken out of a th in metal foil into air . I t is principally composed of DC power supply unit , acceleration unit , conveyance unit, control unit, and the like.
Shielding against bremss t rah lung X-rays which are generated upon irradiation of electron beam is easily done since the energy of electron beam is as low as not more than 300 keV. Accordingly, self-shielding method where the acceleration unit and irradiat ion chamber a re shielded from X-rays with lead plates and steel plates is employed. Therefore, this system is small-sized and compact.
Fig.5 and 6 show Area Beam Type EB systems, "CURETRON". The total number of the systems supplied is shown in the pa r t s , where symbols, "CURE" and "R & D", a re noted, of Fig.7.
2.Medium-and h igh-energy EB systems
EB systems belonging to th is energy region ranging from 350 to 5,000 kV a re what is called scanning type where spot-l ike electron c u r r e n t tha t a re accelerated in an acceleration tube is scanned within the width of i r radiated ar t icles . In the same manner as the low-energy EB system, these systems are
- 26 -
JAERI-M 93-160
Fig.3 shows the optimum thickness for double bombardment (both sides
irradiation). Thicker materials can be treated by lower acceleration voltage
irradiation from both sides.
Fig.4 shows the relation between acceleration voltage and application, and the
relation between dose and application.
N. EB SYSTEMS
1. Low-energy EB system
The low-energy EB system(commercial name of NHV : Area beam type EB
system "CURETRON") is a processing system that accelerates thermal electrons
which are emitted from an electron gun having a fi1ament arrangement of the
length appropriate for the width of irradiated articles by applying a high DC
voltage and then irradiates a f1at electron beam taken out of a thin metal foil
into air. It is principally composed of DC power supply unit, acceleration unit,
conveyance unit, control unit, and the like.
Shielding against bremsstrahlung X-rays which are generated upon
irradiation of electron beam is easily done since the energy of electron beam is
as low as not more than 300 keV. Accordingly, self-shielding method where the
acceleration unit and irradiation chamber are shielded from X-rays with lead
plates and steel plates is employed. Therefore, this system is small-sized and
compact.
Fig.5 and 6 show Area Beam Type EB systems, "CURETRON". The total number
of the systems supplied is shown in the parts, where symbols, "CURE" and "R &
D", are noted, of Fig.7.
2.Medium-and high-energy EB systems
EB systems belonging to this energy region ranging from 350 to 5,000 kV are
what is called scanning type where spot.-1ike electron current that are
accelerated in an acceleration tube is scanned wil.hin the width of irradiated
articles. In the same manner as the low-energy EB syst.em, these systems are
-26-
JAERI-M 93-160
principally composed of DC power supply unit , acceleration tube unit , conveyance unit, control unit , and the like.
(1) Principle and construct ion Pig.8 and Fig.9 show a principle and construction of the EB system (also called
EPS : Electron Processing System). This system produces thermal e lec t rons from cathode in a high vacuum, accelerates (give energy to) them in an acceleration tube by means of a high voltage electric field into a beam of high energy electrons, and th is electron beam which is taken out in the open a i r after passing th rough a titanium foil is i r radiated to a material. As a resu l t , the irradiated material undergoes a chemical reaction. Fig.10 ~ 14 show the main components of the EB system.
(2) Shielding against X-rays X-rays generated as bremss t rah lung when electrons collide with material a r e
quite high in penet ra t ing power and harmful to the human body. Therefore, the shielding against X-rays is necessary . Fig.15 shows an example of concrete-shielded type X-ray shielding room for
the EB system of 800kV and h igher energy . Fig. 16 shows 800kV 35mA self shielded type EB system for the crossl inking of
wire and cable insulations. This EB system is designed for reduced floor space and is able to be readily relocated to meet the needs of changing product ion lines. NHV has succeeded in producing such selfshielded EB system up to 800kV.
(3) Electric power efficiency of the EB system The DC power supply of NHV's EB system adopts a Cockcroft-Walton ci rcui t
and the high frequency power supply applies the solid s ta te i nve r t e r s . The frequencies of the i n v e r t e r s a r e 1kHz or 3kHz. 1kHz is for system up to 1.5MV and 3kHz is for above 1.5MV. Therefore, this system produces good electric power efficiency. The electric power conversion efficiency from the wall (commercial 50 or 60Hz) to the beam power is 85% for the system up to 1.5MV and 75% above 2MV as shown in Fig.17. (4) 5MV EB system Fig. 18 shows a 5MV 30mA EB system delivered to Radia Industry Co., Ltd. in
Japan for the sterilization of the medical supplies . The DC power supply uses a Cockcroft-Walton circuit with pressur ized S F 6 gas in the vessel using a
- 27 -
JAERI -M 93-160
principally composed of DC power supply unit., acceleralion tube unit.,
conveyance unit, control unit, and t.he like.
(1) Principle and construction
Fig.8 and Fig.9 show a principle and construction of the EB system (also called
EPS : Electron Processing System). This syst.em produces thermal electrons
from cathode in a high vacuum, accelerates (give energ.y to) them in an
acceleration tube by means of a high voltage electric field into a beam of high
energy electrons, and this electron beam which is taken out in the open air
after passing through a titanium foil is irradiated to a material. As a result,
the irradiated material undergoes a chemical reaction.
Fig.lO ~ 14 show the main components of the EB system.
(2) Shielding against X-rays
X-rays generated as bremsstrahlung when electrons collide with material are
quite high in penetrating power and harmful to the human body. Therefore,
the shielding against X-rays is necessary.
Fig.15 shows an example of concrete-shielded t.ype X-ray shielding room for
the EB system of 800kV and higher energy.
Fig.16 shows 800kV 35mA selfshielded type EB system for the crosslinking of
wire and cable insulat.ions. This EB system is designed for reduced floor space
and is able t.o be readily relocated to meet. t.he needs of changing production
lines. NHV has succeeded in producing such selfshielded EB system up to
800kV.
(3) Electric power efficiency of the EB system
The DC power supply of NHV's EB system adopts a Cockcroft-Walton circuit
and the high frequency power supply applies the solid state inverters.
The frequencies of the inverters are 1kHz or 3kHz. 1kHz is for system up to
1.5MVand 3kHz is for above 1.5MV. Therefore, this system produces good
electric power efficiency. The electric power conversion efficiency from the
wall (commercial 50 or 60Hz) t.o t.he beam power is 85% for the syst.em up to
1.5MV and 75% above 2MV as shown in Fig.17.
(4) 5MV EB system
Fig.18 shows a 5MV 30mA EB system delivered to Radia lndustry Co., Ltd. in
Japan for the sterilization of the medical supplies. The DC power supply uses a
Cockcroft-Walton circuit wit.h pressurized SFG gas in lhe vessel using a
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JAERI-M 93-160
relatively low frequency which provides low loss and stable operation. Therefore, this EB system has a high electric power conversion efficiency and a high reliability. This 5MV 30mA EB system can also genera te in tense X-rays equivalent to a 2.5
million cur ie cobalt 60 source by using X-rays t a rge t .
The total number of the EB systems of th i s energy region supplied is shown in the pa r t s , where symbols except "CURE" and "R & D", a re noted, of Fig.7. I t shows remarkable increases in the fields of wires, t i r es and foams.
V. POSTSCRIPT The application field of electron beam irradiat ion is expected to expand and
develop toward 21 s t cen tu ry , because of i t s many merits which o the r sources such as thermal r ays , ultraviolet r a y s , gamma r a y s , e tc . do not have.
(July, 1992)
- 2 8 -
JAERI-M 93-160
rc!atively low frequency which provides low loss and stable operation.
Therefor~ , this EB systern has a high electric power conversion efficiency and
a high reliability.
This 5MV 30rnA EB systern can also generate intense X-rays equivalent to a 2.5
mi11ion curie cobalt 60 source by using X-rays target.
The total number of the EB systems of this energy region supplied is shown in
the parts, where syrnbols except "CURE" and "R & D", are noted, of Fig.7. It
shows remarkable increases in the fields of wires, tires and foarns.
v. POSTSCRIPT The application field of electron bearn irradiation is expected to expand and
develop toward 21 st century, because of its rnany merits which other sources such as therrnal rays, ultraviolet rays, garnrna rays, etc. do not have.
(July, 1992)
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JAERI-M 93-160
• Electric wires and cables • Foamed polyethylene • lleat-shrinkable tubings • Tire rubber sheets
• Ion-exchange membranes
• SteriIi2ation for food, medical supplies and packaging materials
• Disinfection of sewage sludge • Removal of S0 2, NOx from exhaust gas • Decomposition of biomass
Number of EB equipment, sold since 1960 Approx. 130 I Approx. 300 I Approx. 145
• Hard coats for transfer foil and film • Anti-fogged fiIms • Release films / papers • Floppy disks, Video tapes • Glossy papers • Coated metal sheets • Gypsum tiles • Laminated products (Credit cards, Metal sheets,
Bank notes, Securities etc.) • Super absorbent non-woven fabrics • Flame-resisting fabrics •Heat-shrinkable packaging films •Heat resistant PVC tapes
Number of EB equipment, sold since 1960 Approx. 100 I Approx. 200 I Approx. 120
Japan • North America • Europe
Fig. 1 Relation between EB energy and application fields (including R & D )
- 2 9 -
]AERI-M 93-160
• Electric wires and cables • Foamed polyethylene . Ileat-shrinkable tubings • Tire rubber sheets
5000
• lon-exchange membranes
• Sterilization for food. medical supplies and packaging materials
• Disinfection of sewage sludge
• Removal of 502. NOx from exhaust gas
• Decomposition of biomass 〈〉ぷ〉
Number of EB eQuipment. soJd since 1960 130 I Approx. 300 ___ I Approx. 145
• Hard coats for transfer foil and film • Anti-fogged films • Release films I papers • Floppy disks. Video tapes • Giossy papers • Coated metal sheets • Gypsum ti les
Approx. 300
ω切
dH-op
• Laminated products (Credit cards. Metal sheets. furnitures. Metal I ized papers etc.)
• Printing (Printed circuit boards. Juice carton, Bank notes. 5ecurities etc.)
• Super absorbent non-woven fabrics • flame-resisting fabrics
ロo-Hd』
ω『
ωυυ〈
.Heat-shrinkable packaging films
.Heat resistant PVC tapes
Number of EB equipment, sold sinc怠 1960A仰p仰附ppro肝附ro札 l ω Approx. 200 Approx. 120
150
Europe North America Japan • Fig. 1 Relation between EB energy and application f1elds
(including R & D)
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JAERI-M 93-160
Depth Dose Curve
100
« m o Q 50 s >
Ti <r
0
\300kv\500l.v\750kV \>W0'>v
100
« m o Q 50 s >
Ti <r
0 O.S 1.0 I.S 2.0 Z.5 3.0 3.S 4.0 4.S
Depth in unit gravity (mm)
100
S t^\\ • O
Q 50 « > m
1.5Mv\ \ ? . 0 M v \ j - 0 M V
0 • . \ \ " ^ 1 0 3 Z 4 6 8 10 12 14 16
Depth in unit gravity (mm)
Depth in unit gravity (mm)
F i g . 2
e
o T3
100
80
60
40
Z0
_ _ Optim singl
um thickness for _ e bombardment
/ VJ
> s — "/ s
\ 1 N • S
N • •
1 • •>* "S.
*
0 . 1 0 . 2 0 . 3 0 . 4 O.S 0 . 6 Depth in g r a m s p e r c m
- Optimum thickness for double bombardment with 1 M e V - e l e c t r o n s
At present, electron irradiation is applied to the industrial fields as shown in Fig. 1.1. The output power of electron accelerator is up to 100kW, but in the newly developed fields which are considered to spread in near future, the more output-power wil l be required. For example, some hundreds of kW accelerator are necessary in flue-gas treatment technology.
As processing scale becoms larger, electron irradiation seems to be more advantageous, but that advantages should be evaluated individually.
In this paper, in order to prove the advantages of electron irradiat ion, economical evaluation in comparison w i th several conventional methods of some industrial fields are introduced.
2. Feature of electron irradiation Electron irradiation is energy transfer which causes radio chemical
reactions. Energy and current of electron beam depend on reaction and mass-flow of target materials. Necessary dose in various industrial fields distributes as shown in Fig. 2.1, from few kGy to several hundreds kGy. This is related to electricity consumption of electron accelerator and it's economy.
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JAERI-M 93-160
2.3. Economical Aspects oflndustrial Electron Accelerators
T. Doi
NKK Corpora七ion
1. Introduction
Utilization of industrial electron accelerators has been spread
remarkably in many fields of industry in recent years. This
popularization was brought by the advantages of electron irradiation;
(1) Technological capability
(2) Economy
(3) Compact facility
(4) Easy operation, maintenance
(5) Safety
(6) Environmental protection
At present, electron irradiation is applied to the industrial fields as
shown in Fig. 1.1. The output power of electron accelerator is up to
100kW, but in the newly developed fieJds wh1ch are considered to
spread in near future, the more output-power will be requirt"'!d. For
example, some hundreds of kW accelerator are necessary in fJue-gas
treatment technology.
As processing scale becoms larger, electron irradiation seems to be
more advantageous, but that advantages should be evaluated
individually.
In this paper, in order to prove the advantages of electron
irradiation, economical evaluation in comparison with several
conventional methods of some industrial fields are introduced.
2. Feature of electron irradiation
Electron irradiation is energy transfer which causes radio chemical
reactions. Energy and current of electron beam depend on reaction
and mass-flow of target materials. Necessary dose in various industrial
fields distributes as shown in Fig. 2.1, from few kGy to several
hundreds kGy. This is related to electricity consumption of electron
accelerator and it's economy.
-41一
JAERI-M 93-160
Secondary X-rays are emitted as target materials are irradiated wi th electron beam. Electron accelerator and irradiation apparatus are equipped inside of radiation shield for biological protection as shown in Fig. 2.2. For economical evaluation, electron accelerator and radiation shield should be taken into consideration.
Radiation dose rate at the outside of radiation shield is limited to a certain level by Government regulation. It is less than the level of one breast photo by X-ray as shown in Fig. 2.3. In actual plant, radiation dose rate at the outside of radiation shield is less than the regulated value, as same level as natural background.
3. Economical Evaluation One of the most important parameter for the evaluation of
industrial processes is economy. The spread of electron irradiation method is mainly due to economy.
In this chapter, economical advantages of electron irradiation method are introduced from several papers.
Electron irradiation method is compared to conventional method or other radiation processes in view of capital cost, operation cost including amortization and product cost in the field of
(1) Rubber crosslinking (2) Cable crosslinking (3) Paint curing (4) Sterilization of medical products
3.1 Rubber crosslinking (1) Automobile-tire production
About 70% of new rubber is used for automobile-tire production in Japan. More than 80% of radial tire are irradiated with electron beam.
Structure of radial tire is shown in Table 3.1.1. Electron irradiation contr ibutes to reduction of rubber amount , manufactur ing stabilization and quality stabilization.
Rubber sheets are irradiated wi th electron beam in the irradiation facility shown in Fig. 3.1.1.
- 42 -
JAERI -M 93 -160
Secondary X-rays are emitted as target materia!s are irradiated with
electron beam. Electron accelerator and irradiation apparatus are
equipped inside of radiation shield for biological protection as shown
in Fig. 2.2. For economical evaluation, electron accelerator and
radiation shield should be taken into consideration.
Radiation dose rate at the outside of radiation shield is limited to a
certain level by Government regulation. It is less than the level of one
breast photo by X-ray as shown in Fig. 2.3. In actual pJant, radiation
dose rate at the outside of radiation shield is less than the regulated
value, as same Jevel as natural background.
3. Economical Evaluation
One of the most important parameter for the evaluation of
industrial processes is economy. The spread of electron irradiation
method is mainly due to economy.
In this chapter, economica! advantages of electron irradiation method
are introduced from severaJ papers.
Electron irradiation method is compared to conventional method or
other radiation processes in view of capital cost, operation cost
including amortization and product cost in the field of
(1) Rubber crosslinking
(2) Cable crosslinking
(3) Paint curing
(4) Sterilization of medical products
3.1 Rubber crosslinking
(1) Automobile-tire production
About 70% of new rubber is used for automobile-tire production
in Japan. More than 80% of radial tire are irradiated with electron
beam.
Structure of radial tire is shown in Table 3.1.1. Electron irradiation
contributes to reduction of rubber amount, manufacturing
stabilization and quality stabilization.
Rubber sheets are irradiated with electron beam in t!,e irradiation
facility shown in Fig.3.1.1.
42 -
JAERI-M 93-160
(2) Economical evaluation Energy cost (Utility cost / productivity) and product cost of rubber
sheet crosslinking by electron irradiation are compared wi th that of other conventional methods, rotecure, micro-wave, thermal and molten-salt method for contineous process.
Comparison of electron irradiation and rotecure is shown in Table 3.1.2.
Electron accelerator of 1.5MeVx50mA is used to attain lOOkGy of absorbed dose.
Product cost of electron irradiation method is 1/6 and energy cost is 1/6 of rotecure method.
Energy cost comparison is shown in Table 3.1.3. In this table, relative energy costs are shown. Energy cost of electron irradiation method is 1/2 ~ 1/9 of other conventional methods.
From the above, electron irradiation method is much more advantageous than other methods not only in productivity but also economy.
3.2 Cable crosslinking (1) High-voltage cable production
Electron irradiation crosslinking in cable production is popular technology in Japan. There are already 20 ~ 30 accelerators of total power more than 1000kW. But these are only for thin cables not big high-voltage cables.
Cables are stretched under the accelerator and irradiated wi th electron beam as shown in Fig. 3.2.1.
Electron irradiation method of high-voltage cable is considered to be more economical rather than that of thin cable.
In this chapter, energy cost of electron irradiation crosslinking method of high-voltage cable is compared to that of other methods.
(2) Economical evaluation There are several methods for crosslinking of high voltage power
cable. Energy costs of four methods are compared in case of high voltage power cable of 6.6kV, 22mm 2 CV core as shown in Table 3.2.1.
In electron irradiation method, accelerator of 1.5MeVx25mA is used to attain 250kGy.
- 4 3 -
JAERI-M 93-160
(2) Economical evaluation
Energy cost (Utility cost I productivity) and product cost of rubber
sheet crosslinking by electron irradiation are compared with that of
other conventional methods, rotecure, micro-wave, thermal and
molten-salt method for contineous process.
Comparison of electron irradiation and rotecure is shown in Table
3.1.2.
Electron accelerator of 1.5MeV x 50mA is used to attain 100kGy of
absorbed dose.
Product cost of electron irradiation method is 116 and energy co坑
is 116 of rotecure method.
Energy cost comparison is shown in Table 3.1.3. In this table,
relative energy costs are shown. Energy cost of electron irradiation
method is 1/2 -1/9 of other conventional methods.
From the above, electron irradiation method is much more
advantageous than other methods not only in productivity but also
economy.
3.2 Cable crosslinking
(1) High-vo/tage cab/e production
Electron irradiation crosslinking in cable production is popular
technology in Japan. There are a/ready 20 -30 accelerators of total
power more than 1000kW. But these are only for thin cables not
big high-voltage cables.
Cables are stretched under the accelerator and irradiated with
electron beam as shown in Fig.3.2.1.
Electron irradiation method of high-voltage cable is considered to
be more economical rather than that of thin cable.
In this chapter, energy cost of electron irradiation crosslinking
method of high同 voltagecable is compared to that of other methods.
(2) Economical evaluation
There are several methods for crosslinking of high voltage power
cable. Energy costs of four methods are compared in case of high
voJtage power cable of 6.6kV, 22mm2 CV core as shown in Table
3.2.1.
In electron irradiation method, accelerator of 1.5MeVx25mA is
used to attain 250kGy.
守d
aaτ
JAER1-M 93-160
Energy cost of electron irradiation method is very cheap compared to that of other methods.
For saving energy, electron irradiation method is obviously much more advantageous.
3.3 Paint curing (1) Feature of curing
In the field of paint curing, electron irradiation is applied, but it r. only for high-polymer paint of radical grafting, not for all kinds of paints.
Feature of curing is shown in Table 3.3.1. Electron irradiation method has high productivity but limited to planner painting and special paints. Schematic view of electron irradiation curing apparatus is shown in Fig. 3.3.1. In paint curing, paint must be irradiated wi th electron in special gas atmosphere.
(2) Economical evaluation Curing cost of electron irradiation method is compared to that of
thermal curing method in case of veneer plate product ion, 90cm x 180cm in size and 4000plates per day.
Two cases of different dose 17kGy and 35kGy are investigated in this chapter.
Results are shown in Table 3.3.2. Product cost in case of 17kGy, is less than 1/2 of thermal curing cost, and cost in case of 35kGy, is about 20% less of thermal curing cost.
Electron irradiation method is more economical than thermal curing method if dose is less than about 35kGy.
Another cost comparison of electron irradiation of 20kGy wi th thermal curing by difference of operation time is shown in Table 3.3.3. Electron irradiation is economically superior to thermal curing at any operation t ime. And as productivity increases, electron irradiation becomes more advantageous.
3.4 Sterilization of medical products (1) Medical sterilization
Because of development of medical technology, large amount of medical products should be sterilized. Ethylene-oxide was used for chemical sterilization, but recently it is considered to be harmful. So, sterilization by radiation was remarkably developed.
- 44 -
JAERI-M 93-160
Energy cost of eJectron irradiation method is very cheap compared
to that of other methods.
For saving energy, eJectron irradiation method is obviousJy much
more advantageous.
3.3 Paint curing
(1) Feature of curing
Jn the field of paint curing, electron irradiation is applied, but it i-:
only for high-polymer paint of radical grafting, not for all kinds of
paints.
Feature of curing is shown in TabJe 3.3.1. EJectron irradiation
method has high productivity but limited to planner painting and
special paints. Schematic view of electron irradiation curing
apparatus is shown in Fig. 3.3.1. In paint curing, paint must be
irradiated with electron in special gas atmosphere.
(2) Economical evaluation
Curing cost of electron irradiation method is compared to that of
thermal curing method in case of veneer plate production,
90cm x 180cm in size and 4000plates per day.
Two cases of different dose 17kGy and 35kGy are investigated in
this chapter.
Results are shown in Table 3.3.2. Product cost in case of 17kGy, is
less than 1/2 of thermal curing cost, and cost in case of 35kGy, is
about 20% less of thermal curing cost.
Eleetron irradiation method is more economical than thermal
curing method if dose is less than about 35kGy.
Another cost comparison of electron irradiation of 20kGy with
thermal curing by difference of operation time is shown in Table
3.3.3. Electron irradiation is economically superior to thermal curing
at anyoperation time. And as productivity increases, electron
irradiation becomes more advantageous.
3.4 Sterilization of medical products
(1) Medical sterilization
Because of development of medical technology, large amount of
medical products should be sterilized. Ethylene-oxide was used for
chemical sterilization, but recently it is considered to be harmful.
So, sterilization by radiation was remarkably developed. -44一
JAERI-M 93-160
In this chapter, sterilization by electron irradiation and gamma-ray irradiation are compared.
Fig. 3.4.1 shows an example of electron irradiation facility for sterilization. Medical products are transported by conveyer through the irradiation facility, and irradiated with electron beam at the accelerator contineously.
(2) Economical evaluation Electron irradiation by electron accelerator and gamma-ray
irradiation by Co-60 source are compared in case of same radiation dose 30kGy.
Results are shown in Table 3.4.1. Gamma irradiation cost is about 4 times more than electron
irradiation cost because of high cost of facility, Co-60 source and low productivity.
4. Conclusion Economical advantages of electron irradiation were evaluated in the
field of rubber crosslinking, cable crosslinking, paint curing and sterilization of medical products.
Some of data referred in this paper are some what old one, but relative comparison wi th conventional methods is possible today. Therefore, economical advantage of electron irradiation process is obviously valid. And as productivity increases, electron irradiation becomes more advantageous.
- 45 -
]AERI-M 93-160
In this chapter, sterilization by electron irradiation and gamma-ray
irradiation are compared.
Fig. 3.4.1 shows an example of electron irradiation facility for
sterilization. Medical products are transported by conveyer through
the irradiation facility, and irradiated with electron beam at the
accelerator contineously.
(2) Economical evaluation
Electron irradiation by electron accelerator and gamma-ray
irradiation by Co -60 source are compared in case of same radiation
dose 30kGy.
Results are shown in Table 3.4.1.
Gamma irradiation cost is about 4 times more than electron
irradiation cost because of high cost of faciI ity, Co -60 source and
low productivity.
4. Conclusion
Economical advantages of electron ir悶 diationwere evaluated in the
fie!d of rubber crosslinking, cable crosslinking, paint curing and
sterilization of medical products.
Some of data referred in this paper are some what old one, but
relative comparison with conventional methods is possible today.
Therefore, economical advantage of electron irradiation process is
obviously valid. And as productivity increases, electron irradiation
becomes more advantageous.
Fhd
aaz
Tread Belt
Sidewall Utilization of irradiation to tire parts
Parts Decrease of volume
Stabilization of
manufacturing
Stabilization of quality
Inner-liner O O o Carcass o o o Sidewall o o o Belt o Tread o Bead o Rubber tube o ° °
Cross section of radial tire
Table 3.1.1 Effects of electron irradit ion to rubber
」〉阿見-ー
ζ
∞ωi】
町
{
}
Utilization of irradiation to tire parts
Decrease of Stabilization
Stabil ization Parts
volume of
of quality manufacturing
Inner-liner O O O
Carcass O O O
Sidewall O O O
Belt O
Tread O
Bead O
Rubbertube O O O
Sidewall
Tread
中‘。、
Effects of electron irradition to rubber Table 3.1.1
Cross section of radial tire
JAERI-M 93-160
Table 3.1.2 Ccvparison of electron irradiation method and rotecure method
Items Electron irradiation (1.5MeVx50mA) Double band rotocure
Quated from "Proceeding of the 15th Japan Conference on Radioisotopes" Japan Atomic Industrial Forum (1981)
- 47 -
+uo u d 、
c 。+-' ゐ4司.
ω a. O
JAERI-M 93-160
Table 3.1.2 Cl'!i'parison of electron irradiaLion method and rotecure method
Items Electron irradiation
Double band rotocure (1.5MeV x 50mA)
Capital cost $ 620,000 $ 585,000
Amortization (IOyears) $ 62,000 $ 58,500
Direct labor $ 36,000 $ 36,000
Overhead $ 36,000 $ 36,000
Utilities $ 43,200 (240kVA) $ 42,000 (220kVA)
Maintenance $ 18,000 $ 6,000
Total $ 195,200 $ 178,500
Cost ($/hr) $ 32.5 $ 29.8
Productivity (Ibs/hr) 3,000 500
Product C05t (I,t/lb) 11,t 61,t
Energy cost (Utility/Productivity)
$14.4 $84
Parameters
. Operation hour/year
. Amortization period
. Labor cost
. Electricity c05t
6,000
10years
$ 6/hr
31,t/kW.hr
Quated from "proceeding of the 15th Japan Conference on
Radioisotopes" Japan Atomic Industrial Forum (1981)
47 -
JAERI-M 93-160
Table 3 .1 .3 Comparison of energy cost in rubber c ross l inking
Crosslinking methods Energy cost Product cost
Electron irradiation 1 1
Rotocure 5 . 8 - 8 . 5 6
Micro-wave 5 —
Thermal 2 —
Molten-salt 1.1 - 2 . 3 —
Relative energy costs are shown in this table.
Quated from "Proceeding of the 15th Japan Conference on Radioisotopes" Japan Atomic Industrial Forum (1981)
Table 3.2.1 Energy cost of crosslinking methods of HV power cable
Methods Facility Energy cost (¥/kg) Relative cost
Electron irradiation 1.5MeVx25mA Accelerator 2.8 1
Chemical Crosslinking
Vapour CCV facility 43 15 Chemical Crosslinking SFe Gas CCV facility 57 20
Silane crosslinking 26 9
Parameters ° Electricity cost ¥ 20/kw-h oVapour
650kg/Hr, ¥ 6800/t for chemical vapour method
Quated from "Proceeding of the 15th Japan Conference on Radioisotopes" Japan Atomic Industrial Forum (1981)
- 48 -
JAERI-M 93-160
Table 3.1.3 Comparison of energy cost in rubber crosslinking
Crosslinking methods Energy cost Product cost
Electron irradiation 1
Rotocure 5.8"'" 8.5 6
Micro・wave 5 一
ThermaJ 2 一
Molten-salt 1.1 ..... 2.3 一
Relative energy costs are shown in this table.
Quated from "Proceeding of the 15th Japan Conference on
Radio;sotopes" Japan Atomic Industria! Forum (1981)
Table 3.2.1 Energy cost of crosslinking methods Qf HV power cable
Methods Facility Energy cost
Electron irradiation 1.5MeV x 25mA Accelerator
Chemical Vapour CCV facility
Crosslinking SF6 Gas CCV facility
I Si
Parameters 0 EJectricity cost ¥20/kw.h
。Vapour
(¥/kg)
2.8
43
57
26
ReJative cost
lS
20
9
650kg/Hr,¥ 6800/t for chemical vapour method
Quated from "Proceeding of the 15th Japan Conference on
Radioisotopes" Japan Atomic Industrial Forum (1981)
-48-
Table
Items
Curing time
Facility
Start-up and shut-down
Energy efficiency
Others
JAERI-M 93-160
3 . 3 . 1 Comparison of i
Thermal curing
5 ~ 60min
Long heating furnace
Several hours
0.2%
(D Catalysis, Promoting materials are necessary
@ Solvent recovery
Electron irradiation
0.1 - 5sec
Compact size
Instantaneous
2.5%
(D Planner painting only
@ Restriction in paint selection
- 4 9 -
JAERI -M 93-160
Table 3.3.1 Comparison of feature
Items Thermal curing Electron irradiation
Curing time 5 -60min 0.1 -5sec
Facility Long heating furnace Compact size
Start-up and shut-down Several hours Instantaneous
Energy efficiency 0.2% 2.5%
Others ① Catalysis, Promoting ① Planner painting materials are only
necessary ② Restriction in paint
② Solvent recovery selection
-49ー
JAERI-M 93-160
Table 3.3.2 Comparison of curing cost
(Uni t : 1000Yen) 1 Thermal
curing Electron irradiation
JIKJJI Thermal curing 17kGy 35kGy
Inve
stm
ent
Building Dry furnace Accelerator Shield
6,000 25,000
28,500 2,850
51,000 5,100
Inve
stm
ent
Total 31,000 31,350 56,100
Ope
ratio
n co
st
Catalysis 7,500 — —
Ope
ratio
n co
st
Steam 420 — —
Ope
ratio
n co
st Electricity — 120 210
Ope
ratio
n co
st
Labor 2,400 1,200 1,200
Ope
ratio
n co
st
Maintenance 620 1,260 2,520
Ope
ratio
n co
st
Taxes (0.77% of invest) 240 240 430
Ope
ratio
n co
st
Amortization (lOyears) 3,100 3,140 5,610
Ope
ratio
n co
st
Total 6,360 5,840 9,760
Interest (5%) 1,550 1,570 2,810
Total 15,830 7,530 12,780
Product cost (¥/plate) 13.2 6.3 10.6
Parameters » Decreased area for electron irradiation process 330m 2 (6M¥) o Dry furnace 25M¥ o Steam 0.4t/h, ¥ 500/kg ° Electricity 20kVA, 35kVA, cost ¥ 3/kW-h o Labor 1.2M¥/year, 2men
Fig. 1.1 Industrial fields of electron accelerator
52-
]AERI -M 93-160
Food irradiation Sterilization
10
(〉
ω豆}〉町
cl
‘-。c ω c 。ゆd
勾
‘-ω :: 1 ω u u <t
Present application
Sewege, sludge treatment
Future application
0.1 10 100 1000
Output power (kW)
Fig. 1.1 lndustrial fields of electron accelerator
-52-
Dose (kGy)
10 20 30 40 50 60 70
I
Sterilization Polyethylene foam
Curing
PVC cable
PVC tape
Rubber tire
Flue-gas treatment
PE cable
Shrink tube
Fig. 2.1 Necessary dose in various industrial fields
』〉何回州日|富由ω|回目。
Dose (kGy)
10 20 31 0 40 51 0 60 70
E E
' s ' , ,
Sterilization Polyethylene foam PE cable
Curing
' E PVC cable E
PVC tape Shrink tube
Rubber tire • ' ' Flue-gas treatment '
'
' ‘ a
'
' ' 『
c.n w
Necessary dose in various industrial fields Fig. 2.1
JAERI-M 93-160
Natural background level
X-ray
Radiation shield
Accelerator
Target material
Fig. 2.2 Radiation shield of electron accelerator
- 54 -
JAERI -M 93-160
Accelerator
f
e
l--・22
・w,
131v
n
ot-,申,
v' dl+
同
18+
FE
-81V
SIB-t↓
v
m¥ーに
Natural background level
Radiation shield of electron accelerator
-54-
Fig. 2.2
Japanese na tu ra l
tv j^^-r, background
Natura l background in Brazil
(year average)
/
f r o m Television (annual )
Electron i r rad ia t ion fac i l i ty
( restr ic ted area)
Unit: mSv
Fig. 2.3 Radiation dose of everyday-l i fe
-""二与:::~~..-盛,þ,フ
hom Aerospoce 5_・・・・〓司,(ann川 J・E園田5
三匂手ぷ-0.35叩5ν
Japanese rwturill
background
(ycar avCra日e)
U可U可
日fケう日
l同!ョヲii |; (1 time)
Unlt: mSv
Fig. 2.3 Radiation dose of everyday-life
仁,1l1Cercurtc? (apart of body)
』〉
Eh--ζ<.0 しa
g
Continuous irradiation facility for tire rubber sheet
Space for spare accelerator
Accelerator
CT5
I
Scanning horn
> m 73
Winder Fig. 3.1.1 Electron Irradiation facility of rubber sheet
仁ontinuousirradiation facility
for tire rubber sheet
」〉何河【
lgs-50
Space for spare accelerator
Accelerator
Rubber sheet
c.n 。、
、、ミミScanning horn
Winder
Electron irradiation facility of rubber sheet Fig. 3.1.1
JAERI-M 93-160
Accelerator
Fig. 3.2.1 Apparatus of cable irradiation with electron beam
-57 -
JAERI-M 93-}印
Accelerator
Winder Scanning horn
Fig. 3.2.1 Apparatus of cable irradiation with electron beam
句,EU
Coating Reservoir
Chamber
Shielding
Electron Beam Gun
Vacuum Roll Coating Station
Unwind Roll Station
Window (Titanium)
Infeed Collimators
Outfeed Collimators
Rewind Rol Station
>
Fig. 3.3.1 Schematic view of electron irradiation curing
』〉阿wmHl富山田ω150
Electron Beam Gun
Roll Coating Station
留
Rewind Roll Station
Outfeed Collimators
Schematic view of electron irradiation curing
Infeed Col¥imators
Fig. 3.3.1
Unwind RolI Station
Accelerator
Scanning horn
Irradiated products
Conveyer
> S3
to I
Fig. 3.4.1 Electron irradiation faci l i ty
』〉阿見回
lguω
】由。
Accelerator
Scanning horn
Irradiated products
U司~
Electron irradiation facility Fig. 3.4.1
JAKRI-M 93-160
2.4. Polymer Processing with Electron Accelerators K. Makuuchi
Takasaki R a d i a t i o n Chemistry Research E s t a b l i s h m e n t Japan Atomic Energy Research I n s t i t u t e
More than one hundred electron accelerators are put to use to modify polymeric materials in industries in the world. One of the principal effects of radiation on polymers is the formation of radicals through ionization and excitation. Recombination of alkyl radicals formed in main chain of polymer is termed crosslinking. Main chain scission causes degradation of polymers. In general, crosslinking and degradation occur simultaneously in polymers. Graft polymerization is initiated by addition of monomers to the alkyl radical in the presence of monomers. Crosslinking is the most accepted electron beam (EB) processing followed by degradation of polymers and radiation grafting.
The predominant reaction that occurs in polyethylene, polyolerfins and elastomers by EB irradiation is crosslinking. Polyfunctional monomers such as diacrylates and triacrylates are being widely used to enhance crosslinking of polypropylene and poly(vinyl-chloride). The effects of crosslinking on the physical properties of polymers are increases in tensile strength, heat resistance and chemical resistance and decreases in elongation. The industrial applications of crosslinking are as follows:
Wire and cable Heat -shrinkable tubing and film Plastic foams Tires
EB crosslinking are applied to the auto-temperature controlling heater systems that consist of polymers and carbon. Crosslinked polyurethane has been developed to improve hot water resistance of the outside jacket of the sensor cable for anti-lock brake systems. EB crosslinking technique is spread to the engineering plastics such as polyesters and Nylons are also crosslinked with EB to increase the heat stability.
Poly(tetrafluoroethylene), and butyl rubbers are typical polymer that degrade by irradiation. The degraded poly(tetrafluoroethylene) is utilized as solid lubricants. Butyl rubbers are reused as raw elastomers.
Numbers of applications of graft polymerization are increasing steadily for the manufacture of functional materials. The battery separators are prepared by grafting acrylic acid onto polyethylene films. Adsorbents that can adsorb ammonia and amines are developed by grafting
sodium p-styrenesulfonate and acrylic acid onto non-woven fabric.
- 60 -
JAERI ー←~ 93-160
2.4. Polymer Processing with Electron Acce)erators
K. Makuuchi
Takasaki Radiation Chemistry Research Establishment Japan Atomic Energy Research lns七i七ute
More than one hundred electron accelerators are put to use to mod-ify polymeric materials in industries in the world. One of the principal effects of radialion on polymers is the formation of radicals through ion-ization and excitation. Recombination of alkyl radicals formed in main chain of polymer is termed crosslinking. Main chain scission causes degradation of polymers. ln general, crosslinking and degradation occur simultaneously in polymers. Graft polymerization is initiated by addition of monomers to the alkyl radical in the presence of monomers. Crosslinking is the most accepted electron beam (EB) processing fo1-lowed by degradation of polymers and radiation grafting.
The predominant reaction that occurs in polyethylene, polyolerfins and elastomers by EB irradiation is cross1inking. Polyfunctional monomers such as diacrylates and triacrylates are being widely used to enhance crosslinking of pυlypropylene and poly(vinyl-chloride). The ef-fects of crosslinking on the physical properties of polymers are increases in tensi1e strength, heat resistance and chemical resistance and decreases in elongation. The industrial applications of crosslinking are as follows:
Wire and cable Heat -shrinkable tubing and film Plastic foams Tires
EB crosslinking are applied to the auto-temperature controlling heater systems that consist of polymers and carbon. Crosslinked polyurethane has been developed to improve hot water resistance of the outside jacket of the sensor cable for anti-lock brake systems. EB crosslinking tech-nique is spread to the engineering plastics such as polyesters and Nylons are also crosslinked with EB to increase the heat stability.
Poly(tetrafluoroethylene), and butyl rubbers are typical polymer that degrade by irradiation. The degraded poly(tetrafluoroethylene) is utilized as solid lubricants. Butyl rubbers are reused as raw elastomers.
Numbers of app1ications of graft po1ymerization are increasing steadily for the manufacture of functiona1 materials.百四 batterysepara-tors are prepared by grafting acrylic acid onto polyethylene films. Ad-sorbents that c如 adsorbammonia and amines are developed by grafting
sodium p-styrenesu1fonate and acrylic acid onto non-woven fabric.
-60
JAERI-M 93-160
2.5. Potential Application of Electron Accelerators in Thailand Chyagrit Siri-Upathum
Department of Nuclear Technology, Faculty of Engineering, Chulalongkom University
1. Infcroducti on
High-energy electron can penetrate and give most of their energies to a material through interaction with the material. The energy given to the material results in excitation and ionization of molecules which lead to chemical reactions. Various chemical reactions induced by high-energy electons can produce new functional materials. Electron beam processing (EBP) is now considered to be industrial procasses with high efficiency, room temperature capability, free of catalyst and good controllability.
EBP has a broad range of applications in industry which lead to ma^aficture of many products of high quality such as crosslinked wire and cable insulation, crosslinked PE foam, heat shrinkable tube and sheet, ion exchange membrane, battery separator, adhesive tape, computer floppy disc etc. A very useful alternative to conventional curing of coating is also done by EBP. Now EBP has been extended to apply successfully for environmental preservation such as flue gas treatment, waste water treatment, treatment of sewage sludge etc. The applications of EBP in radiation processing, grouping according to levels of development are shown in Table 1. The EB energies for pertinent applications are shown in Table 2.
Although EBP has been developed in USA, Europe and Japan for more than 30 years and has been developed in our neighboring countries like Indonesia and Malaysia for some years, it has not yet been developed in Thailand. R&D in radiation processing, however has been
- 61 -
]AERI-M 93-160
2.5. Potential Application of Electron Accelerators in Thailand
CJ,りlagritSiri-Upathum
Depar七men七 ofNuclear Technology, Faculty of Engineering, Chulalongkorn University
1. Inもroduction
High-energy electron can penet1'ate and give mosも of'もheir
ene1'g'ies to a mal:.eri81 I:.hrough inもe1'ac七ion wi th t.he m8もe1'ia1. The
ene1'gy given 1:.0 the maむeria1resu11:.s in exciもaもionand ionization of'
molecules which lead to chemic81 reactions. Va1'ious chemical
reactions induced by high-energy elecもonscan p1'oduce new functional
materials. Elect1'on beam processing (EBP) is now considered七obe
indust1'ial procasses wil:.h high ef'ficiency, roomもempe1'aturecapability,
free of catalyst 8nd good cont1'o11abiliもy.
EBP has a b1'oad 1'ange of app1ications in indusも1'ywhich 1ead
七o ma. <.tf~c七u1'e of many produc七5 of high qua1ity such as crosslinked
wi1'e and cable insula七ion, c1'osslinked PE f'08m, heat shrinkableもube
and sheet, ion exchange memb1'ane, battery sepa1'ato1', adhesiveもape,
computer f10ppy disc e七c. A very usef'u1 alter‘naもiveto convenもiona1
cu1'ing of coating is a1so done by EBP. Now EBP has been extendedもo
app1y successf'u11y f'o1' envi1'onmental p1'ese1'vaもionsuch as flue gas
treaもment, waste wate1' t1'eatment, t1'eaもmenも ofsewage sludge e七c. The
applications of' EBP in 1'adiaもionp1'ocessing, g1'ouping acco1'ding 1:.0
levels of' development 81'e shown in Table 1. The EB ene1'gies f'o1'
pertinent applica七ionsa1'e shown in Table 2.
Although EBP has been developed in USA, Europe and Japan fo1' mo1'e than 3O years and has been deve10ped in our neighbor、ingcounも1'ies
like lndonesia and Malaysia for some year‘5, it has no乞 yet been
developed in Thailand. R&D in 1'adiaもionp1'ocessinS', however、hasbeen
-61 -
JAERI-M 93-160
actively conducted in the field of food preservation, environmental preservation (radiation treatment of sludge and waste water), prevulcanize of rubber latex and grafting of cellulose using gamma-ray irradiator at OAEP. In 1984, Gammafcron Co. (now Kendal Gammatron) has commercialized radiation sterilized medical products, also by using gamma irradiator. In 1991, Chulalongkorn University received a UV curing system from IAEA to commence R&D on UV curing of printing ink. The machine is under setting up for testing now.
2. The necessity bo conduct R&D on EBP in Thailand
As the EB unit with its protective shielding have very high capital costs and EBP including its benefits are still very new to the local industries, prior the investment for such machine to the industry, the Government Agency (OAEP) should have a role to support the R&D on EBP. Extensive R&D on EBP connot be done unless an EB machine has been installed. The provision of EB machines (low and medium energies) can be done through technical co-operation or by government's budget. The objective of implementation should be aimed at
1) carrying out R&D on EBP 2) promotion of EBP as means to manufacture products of high
quality with low cost 3) selection of the suitable EBP for local products on value-
added purpose for export 4) development of manpower to support private sector on EBP 5) provision of technical assistance eg. through training
course, work shop.
The R&D on EBP should be emphasized on technology transfer rather than developing our own technology to shorten the time to move forwards to pilot scale production and transfer to the industrial
- 62 -
JAERI -M 93-160
ac七ively conducもed in the field of food prese~vaもion, environmenta1
preservaもion (radiation もreatment of sludge and waste wa七er), prevulcanize of rubber latex and grafもingof cel1ulose using ga町田¥B-ray
irradiaも01' aも OAEP. ln 1984, GammaもronCo. (now Kendal Gammatron) has
commercialized radia¥:.ion s¥:.erilized medical p~oducもs , 61so by using
gamma irradiator. In 1991, Chulalongkorn Universiもyreceived a UV
curing systerrl from IAEA to commence R&D on UV curing of printing ink.
The machine is under、seももingup for tes¥:.ing now.
2. The J碍 cessi t.y to conducも R&Don EBP in Thai lw叫
As the EB unit wi七h 七spro七ectiveshielding have very high
oapi七slcosもssnd EBP including 七sbenefi¥:.s sre 5もil1very new ¥:.0 the
loos1 industries. prior 七he inves七ment for such machine もoもhe
industry,七he Gover、nmentAgency <OAEP) Sh01ll d ha ve a 1"01 eもosuppor七
七he R&D on EBP. Exもensive R&D on EBP conno七 bedone unless an EB
machine has been insl:.al1ed. The prcvision of EB machi.les (low and
medium ener'gies) osn be done ¥:.hrough technical co-operation or by
gover可1ffient' s budget. Th9 object i ve of j mp 1 emen七ationshould be aimed
a七
1) carrying ouも R&Don EBP
2) promotion of EBP as mesnsもomanufacture producl:.s of high
qual il:.y wiもh low cosも
3) selec七ionof the sui七ableEBP for loos1 products on value-
added purpose for expor七
4) development of manpowerもosupport privaもesecもoron EBP
5) provision of もechnicalassisもanceeg. through training
coul'se, work shop.
The R&D on EBP should be emphasized on technology trBnsfer
rsther than developing our口wnもechnologyto shorten七heもime七omove
forWBrds to pilot scale production Bnd transferもothe indus七rial
-62-
JAERI-M 93-160
sectors. This can be done through regional training course and technical assistance in the form of expertise.
3. Potential Industrial Applications of EBP in Thailand
3.1 Curing of surface coating
Considering the established EBP technologies shown in Table 1 and the development of semi-fimish and finish products for export today, reveals that although the conservation of wood and forests has been promulgated, there is still a large momentum of wood products and manufacturing industry. Table 3 shows the export of particle board, fiber board and plywood in 1989. The relative small volume of the export might come from the consumption of furniture manufacturing industry and domestic uses. Table 4 shows the export of wooden furniture and furniture of cane. Although the total export of furniture of about 40,000 ton in 1989, this volume is just sufficient for a commercial EB cured wood coating line with the break-even figure of 40,000 m per year. Another potent i a1 app1i cat i on of EBP for curing on substrate is ceramic tiles, the volume exported in 1989 exceeded 86,000 ton. Cement board, gypsum board are also products which can be put to EBP for curing of surface coating.
3.2 Radiation Cross linking
There is a trend that in the future the cross linked and halogen-free insulated wire and cable will dominate the world market. Many countries in Europe has already standard requirement that the insulation material must be crosslinked to enhance the properties in case of fire. The sheath must also be crosslinked to pass the requirement of hot set test. The crosslinked and halogen-free insulator is also necessary for health and environmental safety standard.
- 63 -
JAERI-M 93-160
secto1's. This can be done もhrough 1'egional も1'ainingcourse and
technical assisもancein the fo1'm of expe1'tise.
3. Pot目 ltialIndusもrialApplications of EBP in Thail田 d
3.1 Cu1'ing of su1'face coaもing
Gonside1'ing七heestablished EBPもechnologiesshown in Table 1
and the deve1 opment of semi-fimish and finish producもsfo1' export
七odaYt revealsもhaも alもhoughもheconse1'vaもionof wood and fo1'es七s-has
been p1'omulgated,もhe1'e is sti11 a 1a1'ge momentum of wood p1'oducもs
and manufacもuring indust1'Y. Table 3 shows the expo1'も ofparもicle
boar、d,fiber boar、dand plywood in 1989. The 1'ela七ivesmal1 volume of
もhe expo1't might come f1'om the consump七ionof fu1'nitu1'e manufactu1'ing
industry and domestic u.ses. Table 4 shows the exporも ofwooden
furni七u1'e and furniture of cane. Alもhough 七l1e total expo1'七 of
furniture of about 4O,OOO ton in 1989, this volume is just sufficienも
fo1' a commer、cia1EB cured wood coating 1ine with the break-even figure
of 4O,OOO m3
per year、 Ano七he1' poもenもia1applica七ionof EBP fo1'
cu1'ing on subst1'ate is ceramic tiles. the v01ume expor七edin 1989
which can be put to EBP for curing 0ず surfacecosting.
3.2 Radi.ation Crosslinking
There is s もrend 七ha七 1n the future七hecrosslinked and
ha1ogen-free insulated wi1'e end cable will dominsteもheworld marke七.
Many counb1'ies in Eu1'ope has already standard 1'equiremen七もhaももhe
insulaもion material must be c1'osslinked to enhance the properもiesin
case of fi1'e. The sheath must a150 be crosslinkedもopassもhe
requirement of ho七 set もest. The c1'osslinked and halogen-f1'ee
insulaも01' is alsc necessary fol' health and environment.al safety
sもandard.
-63-
JAERI-M 93-160
Crosslinking of wire and cable insulation by EBP has advantage over conventional peroxide and si lane crosslinking in many aspects such as process is less complicated, high throughput, room temperature capability etc. It is important, therefore to note that EBP for crosslinking of wire and cable insulator is a potential technique. The plant capacity for such manufacturing is very large as dictated by the EB power of medium energy. The EB machine of 3.0 MV, 30 mA which normally used for this purpose, radiation dose of 25 Mrad is needed eg. for P.E. insulator, through put is roughly 300 t (PE)/ month. In the future, however if the demand for the cable of this kind is higher and locally produced commodity plastic resin : PE.PP, PS are available, crosslinked cable insulator manufacturing might be of interest for the industry.
Radiation crosslinking also finds wide applications in production of polyolefin foam. The production cost, however can be competitive with conventional chemical technique only if the production amount is more than about 100 t/month.
Another potential application of radiation crosslinking is the manufacturing of heat shrinkable tube and sheet. These products are widespread used for packaging, insulation of electrical parts, connector for telecommunication cables, corrosion protection of welding line of steel pipe, etc.
3.3 Pre-curing of tire rubber
Tire manufacturing process can be improved through the use of precured rubber sheet by EBP. In the process, bead insulation, innerliner, tread, sidewal1 and compounding applied to ply are to be irradiated by electron beam to improve their green strength or toughness so that they can withstand the rough handling of the tire building drum. It is one of the potential applications for domestic
- 64 -
JAERI-M 93-160
Crosslinking of wire and coble insulaもion by EBP has
advantage over、 convenbionalpero託ideand 5ilane c1'os51inking in many
aspecもS slJ:ch as p1'ocess 1S le55 compl icated, highもhroughput,room
kind is higher and Iocally produced commodity plastic 1'esin PE,PP,
PS are avai lable, cr0551 inked cable instthtor manufacturing mighも be
of intere5t for七heindust1'Y.
Radiation cros51inking also find5 wide applicaもion5 in
producむion of polyolefin foam. The production cost, however cem be
competitive with conventional chemical technique only if 七he
p1'oducもion amount j 5 mo1'e than abouも lOOも!mon七h.
Another‘ poteotial application of 1'adiation crosslinking is
the manufac七uring of heat shrinkable tube and sheet. These p1'oducもs
a1'e widesp1'ead used fo1' packaging, in5ulaもionof elecも1'icalpa1'もs.
connec七01' fo1' telecommunication cables. corrosion p1'otection of
welding line of steel pipe, etc.
3.3 Pre-cul" i ng of t i I"e l'ubbel"
Til"e manufacもuringprocess can be improved through the use of
p1'ecu1'ed 1'ubber sheet by EBP. In the proceS5, bead insulation, innel'l ine1'.も1'ead,sidewal' and compounding applied to ply 81"eもobe
irradiaもed by elec七I"on beam もo impl'ove their green st1'ength 01'
toughness 50 もhat they can wiもhstandもhe1'ough hand 1 i ng of theもi1'e
building drum. も isone of the poιen七ia1appl icaもiQnsfor domeseic
-64-
JAERI-M 93-160
industry in the future as the export is increasing expecially tires for busesi lorries and motocycles. The total number of exports were about 1.2 million in 1989.
3.4 Other applications
R&D on radiation vulcanization of natural rubber latex is now in good progress using gamma irradiator. Its potential products are medical products of non-cytofcoxic and corcinogen-free. EBP can be very useful for large scale production of prevulcanized latex, either for domestic industries or for export to secure higher value added. It has been investigated that for the production rate of greater than 12,000 ton per years the unit cost of production is cheaper than that of using gamma irradiator (Table 5).
4. EBP For environmental preservation
As mentioned earlier, EBP has been successfully extended to use for environmental preservation, a good example is the treatment of industrial flue gases to remove N0 x and S0 a from stack gases. Conventional method of treatment is by wet scrubber and selective catalytic reduction for S0 2 and N0 x respectively. EBP for flue gas treatment is a dry scrubber which can eleminate SO to nearly 100% and N0 x to 85-90JJ. In 1997, all lignite or coal-fired power stations in the country have to be attached with S0 2 scrubber to prevent acid rain. lb is of interest to consider EBP for such purpose.
5. Conclusion
EBP should be of great potential to be used in industries in Thailand in the future. To begin with it, however the Government Agency should have a role to support R&D on EBP and its utilization. The first thing to do is to provide EB machines of low and medium
- 6 5 -
]AERI-M 93-160
indus七ry i n the flt七ureasもheexporも is increasing expeciallyもire5
Tor bU5es. ¥orr1e5 and motocycles. The total number、of'expor七5were
about 1.2 million in 1989.
3.4 0もherapplica七ions
R&D on radiaもionvulca.niza.もionof natural rubber、1a七exis now
in 800d pl"ogre5s using gamma irradiator. 七spotential produoも5a1'e
medica1 product5 of non-cyもoもoxic and c01'cinogen-free. EBP can be
very useful f'or large scale production of prevulcanized 1atex, ei七her
f'o1' domesもic indus七ries 01" for expor七七osecure higher value added.
It ha5 been inves七igatedもhatfo1'もheproducもionrate of greate1' 七han
12,000 もonper year5もheuniち costof production is cheaper、七han七hat
of u5ing gamma irradiator <Table 5).
4. EBP 1"01' envi1'ollllliヨロtslpre5e1'VS"むion
A哩 mentioned earlier, EBP has been successfu11y exもended七O
use for environmenもa1preservation, a good example is theもreatmentof
indusもria1 flue gases もo remove NO and 50_ from stack gases. x --'2
Conventiona1 method of もreaもment is by wet scrubber and selective
caもalytic reducもion for SO_ and NO respecもively. EBP for f1ue 2 ><
g8S treatmenも is a dry scrubber which can e1eminaもe502
to nearly
100r. and NO>c to 85-90~. Jn 1997, a11 1ignite 01" coal-fired power
Sもaもions in the counもry have もo be aももachedwith 502
scrubber もo
prevent acid rain. It is of in七eresももoconsider EBP for such purpose.
5. Conclusion
EBP should be of great poten七ia1to be used in industries in
1・hai1and in もhe futUJ'9. To begin with 七, however、もheGover、nment
Agency shou1d have a ro1eもosupport R&D on EBP and its uもi1izaもion.
The firsももhing七odo i5 もoprovide EB mBchines of ]ow and mediwη
"同
uno
JAERI-M 93-160
energy to be installed at a Government Agency such as OAEP. This can tie done through the government budget or through a research contract with foreign assistance. The most promising industrial application of EBP in Thailand in the near future, considering from potential export items, may be in the field of curing of surface coating. This is to secure value added and higher quality of semi-finish products like partitioned boards, ceramic tiles, gypsum tiles, fiber board or finish products such as funiture for export.
(Mrad) Annual production (MT 20,000 12,000 Annual operating cost ¥ 450 M ¥ 250 M Cost/ton 22,500 20,850
- 6 9 -
JAERI-M 93-160
Table 4 Export of furniture in 1989
一一expOf't (1989) value
(MT> (mi 11 ion of TB)
Wooden furniもure 35.197.3 1.988.477
Fu.l'niもUf'eof cane 4,755.262 373.899
Table 5 Cost of RVNRL produced by gamma rays and EB
Co-6O EB
SOttf'ce 2 MCi 5 MV, 3O mA Power、(KW) 3O 15O
Efficiency (y,) 4O 95
Annua 1 operaもion<h) 6.OOO 6.OOO
Sensiもizef' n-BA none
Vu1caniza七iondose 1 25
(Mf'ad)
Annua1 pf'oduction (MT 2O,OOO 12,OOO Annua1 operating cos七 ¥ 45O M ¥ 25O M
Cost/ton 22,5目白 2O.B5O
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2.6. Food Irradiation with Electron Accelerators Chettachai Banditsing
Biological Science Division, Office of Atomic Energy for Peace
Abstract
Both gamma rays and energetic electrons are widely used for the sterilization of disposable devices and for food irradiation. Radioactive isotopes (Co—60, and Cs—137) emiting gamma rays have been the predominant energy source of these processes but particle accelerators producing high power beams of energetic electrons are now taking share of this business. The food irradiation processing requires an electron beams of 10 MeV of energy and more than 10 KW of power. The electron beam which suitable for industrial food irradiation processing can be obtained by an electron linear accelerator having a high accelerating field gradient (10—5 MV/m). High -intensity X—ray convertor are also being considered for applications requiring more penetration than electron beams can provide.
1. Introduction
Food irradiation is a physical means of food treatment comparable to processing food by heating or freezing. The process involves exposing food, either package or in bulk, to gamma rays. X-rays, or electrons in a special room and for a specified duration to achieve the technical purpose. The most common and approved sources of gamma rays for food and Industrial processing are cobalt-60 and caesium-137. These are so called radioisotope sources. There are also 'machine' sources which can produce electrons and/or X-rays for food processing as shown in Fig.1.
80th gamma rays and energetic electrons are widely used for the sterilization ot disposabfe devices and for food irradiation. Radioactive isotopes (Co-60. and CS-137) emiting gamma rays have been '.he predomi-nant energy source of these processes but particle accelerators producing high power beams of energetic electrons are now taking share of this business. The food irradiatios pfOcess加9requlres an eJectron beams 01 10 MeVol energy and more than 10 KW 01 power. The electmn beam which suitable for industrial food irradiation processing can be obtained by an eJectron IInear accelerator having a high acceleratlng field gradient れ0-5MVjm). High-intensity X-ray convertor a.re also being considered for applica首onsrequiring more penetration than electron beams can pfO'叫de.
1. Introduction
Food irradiation is a physical means 01 food treatment comparable to processing food by heating or freezing. The process involves exposing food. eJther package or in bulk. to gamma rays. X -rays. or electrons in a speclal room and for a specifled duration to achleve the technical purpose. The most common and approved sources of gamma rays lor food and Industrial processing are cobalt-60 and caesium-137. These are so called radiolsotope sources. nlere are also 'machine' sources which can produce electrons and/or X-rays for food processlng as shown加 Flg.1.
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JAERI-M 3-160
2..Benefits of food irradiation.
Benefits of food irradiation are to extend the shelf life, decontamination of both pathogenic and spoilage microorganisms, disinfection of parasites, disinfestation of insects and inhibition of sprout of agr i cultural produce and products. This technology will not only reducing spoilage losses of food but also increasing trade in a number of food items in many regions.
The cost of irradiation for food preservation should be less than comparable physical methods in view of its lower energy requirement and competative with chemical treatment in significant volume of products is treated in a plant within a given a unit of time. Techno-economic feasibility studies proved that food irradiation is economic efficient and convenient method for processing of food in many countries (Banditsing 1985, Banditsing 1988, Martin 1988, Lustre 1985, Maha 1988, Khan 1988, and Moy 1984.).
3.Sources of radiation
The choice of energy source for a specific application depends on the process requirements such as product configuration and handling pro— ceedure through put rate, minimum dose and max/min dose rate, as well as the user's criteria for capital and operating costs, process versatility, equipment availability and reliability, social acceptability and risks.
4.Penetration
Industrial electron accelerators provide concentrated, high— intensity radiation with limited penetration in solid materials. In contrast, gamma—ray source provide diffuse, low intensity radiation with greater penetration. However, X—ray converter having high penetration is now available.
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jAERI -M 3-160
2..BeneIJ極 01food irradiation.
Benell旬。,ffood irradiation are to extend the shelflile. decon-tamination of both pathogenic and spoilage町aicroorganisms,disinfection of parasites, dis加festationof insects and inhlb耐onof sprout of agn-cultural produce and produc脂.This tt招 hnologywill not only reducing spollage losses 01 food but also加creasingtrade in a number of food items in many regions.
The cost of Irradiatlon for food preservation should be less曲 ancomparabJe physical methods加 view01 i陰 lowerenergy req凶rementandcompetative w詑hchemical treatment in sig川目cantvolume of products is treated in a plant within a given a unit of time. Techno-economic feasib耐tystudfes proved that food irrad陥tlonis economlc efficient and convenient method for process加9offood加 manycountries (Bandi陰加g官985,Bandlts加91988. Martin 1988. Lustre 1985, Maha 1988,開lan唱988.and Moy 1984ふ
3.Sources of radlation
The choice of energy source for a specific application depends on the process require町lentssuch as product configuration and handling pro-ceedure through put rate. minimum dose and町laxJmin伽 serate, as well as the user's 削除rJafor capi凶 andoperating costs. proc関 sver:錨閥均,
eq凶pmentavailability and陪Iiab揃旬, social accep旬b揃tyand risks.
4.Penetration
Industrlal electron accelerators pr。叫deconcentrated. hlgh-加tensityradiation with limited penetration加 solidmaterials.加
contrast. gamma-ray source pro凶dedlffuse, low加tensityradiation wi曲greater penetratlon. However. X-ray conve目。rha'叫nghigh penetraUon is now available.
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JAERI -M 93-160
The percentage depth dose distribution in water or unit density materials for single—sided irradiation is shown in Fig.2. In addition the max/min dose ratio versus unit-density product thickness two—sided irradiation of gamma ray and X—ray is shown in Fig.3.
5.Advantages and disadvantages of gamma ray, electron beam.and X-ray.
Comparisons of the advantages and disanvantages of gamma ray, electron beam, and X-ray for radiation processing of medical devices and food have been reported by Cleland 1987 as it is shown in Table 1. Each type of energy sources has a number of advantages and disadvantages which make the choice for new facilities a rather complex issue. Gamma-ray processing in terms of numbers of installations and aggregate experience Is still the dominant technology in this fields. However, utilization of linacs for industrial processing in various fields is also existed in many countries as shown in Table 2.
6.Economics.
Comparisons of X—ray and gamma—ray sources for industrial irradiation process have been reported by Cleland et. al. (1987) and economical evaluation in comparison of sterilization of medical products by electron and gamma irradiation was also conducted by Doi (1992). It was founded that the operating costs (unit cost/ft3) of gammas : X-rays was $ 0.64 : $ 0.52 whereas the irradiation cost electron : gamma was 1150 Y : 5050 Y m 5 .
7.Conclusion.
Food Irradition has been proven to be a safe and wholesome physical means of food treatment by exposing food to gamma rays. X-rays, or electrons to achieve the technical purpose of reducing spoilage loss. Each type of radiations has a number of advantages and disadvantages. Gamma rays processing in terms of numbers of installations and aggregate experience is still the dominant technology in these fields. However, high-power beams of energetic electrons are now taking share of this business.
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JAERI -M 93-160
The percentage depth dose distribution加 wateror unit density materials lor slngle-slded irradiation is shown In Flg.2. In addition the max/min dose ratio versus uniト densilyproduct thickness two-sided irradiation of gamma ray and X-ray is shown加 Fig.3.
5.AdYantages and disadYantages of gamma ray. electron beam.and X-ray.
Comparisons 01 the adYantages and disanvantages 01 gamma ray. electron beam. and X-ray lor radiation processing 01 medical de叫cesand food have been reported by Cfeland 1987 as it is shown in Table 1. Each type 01 energy sources has a number of advantages and disadYantages which make the choice lor new lacilities a rather complex issue. Gamma-ray processing in terms of numbe陪 ofinstallations and aggregate experlence Is stifl the dominant technology in this fields. However. ulilization of Ilnacs for industrial processing in various fields is also existed in many countries as shown in Table 2.
6.Economics.
Comparisons of X-ray and gamma-ray sources for industrial Irradia.tion process have been reported by Cleland et. al. (198乃 andeconomlcaJ evaluatlon In comparison of sterilizatlon of medical produc恒by electron and gamma irradlation was also conducted by Doi (1992). It was founded that the operating cos恒 (unitcostf1貨3)of gammas: X-rays was $ 0.64: $ 0.52 whereas the irradiatlon cost electron : gamma was 1150 Y: 5050 Y m 3•
7. Conclusion.
F∞d Irrad耐onhas been proven to be a safe and wholesome physlcal means olf(旭 d甘'eatmentby exposlng food to gamma rays. X -rays. or electrons 10 achieve the technical purpose of reducing spoilage loss. Each type of radiations has a number of adVantages and'disadYantages. Gamma rays pr'ωessing加 termsof numbers of installations and aggregate experlence is stlll曲 edom加anttechnology in these fieJds. However. high-power beams of energetic electrons are now抱 kingshare of白isbusiness.
-72 -
JAER1-M 93-160
Considering of the electron beam processing of food, interesting suggustion which should be taken in account has been given to accumulate of data in commercial plants and pilot plants in USA and France. Meanwhile, linac technology must be prepared for propable development of the demands on larger power rating for processing of the larger volume of food stuffs, higher efficiency of power conversion from wall to beam, and the development of X-ray convenor to accomodate thick samples.
As far as the promoting electron accelerators utilization of food irradiation in development countries is concerned, government organization which responsible for nuclear science and technology R&D should have this facility through the national budget and/or through international agency technical assistance, this machine not only giving opportunity for scientists to gain operation and maintainance of irradiation facility experience but aiso to bridge the food irradiation technology to the private investor through technology transfer process.
- 73
JAERI-M 93-160
Considering 0' the electron beam process加9offood.加terestingsuggustion which should be taken In account has been glven to accumulate of dala in commercial plan陰 andpilot plan胎 加 USAand France. Meanwhile.linac technology must be prepared for propable development of the demands on larger power rating for processing of the larger volume of food ~tu筒s. higher efficiency of power conve陪 ionfrom wall to beam. and the development of X-ray convertor to accomodate thick samples.
As far as the promoting el~ctron accelerators utilization of food iπ'adiation 加 developmentcountries is concerned. government organization which陪 sponsiblefor nuclear science and technology R & 0 should have this fac蹴tythrough the national budget and/or through international agency technical assistance. this machine not onJy gi叫ngopporlunUy fOT scienljs也 10gain opeTalion and maintainance of irradiation facility experience but aiso to bridge the food irradialion technology to the private investor through technology transfer process.
一73
JAERI-M 93-160
References
Banditsing, C. 1985. The multipurpose food irradiation plant in Thailand. In Food Irradiation Processing. Proc. IAEA/FAO Symposium, Washington D.C. . 4 - 8 March, pp. 365-377.
Banditsing, C. 1988. Food irradiation for national development J. Nutr. Assoc. Thailand. 1988, 4, 435-443.
Cleland, M.R. and G.M. Pageau. 1987. Comparisons of X-ray and gamma-ray sources for industrial irradiation processes. Nuclear Instruments and Methods in Physics Research B24/25, 967-972.
Cleland, M.R. and G.M. Pageau. 1987. Radiation processing of medical devices and food. In: Preprint of an invited paper for 20 th Midyear Topical Meeting of the Health Physics Society. 6—12 February, 15 pp.
Doi, T. 1992. Economical aspects of industrial electron accelerators. Proc. OAEP/JAERI/JAIF Workshop on Industrial Utilization of Electron Accelerators, 9 July 1992.
Khan, T. 1988. Commercial trial on radiation preservation of onions under tropical conditions. In: Final meeting of project committee of RPFi phase II. Office of Atomic Energy for Peace. Bangkok 1988.
Lustre, A.O.,Ang, L., Dianco, A., Cabalfin, E.G., and Narvarro, Q.O., Philippines experience in marketing irradiated foods. Proc. ASEAN Workshop on Food Irradiation, Bangkok 1985, Association of South East Asean Nations. Food Handling Bureau, Kualalumper, 1985. 52-59.
Maha, M. 1988. Technology transfer of irradiation of frozen shrimps, dried fish and spices. In: Final meeting of project committee of RPFI Phase II. Office of Atomic Energy for Peace, Bangkok, 1988.
Martin, M. 1988. Commercialization storage and transportation studies of irradiated dried fish and fishery products and onions. In: Final meeting of project committee of RPFI Phase II. Office of Atomic Energy for Peace., Bangkok 1988.
Moy, J. 1984. Economic feasibility study:Irradiation of Mexican fruits, in IAEA Project MEX/5/01-01 Report. 42 pp.
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jAERI-M 93-160
References
Banditslng. C. 1985.τhemu附purposefood Irradlatlon plant加 τhailand.In Food Irradiation Processing. Pr,ω. IAEA/FAO Symposium. W箇 hingtonD.C. ,4-8 March, pp. 365-377.
Dandits'ng. C. 1988. Food irradiation for national development J. Nutr. Assoc. Thalland. 1988, 4. 435-443.
Cleland. M.R. and G.M. Pageau. 1987. Comparisons 01 X-ray and gamma-ray sources for加dustrlalIrradlatlon processes. Nuclear Ins加 .men包 andMethods in Physics Research 824/25. 967-972.
Cleland. M.R. and G.M. Pageau. 1987. Radlatlon processlng 01 medlcal de叫C3Sand food. In: Preprint of an invited paper for 20 th Midyear Topical Meeting of the Health Physfcs Society. 8-12 February,唱5pp.
Dol. T. 1992. Economical aspects 01 Industrial elt:掲:tronaccelerators. Proc. OAEP/JAERI/JAIF Workshop on Industrlal Utilization 01 日曜掲:tronAccelerators. 9 July 1992.
附lan.T.唱988.Commercial trial on radiation pn措 erval旬。n01 onions under 位。picalcond闘ons.加:Flnal mee百四901 project comml位:ee01 RPFI phase 11. Office of Atomic Energy for Peace. Bangkok 1988.
Lustre. A.O..Ang. L. Dianco. A.. Caba附n.E.G., and Narvarro. Q.O.. Phiー
lippines experience in marketing Irradiated loods. Proc. ASEAN Workshop on Food Irradiatlon. 8angkok 1985. Association 01 South East Asean Nations. Food HandlJng 8ureau.陥.ala加mper.1985. 52-59.
Maha, M.官988.Technology transler 01 irradiatlon ollrozen shrimps, drled fish and spices. In: Final meeting 01 project commlttee of RPFI Phase 11. Off.ce of Atomlc Energy for Peace. 8angkok. 1988.
Martin. M. 1988. CommercializaUon storage and transportation studles 01 Irradiated drled flsh and目sheryproducts and onlons.加:Flnal meeting of project committee of RPFI Phase 11. Offic~ 01 Atomlc Energy for Peace., 8angkok 1988.
Moy, J. 1984. Economlc fe舗 Ibllitystudy:lrradlatlon 01 Mexican Irul箇.
In IAEA Pr叫曜掲:tMEX/5/01-01 Rep。同.42pp.
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JAKKI-M 93-160
Table 1 Advantages and disadvantages of gamma-ray, electron beam and X-ray
Radiation 1.Advantages
Gamma-ray (l)The penetrating quality
of radiation permits the treatment of variety of medical and agricultural products packed in shipping cartons.
(2)Steady emission of energy assures the availability of power when need and gives producible results from the treatment process.
(3) Modular source capsules permit matching the power output to the production requirements.
(4)The irradiation process can be monitored by physical means (dosimetry) and controlled
by a single parameter (exposure time).
(5)The efficacy and reliability of gamma—ray processing has been demonstrated in numonus facilities over many years.
(6)This technology is suitable for the underdeveloped countries because the operation and maintainance of irradiation facility does not require highly skilled personel.
Electron beam (1)The radiation intensity
within the beam is very high so the exposure time is very shot and product degradation is minimized.
(2)The product conveyor is simpler and less expensive than in a gamma-ray facility since a single pass or at most two passes through the beam is sufficient.
(3)The power utilization is higher than with gamma rays due to the forward concentration of the beam and its controlled penetration.
(4)Operating exposures can be minimized by running the accelerator only when it is needed.
(5) Process validation proceedures need not be repeated after the accelerator is serviced, provided that tho operating parameters have not changed.
(6)The accelerator can be installed above ground within an ordinary building.
(DAccelerators facilities are licensed by state agencies in the same manner as medical X-ray equipment and the procedure are less than the licensing of large gamma-ray facilities.
(8)The future availability and price of accelerators will be determined by the market place rather than by governmental policies.
(9)The total cost of electron beam processing is less than gamma ray sterilization in facilities with throughput capacities of 1 million cubic feet per year or greater.
X-ray (l)Most of the advantages
of electron beam processing also apply to X—ray processing, w/o the disadvantage of low electron penetration.
(2)The greater penetration of 5 MeV X-rays versus Co-60 gamma rays will reduce the max/min dose ratio in pallet loads of heavy products, especially agricultural commodities.
(3)The forward concentration of the X-rays versus isotopic gamma-rays will reduce the irradiation time, there by reducing product degradation.
(4)The smaller radiation zone will simplify the product conveyor, there by improving its reliabilty and reducing its cost.
(5)The smaller volume of material in the irradiation chamber will increase operating efficiency by reducing the time lost between production lots with different dose requirements.
(6)An X-ray generator can provide the comfort and convenience of a controllable eletrical device with the product penetration and dose uniformity now obtainable only from radioactive materials.
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JAER[-M 93-160
Table 1 Advantages and disadvantages of gamma-ray, electron beam and X-ray
Aadiation Gamma-ray Electron beam X-ray
1.Advar詑ages 。)The阿南町atingq咽 I町 。)Therad凶 lonintensily (1)Most of rt栂 advantagesof radiation permi1s廿砲 w耐lin智満 beamis very high of elec甘onbeampro回 ss耐喝
treatment of var恰,tyof 80世l6expos .... e time is very also apply to X-ray pro-medi国 Iand agriω,ltlI'al shot and prodl胤 degradation 同 ssing,w/o廿裕 dis-prod凶 tspacked in sh恥ー isminim包,ed. a耐 antage01 Iow ele曲。np!::-羽 cartons. per晦tration.
(2)腎裕 prodl応t∞m肉9yor(2)Steady emission of is slmpler ar凶 lessexpen- (2)The greater pene智ationer栂rgyass .... es官時 sive甘首iT'Iin a gamma-ray 01 5 MeV X -rays versus availabiliザofpowerw同 n facility since a single pass Co-60 gamma rays will need ar凶 givesprod凶 ible 。rat mosth¥o passes redu曲甘l6max/min dose results 110m曾l6treatment 甘V"ough甘l6beamis ratio in pallet Joads of 加卸yprocess. 8U何Icler官,. prodl応ts,especial¥y agri-
削除lal∞mmodities.。,)Modular80 .... '伺 (3)The power util回,tion
G申書ulespermlt mat- is hlgher曽祖nw,附E (3)The forward∞m割問釘ationching廿l6power out- gamma rays due to廿砲 01廿晦 X-raysversus is010pic putto曾l6prod,凶tion forward cor時entrationof gamma-rays will reduce世W
(4)The irradlatlon pro-国 ssc叩 bemon陶 red (4)Operati司 exposぽ'es (4)育時 smallerradiation zone by physぬalmeans canbe minim包:edby will simplify曽裕 prod田 t(dosime町)and∞n加lIedrLn'lir唱曾l6ae<渇lerator col1¥f8yor,世l6reby Improvir喝by a single parameter onlyw同 nit is needed. its reliabilty ar刈 reducing(exposu-e time). I旬 cost.
(5)Pro回 ssvalidation (5)羽鳩柑i岨 cyand pro回 edU'e8need not be 側冒喝事mallervolume of rellablllty of gamma-ray repeated after rtl6 material in rtl6 irradiatlon pro旬 sslnghas been ao明 leratoris servi曲 d, chamber will inore舗申
(8)The fI胤...e副 al抱bilityandp同国。fac四 leratorswill be determlned by世W
marketpla曲 rartl6r世1artbygO¥自由mmentalpolicies.
(9)The total cost of electron beam pro同時ingis less世180
gamma ray sterllizatlon In facllities wilh廿官01喝hputcapac削倒。,f1 mllllon CLbic feet per year or greater.
phu 弓,
JAliRl-M 93-160
Table 1 (continued) Radiation
2.Disadvantages Gamma-ray Electron beam X-ray
2.Disadvantages (1)Th* relatively low (1 }The penetrating quality of (1)The cost of X - ray will be intensity of the radiation electrons is less than that of higher than electron beam require* long exposures gamma-rays and some thick processing because of the low during which the quality of objects cannot be processed efficiency for converting the product may be degraded by oxidative
with this kind of radiition. electrons to X-rays.
reactions . (2)Detailed dose of mapping (2)Further development on must be done within the the efficacy and reliability of
(2)The power utilization shipping cartons and inside X- ray processing In a efficiency is low due to the the various p oducts during commercial operation should iaotopic distribution and the process qualification be conducted. excessive penetration of procedures to assure the radiation.
(3)The radiation facility
adequate treatment of all materials.
must be operated (3)The operating parameters continuously to avoid of the accelerator may have wasting the energy of the to be varied to obtain the radioactive sources.
(4)The process validation
optimum dose uniformity and process efficiency.
procedures must be (4)Several machine parameters repeated whenever the in addition to the conveyor source loading is changed. speed must be monitored to
control the quality of the (5)Once built, a large
gamma irradiator with an treatment process.
in-ground storage pool (5)While highly reliable, an and thick concrete walls electron accelerator cannot is a permanent match the dependability of a installation that cannot easily be moved or
radioactive source.
converted to one other (6)The capital cost of an industrial use. industrial accelerator does not
scale down linearly with its (6)The approvals of various beam power rating for low-
federal and state agencies are required for the design.
capacity facilities.
construction and operation (7)The few electron machines of gamma facilities as well now being used for sterilization as for the procurement. have accumulated less ] transportation and installation operating time than the many of the source capsules. gamma—rays facilities.
(7)The growing antipathy of (8)Th* accelerator specifications the public and the news for new processing facilities may media regarding nuclear exceed the ratings of existing installations may impede the equipment, thereby requiring the construction and operation of development of new models with new facilities in some localities.
(8)The persistent emission of energy from the radioactive sources can be a continuing liability in the event of unforeseen equipment m a l function* or deliberate acts of sabotage.
no operating experience.
- 76 -
JAEI~I-M 93-160
Table 1 (continued)
Radiation Gamma-ray EI.ctron b・am X-ray
2.0i・advantag..。)Th・F・I・tiv・/ylow 。)Thepen柑 'atingquality 01 。)Th・co.t0' X-ray will b・int・nolty0' th・radiation .1・ctron・1・1・・・thanthat of high・rthan・lectronb・amv・quir..long・xpo.ur.o gamma-ray. and .om・thick proc...ing b・cau..0' th. 10'" during whlch th・quality0' 。bj・e句 cannotb・proceooed -筒cl・ncyforconv・rtingth・productmay b・ W詑hthi・kind0' radi'ltlon. el・ctron.to X-ray.. degraded by oxidldive
(2)τh・po_rutlli四 tion .hipplng carton・andin・Id・ X-ray proce..ing In a efficl・ncy抱 lowdue to th・th・V町iou.r: 'oduc'旬 during comm・問凶。pera量ion・houldiltQtopic dietribution and the proc... qualiflcation b・conduct.d.exce.eiv・p・n・,trationof proc.dur.e to ae.ur,・the radiatlon. ad.quate tr・atmentofall
mat.r陥1..。I)Theradiation facility mu.t be op・rat.d 例。Theop・ratingparamet'・mcontinuou・Iyto avold 。.fth・・M・E・ratormay have waating愉・・n・r9)'ofth. to b・var拘dto obtain th・radioactive lIource.. optimum doee unlformity and
procee・・町ici・ncy.(4)Th・proc....valida針。nproc・dure.mu.t b・ (4)8・V・ralmachin・param・terer・p・at,・dwh・n・v・rthe in addltlon to th・conv,・yoreouro・loadlngi・changed. ep・edmuat b・mon民。r.dt。
con加Ith・qu副ity0' th・t句Oncebullt. a larg・ tr・atm・ntDro<:ell・.gamma irradiator w民han in-ground・torag.pool (5)Whil・high/yr・lIabl・.an and thick concret,・ wall. el・e甘onacc・I・ratorcannot ie ap・rmanent match th・d・P・M・bilityof a inetallatlon that cannot radioac:tive eource. .踊l/yb・冊。v・dor 。onv・rt・dto on. oth・F {匂Th・capitalcoat 0' an indu・trialu.e. Indu柑 ialacc・I・ratordoe. not
.c.1・downIin・ar/ywith捻・{唖1)Th. approv・1・ofvario~!. beampow・rrating for low-f・d・raland .tat. ag・nci.1I capacity 'acllitlell. 町・r・quir,・df,町仙・d・・ign.conetruc泊。nand op・ration t乃Th・f.w・1・ctronmacllin.1I 。fgammafacil術elluw.1I nowb・ingu・・dfor IIt,・rilizationae for th. procur.m・nt. h酎・aocumulated1... tran.porta針。nand inetallation 。peratingtim. than th. many 。'the.ourc・cap・ul・・- gamma-ray. facil悩・..{乃Th・growing・ntipathy0' (8)Th・制e・I,rator・p・cifioation・th・pub“e・ndthe n・we lor n・wprocelllling facil付t・・ maymedia reg・rdingnuclear exceed the ratingll 0'・x拘tingIn・tallation・mayimp・d・the equipm・nt.thereby r.quiring th・。one甘uction・ndop・ration0' d・v・lopm・nt0' n・wmod・IlIwithn・wfacll侃f・IIln.om・ no op・r副 ng・xp・巾nce.locallti・・.(8)The p・v・l・t・M・mill討。n。,.ner9)' from th・radloactive.ouroe. o.n b・.oontinulng liabll仕yin th・・v・nt01
un'or・・・・n・qulpm・ntmal-function. or do・IIb・rate“"。f・abotage.
76
JAERI-M 93-160
Table 2 Linacs for industrial processing
FACTORY ENERGY POWER Mfg YEAR APPL OF INST. (MeV)
TWorSW (kw) COM. ICA.
IRT.San Diego 6 - 1 8 TW 2 X 7 ARCO S RISO,Denmark 6 - 1 4 TW 10 HAIMSON 1975 S&R Raychem,Denmark 6 - 1 4 TW 10 Varian 1976 O CARIC, France 7TW 7 C G R - M e V 1967 S Waesaw, Poland 13 TW 9 Efremov R.S Harwell, UK 8 - 1 2 TW 25 Tech.Sys.L. 1985 R.S SPI, France 8 V H F 5 C G R - M e V 1986 F CARIC 10 TW 20 C G R - M e V 1987 S SCAN-CARIC, 10 TW 25 C G R - M e V 1988 S Sweden Florida-USA 10(E3)TW 10 C G R - M e V 1990 F Florida-USA 5(X-ray) 20 Iowa-USA 10 TW 20 C G R - M e V 1990 F ChampArdenne 10 TW 20 C G R - M e V 1990 S SPI, France 10 TW 20 C G R - M e V 1990 F Molnlycke.Sweden 10TW 2 5 X 2 C G R - M e V 1991 S Karlsruhe, 10 TW 20 C G R - M e V 1991 F.S West Germany Aerospatial, France 10 TW 20 C G R - M e V 1991 O
Fig. 1 A linac facility for research of food processing by electrons. It has two beam lines and scanners. One for direct electron irradiation at 10 MeV and another for generation of and processing by 5 MeV X-rays. Energy of electrons incident on samples is limited within a narrow range by a bending magnet.
/
, 、,
,
, " 、‘ノ.一,
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、 ,、ι
一‘''一、ーe 、 、 一一'、
~ " ,/ ' 、 ι ,,也, ' 、,、、 A
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" ,
,
, , , ,
, ,
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8150
¥t
同日一
, ,
TREATMENT OF PALLETS 、
、a∞
X-RAY SCANNING HORN
ELECTRON BEAM SCANNING HORN
A linac facility for research of food processing by electrons. It has two beam lines and scanners. One for direct electron irradiation at 10 MeV and another for generation of and processing by 5 MeV X-rays. Energy of electrons incident on samples is limited within a narrow range by a bending magnet.
1 Fig.
JAERI-M 93-160
0 10 20 30 40 50 60 70
Fig. 2 Percentage depth dose distribution in water or unit density materials for single-sided irradiation: (A) 10 MeV X-rays: (B) 5 MeV X-rays: (C) 60Co gamma-rays: (D) 137Cs gamma-rays.
- 79 -
]AERI-M 93-160
DEPTH DOSE DISTRI8UTION
SINGLE SIDE -UNIT DENSITY
↑zωυg凶仏
100
90
60
60
50
70
40
30
20
10
9
8
7
6
5
X-RAYS A 10 MeV 4
5 MeV X-RAYS B
Co-60 GAMMAS C 3
Cs-13アGAMMASD
2
THICKNESS-CM
。 70 60
Percentage depth dose distribution in water or unit density materials for single-sided irradiation: (A)_lO MeV X-rays: (B) 5 MeV X-rays: -(C) 60Co gamma-rays: (D) 137Cs gamma-rays.
-79-
50 40 30 20 10
Fig. 2
JAERI-M 93-160
10 T 1 1 1 1 1 1 1 1 1 1 r
MAX/MIN DOSE RATIOS OPPOSITE SIDES-UNIT DENSITY
A 10 MeV X-RAYS
6 5 MeV X-RAYS C C o - 6 0 GAMMAS D Cs-137 GAMMAS
Fig. 3 Max/min dose ratio vs unit-density product thickness for two-sided irradiation: (A) 10 MeV X-rays: (B) 5 MeV X-rays: (C) *>°Co gamma-rays: (D) 1 3 7 C s gamma-rays.
- 80 -
jAERI-M 93-160
10
MAX/MIN DOSE RATIOS
OPPOSITE SIDES-UNIT DENSITY
10 MeV X-RAYS A
9
8
7
5 MeV X-RAYS
Co-60 GAM MAS
Cs-137 GAMMAS
B
C
D
(Z-2}O¥{X42}O
6
5
4
3
2
THICI<NESS -CM
o o 70
Max/min dose ratio vs unit-density product thickness for two-sided irradiation: (A) 10 MeV X-rays: (B) 5 MeV X-rays: (C) 60Co gamma-rays: (D) 137Cs gamma-rays.
-80一
60 50 40 30 20 10
Fig. 3
JAER1-M 93-160
2.7. EB Treatment of Wastewater and Sewage Sludge S. Hashimoto
Takasaki Radiation Chemistry Research Establishment Japan Atomic Energy Research Institute
ABSTRACT Ionizing radiation is useful for decomposition of pollutants
in wastewater and disinfection of solid waste as sewage sludge. For application of electron beam, quite different technologies from those of gamma-ray are required because of short penetration range and high dose rate of electron beam. In this report, differences of irradiation effect between gamma-ray and electron beam and irradiation technologies are introduced from a viewpoint of application of electron beam to environmental conservation.
1. Introduction Applications of ionizing radiation to environmental conservation are well known. There are several effects of radiation on pollutants as follows;
1) Removal of pollutants by oxidative degradation. 2) Elimination of toxicity, color and smell of pollutants and
addition of biodegradability by changing chemical structure. 3) Inactivation of dangerous microorganisms and parasites. 4) Improvement of precipitation and filtration properties of fine
particles of pollutant. Recently, an electron accelerator has been evaluated as a practical and economical radiation source because of large output power. But, penetration range of electron beam is usually very short and dose rate is very high compared with gamma-ray from cobalt-60. These properties require quite different technologies from those of gamma-ray for the application of electron beam.
In this report, effects of penetration range and dose rate of electron beam on decomposition of organic pollutants and disinfection of bacteria are discussed. Irradiation technologies for liquid and solid are also introduced from a
81
jAERI-M 93-160
2.7. EB Treatment of'司1astewater and Sewage Sludge
S. Hashimolo
ABSTRACT
Takasaki Radia七ionChemistry Research Establishment Japan A七omicEnergy Research工ns七i七U七e
10nizing radiation is useful for decomposition of pollutants in wastewater and disinfection of solid waste as sewage sludge. For application of electron beam, quite different technologies from those of gamma-ray are required because of short penetration range and high dose rate of electron beam. 1n this report,
differences of ir・radiationeffect between gamma-ray and electron beam and irradiation technologies are introduced from a viewpoint of application of electron beam to environmental conservation.
1. 1ntroduction
Applications of ionizing radiation to environmental conservation are well known. There are several effects of radiation on pollutants as follows;
1) Removal of pollutants by oxidative degradation. 2) Elimination of toxicity, color and smell of pollutants and
addition of biodegradability by changing chemical structure. 3) Inactivation of dangerous microorganisms and parasites. 4) Improvement of precipitation and filtration properties of fine
particles of pollutant.
Recently, an electron accelerator has been evaluated as a practical and economical radiation source because of large output power. But, penetration range of electron beam is usua11y very short and dose rate i8 very high compared with gamma-ray from cobalt-60. These properties require quite different technologies from those of gamma-ray for the application of electron beam.
1n this report, effects of penetration range and dose rate of electron beam on decomposition of organic pollutants and disinfection of bacteria are discussed. 1rradiation technologies for 1iquid and solid are a1so introduced from a
81
JAERI-M 93-160
viewpoint of applications of electron beam to environmental conservation.
2. Treatment of wastewater
Experimental results on decomposition of pollutants by ionizing radiations are summarized in Table 1. Various kinds of organic pollutants are possible to decompose by radiation. ' It is well known that oxygen often shows important roll on the decomposition of organic pollutants. Effect of oxygen on radiation decomposition of phenol in aqueous solution is shown as an example. ' The initial concentration of the phenol was adjusted to be 1CP 3 mol/1. Irradiation dose to decrease the concentration to 1/10 is about 8 kGy in the solution with oxygen, but, more than 30 kGy is necessary without oxygen. Oxygen is also effective for decoloration of dye in wastewater. '
3. Disinfection of sewage sludge
Ionizing radiation is also useful for disinfection of solid wastes as sewage sludge. Fig. 2 shows reduction of total coliforms in sludge after irradiation by electron beam. In this case, dose rate was adjusted to be the same order of gamma-ray by special irradiation method. Initial value of total coliforms in sludge is about 10 cells/g. The irradiation dose for two log cycle reduction of surviving fraction is about 0.15 kGy in aerobic condition, but, more than 0.75 kGy in anaerobic condition. Oxygen shows very important roll for effective disinfection as same as radiation decomposition of organic pollutants.
4. Important factors for EB irradiation
1) Depth dose
One of the big differences between gamma-ray and electron beam is dose distribution along the pass in the sample to be irradiated. A depth dose curve for gamma-ray from cobalt-60 in the water is shown in Fig. 3. Relative dose decrease exponentially with thickness of water. Half-value layer in water is abrut 11 cm. Fig. 4 shows depth dose curves for electron beam. Dose in water increases at first with increase of thickness and then decreases. Maximum penetration range ( mass thickness, g/cm2 ) is different depend on beam energy and the value is 1.1 cm for 2 MeV. The thickness to give the same dose as that at the surface is called
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jAERI -M 93-160
viewpoint of appllcations of electron beam to environmental conservation.
2. Treatment of wastewater
Experimental results on decomposition of p011utants by ion工zlngradiations are summarized in Table 1. Various kinds of organic
1) p011utants are possib1e to decompose by radiation.~J It is we11 known that oxygen often shows important r011 on the decomposltion of organic p011utants. Effect of oxygen on radiation decomposition of phen01 in aqueous solution is shown as an
2) examp1e.~J The initia1 concentration of the phen01 was adjusted to be 10-0 m01/1. Irradiation dose to decrease the concentration to 1/10 is about 8 kGy in the s01ution with oxygen. but. more than 30 kGy is necessary without oxygen.Oxygen is
3) a1so effective for dec010ration of dye in wastewater.
3. Disinfectlon of sewage s1udge
Ionizing radiation is a1so usefu1 for disinfection of s01id wastes as sewage s1udge. Fig. 2 shows reduction of tota1 c01iforms in sludge after irradiation by electron beam. 工nthis case. dose rate was adjusted to be the same order of gamma-ray by specia1 irradiation m~thod. Initia1 value of tota1
7 c01iforms in sludge is about 10' ce11s/g. The ir・radiationdose for two 10g cyc1e reduction of surviving fraction is about 0.15 kGy in aerobic condition. but. more than 0.75 kGy in anaerobic condition. Oxygen shows very important r011 for effective
disinfection as same as radiation decomposition of organic po11utants.
4. Important factors for EB irradiation
1) Depth dose
One of the big differences between gamma-ray and e1ectron beam is dose distribution along the pass in the samp1e to be irradiated. A depth dose curve for gamma-ray from cobalt-BO in the water is shown in Fig. 3. Relatlve dose decrease exponentially with thickness of water. Half-va1ue layer ln water is ab~ut 11 cm. Fig. 4 shows depth dose curves for electron beam. Dose in water increases at first with increase of thickness and then decreases.
2 Maximum penetratlon range ( mass thickness. g/cm~ ) Is different depend on beam energy and the value is 1.1 cm for 2 MeV. The thickness to give the same dose as that at the surface is called
-82 --
JAERI-M 93-160
"Effective penetration range".
Fig. 5 shows surviving fraction of total bacteria in sludge after irradiation. To kill bacteria effectively, sludge thickness must be less than 6 mm for beam energy of 2 MeV and 3 mm for 1 MeV. These values correspond to the effective penetration ranges for those energies. '
2) Dose rate
Usually, dose rate of electron beam is very high compared with gamma-ray because output power of electron accelerator is very large and penetration range of electron beam is very short. The dose rate of electron beam is, sometimes, higher more than 100 times compared with that of gamma-ray irradiation. This deference of dose rate often give a large deference of reaction rate for polymerization. But the effect of dose rate is not so large for decomposition of organic pollutants like phenol as shown in Fig. 6. '•°' Fig. 7 shows effect of dose rate and energy of electron beam on disinfection of microorganisms in sludge. Results for gamma ray irradiation are also shown in this figure. No effects of energy and do^e rate can be seen in the survival curves of total bacteria and conforms. '
5. Irradiation technology for electron beam
1) Wastewater
By an electron accelerator, short time is enough to give a certain dose because dose rate is -rery high as mentioned before. So, it is necessary to remove the wastewater quickly from the penetration range (reaction zone) of electron beam. In addition to this, effective oxygen supply is required during irradiation for aerobic decomposition of organic pollutants and disinfection of microorganisms.
A thin layer reactor as shown in Fig. 8 is possible to get a uniform irradiation and suitable for removing the wasterwater quickly from the reaction zone. Oxygen in the reactor decreases during the irradiation according to the G-value of oxygen consumption by chemical reactions caused by the irradiation. The concentrations of oxygen were calculated ' and shown in Fig. 9. It can be seen that the oxygen concentrations decrease rapidly with irradiation dose. This means, oxygen supply during irradiation can not be expected. But, this reactor is effective
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]AERI-M 93-160
"Effectlve penetratlon range".
Flg. 5 shows survlvlng fractlon of tota1 bacteria ln sludge after irradlation. To kl11 bacteria effectively, sludge thickness must be 1ess than 6 mm for beam en己rgyof 2 MeV and 3 mm for 1 MeV. These va1ues corr~spond to the effectlve penetration
4) ranges for those energies.
2) Dose rate
Usua11y, dose rate of e1ectron beam is very high compared with gamma-ray because output power of e1ectron acce1erator Is very 1arge and penetration range of e1ectron beam is very short. The dose rate of e1ectron beam is, sometlmes, hlgher more than 100 times compared with that of gamma-ray irradiation.
Thls deference of dose rate often give a 1arge deference of reaction rate for polymerizatlon. But the effect of dose rate
rate and energy of e1ectron beam on disinfection of microorganisms in sludge. Results for gamma ray ir・radiationare a1so shown in thls flgure. No effects of energy and do~e
rate can be seen in the surviva1 curves of tota1 bacteria and co1iforms.6)
5. Ir・radiationtechno1ogy for electron beam
1) Wastewater
By an e1ectron acce1erator, short time Is enough to give a certain dose because dose rate isηery high as mentioned before. So, it is necessary to remove the wastewater quickly from the penetration range (reaction zone) of electron beam. In additlon to this, effective oxygen supply is required durlng ir・radiatlon for aerobic decomposition of organic pollutants and disinfection of microorganisms.
A thin layer reactor as shown ln Fig. 8 Is possible to get a uniform irradiation and suitable for removlng the wasterwater qulckly from the reaction zone. Oxygen in the reactor decreases during the irradiation according to the G-value of oxygen consumption by chemlcal reactions caused by the ir・radiation.
1) The concentrations of oxygen were ca1culated~J and shown in Flg. 9. It can be seen that the oxygen concentrations decrease rapidly wlth irradiation dose. This means, oxygen supply during ir・radlatloncan not be expected. But, this reactor is effective
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JAERI-M 93-160
when oxygen supply is not necessary. A flat nozzle is also possible to use for making thin layer of wastewater.
A spray tower reactor as shown in Fig. 10 is more effective to supply oxygen because the surface area, which contacts with the gas, is larger than that of thin layer reactor. But, oxygen supply is not enough even in this reacto .
Fig. 11 shows a mixing-type reactor. Irradiated liquid is removed from the reaction zone by mixing. Oxygenated liquid is continuously supplied from the area under reaction zone.
A dual-tube bubbling column reactor is improved from the mixing-type reactor. As shown in Fig. 12, this reactor has a outer tube and a inner tube. Wastewater circulates in the reactor by airlift. Oxygen is effectively supplied to the liquid in the oxygen absorption zone under the reaction zone and go to the reaction zone by circulation. After irradiation, the liquid quickly flow down from the reaction zone. Oxygen concentrations in the liquid were calculated and shown in Fig. 13. Compared with those for the thin layer reactor, values for the dual-tube bubbling column reactor are higher. This shows that oxygen supply in the bubbling column is effective.
A multi-stage bubbling column reactor as shown in Fig. 14 was used in our study to treat a larger amount of wastewater. ' , i 5' Five dual-tube bubbling columns were connected together. In this case, we can make the irradiation dose for each culumn small. This means that oxygen supply become easier and it is also possible to prevent back mixing which make the treatment ineffective.
2) Sewage sludge cake
In dewatered sewage sludge irradiation with moisture content of 75 to 80 %, it is very difficult to supply oxygen during irradiation because effective mixing is impossible and diffusion factor of oxygen in sludge cake is very small. In addition to this, sludge contains large number of microorganisms and the consumption of oxygen by respiration of microorganisms is very large even without irradiation. As conclusion, effect of oxygen can not be expected in practical treatment of sewage sludge cake and most important technology is how to make a thin layer of sludge cake for enough penetration of electron beam.
Fig. 15 shows the machine we used for making thin layer of sludge cake. This machine was set under the scan horn of electron accelerator in the irradiation room. The raw sludge was
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JAERI-[¥1 93-160
when oxygen supply is not necessary. A flat nozzle Is also possible to use for making thin layer of wastewater.
A spray tower reactor as shown ln Fig. 10 Is more effective to supply 0λygen because the surface area. whlch contacts wlth the gas. is larger than that of thin layer reactor. But. oxygen supply Is not enough even in thls reacto
Flg. 11 shows a mlxlng-type reactor. Irradlated 11quid is removed Irom the reaction zone by mlxing. Oxygenated liquid is continuously supplled from the area under reactlon zone.
A dual-tube bubbllng column reactor Is lmproved from the mlxing-type reactor. As shown in Fig. 12. this reactor has a outer tube and a lnner tube. Wastewater clrculates ln the reactor by airlift. Oxygen Is effectively supplied to the 11quld in the oxygen absorption zone under the reaction zone and go to the reaction zone by clrculation. After irradlation. the 11quld qulcklY flow down from the reaction zone. Oxygen concentratlons in the liquld were calculated and shown ln Fig. 13. Compared with those for the thin layer reactor. values for the dual-tube bubbling column reactor are hlgher. Thls shows tt.at oxygen supply ln the bubbllng column Is effective.
A mUltl-stage bubbllng column reactor as shown ln Flg. 14_.w~~ used ln our study to treat a larger amount of waste;ater.3).5) Flve dual-tube bubbling columns were connected together. ln this case. we can make the lr・radlatlondose for each culumn small. This means that oxygen suptly become easier and lt Is nlso possible to prevent back mixlng whlch make the treatment lneffective.
2) Sewage sludge cake
ln dewatered sewage sludge irradiation wlth molsture content of 75 to 80 %. it Is very difficult to supply oxygen during ir・radiationbecause effective mixing Is imposslble and diffuslon factor of oxygen ln sludge cake Is very small. ln addition to thls. sludge contains large number of microorganisms and the consumptlon of oxygen by respiratlon of mlcroorganisms Is very large even without lr・radiation. As concluslon. effect of oxygen can not be expected ln practlcal treatment of sewage sludge cake and most lmportant technology Is how to make a thln layer of sludge cake for enough penetratlon of electron beam.
Fig. 15 shows the machlne we used for maklng thln layer of sludge cake. This machlne was set under the scan horn of electron accelerator ln the lrradlation room. The raw sludge was
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transported from a reservoir to flat nozzle by a sludge pump. The width of the nozzle was 20 cm and sludge thickness was adjusted to be 6 mm. The maximum feed rate of sludge is 300 kg/hr. It was proved that continuous disinfection of sludge cake is possible by the combination of an electron accelerator and this machine. '
REFERENCES 1) S. Hashimoto; "A study on Radiation Treatment of Wastewater
Using an Electron accelerator", JAERI-M 9940 (1982). 2) S. Hashimoto et al.,"A liquid Chromatographic Study on the
Radiolysis of Phenol in Aqueous Solution", Environmental Science & Technol.. Vol. 13, p. 71 (1979).
3) S. Hashimoto et al., "Decoloration and Degradation of an Anthraquinone Dye Aqueous Solution in Flow System Using as Electron Accelerator, Radiat. Phys. Chem., Vol. 13, p. 107 (1979).
4) S. Hashimoto et al., "Economic Feasibility of Irradiation-Composting Plant of Sewage Sludge, Radiat. Phys. Chem., Vol. 31, p. 109 (1988).
5) S. Hashimoto et al., "Radiation-Induce Decomposition of Phenol in Flow System, Radiat. Phys. Chem., Vol. 16, p. 59 (1980).
6) S. Hashimoto et al, "Disinfection of Sewage Sludge Cake by an Electron Accelerator", J. Ferment. Technol., Vol. 64, No. 4, p 299 (1986) .
7) S. Hashimoto et al., "Pilot Plant Test of Electron-Beam Disinfected Sludge Composting", Wat. Sci. Tech., Vol. 23, Kyoto, p. 1991 (1991).
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JAERI-M 93-160
transported from a reservoir to f1at nozz1e by a sludge pump. The width of the nozz1e was 20 cm and sludge thickness was adjusted to be 6 mm. The maximum feed rate of sludge is 300 kg/hr. It was proved that continuous disinfection of sludge cake is possib1e_ty the combination of an e1ectron accelerator and this ~achine.7)
REFERENCES
1) S. Hashimoto; "A study on Radiation Treatment of Wastewater Using an Electron accelerator". JAERI-M 9940 (1982).
2) S. Hashimoto et a1....A 1iquid Chromatographic Study on the Radio1ysis of Phenol in Aqueous Solution". Environmenta1 Science & Techno1.. Vol. 13. p. 71 (1979).
3) S. Hashimoto et a1.. "Decoloration and Degradation of an
Anthraquinone Dye Aqueous S01ution in F10w System Using as E1ectron Acce1erator. Radiat. Phys. Chem.. Vol. 13. p. 107 (1979).
4) S. Hashimoto et a1., "Economic Feasibility of Irradiation-Composting P1ant of Sewage S1udge. Radiat. Phys. Chem.. Vo1. 31. p. 109 (1988).
5) S. Hashimoto et a1., "Radiation-Induce Decomposition of Pheno1 in Flow System. Radiat. Phys. Chem., V01. 16. p. 59 (1980) .
6) S. Hashimoto et a1, "Disinfection of Sewage S1udge Cake by an E1ectron Acce1erator", J. Ferment. Techn01.. Vo1. 64. No. 4, p 299 (1986).
7) S. Hashimoto et a1.. "Pilot P1ant Test of E1ectron-Beam Disinfected S1udge Composting・, Wat. Sci. Tech., V01. 23,
Kyoto. p. 1991 (1991).
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Table 1 Decomposition of various pollutants by ionizing irradiation
Fig. 4 Dose distribution of electron beams in water
O
1
S 10-2 CD
I 10-4 >
co 10-6
Surface dose: 10 kGy Dose rate: 10 kGy/sec
Voltage 1MV
0
--o-0'
4>^i—^
2MV
2 4 6 8 10 Sludge thickness (mm)
Fig. 5 Surviving fraction of bacteria in sludge irradiated with various thickness
- 8 8 -
JAERI-M 93-1印
1.0
<J.) 0.8
(J)
O てコ 0.6
(]J
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庄
。o 0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.6 1.8 2.0
Depth in water (cm)
Fig. 4 Dose distribution of electron beams in water
Surface dose: 10 kGy Dose rate: 10 kGy/sec
ハ---ベコー-一一0-一戸-~~VoL tage
1MV 戸ηJ」nHU
A--
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/ J
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nHU
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2 4 6 8 10 Sludge thickness (mm)
Fig. 5 Surviving fraction of bacteria in sludge irradiated with various thickness
-88一
JAERI-M 93-160
o 5kGy/hr| A 2 kGy/hr> Gamma ray D 1 kGy/hri
Electron beam
4 8 Dose (kGy)
Fig. 6 Effect of dose rate on decomposition of phenol
> "> to
1
10'1
10"2
10 " 3
10"*
10
10"
-5
Energy and dose rate (MeV, MGy/h): 2, 0.02 (O), 2, 18 (A), 2, 36 (O), 2, 65 (O), 0.5, 25 (V). Sludge thickness: 1 mm. The result of y-ray irradiation is shown by •&•. Open symbols represent total bacteria, and solid ones total coliforms.
Dose (kGy) 10
Fig. 7 Effect of dose rate and energy on disinfection of bacteria in sludge
- 89 -
JAERI-M 93-160
-、
12
o 5 kGY/hr) D. 2 kGy/h叶r}Ga附 na悶
口 1kGY/1向hrJ
Ql 〉
1 1 1 1 1 1 1 1 1 1 1 1 ¥ ¥ ¥ ¥ ¥ ¥ ¥
¥ ¥
¥ ¥
u c
8 0.5 ー--Electron beam
↑。一ω庄
。 4 8
Dose (kGy)
Fig. 6 Effect of dose rateμn decomposition of phenol
10斗
c 10・2。→ーιJ z 10・3。、〉C
と 10-1;コω
10-5
10-6
O
Energy and dose rate (MeV, MGyfh): 2, 0.0但2
i(O山Sludg酢et山hic】kness:1 mm. The result of yγ-ray irra-
diation is shown b匂Y"'i食苛 Opensymbols represent
5
Dose (kGy)
10
Fig. 7 Effect of dose rate and energy on disinfection of bacteria in sludge
ー 89
JAERI-M 93-160
Electron accelerator
INI Liquid
Gas
<j O O _ O O O O O O
• » ° o ° oh o o o o
Bubble
G..L
Fig. 8 Thin layer reactor
Initial cone. 40 ppm o c o a g 0.5 CD
Dose (kGy) Fig. 9 Oxygen concentration in thin layer reactor
Fig. 15 Irradiation of dewatered sludge by electron beam
~94-
jAERI-M 93-160
Reservoir tor raw slUdge
I Ftαt nozzle
A +¥
Feed Tump Grinder
stainless conveyor /
議J
Raservorr tor lrradiated sludge
Fig. 15 lrradiation of dewatered sludge by electron beam
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JAER1-M 93-160
2.8. Flue Gas Purification with Electron Accelerators W. Kawakami
Takasaki Radiation Chemistry Research Establishment Japan Atomic Energy Research Institute
1. INTRODUCTION Higher industrialization and living standard have been realized on much
consumption of fossil fuel as a major source of energy. Consumption of fossil fuel accompany with emissions of S 0 2 and NOx which cause acid rain of recent serious global environmental problem.
Diversification of energy sources, on the other hand, has been important in Japan from a viewpoint of energy security. Use of coal, in addition to natural gases as fuel in electric power stations have been revaluated to avoid being partial to petroleum. So a new process has been required for S0 2 and NOx removal from coal-fired flue gas.
Most of municipal waste, further, have been treated by incineration, in Japan. Recently, municipal governments are asked often to make slow down operation of incinerators in sunny days of summer to reduce emission of NOx which cause photo-chemical smog.
EB treatment technology of flue gases for simultaneous removal of S0 2
and NOx has a long history in its developmental research as shown in Table 1. We started two pilot tests for applying this technology to treatment of coal-fired flue gas and exhaust gas from municipal waste incinerator 1991.
This paper reviews JAERI's R & D of this technology for applying to flue gases from heavy-oil burning boiler, iron-ore sintering furnace, coal-fired power station and municipal waste incinerator.
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JAERI-M 93-160
2.8. Flue Gas Purification with Electron Accelerators
W.Kawa.加mi
Takasaki Radiation Chemistry Research Establishment Japan Atomic Energy Research Insti七ute
1. INTRODUCTION
Higher industrialization and living standard have been realized on much
consumption of fossil fueI as a major source of energy. Consumption of
fossi1 fuel accompany with emissions of S02 and NOx which cause acid
rain of recent serious globaI environmentaI problem.
Diversification of energy sour,切ら onthe other hand, h路 b民,nimportant
in Japan from a viewpoint of energy security. Use of∞al, in addition to
natural gases as fuel in electric power stations have been revaluated to
avoid being partial to p抑 oleum. So a new pro回 sshas been required for
S02 and NOx removal from∞al-畳間dflue gas.
Most of municipal waste, further, have been tieated by incineration, in
Japan. Recently, municipal governments are asked often to make slow
down operation of incinerators in sunny days of summer to reduce emission
of NOx which cause photo-chemi伺 lsmog.
EB treatment technology of flue gases for simultaneous removal of S02
and NOx has a long history in its developmental research as shown in
Table 1. We started two pilot tests for applying this technology to treat-
ment of∞al-fired flue gas and exhaust gas from municipal waste incinera-
tor 1991.
This paper reviews JAERI's R & D of this technology for applying to flue
gases from heavy-oil burning boiler, iron-ore sintering furnace,∞al一面'ed
power station and municipal waste inciner:ator.
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JAERI-M 93-160
2. TREATMENT OF HEAVY OIL BURNING FLUE GAS The systematic research of the EB process of flue gas treatment was
started under the cooperation of JAERI and Ebara Co., in 1972(1). In this
research, a small scale flow-type apparatus(60 Nm3/h) shown in Fig.l was
used. Flue gas from a heavy oil burner was led to the irradiation chamber
after removing dust by an electrostatic precipitator. The gas contained
600-900ppm S 0 2 and 80ppm NOx. The gas was circulated using a blower
at a higher flow rate than the supplying rate between the chamber and an
electrostatic precipitator for mixing gas to get uniform irradiation.
Fig. 2 shows effect of EB irradiation on S 0 2 and NOx removal for
various conditions. It was firstly found that the EB treatment of exhaust
gas could remove S 0 2 and NOx in it, simultaneously.
3 . FLUE GAS FROM AN IRON-ORE SINTERING FURNACE
The EB technology was applied to removal of NOx in exhaust gas from
iron-ore sintering furnace. The exhaust gas from the furnace contains high
concentration of dust which make the life time of the catalyst for removal
of NOx shorter, so a new process was required for NOx removal. JAERI
carried out a basic research (gas flow rate: 1 Nm3/h) using synthetic gas to
develop this technology(2). It was shown that S02 and NOx could be
effectively removed by EB irradiation in the presence of added Ammonia.
Based on these results, a pilot plant test was carried out at the scale of
10,000 Nm3/h by Research Association for Abatement and Removal of
NOx in the Steal Industry and Ebara Co. at Wakamatsu Works of Nippon
steel Corporation(3). In this plant two electron accelerators of 750keV,
60mA each were installed. Fig.3 shows the result of pilot plant test. As
seen in this figure, the S 0 2 and NOx removal efficiencies were maintained
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JAERI-M 93-160
2. TREATMENT OF HEAVY OIL BURNING FLUE GAS
The systematic research of the EB process of flue gas treatment was
started under the cooperation of JAERI and Ebara Co.,担 1972(1).In出s
research, a small scale flow-type apparatus(60 Nm3/h) shown面白g.1w槌
used. Flue gas from a heavy oi1 bumer was led to血eirradiation chamber
after removing dust by an electrostatic precipitator. The gas contained
600-900ppm S02 and 80ppm NOx. The gas was circulated using a blower
at a higher flow rate than the supplying rate between the chamber and an
electrostatic precipitator for mixing gas ωget uniform irradiation.
Fig. 2 shows effect of EB irradiation on S02 and NOx removal for
various conditions. It was first1y found that the EB treatment of exhaust
gas could remove S02 and NOx in it, simultaneously.
3. FLUE GAS FROM AN IRON-ORE SINTERING FURNACE
The EB technology was applied to removal of NOx in exhaust gas世om
ir:m-ore sintering fumace. The exhaust gas from the fumaα∞ntains high
concentration of dust which make the life time of the catalyst for removal
of NOx shorter, so a new process was required for NOx removal. JAERI
carried out a basic research (gas flow rate: 1 Nm3/h) using synthetic gas ω
develop this technology(2). It was shown that 502 and NOx could be
effectively removed by EB irradiation in the presence of added Ammonia.
Based on these results, a pilot plant test was carried out at the scale of
10,000 Nm3fh by Research Association for Abatement and Removal of
NOx in the Steal Industry and Ebara白.at Wakamatsu Works of Nippon
steel Corporation(3). In this plant two electron accelerators of 7S0ke V,
60mA each were installed. Fig.3 shows the result of pilot plant test. As
seen in this figure, the S02 and NOx removal efficiencies were maintained
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JAERI-M 93-160
over 95% and 85% at 15kGy and 80°C, respectively.
4. FLUE GAS FROM COAL-BURNING POWER STATION For EB treatment of coal-burning flue gas, systematic experiments were
carried out using simulated gases and a small scale flow-type apparatus shown in Fig.4(4). Standard gases were led a mixing vessel to get the simulated gas. The simulated gas was led to a irradiation chamber, before irradiation NH3 gas was added. Products in the irradiated gas were collected in an electrostatic precipitator and filter. In these experiments, multi-stage irradiation was examined to get higher removal efficiency for the same dose irradiation. The irradiation chamber are divided to three section as shown in the figure. Unirradiated time was 0.5 second, which is the gas passing time through the irradiation zone. So gas is irradiated intermittently.
Fig.5 shows effect of multi-stage irradiation on removal of NOx. It was found that higher NOx removal efficiency could be achieved by this method. Fig.6 shows effect of irradiation temperature on S0 2 removal. At 65 °Q higher removal efficiency is obtained than 70 °C.
Fig.7 shows th. nechanism of NOx and S02 removal reactions which are composed of both radical and thermal reactions(5). Solid lines indicate radical reaction, while dotted lines indicate thermal reactions. Formation of HN0 2 is very important for removal of NOx. Under irradiation, HN0 2
react with OH to produce NO via N0 2 , that is a reverse reaction. Without OH, HN0 2 decomposes thermally to HN0 3. This mechanism is reason why the multi-stage irradiation give higher removal efficiency of NOx. In SO z removal, there are thermal reactions between S 0 2 and NH3 as shown in this figure.
- 9 7 -
]AERI-M 93-160
over 95%組 d85% at 15kGy祖 d80oC, respectively.
4. FLUE GAS FROM COAL-BURNING POWER STATION
For EB treatment of∞al-buming flue gas, systematic experiments were
carried out using simulated gases and a small scale flow-type apparatus
shown in Fig.4(4). Standard gases were led a mixing vessel to get the
simulated gas. The simulated gas was led to a irradiation chamber, before
irradiatioD NH3 gas was added. Products in the irradiated gas were col-
lected in av electrostatic precipitator and filter. 1n these experiments,
multi-stage irradiation was examined to get higher removal efficiency for
the same dose irradiation. The irradiation chamber are divided to three
section as shown in the日gure.Unirradiated time was 0.5 second, which is
the gas passing time through the irradiation zone. Sc gas is irradiated
intermittentIy.
Fig.5 shows effect of multi-stage irradiation on removaI of NOx. It was
found that higher NOx removal efficiency could be achieved by this
method. Fig.6 shows effect of irradiation tempera旬reon S02 removal. At
65 oC, higher removal efficiency is obtained than 70 oC.
Fig.7 shows th. .nechanism of NOx and S02 removal reactions which
are ∞mposed of both radical and thermal reactionsσ). Solid lines indiαte
radical reaction, while dotted 1ines indicate thermal reactions. Formation
of HN02 is very important for removal of NOx. Under irradiation, HN02
react WIth OH to produce NO via N02, that is a reverse reaction. Without
OH, HN02 decomposes thermaI1y to HN03・Thismechanism is reason
why the multi-stage irradiation give higher removal efficiency of NOx.
In S02 removal, there are thermal reactions between S02 and NH3 as
shown in this figure.
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JAERI-M 93-160
On these basic results, a pilot-scale test for EB treatment of flue gas from coal-burning boiler has been started under the joint research of JAERI, Chubu Electric Power Company and Ebara Corporation. The plant was constructed in the site of Shin-Nagoya thermal power plant of Chubu Electric Power Company in Nagoya in October, 1992. The operation will be carried out for one year until December, 1993. The main purposes are to evaluate the three-stage irradiation method and the reliability of this process in long term operatioa.
Fig.8 shows a flow diagram of the pilot plant(5). 12,000Nm3/h coal fired flue gas is led to the pilot plant. The temperature is supposed to be 110 °C, and concentration of S 0 2 is 800ppm, NOx is 225ppm. Firstly, gas is cooled at the cooling tower to 65 °C. After adding NH3, the gas is led to irradiation vessel and irradiated by electron beams using 3 electron accelerating tubes. Voltage is ranging from 400 to 800kV, current is 135 mA maximum. Irradiated gas is led to the electrostatic precipitator and bag filter to remove by-products; ammonium sulfate and ammonium nitrate. Treated gas is vented from a stuck. Target of the test are; S 0 2 concentration is reduced to lower than 50ppm from inlet concentration of 800ppm, NOx is reduced to lower than 45ppm from 225ppm.
In Table 2, engineering problems in application of the EB process for treatment of flue gas from coal-fired power generation plants are summarized. The first one is saving of electricity consumption. It is required that energy consumption should be less than 2-3% of electricity generation of the plant. When the required dose is lOkGy, the consumed electricity for EB is about 0.6%. The total required electric energy will be less than 2% including utility. The second is non-uniform distribution of dose rate and flow rate in reactors, which will be large scale for stem power stations. In
- 9 8 -
JAERI -M 93-160
On these basic results. a pilot-scale test for EB treatment of flue gas
from coaI-burning boiler has been started under the joint research of
JAERI, Chubu Electric Power白 mpany佃 dEbara白甲oration. The plant
was ∞nstructed in the site of Sh担-Nagoyathermal power pl祖 tofChubu
Electric Power白 mpanyin Nagoya in October,1992.百 eoperation w迎
be carried out for one year until December, 1993.τbem副npu中O毘 S紅 e
to evaluate the three-stage irradiation method and the reliability of this
process in long term operatiou.
Fig.8 shows a flow diagram of the pi10t plantσ). 12,000Nm3fh∞al
fired flue gas is led to the pilot plant. The temperature is supposed to be
110 oC, and ∞ncentration of SOz is 800ppm, NOx is 225ppm. F註st1y,gぉ
is∞oled at the ∞oIing tower to 65 oC. After adding NH3, the gas is led to
irradiation vessel and irradiated by electron beams using 3 electron acc渇ler-
ating tubes. Voltage is ranging fro.c:l 400 to 800kV, current is 135 mA
maximum. Irradiated gas is led to the electrostatic precipitator and bag
filter to remove by-products; ammonium sulfate and ammonium nitrate.
Treated gas is vented from a stuck. Target of the test are; S02∞ncentra-
tion is reduced to lower than 50ppm from inlet ('..()ncentration of 800ppm,
NOx is reduced to lower than 45ppm from 225ppm.
In Table 2, engineering problems in application of the EB process for
treatment of f1ue gas from ∞al-fired power generation planぉaresumma-
rized. The first one is saving of electricity ∞nsumption. It is required that
energy consumption should be less than 2-3% of electricity generation of
the plant. When the required dose is 10kGy, the ∞nsumed electricity for
EB is about 0.6%. The total required electric energy will be less than 2%
inc1uding utility. The second is non-uniform distribution of dose rate and
flow rate in reactors, which will be Iarge scale for stem power stations. In
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JAERI-M 93-160
this pilot plant, flow regulator are installed to adjust flow rate to dose rate distribution in the reactor. The third is use of by-products. Production of by-products is estimated as follow: When the treatment capacity is 3 MNm3/h which correspond to flue gas flow rate from 1 MkW power generation plant, and the inlet concentration is 1,000 ppm, and removal efficiency is 80%, the production rate of (NH.3)2S04 is estimated to be 124 kton/y(26 N-equivalent kton/y), and correspond to about one tenth of pro-duction(340 N-kton/y) in Japan, 1990 as shown in Table 3. So use of N-fertilizer should be discussed of compatibility with conventional industries.
5. FLUE GAS FROM MUNICIPAL WASTE INCINERATOR More than 70% of municipal waste have been treated by burning, in
Japan, as shown in Table 4. Other is treated by landfill. Recently, municipal government are asked often to make slow down operation of incinerators in sunny days in summer to reduce emission of NOx.
To apply the EB process for treatment of flue gas from incinerators, simultaneous removal of NOx, S0 2 and HC1 was studied by EB irradiation in the presence of Ca(OH)2 using a small scale apparatus(5 Nm3/h). Fig. 9 shows example of experimental results of NOx removal. Inlet gas composition are shown in the figure. Lower irradiation temperature give higher removal efficiency. In this case, we used Ca(OH)2 powder instead of NH3. S0 2 and HC1 were shown to be removed almost 100%.
On these basic data, a pilot-scale test was also planned, and has been started under the joint research of JAERI, Matsudo-city and NKK. Fig. 10 is a flow diagram of the pilot plant at Matsudo-city(6). 1,000 Nm3/h flue gas is led to the pilot plant from the incinerator which generates 30,000 Nm3/h. The gas is irradiated under spray of Ca(OH)2 slurry. Electron accelerator is from Russia and is .9 MV in voltage and the current is 45 mA
- 99 -
JAERI-M 93-160
this pilot plant, flow regulator are installed to adjust flow rate to dose rate
distribution in the reactor. The third is use of by-products. Production of
by-products is estimated as follow: When the treatment capacity is 3
MNm3fh which correspond to flue gas flow rate from 1 MkW power
generation plant, and the inlet concentration is 1,000 ppm, and removal
efficiency is 80%, the production rate of (NH:J2S0 4 is estimated to be 124
ktonfy(26 N-equivalent ktonfy), and ∞rrespond旬 aboutone tenth of pro-
duction(340 N-ktonfy)担 Japan,1990ぉ shownin Table 3. So use of N-
fertilizer should be discussed of∞mpatibility with conventional indus位les.
5. FLUE GAS FROM MUNICIPAL WASTE INCINERATOR
More than 70% of municipal waste have been 紅 白tedby buming, in
Japan, as shown in Table 4. Other is treated by landfill. Recent1y, munici-
pal government are asked often to make slow down operation of incinera-
tors in sunny days in summer to reduce emission of NOx.
To apply the EB process for treatment of flue gas from incinerators,
simultaneous removal of NOx, S02 and HCl was studied by EB irradiation
in the presence of Ca(O町2using a small scale apparatus(5 Nm3/h). Fig.9
shows example of experimental results of NOx removal. lnlet gas ∞mpo-
sition are shown in the figure. Lower irradiation temperature give higher
removal efficiency. In this case, we used Ca(OH)2 powder instead of阻 3.
S02 and HCl were shown to be removed almost 100%.
On these basic data, a pilot-scale test was also planned, and has been
started under the joint research of JAERI, Matsudo-city and NKK. Fig.
10 is a flow diagram of the pilot plant at Matsudo-city(6). 1,000 Nm3fh
flue gas is led to the pilot plant from the incinerator which generates 30,000
Nm3fh. The gas is irradiated under spray of Ca(OH)2 slurry. Electron
accelerator is from Russia and is .9 MV in voltage and the current is 45 mA
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JAERI-M 93-160
maximum. Irradiated gas is led to the bag house to remove calcium sulfate, chloride, and nitrate. Treated gas is vented from a stuck.
Target of the test are; NOx is reduced to lower than 50ppm from inlet concentration of lOOppm, HCl is reduced to lower than lOppm from l,000ppm, and S 0 2 is reduced to lower than lOppm from lOOppm. The main purposes are to evaluate simultaneous removal of NOx, HCl and S0 2 . The plant was already completed in Matsudo city and was started to operate from June, 1992.
References 1. KKawamura et al., "Treatment of exhaust gases by irradiation", IAEA-
SM-194/707(1975). 2. O.Tokunaga et al., Radiat. Phys. Chem.,24,145(1982).
3. K.Kawamura et al., Environ. Sci. Technol., 14,288(1980). 4. O.Tokunaga et al, "ELECTRON BEAM IRRADIATION TECHNOLO
GY FOR ENVIRONMENTAL CONSERVATION", Proceeding of the International Conference on Evolution in Beam Applications, Takasaki, 1991.
5. H.Namba et al, "BASIC STUDY ON ELECTRON BEAM FLUE GAS TREATMENT FOR COAL-FIRED THERMAL PLANT", ibid.
6. T. Doi et al, "PILOT-PLANT FOR NOx, S02, HCl REMOVAL FROM FLUE-GAS OF MUNICIPAL WASTE INCINERATOR BY ELECTRON BEAM IRRADIATION", ibid.
7. S. Machi et al, "RADIATION TREATMENT FOR ENVIRONMEN-TAI CONSERVATION", The third International Symposium on Advanced Nuclear Energy Research, Mito, 1991
- IOO -
JAERI-M 93-1印
maximum. Irradiated gas is led to the bag house to remove calcium sul-
fate, chloride, and nitrate. Treated gas is vented from a stuck.
Target of the test are; NOx is reduced to lower than 50ppm from inlet
concentration of 100ppm, HCI is reduced to lower than 10ppm from
1,OOOppm, and S02 is reduced to lower than 10ppm from 100ppm. The
main pu中osesare to evaluate simultaneous removal of NOx, HCI and S02'
The plant was already ∞mpleted in Matsudo city and was started to oper-
ate from June, 1992.
References
1. K.Kawamura et a1., "Treatment of exhaust gases by irradiation", IAEA-
SM-194/707(1975).
2. O.Tokunaga et a1., Radiat. Phys. Chem.,24,145(1982).
3. K.Kawamura et a1., Environ. Sci. Techno1., 14,288(1980).
4. O. Tokunaga et al, "ELECTRON BEAM IRRADIATION TECI到 OLO-
GY FOR ENVIRONMENTAL CONSERVATIONヘProceedingof the
Int'~rnational 白nference on Evolution in Beam Applications, Takasaki,
1991.
5. H.Namba et al, "BASIC STUDY ON ELECfRON BEAM FLUE GAS
TREA1乱ffiNTFOR COAL-FIRED THERMALPLANT", ibid.
6. T. Doi et al, "PILOT-PLANT FOR NOx, S02, HCl REMOVAL FROM
FLUE-GAS OF MUNICIPAL WASTE INCINERATOR BY ELEC-
TRON BEAM IRRADIATION", ibid.
7. S. Machi et al, "RADIATION TREATMENT FOR ENVIRONMEN-
TAJ. CONSERVATION't, The third International Symposium on Ad-
vanced NucIear Energy Research, Mito, 1991
一 100
JAERI-M 93-160
Table 1 History of development of EB process for flue gas treatment
Fig. 10 Flow chart of the pilot plant for treatment of flue gas from an incinerator at Matsudo-City
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JAKR1-M 93 160
2.9. Potential Industrial Application of Electron Accelerators in Indonesia
Mirzan T. Razzak
Center for the Application of Isotopes and Radiation, BATAN
INTRODUCTION
Today's technology concerns with high quality and high performance products, save in energy and preserve environment.
Since the last decade, radiation technology has made a great progress in the production method, particularly in the production of high quality sterilized medical products, wire and cable and shrink tubing,heat shrinkable film, the partial curing of tire components, and foam manufacture (1-4).
The near future, the electron beam (EE) accelerators will aplicable in crosslink-ing packaging films and in curing coatings and inks (5). New materials like pressure sensitive adhesives, silicone release coatings and other specialty coatings will expand the market potential of EB accelerator (6).
Very recently, the surface sterilization of medical devices and food packages and the treatment of stack gases to remove sulfur and nitrogen oxides are also being explored (7,8).
Indeed advanced countries such as Japan, Germany, France and USA have used the radiation technology to improve their industrial performance and capability. In Asia region, Taiwan and South Korea are recognized as the new industrial countries who are also applying EB accelerator in their production line.
Indonesia however, has a great potential in the application of EB accelerator. This is because of a remarkable growth of industrial sector ,the abundant of natural resources, and the increasing demand of the product quality to support high-tech and high risk industries.
The present paper discusses the potential industrial application of EB accelerator in Indonesia. It is expected that the paper could be able to presence informations and to invite a useful discussion.
STATUS OF RADIATION PROCESSING IN INDONESIA
National Atomic Energy Agency, Centre for Application of Isotops and Radiation (CAIR-BATAN) is the only institute to take initiative to conducting research and development of radiation technology in Indonesia.
Two gamma ray irradiators with a total power of 225 kCi Cobalt-60 source and Electron Beam (EB) accelerator of 300 KeV are available at the CAIR-BATAN.
During the last 10 years, CAIR-BATAN has gained a great progress in the depelopment of irradiation techniques, particularly to produce pre-vulcanized Natural Rubber(NR) latex, diffe- rent kind of preserved spices, to sterilization of medical and pharmaceutical products and to curing of wood surface coating (9,10). The present
- 108 -
J.¥ERI--¥1 93-160
2.9. Potential Industrial Application of Electron Accelerators in Indonesia
lUi.πan T. Razzak
Center for the Applicatiorl of Isotopes and Radiation, BATAN
町 TRODUCTION
Today's technology concems with high quality and high performance produc民save in energy and preserve environment.
Since the last decade, radiation technology has made a great progress in the production method, particularly in the production of high quality sterilized medical products, wire and cable and shrink tubing,heat shrinkable film, the partial curing of tire components, and foam manufacture (1・4).
The near future, the electron beam (EB) accelerators will aplicable in crosslink-ing packaging films and in curing coatings and inks (5). New materials like pressure sensitive adhesives, silicone rel回 secoatings and other sp配ial~y coatings wiII expand the market potential of EB accelerator (6).
Very recentIy, the surface sterilization of medical devices and food packages and the treatment of stack gases to femove sulfur and nitrogen oxides are also being explored (7,8).
Indeed advanced countries such as Japan, Germany, Fr叩 ceand USA have used the radiation technology to improve their industrial performance and capability. In Asia region, Taiwan and South Korea are recognized as the new industrial countrie~, who are also applying EB accelerator in their production line.
Indonesia however, has a great potential in the application of EB accelerator. This is because of a remarkable growth of industrial sector ,the abundant of natural resources, and the increasing demand of the product quality to support high-tecr and high risk industries.
The present paper discusses the potential industrial application of EB accelerヨtorin Indonesia. It is expected that the paper could be able to presence informations and to invite a useful discussion.
STATUS OF RADIATION PROCESS悶 GIN町 DONESIA
National Atomic Energy Agency, Centre for Application of Isotops and Radia-tion (CAIR-BATAN) is the only instItute to take initiative to conducting research and development of radiation technology in Indonesia.
Two gamma ray irradiators with a total power of 225 kCi Cobalt-60 source加 dElectron Beam (EB) accelerator of 300 KeV are available at the CAIR-BATAN.
During the last 10 years, CAIR-BATAN has gained a great progress in the depelopment of irradiation techniques, particularly to produce pre-vu1canized Natural Rubber(NR) latex, diffe-rent kind of preserved spices, to sterilization of medical and pharmaceutical products and to curing of wood surface coating (9,10). The present
-108-
JAERI-M 93-160
EB accelerator available in CAIR-BATAN is a low voltage (300 keV) and low penetration of electron beam. It is only applicable for curing of surface coating and other surface treatments.
In order to perform R&D in polymer crosslinking such as crosslinking of wire and cable insulators, heat shrinkable tube and film, polyethylene foam and other possible industrial application of radiation technology, then a higher voltage ( energy) EB accelerator is necessary.
CAIR-BATAN plans to build a new EB accelerator with a medium energy of 2 MeV. The building and shielding will be constructed this year and the EB accelerator will be installed later in 1993.
The most important progress in the transfer technology program is the establis-ment of a commercial plant of gamma rays iradiator in near Jakarta. The irradiator with an initial loading of 400 kCi Cobalt-60 source is belong to private company, INDO-GAMA, and it is commissioned last month (May 1992)
The irradiation facility will be mainly used as an irradiation sevice centre for the sterilization ox medical and pharmaceutical products.
A bilateral research cooperation between JAERI and BATAN has successfully developed the adhesive and thermoplastic elastomer made from irradiated natural rubber (NR) latex (1 l).The bench scale results, however needs further efforts to bring it to be industrial scale. Another results as an output of the bilateral research cooperation are the development of hydrogels for biomaterials which are now under progress. Some of the results have been jointly patented in Japan.
ELECTRON BEAM CROSSLINKING
In fact the biggest applications of EB accelerator is occupied by the process of crosslinking of wire insulation (12).
There are at least 123 electric industries available in Indonesia i.e. 7 companies are foreign invesment and the rest are domestic companies. Not less than 26802 ton of different types of wire and cable products are produced annually by 14 companies as shown in Table 1. Its clear that wire and cable industries could be a great potential of EB accelerator processing, particularly when a heat resistant wire and cable insulation is required to support the industrial development in Indonesia.
The crosslinking technologies that are available to the industry are mainly chemical method.
- Continuous Vulcanization = CV Technology(peroxide and salt bath crosslinking) - Monosil crosslinking and - Sioplas crosslinking (silane crosslinking).
Each type of crosslinking has its specific advantages and an disadvantages. The CV crossliking is the most widely used technology to date.
However, it is necessary to discuss the advantages of EB crosslinking over the conventional process.
As compared to the CV method, the important advantages factor to EB cross-linking are:
- 109 -
]AERI-M 93-160
EB accelerator available in CAIR-BATAN is a low voltage (300 keV) and low penetra事
tion of electron bf'.am, It is only applicable for curing of surface coating and other surface treatments.
In order to perform R&D in polymer crosslinking such as crosslinking of wire and cable insulators, heat shrinkable tube and film, polyethylene foam and other possible industriaI application of radiation technology,then a higher voltage ( energy) EB acceler.‘
ator is necessarv. CAIR":BATAN plans to build a new EB accelerator with a medium energy of 2
Me V. The building and shielding wil1 be constructed this year and the EB accelerator will be insta1led later in 1993.
The most important progress in the transfer technology program is the回 tablis-ment of a commercial plant of gamma rays iradiator in n伺 rJakarta. The irradiator with an initial loading of 400 kCi Cobalt-60 source is belong to private company, INDO-GAMA, and it is commissioned last month (May 1992)
The irradiation facility will be mainly used as an irra<liation sevice centre for the sterilization 0I medical and pharmaceutical products.
A bilateraI research cooperation between JAERI and BATAN has successfully developed the adhesive and thermoplastic elastomer made from irradiated naturaI rubber (NR) latex (11). The bench scale results, however needs further efforts to bring it to be industrial scale. Another results as an output of the bilateraI res回 rchc∞lperation are the dev~lol?men~ of hy~r~gels for bi?!lla!eriaIs which are now under progress. Some of the results have been jointly patented in Japan.
ELECTRON BEAM CROSSLINKING
In fact the biggest applications of EB accelerator is occupied by the process of crosslinking of wire insulation (12).
There are at least 123 electric industries available in Indonesia I.e. 7 companies are foreign invesment and the rest are domestic companies. Not Iess than 26802 ton of different typL'S of wire and cable products are produced annually by 14 companies as shown in Thble 1. Its c1ear that wire and cable industries could be a great potentia1 of EB accelerator processing, particularly when a heat resistant wire and cable insulation is required to suppo此 theindustrial development in Indonesia.
The crosslinking technologies that are available to the industry are mainly chemical method. -Continuous Vulcanization = CV Technology(peroxide and salt bath crosslinking) ーMonosi1crosslinking and ーSioplascrosslinking (silane crosslinking).
Each type of crosslinking has its sp民 ificadvantages and an disadvantages. The CV crossliking is the most widely used technology to date.
However, it is necessary to discuss the advantages of EB cross1inking over the conventional process.
As compared to the CV method, the important advantages factor to EB cross-linking are:
- 109
JAERI-M 93-160
1. Eliminate start-up and end scrap. By using the CV method, the start-up or end scrap is generally about 100 m long with the EB method, on the other hand , there is absolutely no star-up scrap.
2. Lower energy consumption. The CV method requires up to five times more.
3. Less factory space needed. EB crosslinking requires only about 50 % of the space needed by the CV method.
5. A longer spectrum of possible coss section can be terated 6. Faster and more flexible processing 7. Process control. It is easier to reproduced the crosslinking.
The factor that are often under estimated by those who are not thoroughly fami-lier with radiation process:
- the cost of instalation and handling - the length of time during which radiation process is interupted due to reel changes,
different cross-sections or materials.
It should also be noted that no radiactivity can be induced in materials with accelerator energy levels up to 8 MeV and therefore it is a safe technology.
Some success companies that using EB crosslinking in USA, Europe and Japan are: Brond-Peek
ESSEX Nothern Telecom Shan Siemens Supernant Sumitomo Electric Furukawa Electric Hitachi Cable Taisho Electrical Oki electric Showa Cable etc.
Indeed, the use of EB accelerator is very important to produce the common good of mankind, especially in high risk area such as in the chemical industry, nuclear power plant, public building etc.
RADIATION CURING
There are 110 plywood mill with total capacity 10,700,000 cubic meters per year. In addition there are 58 blockboard industry and 8 particle board factory with total annual capacity of 981,500 cubic meters and 435,000 cubic meters (13). These are a potential raw materials that can be proceeded further by using EB accelerator technology in order to obtain value-added items.
- no -
JAERI-M 93-160
1. Eliminate start-up and end scrap. By using the CV method, the start噂 upor end scrap is genera1lyabout 100 m long with the EB method, on the other hand , there is absolutely no star-up scrap.
2. Lower energy consumption. The CV method requires up to five times more.
3. Less factory space needed. EB cross1inking requires only about 50 % of the space needed by the CV method.
5. A longer sp民 trumof possible coss section can be terated 6. Faster and more tlexible processing 7. Process control. It is easier to reproduced白ecrosslinking.
The factor that are often under estimated by those who are not thoroughly fami-lier with radiation prlωess: -the cost of insta1ation and handIing -the length of time during which radiation prl∞ess is interupted due to rl民 1chang白,
different cross-sections or materials.
It should also be noted that no radiactivitv can be induced in materials with accelerator energy levels up to 8 MeV and therefore it is a回fet配 hnology.
Some success companies that using EB crosslinking in USA, Europe and Japan are: Brond-Peek
ESSEX Nothem Telecom Shan Siemens Supemant Sumitomo Elec凶cFurukawa Electric Hitachi Cable 百ishoElectrical Oki electric Showa Cable etc.
Indeed, the use of EB accelerator is very important to produce the common good of mankind, especially in high risk area such as in the chemical industry, nuclear power plant, public building etc.
RADIATION CURING
There are 110 plywood mill with to凶伺.pacity10,700,0∞cubic meters per y'伺r.In addition there are 58 blockboard industry and 8 particle board factory with~ total annual capacity of 981 ,500 cubic meters and 435,000 cubic meters (13). These are a potentia1 raw materia1s that can be pro白 ededfurther by using EB accelerator technology in order to obtain value-added items.
110
JAER1-M 93-160
EB accelerator can be potentially used to produce PVC-laminated plywood , acrylic-coated plywood and to surface finishing work for several kinds of wood products, paper and metals. These are because the EB accelerator is capable to be used for curing of surface coating instead of conventional heating technique.
Technical and economical evaluation on the application of EB accelerator for curing of wood surface coating will be presented in another manuscript at this meeting.
RADIATION STERILIZATION
A wide variety of medical devices are sterilized by gamma rays irradiator and EB accelerator. Included are items such as syringes, catheters.cotton balls, miscellaneous vials, latex gloves, blood lancet, disposable scalpel, birth control rings,surgical suture, artificial joint, gauze and dialysis unit (14).
The major competing sterilization method for medical disposables is Ethylene Oxide (EtO) method. The share of EtO sterilization method is gradually decreases from 70 % in 1988 to 55 % in 1993, whereas Gamma rays sterilization method increases from 27 % to 40 % and the EB method is 3 % in share during the same period. The changing market share of EtO to Gamma rays is mainly because of some disadvantage factors of the use EtO. For example, product residues and patient health concerns, worker safety, environmental emissions of the gas, legislation regarding the use of a hazardous chemicals, increasing capital and operating costs (15).
For die sterilization of medical supplies, it needs a high voltage ( energy) EB accelerator type. For example EB accelerator with voltage in the range of 3 to 10 MeV. Only few such high voltage EB accelerators are available in the world (16).
To estimate the voltage requirement for the sterilization of 2 ml disposable syringe, the following formula can be applied (16):
Voltage = 2.63 TD + 0.32 (single sided treatment) Voltage = 1.19 TD + 0.32 (double sided treatment)
where Voltage is in MeV, T is thickness in cm, and D is density. Alternatively, the value of TD can be expressed as the ratio of weight (g) per unit area (cm ). Unit area is the length and width normal to the electron beam. In case of 2 ml syringe the value of TD becomes 4972/1609 g/cm = 3.1 g/cm
Therefore the voltage of EB accelerator should be,
E = 1.19x3.1 +0.32 (double sided treatment)
= 4.0 MeV
The potential application of EB sterilization technique in Indonesia can be estimated by the health care activities such as the existence of hospitals, physicians, pharmacists, nurses and medical doctors as well as Indonesian population as shown in Table 2.
- i n -
]AERI-M 93-]60
~B accelerator can be potentially used toproduce PVC-Iaminated plywood, acrylic-coated plywood and to surface finisbing work for several kindS -of wood products, paper and metals. Tbese are because tbe EB accelerator is capable to be used for curiog of surface coating instead of conventional beating tecbnique.
Technical and economical evaluation on tbe a!lplication of EB accelerator for curing of wood surface coating will be presented in anotber manuscript at由民meeting.
RADIATION STERILIZATION
A wide variety of medical devices are sterilized by gamma rays irradiator and EB accelerator. Included are items such as sy司nges, catbeters,cotton ~a1Is, miscellaneous vials, latex gloves, blood lancet, disposable scalpel, birtb con釘01rings,surgical suture, artificial joint, gauze an¥l dialysis unit (14).
The m吋orcompeting sterilization metbod for medical disposables is Etbylene Oxide (EtO) method. The share of EtO sterilization method is gradually decreases from 70 %血 1988to 55 % in 1993, wbereas Gamma rays sterilization metbod increases from 27 % to 40 % and tbe EB metbod is 3 % in sbare during tbe s~me peri~d Tbe cbanging market sbare of Et() to Gamma rays is mainly because of some disadvantage factors of tbe use EtO. For example, product residues and patient health concems, worker safe旬, environmental emissions of the gas, legislation regarding the use of a bazardous cbemicals, increasing capital and operating costs (15).
For也esterilization of medical supplies, it needs a high voltage (energy) EB acceleratnr type. For example EB accelerator with voltage in tbe range of 3 to 10 MeV. Only few such high voltage EB accelerators are available in tbe world (16).
To estimate tbe voltage requirement for the sterilization of 2 ml disposable syringe, the iollowing formula can be app1ied (16):
Voltage = 2.63 TD + 0.32 (single sided treatment) Voltage = 1.19 TD + 0.32 (double sided treatment)
where Voltage is in MeV, T is thickness阻 cm,and D is density. Altematively,血evalue of TD can be expressed as曲eratio of weight (g) per unit area (cm ). Unit area is曲elength and width normal to tbe electron beam. In case of 2 ml可巾gethe value of TD becomes 4972116ω g/cm = 3.1 g/cm
Therefore the voltage of EB accelerator should be,
E = 1.19 x 3.1 + 0.32 (double sided treatment)
= 4.0 MeV
The potentiaI appIication of EB sterilization technique in Indonesia can be estimated by the bealtb care activities sucb as tbe-existence of bospitals, physicians, pbarmacists, nurses and medical doctors as well as IndonesiaJ) population as shown in Table 2.
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JAKR1-M 93-160
The most important factors in determined a cost for the EB accelerator faciliity in general are : - the accelerator voltage - the building and shielding - the product conveyor and - the people involved
FOOD IRRADIATION
The most promising application of radiation technology in food treatment seems to be the irradiation of spices. As well as gamma irradiator, EB accelerator has also a great potential to be applied as far as the public acceptance and the legislation of the technology are world wide approved. Table 3 shows export statistic of different spices which are considered profitable (17).
FLUE GAS TREATMENT
The growing of industrial sector in Indonesia needs an early awarness to environmental concervation. Recently, EB accelerator has been examined to be used at pilot scale for the treatment of exhaust gas from steei sintering plant and Coal electric power plant (2,8). Figure 1 shows a process flow diagram of EB flue gas treatment system. Briefly, the exhaust gas or flue gas is introduced into a cylinder vessels at 100 C to be irradiated with two accelerators. Small amount of ammonia is added before irradiation to enhance removal rate of NO and to decrease the formation of N02. Under irradiation, SOx and NOx are converted to complex salt of ammonia sulfate and nitrate, which is collected in an electron precipitator. Details will be reported in this workshop.
Indeed all the combustion gas from heavy oil and coal factories should be treated before it is released to the environment. At present, at least 2 (two) coal electric power plants and several oil electric power plants as well as different chemical plants are available in Indonesia. The radiation treatment of combustion gases to remove sulfur dioxide and nitrogen oxide is one alternative to have a clean environmental industry.
CONCLUSION
The potential applications of EB accelerator in Indonesia, particularly in the production of heat resistance wire and cable insulators, surface coated of plywood by radiation curing techniqnue, electronic parts by radiation curing technique, spices and herbs treatment for export, heat shrinkable film and sheet for packaging materials, treatment of a part of tire component, sterilization of some selective medical divices and treatment of flue gas from different industries have been presented.
Research and development in the field of radiation technology and some progress of a bilateral research cooperation between TRCRE-JAERI and BATAN have been reported.
The application of EB accelerator in industrial line is much depended on the good will and attitude of Indonesian's enterprenuer as weil as the ability to absorb the knowledge and know how of radiation technology. BATAN as the only research institute in Indonesia who is doing a lot of work in this field is ready to provide necessary informations and consultations.
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JAERl-M 93-160
The most important factors in determined a cost for the EB accelerator faciliity in general are : ーtheaccelerator voltage ーthebuilding and shielding -the product conveyor and -the people involved
FOOD IRRADIATION
The most proml!~s~ng application of radiation technology in food treatment seems to be the irradiation of spices. As well as gamma irradiator, EB ac白 leratorhas also a great potential to be applied as far酪 thepublic acceptance and the legislation of the technology are world wide approved. Table 3 shows export statistic of different spices which are considered profitable (1乃.
FLUE GAS TREATMENT
The growing of industrial sector in Indonesia needs an earIy awamess to envi-ronmentaI concervation. R配 enuy,EB accelerator has been examined to be used at pilot scale for the treatment of exhaust gas from st民 isintering plant and Coal electric power plant (2,8). Figure 1 shows a process flow diagram of EB flue gas treatment system. Briefly, the exhaust gas or flue gas is introduced into a cyIinder vessels at 100 C to be irradiated with two accelerators. Small amount of ammonia is added before irradiation to enhance removal rate of NO and to decrease the formation of N02. Under irradiation, SOx and NOx are converted to complex saIt of ammonia sulfate and nitrate, which is colIected in an electron pr'民 ipi凶 or.Details will be reported in this workshop.
Indeed all the combustion gas from h回 vyoil and coal factories should be tr伺 t-ed before it is released to the environment. At present, at least 2 (two) coal electric power plants and several oil electric power plants as weli as different chemicaI plants are available in Indonesia. The radiation treatment of combustion gases to remove sulfur dioxide and nitrogen oxide is one altemative to have a clean environmentaI indus町.
CONCLUSION
The potential appIications of EB accelerator in Indonesia, particul訂 lyin the production of heat resistance wire and cable insulators, surface coated of plywood by radiation curing techniqnue, electronic parts by radiation curing technique, spices and herbs tr伺 tmentfor export,h回 tshrinkable film and sheet for packaging materials, tr回 t-ment of a part of tire component, steriliz?tion of some selective medical divices and treatment of flue gas from different industries have been presented.
Research and development in the field of radiation technology and some progress of a bilateral research cooperation between TRCRE-JAERI and BATAN have been reported.
The application of EB accelerator in industrial line is much depended on the good wil1 and attitude of Indonesian's enterprenuer as weil as the abi1ity to absorb the knowledge and know how of radiation technology. BATAN as the only res回 rchinstitute in Indonesia who is doing a lot of work in this field is r回 dyto provide n民間姐ryinfor-mations and ~Gnsultations.
- 112一
JAERI-M 93-160
REFERENCES
l.BENNET Jr.E.W.,Application of Irradiation to Industrial Wires and Cables, Radiat. Phys.Chem., Vol. I4,No.3-4,pp.947-951 (1979).
2.MACHI S..Industrial Application of Radiation Processing in Japan, Radiat. Phys.Chem., 14 (1979)155.
3. ANONYMOUS, Prospect for Industrial Electron Beam Processing, Beta-gamma l/88.p.4.
4.HUNT J.D. and ALLIGER G., Rubber Application of Radiation to Tire Manufacture, Radiat.Phys.Chem, 13 (1978) 39.
5.EDWIN P.,TRIPP III, Low Volatge Shelfshielded Electron Beam Accelerators Offer New Opportunities in Crosslinking,Beta-gamma l/89,p. 11.
6.HANS F.HUBER and HARTMUT MULLER, Radiation Curable Polyesters for The Formulation of Pressure Sensitive Adhesives, Radiat. Phys. Cliem., Vol.33,No.5 (1989)p.443.
7.TIMOTHY G.HENRY, Electron beam a case history, Radiat. Phys. Chem., Vol.35,No.4-6 (1990) 528.
8.ANDRZEJ G.CHMIELEWSKI, EDWARD ILLER AND MICHAL ROMANOWSKI, Pilot plant for electron beam S02 and NOx Removal from combustion flue gases, Institute of Nuclear Chemistry and Technology, Warsawa 1991. INCT-2125/VI.
9.MUNSIAH MAHA, Status of Food Irradiation in Indonesia, BATAN, Jakarta (1989).
lO.SUGIARTO DANUjEconomic analysis of wood surface coating using radiation technology, Excecutive Seminar on Application of Radiation Surface coating technique in industry, March 15, BATAN, Jakarta 1990.
ll.MIRZAN T.RAZZAK, FUMIO YOSHII.KEIZO MAKUUCHI and ISAO ISHIGAKI, Thermoplastic elastomer by radiation grafting,I.Evaluation of
12.KEIJI UENO, The radiation crosslinking process and new products, Radiat.Phys.Chem,,Vol.35,No. 1-3 (1990) p.126.
13.ANONYMOUS, Forest based industry in Indonesia,Indonesian Wood Panel Association, presented in Regional Executive Manager Seminar on Radiation Curing Coating Technology, March 19-21, Jakarta (1990).
14.YONEHO TABATA, The present status of radiation processing in Japan, Tokay University, Januari 19990.
15.RUTH M.BRINSTON, Future growth in the gamma sterilization of disposable medical products, Radiat.Phys.Chem.,Vol.35, No. 1-3 (1990) p.390.
16.WILLIAM J.MAHER, The application of electron beam equipment for the sterilization of medical devices, Radiat.Phys.Chem,VoU5 (1980) p.99.
17.ANONYMOUS, Monthly Statistic Bulletin, Bureau of Statistic Centre, Jakarta (1989)
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JAERI-M 93-160
REFERENCES
I.BENNET Jr.E. W.,Application of lrradiation 10 lndllstrial Wires and Cables. Radial. Phys.Chcm., ¥'01. J4,No.3-4,pp. 947-95 J (1979).
2.MACHI S.,Indllstrial Application of Radiation Processing in Japan, Radiat. Phys.Chcm., 14 (1979)155.
3.ANONYMOUS, Prospecl for lndllstrial Elcctron B回 mProcessing, Bda-gamma l/88.p.4.
4.HUNT J.D. and ALLlGER G., RlIbber Application of Radialion to Tirc Manllfactllre, Radiat.Phys.Chem, 13 (1978) 39.
5.EDWIN P.,TRIPP III, Low Volatge Shelfshiclded Electron Bcam Accclerators Offer New Opportunities in Crosslinking,Beta-gamma I189,p.ll.
6.HANS F.HUBER and HARTMUT MULLER, Radiation Curable Polyesters for The Formulation of PresslIre Sensitive Adhesives, Radiat. Phys. Chem.. VoI.33,No.5 (1989)p.443.
7.TIMOTHY G.HENRY, Electron beam a case history, Radiat. Phys. Chem., Vo1.35,No.4-6 (1990) 528.
8.ANDRZEJ G.CHMIELEWSKI, EDWARD ILLER AND MICHAL ROMANOWSKI, Pilot plant for electron beam S02 and NOx Removal from combustiol1 flue gases, Institute of Nuclear Chemistry and Technology, Warsawa 1991. INCT-21251V1.
9.MUNSIAH MAHA, Status of Food lrradiation in lndonesia, BATAN, Jakarta (1989).
1O.SUGIARTO DANU,Economic analysis of wood surface coating lIsing radialion technology, Exceclltive Seminar 011 Application of Radiation Surface coating technique in industry, March 15, BATAN, Jakarta 1990.
11.MIRZAN T.RAZZAK, FUMIO YOSHII,KEIZO MAKUUCHI and ISAO ISHIGAKI, Thermoplastic elastomer by radiation grafting,I.Evaluatiol1 of
12.KEIJI UENO, The radiation crosslinking process and new produclS, Radiat.Phys.Chem<, Yo1.35,No. 1-3 (1990) p.126.
13.八NONYMOUS,Forest based indllstry in Inclonesia,Indoncsian Wood Pancl八ssoci-ation, presented in Regional Executive Manager Seminar on Radiation Curing Coating Technology, March 19-21, Jakarta (1990).
14. YONEHO TABATA, The present status of radiation processing in Japan, Tokay UniversitぁJanuari19990.
15.RUTH M.BRINSTON, Future growth in the gamma sterilization of disposable medical products, Radiat.Phys.Chem., Vo1.35, NO.l・3(1990) p.390.
16. WILLIAM J. MAHER, The application of electron beam eqllipment for the steriliza-tion of medical devices, Radiat.Phys.Chell1, Yo1.l5 (1980) p.99.
17.ANONYMOUS, Monthly Statistic BuIIctin, Bureau of Slatistic Ccntrc, .1 akarta (1989)
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Table 1 Some wire and cable industries in Indonesia
No. Name of Company Typical Products Annual Capacity 1 PT. Kabelindo Murni Electrical Wire &
Cable Telephone Cable
4100 ton
2 PT. Kabelmetal Indonesia
Electrical Wire & Cable Telephone Cable
3800 ton
3 PT. Suraco Telephone Cable 1200 ton 4 PT. Terang Kita Electrical Wire &
Cable Telephone Cable
7357 ton
5 PT. Indotrijaya Industries
Telecomm Cable 100 ton
6 PT. IKI Indah Kabel Indonesia
PVC Power Cable Te1ecommunication Cable Medium Voltage Cable
Table 3 Export of spices from Indonesia to different countries in 1988 (7)*
COUNTRY SPICES IN TONNAGE
COUNTRY WHITE PEPER BLACK PAPER NUTMEG
USA 5,934 10,938 704 Netherlands 5,249 235 1,351 France 60 25 444 Belgium &
Luxemburg 275 - 440 Canada 892 160 -
Hungary 855 744 -
China 50 70 -
* Source : Indonesian Central Bereau of Statistic
Table 4 Plywood industries and its capacity
Product Total capacity Production (m T )
Plywood 110 9,000,000
Blackboard 58 700,000
Partickleboard 8 101,000
- 1 1 6 -
JAERI-M 93ー 160
Table 3 Export of spices from Indonesia to different countries in 1988 (7)“
SPICES IN TONNAGE COUNTRY
WHITE PEPER BLACK PAPER
USA 5.934 10,938 Netherlands 5.249 235
France 60 25
BeLlugxiuem m b& urg 275
Canada 892 160
Hungary 855 744
China 50 70
* Source : lndonesian Central Bereau of Statistic
Table 4 Plywood industries and its capacity
Product
Plywood
Blackboard
Partickleboard
TotaI capacity
110
58
8
-116一
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2.10. Progress in Electron Beam Curing in Indonesia F. Sundardi
Center for the Application of Isotopes and Radiation, BATAN
INTRODUCTION
The use of radiation, both ultra-violet (UV) or electron beam (EB) is becoming important in the present time for curing and pigmented film. UV radiation is generally used for smaller scale, slower line speed operation and clear coating, where as EB is more suitable for large volume processing and relatively thick pigmented coating. Commercial application of EB curing of surface coating for wood products had appeared since early of 1970 decade. Today there are several companies using this technology successfully. This technology appears to be attractive to countries producing a large amount of wood panel such as Indonesia, Phillipine, Malaysia etc.
Under a cooperation between IAEA/UNDP and the government of Indonesia, a radiation curing of surface coating pilot plant had been installed in Jakarta (1984). The mission of the plant is for training, demonstration as well as for studying both technical and economic aspect of the technology in the region. Approximately one million US $ was spent for this project. Although the equipments of the plant are commercial size, but the plant was not designed for commercial production.
Several Regional Training Courses on radiation curing had been held in Jakarta from 1984 to 1990 using this plant. These courses were followed by a number of participants from RCA Member States : Bangladesh, India, Pakistan, Thailand, Indonesia, Sri Lanka, Malaysia,China,Rep. of Korea, Singapore,Phillipine and Vietnam.
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]AERI-M 93-160
2.10. Progress in Electron Beam Curing in Indonesia
F. Sundardi
Center for七heApplication of Isotopes and Radiation, BATAN
INTRODUCTION
The use of radiation, both ultra-violet (VV) or electron beam
(EB) is becoming important in the present time for curing and
pigmented fi1m. UV radiation is generally used for smaller scale,
slower 11ne speed operation and c1ear coat1ng, where as EB 1s
more suitab1e for large volume processing and relatively thick
pigmer】ted coating. Commercia1 app1ication of EB curing of surface
coating for wood products had appeared since ear1y of 1970
decade. Today there are several companies using this techno1ogy
successfully. This techno1ogy appears to be attractive to
countries producing a large amount of wood panel such as
Indonesia, Phillipine, Ma1aysia etc.
Under a cooperation between IAEA/UNDP and th, government of
Indonesia, a radiation curing of surface coating pi10t plant had
been instal1ed in Jakarta (1884). The mission of the plant is for
training, demonstration as well as for studying both technical
and economic aspect of the technology in the region.
Approximate1y one mil1ion US $ was spent for this project.
Although the equipments of the plant are commercial size, but the
plant was not designed for commercial production.
Several Regional Training Courses on radiation curing had been
he1d in Jakarta from 1984 to 1990 using this p1ant. These courses
were fol1owed by a number of participants from RCA Member States
8angladesh, India, Pakistan, Thai1and. Indonesia, Sri Lanka,
Malaysia,China,Rep. of Korea, Singapore,Phillipine and Vietnam.
118
JAERI-M 93-160
PRINCIPLE OF RADIATION CURING TECHNOLOGY
Basic chemistry of the technology is a liquid compound which will undergo polymerization, crosslinking or grafting under EB or UV radiation, forming a hard solid compound. There is a great number of formulation of this compound but generally the compound is a mixture of oligomers with mono or poly functional monomers and additives such as pigmented materials. This is a liquid compound which can be coated readily on any surface ,such as wood panel, using conventional coating equipments: roll coater, curtain coater, sprayer etc. These compounds are commonly called radiation curable materials. The formulation of the radiation curable materials depend on the utilization and technical specification required for the products : for coating on wood panel, metal, ceramic, plastic etc.
Example formulation of radiation curable material for top coat is as following :
Principle flowsheet of radiation curing of surface coating is shown in Fig.l. Wood panel is passed through a coating machine, such as roll coater, where the panel is coated with a radiation curable material. The coated panel then is passed through an EB machine under an inert atmosphere, by flowing N2 gas, where the radiation curable coating is polymerized, crosslinked or grafted, forming a solid hard coating. This process takes about 0.5 minute for one piece of wood panel (1.2x2.4 m) using EBM with beam current about 20 mA. This is a basic flowsheet of the process. In practice to obtain an excellent coating, several times of coating and radiation are required using different formulation
- 119 -
]AERIー恥193-160
PRINCIPLE OF RADIATION CURING ,'ECHNOLOGY Basic chernistry of the tech~clogy is a liquid cornpound which
will undergo polymerization, crosslinking or grafting under EB or
UV radiation, forming a hard solid cornpound. There is a great
number of formulation of this compound but generally the compound
is a mixture of oligorners with rnono or poly functional monomers
and additives such as pigmented materials. This is a liquid
compound which can be coated readily on any surface ,such as wood
panel, using conventional coating equipments: roll coater,
curとain coater, sprayer etc. These compounds are commonly called
radiation curable materials. The forrnulation of the radiation
curable materials depend on the utilization and technical
specification required for the products for coating on wood
panel, metal, ceramic, plastic etc.
Example formulation of radiation curable material for top coat
is as following
Epoxy acrylate (EA-81)
Polyethylene g!ycol diacrylate
1ft part
70
(PEGDA) 30
Silicon oil 1
Principle flowsheet of radiation curing of surface coating is
shown in Fig.l. Wood panel is passed through a coating machine,
such as roll coater, where the panel is coated with a radiation
curable material. The coated panel then is passed through an EB
machine under an inert atmosphere, by flowing N勺 gas,where the L
radiation curable coating is polyrnerized, crosslinked or grafted,
forming a solid hard coating. This process takes about 0.5 minute
for one piece of wood panel (1.2x2.4 m) using EBM with beam
current about 20 mA. This is a basic flowsheet of the process.
In practice to obtain an excellent coating, several times of
coating and radiation are required using different formulation
119一
JAERI-M 93-160
of radiation curable material. Instead of EBH , UV source can be used for radiation, but this
radiation is limited for a clear coating and further more a photoinitiator should be added in the radiation curable formulation. The advantage of using UV radiation is unnecessary of using inert atmosphere and low cost of UV source which consequently resulting low cost of operation.
THE PILOT PLANT
The pilot plant is housed in a building of 720 sqm, steel construction and located inside the area of Center for the Application of Isotopes and Radiation, Jakarta. Building construction and equipments installation were completed in the end of 1984, while a small modification was done in 1989.
Specification of essential equipments available are as following:
1. Electron bean machine (EBM)
This machine is made by Nissin High Voltage Co.,Japan, scanning type EBM with 120 cm beam width, 300 keV , 50 mA maximum beam current, and lead shielded. Inert gas requirement (N2 gas) is normally about 100 NM /hour, or about 150 liter of liquid nitrogen/hour. The speed of conveyor is between 2.5 m and 25 m/min. Conveyor speed and beam current determine the dose of irradiation ( Figure 2).
2. Ultra Violet (UV) source
This source is equipped with an UV lamp of about 80 Watt/cm length. The length of the lamp is about 120 cm while the conveyor speed is between 3 and 6 m/min.
3. Roll ooater
Two kinds of roll coater available in this plant: direct roll
- 120 -
JAERI-M 93-160
of radiation curable material.
Instead of EBH , UV source can be used for radiaticn, but this
radiation is limited for a clear coating and further more a
photoinitiator should be added in the radiation curable
formulation. The advantage of using UV radiation i5 unneoessary
of using iliert atmosphere and low cost of UV source t-lhich
consequently resulting low cos七 of operation.
THE PILOT PLANT
The pilot plant is housed in a building of 720 sqm, steel
construction and located inside the area of Center for the
Application of IsotoQes and Radiation, Jakarta.
construction and equipments installation were completed
end of 1984, while a small modification was done in 1989.
Building
in the
Specification of essential equipments available are as
following:
1. Electron beam machine (EBH)
This machine is made by Nissin High Voltage Co.,Japan, scanning
type EBH with 120 cm beam width, 300 keV , 50 mA rnaximum bearn
current, and lead shielded. Inert gas requirement (N2 gas) is 3 normally about 100 NMv/hour, or about 150 liter of liquid
nitrogen/hour. The speed of conveyor is between 2.5 m and 25
m/min. Conveyor speed and beam current determine the dose of
irradiation ( Figure 2).
2. Ultra Violet (UV) source
This source is equipped with an UV lamp of about 80 Watt/cm
length. The length of the lamp is about 120 cm while the conveyor
speed 1s between 3 and 6 m/min.
3. Roll coater
Two kinds of roll coater available in this plant: direct roll
-120 --
JAERI-M 93-160
coater and reverse roll coater. Both with 120 cm coating width and speed between 10 and 40 m/min. The electrical power requirement is 1.2 kW and 6 kW respectively.
4. Film laminator
The speed of the machine is between 5 and 20 m/min. The size 174 cm width, 135 cm length and 188 cm height. The electrical requirement is about 1 kW. Compressed air is required with pressure between 6 and 7 kg/cm
5. Sanding machine
This machine is equipped with an exhaust blower with capacity 160 nM3/h.
Equipments layout of the plant is shown in Figure 3, but this lining is not reflecting a flowsheet of a typical process. For a typical application, a typical flowsheet of the process is required. Total investment of the plant is about one million US $ (Table 1).
coater and reverse roll coater. 80th with 120 cm coating width
and speed between 10 and 40 m/min. The e1ectrical power
requirement is 1.2 kW and 6 kW respectively.
4. Film 1a皿inator
The speed of the machine i8 between 5 and 20 m/min. The size
174 cm width, 135 cm length and 188 cm height. The electrical
requirement 1s about 1 kW. Compressed air i8 required with
pressure between 6 and 7 kg/cm2
5. Sanding machine
This machine is equipped with an exhaust blower with capacity
160 nM3/h.
Equipments layout of the plant 1s shown in Figure 3, but this
lining is not reflecting a f10wsheet of a typical process. For a
typical application, a typical flowsheet of the process is
required. Tota1 investment of the plant i8 about one million US $
(Table 1).
Table 1 Description of the pilot plant investment
Item8 Cost. US $ Budget
1. EBH 540,000 IAEA/UNDP(1984)
2. Wood hand.equip. 128,500 Batan/Incl.(1984)
3. Lab.equipt. 70,000 Batan/lncl.(1984)
4. Building 259,500 Ba tan/lnd. (1984)
5. UV source 15,000 IAEA (1986)
6. Reverse RG&Laminator 65,000 IAEA (1989)
Tota1 1,078,000
-121一
JAERI-M 93-160
APPLICATION OF THE PILOT PLANT
The equipment of the plant was reported to be running well from the begining of operation, but not for the plant as a whole. The plant has been reported unable in producing a product with property as formerly desired. There were some problems with :
- radiation curable materials - inert gas consumption - poor raw material available - eqipment lining - wood handling equipments
A ready for use of radiation curable materials with desired property and reasonable price was unavailable at the begining of operation.The expert accompanying the equipments did not give any satisfying recommendation. Finally our group decided to develope by themselve the formulation of radiation curable materials for a specific application using the available component. Although it takes a time but we have higher degree of freedom in using the materials. Radiation curing of surface coating technology actually was not a well established technology so far, and that is why a ready for use radiation curable material with reasonable price is not available locally.
Flowing an inert gas is very important in EB curing because the polymerization reaction is retarded with the existance of trace oxygen. In practical purposes, N2 gas is used which is coming from evaporation of liquid nitrogen. It was reported that consumption of liquid nitrogen is between 150 and 200 liters/h. It is easily to understand that this technique cannot be used in region where unavailable liquid nitrogen plant. A very high purity of liquid nitrogen is required. The oxygen content should be less than 1000 ppm, otherwise there will resulting a sticky surface. Unfortunately the purity of commercial liquid nitrogen was unconsistant from one batch to the other, and this will
- 122 -
jAERI-M 93-160
APPLICATION OF THE PIL01'・PLANT
The equipment of the plant was reported to be running well from
the begining of operation, but not for the plant as a whole. The
plant has been reported unable in producing a product with
property as formerly desired. There were some problems with
- radiation curable materials
- inert gas consumption
-poor raw material available
- eqipment lining
-wood handling equipments
A ready for use of radiation curable materials with desired
property and reasonable price was unavailable at the begining of
operation.The expert accompanying the equipments did not give any
satisfying recommendation. Finally our group decided to develope
by themselve the formulation of radiation curable materials for a
specific application using the available component. Although it
takes a time but we have higher degree of freedom in using the
materials. Radiation curing of surface coating technology
actually was not a wel1 established technology so far, and that
is why a ready for use radiation curable material with reasonable
price is not available locally.
Flowing an inert gas is very important in EB curing because the
polymerization reaction is retarded with the existance of trace
oxygen. 1n practical purposes, N2 gas is used which is coming
from evaporation of liquid nitrogen. 1t was reported that
consumption of liquid nitrogen is between 150 and 200 liters/h.
It is easily to understand that this technique cannot be used in
region where unavailable liquid nitrogen plant. A very high
purity of liquid nitrogen is required. The oxygen content should
be less than 1000 ppm, otherwise there will resulting a sticky
surface. Unfortunately the purity of commercial liquid nitrogen
was unconsistant from one batch to the other, and this will
-122-
JAERI-M 93-160
causing a difficulty in adjusting the dose of irradiation required for curing.
After years of operating the wood handling equipments, it was concluded that the equipments were unable to produce a fine coating as formerly expected. One of the reason is the poor wood panel available : unevenness in thickness, defecting on the surface and poor dimensional stability due to humidity. This will causes a great difficulty in the pretreatment processing as a whole. The other reason is coming from the equipments itself.
PROCESS DEVELOPMENT
A number of processes had been developed in the facility either the radiation curable materials or its processing flowsheet: coating on particle board, multiplex and wood parquet flooring. A number of formulation of radiation curable materials, process flowsheet and cost analysis of thechnology had been reported. Example of the process is the process of coating on wood parquet flooring. It had been reported that the coating cost was largerly coming from radiation curable materials(74.3% , based on US $ 8.33/kg), followed by liquid nitrogen cost (16%) and the rest is plant operation (9.7%). Investment required for a plant producing 5 million sqm of wood parquet flooring /year is about two million US $ and the coating cost was about US $ 2.17/sqm.
causing a difficulty in adjusting the dose of irradiation
required for curing.
After years of operating the wood handling equipments, it
was concluded that the equipments were unable to produce a fine
coating as formerly expected. One of the reason is the poor wood
panel available unevenness in thickness, defecting on the
surface and poor dimensional stability due to humidity. This will
causes a great difficulty in the pretreatment processing as a
whole. The other reason is coming from the equip町lents itself.
PROCESS DEVELOPKENT
A number of processes had been developed in the facility either
the radiation curable materials or its processing flowsheet:
coating on particle board, multiplex and wood parquet flooring. A
number of formulation of radiation curable materials, process
flowsheet and cost analysis of thechnology ha~ been reported.
Example of the process is the process of coating on wood parquet
flooring. It had been reported that the coating cost was largerly
coming from radiation curable materials(74.3% , based on US $
8.33!kg), followed by liquid nitrogen cost (16χ) and the rest i5
plant operation (9.7%). Investment required for a plant producillg
5 million sqm of wood parquet flooring Iyear is about tWQ
million US $ and the coating cost was about US $ 2.17/sqm.
Table 2 Coating on wood parquet flooring
Cost, %
Radiation ~urable mat. 74.3
Liquid nitrogen 16.0
e
'e
rn
ua
on
'be
at
-n
,ti
m回
-l'
t
n
ao
r--et
Pa
o--c
t
e
nr1J
ape
-
e
t
pde
9.7
100.0%
-123
JAERI-M 93-160
For clear coating of wood parquet flooring, instead of using EBM it can be used UV source, and this will be resulting of lower investment cost but the production cost may be not so far differ because the production cost is largerly coming from radiation curable materials. The cost of radiation curable materials for UV curing is higher than for EB curing because in UV curing, a photoinitiator is required , which is an expensive material.
Example formulation of radiation curable material for clear coating on wood panel is shown in Table 3.
Table 3 Radiation curable materials for EB curing of wood parquet flooring
For UV curing, 1-5% of photoinitiator is required in the mentioned formulation.
Cost evaluation of pigmented coating on wood panel showing the same result : the cost was largerly coming from radiation curable materials followed by liquid nitrogen and plant operation (Table 4).
- 124 -
jAERI-M 93-160
For clear coating of wood parquet flooring, instead of using
EBM it can be used UV source, and this will be resulting of lower investment cost but the production cost may be not so far differ
because the production cost is largerly coming from radiation
curable materials. The cost of radiation curable materials for UV
curing is higher than for EB curing because in リV curing, ~_
photoinitiator i5 required • which is an expensive material.
Example formulation of radiation curable material for clear
coating on wood panel is shown in Tab1e 3.
Table 3 Radiation curable materials for EB curing of wood parquet flooring
1. Base coat Wt part
Laromer EA-Bl(epoxy acrylate)
01' u1'ethane a1'ylate
PEGD企(polyethyleneglycole
diac1'y1ate)
Ta1c powde1'
11. Top coat
La1'ome1' EA-Bl
PEGDA
Hatting agent
5i1icon oil
60-50
30-40
10
60-70
40-30
5-10
1
For UV curing, 1-5% of photoinitiator is required in the
mentioned formulation.
Cost eva1uation of pigmented coating on wood pane1 showing the
same result the cost was 1argerly coming from radiation curab1e
materials followed by liquid nitrogen and p1ant operation (Table
4) .
-124
JAERI-M 93-160
Table 4 Pigmented c o a t i n g on wood p a n e l
Cost , X Radiation curable m a t e r i a l s 73 .8 Liquid ni trogen 18 .1 Plant operation 8 . 1
Tota l 100.0%
Total operation hours of EBM from 1984 to 1992 is more than 400 hours (Table 5), which is mainly used for process development, laboratory experiments and Regional Training Course (RTC). It was reported that there is no serious problem with regard to the operation of EBM during that time. Process development which is now being done : coating on ceramic, metal, gipsum, marble etc.
Table 5 Total hours of operation of EBM for process development, laboratory experiment and services
A number of customer had sent thousands square meter of wood
- 125 -
jAERI-M 93一160
Table 4 Pigmented coating on wood panel
Radiation curable materials
Liquid nitrogen
Plant operation
Total
Cost. %
73.6
18.1
8.1
100.0%
Total operation hours of EBM from 1984 to 1992 is more than
400 hours CTable 5). which is mainly used for process
development. laboratory experiments and Regional Training Course
(RTC). It was reported that there is no serious problem with
regard to the operation of EBM during that time. Process
development which is now being done coating on ceramic. metal,
gipsum, marble etc.
Table 5 Total hours of operation of EBM for process development. laboratory experiment and services
YEAR Operation.
hours
1984-1985 40
1986 45
1987 27
1988 30
1989 133
1990 85
1991 48
1992 21
Total 一 429
A number of customer had sent thousands square meter of wood
-125-
JAERI-M 93-160
parquet mosaic and wood panel to the pilot plant. The materials were coated using the available equipments. A lot of experiences were obtained by giving this radiation services. Based on this experience, an optimum process for a typical application has established and an economic analysis can be done with a higher accuracy. The results have been published anywhere.
It was concluded that the available pilot plant was unsuitable to be used as a commercial production of coated wood parquet-flooring or pigmented wood panel, although the size is a commercial size: the cost of coating will be very high which mainly due to the liquid nitrogen cost. This is true because the irradiation system of EBM is uncontinuous system, while the inert gas should flowing continuously. It was estimated that the inert gas consumption (N2) can be much reduced ( to one third) by using a continuous irradiation system.
Example :
The consumption of liquid nitrogen of the present EBM for surface coating is about 150 liter/hour. In the present system (uncontinuous), the speed of irradiation is about one piece/min. of wood panel (1.2 x 2.4m). Then the liquid nitrogen consumption is about 2.5 liter/piece of wood panel. If continuous system is applied, the speed of irradiation will be about 7.5 m/min.,or about 3 pieces of wood panel/min., and the liquid nitrogen consumption is about 0.8 liter/piece of wood panel.
REGIONAL TRAINING COURSE
Four times of RTC on radiation curing had been implemented in this facility. The courses were followed by participants from RCA Member States (Table 6). The participants from the last of the course were requested to make an economic analysis of the technology based on the condition available in each country. They concluded that the technology itself was superior technically compared to the conventional one, but for many developing countries they have some difficulties in marketing due to the
- 126 -
JAERI-M 93-160
parquet mos~ic and wood panel to the pilot plant. The materials
were coated using the available equipments. A lot of experiences
were obtain8d by giving this radiation services. 8ased on this
experience, an optimum process for a typical application has
established and an economic analysis can be done with a higher
accuracy. The results have been published anywhere.
It was concluded that the available pilot plant was unsuitable
to be used as a commercial production of coated wood parquet
flooring or pigmented wood panel, although the size i5 a
commercial size: the cost of coating will be very high which
mainly due to the liquid nitrogen cost. This is true because the
irradiation system of E8M is uncontinuous system, while the inert
gas should flowing continuously. It was estimated that the in8rt
gas consumption (N2) can be much reduced ( to one third) by using
a continuous irradiation system.
Example
The consumption of liquid nitrogen of the present E8M for
surface coating is about 150 liter/hour. In the present systeill
(uncontinuous), the speed of irradiation is about one piece/min.
of wood panel (1.2 x 2.4m). Then the liquid nitrogen consumption
is about 2.5 liter/piece of wood panel. If continuous system is
applied, the speed of irradiation will be about 7.5 m/min.,or
about 3 pieces of wood panel/min., and the liquid nitrogen
consumption is about 0.8 liter/piece of wood panel.
REGION企L TRAINING COURSB
Four times of RTC on radiation curing had been implemented in
this facility. The courses were followed by participants from RCA
Member States (Table 6). The participants from the last of the
course were requested to make an economic analysis of the
technology based on the condition available in each country. They
concluded that the technology itself was superior technically
compared to the conventional one, but for many developing
countries they have some difficulties in marketing due to the
-126一
JAERI-M 93-160
high cos t of product ion and high cos t of investment and supply
d i f f i c u l t y of r a d i a t i o n curab le m a t e r i a l s and l i qu id n i t r o g e n .
Table 6 Regional Training Course (RTC) on radiation curing of surface coating on wood panel in Jakarta
Country Number of participants II III IV
Bangladesh China India Indonesia Korea, Rep. Halaysia Pakistan Philipine Singapore Sri Lanka Thailand Vietnan
of
1 3
1 1
1 1 2
1 1
1 1 1 2
1 1 1
2 1 2 1 3
1 2
Total 10 14
Note : I Ol November 19B4 - February 19B5
II 11 November 1985 - December 19B5
III 29 September 19B6 - 24 October 19B6
IV 04 June 1990 - 22 June 1990
- 127 -
jAERI -M 93-160
high cost of production and high cost of investment and supply
difficulty of radiation curable materials and liquid nitrogen.
Table 6 Regional Training Course (RTC) on radiation curing of surface coating on wood panel in Jakarta
Country Number of participants
I II III
Bangladesh
China
lndia
Indonesia
Korea. Rep. of
Halaysia
Pakistan
Phi1ipine
Singapore
Sri Lanka
Thai1and
Vietnam
1
1
3
1
1
1
1 1
1 1
1 1
2 2
1 1
1
1
1 1
1 1
Total 8 9 10
Note 1 01 November 1984 - February 1985
11 11 November 1985 - December 1985
111 29 September 1986 - 24 October 1986
IV 04 June 1990 - 22 June 1990
-127一
IV
2
I
2
1
3
1
1
2
14
JAERI-M 93-160
REFERENCES
1. SUGIARTO DAHU, GATOT TRIMULYADI, ANIK SUNARNI dan DARSONO, Pelapisan perraukaan lantai parket seeara radiasi dengan bahan pelarut Laromer, Risalah Pertemuan Iliniah Proses Radiasi dalam Industri, Sterilisasi Radiasi dan Aplikasi Teknik Nuklir dalam Hidrologi, Jakarta, Desember (1988)
2. SUGIATO DANU, Economic analysis of radiation curing of surface coating of parquet flooring, Risalah Simposium IV Aplikasi Isotop dan Radiasi, Jakarta, 13-15 Desember 1989
3. SUGIARTO DANU, F.SUNDARDI, GATOT TRI HULYADI, KICKY LTK, ANIK SUNARNI and DARSONO, Radiation curing of commercial acrylates and polyester base compound for surface coating, First INDONESIA-JICA Polymer Symposium, Bandung 3-5 April (1989)
4. F.SUNDARDI, Experiences with radiation curing of surface coating pilot plant in Jakarta, Regional Executive Management Seminar on Industrial Radiation Curing Technology, Jakarta, 19-21 March 1990
5. SUGIARTO DANU, Analisis ekonomi pelapisan permukaan dengan teknologi radiasi, Seminar Nasional Para Eksekutif Aplikasi Teknologi Pelapisan Permukaan Secara Radiasi dalam Industri, Jakarta, 15 Maret 1990
- 128 -
JAERI-M 93-160
REFERENCES
1. SUG1ARTO DANU, GATOT TR1HULY企D1,AN1A SUNARNI dan DARSONO.
Pelapisan permukaan lantai parket secara radiasi dengan
bahan pelarut Laromer, Risalah Pertemuan Ilmiah Proses
Radiasi dalam Industri, Sterilisasi Radiasi dan Aplikasi
Teknik Nuklir dalam Hidrologi, Jakarta, Desember (1988)
2. SUGIATO DANU, Economic analysis of radiation curing of
surface coating of parquet flooring, Risalah Simposium IV
Aplikasi Isotop dan Radiasi, Jakarta, 13-15 Desember 1989
3. SUGIARTO UANU, F.SUND企RDI. GATOT TRI HULYADI, KICKY LTK,
ANIK SUNARNI and DARSONO, Radiation curing of commercial
acrylates and polyester base compound for surface coating,
First INDONESIA-JICA Polymer Symposium, Bandung 3-5 April
(1989 )
4. F.SUNDARDI, Experiences with radiation curing of surface
coating pilot plant 1n Jakarta, Reg10nal Executive Manage-
ment Seminar on Industrial Radiation Curing Technology,
Jakarta, 19-21 March 1990
5. SUGIARTO DANU, Analisis ekonomi pelapisan permukaan
dengan teknologi radiasi, Seminar Nasional Para Eksekutif
Aplikasi Teknologi Pelapisan Permukaan Secara Radiasi
dalam Industri, Jakarta, 15 Maret 1990
一 128-
JAERI-M 93-160
Radiation curable materials
Wood panel
O |lc^*uittj
ROLL COATER
ELECTRON BEAM MACHINE (EBM)
Coated wood panel
Fig. 1 Basic flowsheet of EB curing of surface coating process
25
20
15
xn o
Q
10
5-
0 0 5 10 15 20 25
Conveyor speed, tn/min
Fig. 2 Relation between EB irradiation dose and conveyor speed or beam current
- 129 -
巴里旦ー...... ・・
jAERI-M 93-160
ーーー・4惨巨宣言ヨ
Radiatio九
4 …・
巴 2 → δCoated LJood panel ELEC'I曳ONBEAM
MACHlNE (EBM) ROLL COATER
Wood panel
Basic flowsheet of EB curing of surface coating process Fig. 1
mA
mA
50
20 • 。
mA 5 @
dlIloi--1011¥。
25
20
J5 てコ伺'-
芝
~ 10 o D
5
。。 30 25
C on veyor speed I m Imin 20 15 10 5
Relation between EB irradiation dose and conveyor speed or beam current
-129一
Fig. 2
JAERI-M 93-160
as
> CO O S- S-
4-> 3 r— O
4 a> c o s-
-4-> • ! -O E .C u o u
r— CU CO tt) J3 E 4-> c
to
8 8
S"
o O O
O
c •I- i-
•»-> •*-> s- ro 3 O o o
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i . o
4-> (O
c • r - CO I f - I—
P.
c •H
60 a
•H C5
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00 •H Pn
<£§ c CO l/J
8 9
o o
S -a>
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QJ O l/l O s -QJ r— > r— a> o j - s -
- 1 3 0 -
JAERI-M 93-160
ωυLコom
リ
F白戸
OF〉
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Lμ・戸『d
mdmm
日日ロ司同内同
UHOHJ明向日
ωzuロJ明∞
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ou
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EFFhF
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Lω〉
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;13
130 -
。~i
t±^3 &
OB 1 s t SANDER
r r» o H.V1.!' 1VJJ| ^
1 St ROLL COATER
1 s t EBM
GED
2nd SANDER
s I
o
2 T
to I
2nd ROLL COATER
2nd EBM
Fig. 4 Flowsheet of EB curing of surface coating on wood parquet flooring
& 5 -・回圃t礎》
ロココ→。凶→会2nd SANDER
"EBM 1st 1 st ROLL COATER
SANDER 1st
恒〉阿見同窓包
150
圃ー噂・ー・圃圃.. 自主目め。
巴-ヨ
lHωH
EBM 2nd 2nd ROLL COATER
Flowsheet of EB curing of surface coating on wood parquet flooring
Fig. 4
JAERI-M 93-160
2.11. Sterilization with Electron Accelerators M. Takehisa
R a d i a I n d . Co. L t d .
TREND OF RADIATION STERILIZATION IN JAPAN
Radiation sterilization of medical devices has been continuously increasing in Japan for last 20 years, the main items was initially hypodemic needles, and now is dialyzers. There are other items such those hypodemic syringes, surgical knives, sacarpels, catheters, and so on. The advantages of radiation sterilization is well known in Japanese device manufactures, but still more than 50% of the products are sterilized with use of ethylene oxide gas mainly due to the cheaper cost.
Large medical device manufacturers settled their own radiation facilities (in house) with use of Co-60 source. Table 1 shows the radiation facilities used for medical device sterilization.
Table 1 Commercial y irradiation facility in Japan (as of 1991/12)
Company Established Location Capacity Activity Note kCi kCi
Presently two high power 5 MeV electron beam facilities for contract irradiation are in operation by SHI and RIC. However, application to medical device sterilization is in infant stage in Japan. One company, Hogy medical, has just started a sterilization of non-woven fabric products, which is
- 132 -
]AERI-M 93-160
2.11. Sterilization with Electron Accelerators
M. Takehisa
Radia工nd. Co. Ltd.
TREND OF RADIATION STERILIZATION IN JAPAN
Radiation sterilization of medical devices has been con-
tinuously increasing in Japan for last 20 years. the main
items was initially hypodemic needles. and now is dialyzers.
There are other items such those hypodemic syringes. surgical
knives. sacarpels. catheters, and so on. The advantages of
radiation sterilization is well known in Japanese device manufactures. but still more than 50% of the products are
sterilized with use of ethylene oxide gas mainly due to the
cheaper cost.
Large medical device manufacturers settled their own radiation facilities (in house) with use of Co-60 source. Table 1 shows
the radiation facilities used for medical device sterilization.
Table 1 Commercial y irradiation facility in Japan (as of 1991/12)
Company Established Location Capacity Activity Note
Presently two high power 5 MeV electron beam facilities for
contract irradiation are in operation by SHI and RIC. However. application to medical device sterilization is in in-
fant stage in Japan. One company, Hogy medical. ha主 just
started a sterilization of non-woven fabric products. which is
-132一
JAERI-M 93-160
not medical devices in Japan and is classified as miscellaneous products, with use of 10 MeV linac in-house facility this year.
Table 2 shows trend of gamma-sterilization field in RIC, which shows increase in radiation sterilization of non-medical devices. The electron beam sterilization will also follow the trends in near future.
Table 2 Trend of radiation sterilization in Radia (trend as of 1990)
Field Examples Share ( % )
Trend in 1990
Background
Medical Dialyzer, 30-40 Decrease Increase in Device Lancet,
The characteristics of electron beam sterilization is compared to gamma sterilization, because it will compete each other in the future. Tables 3 and 4 shows the characteristics from technical, and economical & social view points for the high power direct current electron beam machines.
Presently, several hundreds of direct current EB machines are in industrial operation in the world, but most of them are generating up to 3 MeV EB for polymer processing. Only several machines are used in sterilization purpose together with
- 133 -
jAERI-M 93-160
not medical devices in Japan and is classified as miscel-
laneous products, with use of 10 MeV linac in-house facility
this year.
Table 2 shows trend of gamma-sterilization field in RIC. which
shows increase in radiation sterilization of non-medical
devices. The electron beam sterilization will also follow the trends in near future.
Table 2 Trend of radiation sterilization in Radia (trend as of 1990)
Field Examples Share Trend Background
( % ) in 1990
Medical Dialyzer, 30-40 Decrease Increase in
Device Lancet, In-house
etc.
Bio-exp. Ptetri Dish. 25-30 Increase Disposable.
Apparatus Culture Flask, Residual EO
etc.
Container, Container, 20-25 Increase Need Asepti c
Packaging Plastic Bag Residual EO
etc.
Ex. Animal Sterile, 20 Balance Exp. Improve
Feeds SPF SPCA Press.
CHARACTERISTICS OF ELECTRON BEAM Sτ官RILIZATION
The characteristics of electron beam sterilization is compared
to 9剖nmasterilization, because it will compete each other in the future. Tables 3 and 4 shows the characteristics from
technical, and economical & social view points for the high
power direct current electron beam machines.
Presently, several hundreds of direct current EB machines are
in industrial operation in the world. but most of them are generating up to 3 MeV EB for polymer processing. Only several
machines are used in sterilization purpose together with
-133-
JAERI-M 93-160
polymer processing in contract irradiators.
Less than ten linear accelerators are used, mostly in European countries, for sterilization with a energy level of 10 MeV. So far the powers are not competitive to direct current machines. Linear cathode low energy machines are proposed to sterile a surface of containers but practical application is not so broad.
Table 3 Technical comparison of EB and y sterilization
Radiation source Sterilization effect Process capacity Dose rate Material deterioration Penetration Dose uniformity
EB ?' electrically radioisotope same same large (10 MCi) small high low small large small large large small
Table A Economic & social comparison of EB & y sterilization
Public acceptance Source investment Conveyor Process cost Product bulk density Product quantity
EB easy advantage in large expensive cheap low (< 0.2 g/cc) need large batch
difficult in small cheap expensive high O0.2) small batch
Tables 3 and 4 clearly show that the EB and y sterilizations have supplementary nature, and should be chosen according to a character to the products to be sterilized or amount of products per batch from customers in the service area.
In the case of 10 MeV class EB with use of linear accelerators the penetration will be similar to the gamma irradiators in a practical application, but the author does not have personal experiences to discuss in detail.
- 134 -
]AERI-M 93-160
polyrner processing in contract irradiators.
Less than ten linear accelerators are used. mostly in European
countries. for sterilization with a energy level of 10 MeV. So far the powers are not competitive to direct curr目立
machines. Linear cathode low energy machines are proposed to
sterile a surface of containers bu仁 practical app1ication is
not so broad.
Table 3 Technical comparison of EB and y sterilization
EB
Radiation source e1ectrically
Steri1ization effect same Process capacity large (10 MCi)
Dose rate high
Materia1 deterioration sma11
Penetration small Dose uniformity large
γ
radioisotope
same smal1
10w
large
large
small
Table 4 Economic & social comparison of EB & Y sterilization
EB γ
Public acceptance easy difficu1t
Source investment advantage in large in small
Conveyor expensive cheap
Process cost cheap expens~ve
Product bulk density 10¥¥7 (< 0.2 g/ccJ high ()0.2)
Product quantity need large batch smal1 batch
Tab1es 3 and 4 clearly sho¥¥7 that the EB and γsterilizations have supplementary nature, and shou1d be chosen according to a
character to the products to be sterilized or amount of
products per batch from customers in the service area.
1n the case of 10 MeV class EB with use of linear accelerators
the penetration will be similar to the gamma irradiators in a
practica1 application. but the author does not have personal experiences to discuss in detai1.
-134 -
JAERI-M 93-160
A bird's eye view of 5 MeV, 30 mA (150 kW) electron beam facility which can also be used as a x-ray facility of RIC is shown in Fig. 1.
A joint research (JAERI - RIC) on an evaluation of EB sterilization of surgical gloves with use of 5 MeV EB show that the RIC's facility can be sterilized 36,000 pairs of surgical gloves at 25 kGy sterilization dose, corresponding 0.86 Million pairs per day at 24 hrs operation. The product unit is 12 gloves in one box and the dose uniformity is 3.3. The dose uniformity is larger than y radiation and the material degradation should be studied. The processing capacity is 5 times larger than 1 MCi ?- irradiator.
The example demonstrate that 150 kW EB facility has a tremendous capability if the products meet EB sterilization.
DOSE SETTING METHODS FOR MEDICAL DEVICE STERILIZATION
Historically 25 kGy has been widely used to attain a sufficient dose to achieve the sterility assurance level (SAL) of 10 to the -6. This is based on an experience of gamma sterilization and is applied to the EB sterilization too. The efficacy of sterilization was considered to be the same for both EB and y sterilizations but Scandinavian countries was regulated the different doses for EB and y sterilizations, 35 and 32 kGy.
At present the formulation of the International Standard of medical device sterilization is under progress in the ISO technical committee (IS0/TC198) and is in the final stage. For radiation sterilization, the revised Draft International Standard is under circulation and will be finalized within a year. In the international standard, the sterilization dose is not differentiated in either gamma, X-ray, and EB. However, the dose setting tests needs more difficult techniques in EB for large medical devices.
The recommended dose setting consists of 2 methods.
a) dose setting using bioburden information b) dose setting using fraction positive information from
incremental dosing
- 135 -
]AERI-M 93-160
A bird's eye view of ラ MeV,ヨomA (150 kW) electron beam
facility which can also be used as a x-ray facility of RIC is
shown in 1"ig・1.
A joint research (JAERI RIC) on an evaluation of EB
sterilization of surgical gloves with use of 5 MeV EB show
that the R1C's facility can be sterilized 36,000 pairs of sur-gical gloves at 25 kGy sterilization dose, corresponding 0.86
Million pairs per day at 24 hrs operation. 宜'heproduct uni t
is 12 gloves in one box and the dose uniformity is 3.3. 官le
dose uniformity is larger than γradiation and the material degradation should be studied.τ'he processing capacity is 5
times larger than 1 MCi r irradiator.
百1e example demonstrate that 150 kW EB facility has a tremen-dous capability if the products meet EB sterilization.
DOSE SETT1NG METHODS FOR MEDICAL DEV1偲 STER1LIZATION
Historically 25 kGy has been widely used to attain a suffi-
cient dose to achieve the sterility assurance level (S且.) of
10 to the -6. 官1is is based on an experience of gamma sterilization and is applied to the EB sterilization too. 官官
efficacy of sterilization was considered to be the same for
both EB and γsterilizations but Scandinavian countries was
regulated the different doses for EB and γsterilizations, 35
and 32 kGy.
At present the formulation of the 1nternational Standard of
medical device sterilization is under progress in the 1SO technical committee (1SO/TC198) and is in the final stage.
For radiation sterilization, the revised Draft 1nternational
Standard is under circulation and will be finalized within a
year. In the international standard, the sterilization dose is not differentiated in either 9副 首na, X-ray, and EB.
However, the dose setting tests needs more difficult tech-
niques in EB for large medical devices.
The recommended dose setting consists of 2 methods.
a) dose setting using bioburden information b) dose setting using fraction positive information from
incremental dosing
Eu qa
噌
E--
JAERI-M 93-160
Methods a) and b) are well known methods as AAMI (Association of Advancement Medical Instrumentation) Bl and B2 methods. These are popularly used in North America, but those are rarely used in our regions due to the regulations and resource oriented method of these. In the near future we can not use the on going dose setting method using biological indicator with B. pumilus for export products. Sterility test is also not recommended due to high false positive probability, 0.001, than SAL of 0.000001.
Table 5 Recommended dose setting methods
Method 1. dose setting from bioburden information
(1) Bioburden consists of known distribution of radiation resistance (obtained from D-value distribution mainly in North America)
(2) measure the bioburden (3) irradiate the sample to SAL=0.01 dose, confirm radiation
resistance of the bioburden is weaker than that of the standard radiation resistance distribution by sterility test of 100 samples
(4) determine the sterilization dose according to the bioburden (5) audit should be made every 3 months
Method 2. dose setting using fraction positive information from incremental dosing
(1) not required bioburden measurement (2) determine SAL=0.01 dose by incremental dosing combined with
sterility tests (3) determine sterilization dose with extrapolation method at
smaller SAL region than 0.01 (4) require 640 samples for sterilization dose determination
and audit
strong point - less assumption, measure with natural bioburden weak point - need large number of samples
- 136 -
JAERI-M 93-160
Methods a) and b) are we~l known methods as AAMI (Association
of Advancement Medical Instrumentation) B1 and B2 methods.
These are popularl~' used in North America, but those are rarely used in our regions due to the regulations and resource oriented method of these. 1n the near future we can not use
the on going dose setting method using biological indicator
with B. pumilus for export products. Sterility test is also not recommended due to high false positive probability, 0.001,
than SAL of 0.000001.
Table 5 Recommended dose setting methods
Method 1. dose setting from bioburden information
(1) Bioburden consists of knO'明1 distribution of radiation
resistance (obtained from D-value distribution mainly in
North America) (2) measure the bioburden
(3) irradiat~ the s剖npleto SAL=0.01 dose, confirm radiation
resistance of the bioburden is weaker than that of the
standard radiation resistance distribution by sterility
test of 100 s剖nples(4) determine the sterilization dose according to the bioburden
(5) audit should be made every 3 months
bioburden 1000 -) sterilization dose 24.9 kGy at (SAL=10-6)
100 21.2
10 17.7
Method 2. dose setting using fracticn positive information from incremental dosing
(1) not required bioburden measurement (2) determine SAL=0.01 dose by incren氾ntaldosing combined with
sterility tests
(3) determine sterilization dose with extrapolation method at
smaller SAL region than 0.01 (4) require 640 samples for sterilization dose determination
and audit
strong point -less assumption. measure with natural bioburden ¥l1eak point -need large number of samples
136一
JAERI-M 93-160
The detail of dose setting are outside of the scope but we have to establish reasonable method with scientific backgrounds.
For EB sterilization two problems for dose setting tests are:
1) correct dosing to test sample for incremental dosing in the target dose of several kGy range within +/- 10 %
2) irradiation of a medical device sample with small Dmax/Dmin, recommended for gamma-sterilization is in the range of 1.0 to 1.05, which will practically prohibiting EB sterilization for large medical devices and will require the dose setting test for small samples by dividing into small pieces with use of SIP (sample item portion) concept.
X-RAY STERILIZATION PRODUCED BY BREMSSTRAHLUNG OF EB
A potential application of EB sterilization of large medical devices, dense and/or thick products can be achieved by use of X-ray by bremsstrahlung of high energy electron beam. The EB can be converted into X-ray by impinging EB to plate of high Z materials. The conversion efficiency of EB energy into X-ray for forward direction is about 8% with use of 5 MeV EB. Table 6 shows characteristics of the bremsstrahlung irradiation.
Table 6 Characteristics of X-ray (bremsstrahlung)
1) Machine generated photon radiation, ease of operation for wide dose range without use of radionuclides
2) High penetration than Co-60 gamma-ray, homogeneous dose distribution can be processed large and/or high bulk density products
3) High dose rate, short processing time less material degradation
4) Processing cost of x-ray with gamma-ray irradiation comparable cost to gamma-ray for dual purpose facility bargaining power for Co-60 price rise no disposal problem for decayed radioisotope source
- 137 -
JAERI-M 93-160
τhe detail of dose setting are outside of the scope but we
have to establish reasonable method with scientific
backgrounds.
For EB sterilization two problerns for dose setting tests are:
1) correct dosing to test sample for incrernental dosing in the
target dose of several kGy range within +j- 10 %
2) irradiation of a medical device sample with srnall Dmax/Drnin,
recommended for gamma-sterilization is in the range of 1.0
to 1.05, which will practically prohibiting EB sterilization for large medical devi.ces and will require the dose setting
test for small samples by dividing into small pieces with
use of SIP (sample item portion) concept.
X-RAY STERILIZATION PRODUCED BY BRE1マSSTRAHLlR可GOF EB
A potential application of EB sterilization of large medical devices, dense and/or thick products can be achieved by use of
X-ray by bremsstrahlung of high energy electron beam. 古田 EBcan be converted into X-ray by impinging EB to plate of high Z materials. The conversion efficiency of EB energy into X-ray for forward direction is about 8% with use of 5 MeV EB. Table
6 shows characteristics of the bremsstrahlung irradiation.
Table 6 Characteristics of X-ray (bremsstrahlung)
1) Machine generated photon radiation. ease of operation for wide dose range without use of radionuclides
2) High penetration than Co-60 gamma-ray. homogeneous dose distribution can be processed large and/or high bulk density products
3) High dose rate. short processing time less material degradation
4) Processing cost of x-ray with gamma-ray irradiation comparable cost to gamma-ray for dual purpose facility bargaining power for Co-60 price rise no disposal problem for decayed radioisotope source
137 -
JAERI-M 93-160
Bremsstrahlung Facility of RIC
Fig. 2 shows x-ray converter located below a beam window of RIC's EB machine. 5 MeV. 30 mA electron beams are converted into x-ray in the high Z target made of tantalum. The x-ray dose rate 40 cm belov the target is shown in Fig. 3 together with experimental measurement by CTA and computer simulation using APEX-P. Discrepancy in conveyor direction between dosimetry and the calculation is due to shadowing to diagonal x-ray by target structure. It is noteworthy that x-ray by bremsstrahlung gives very high dose rate photon irradiation than Co-60 gamma source. We started the commercial activity of the new technology just this year .
Conclusion
Many EB machines in the world are used for polymer processing most of which generate medium energy electron beam in the range of 0.8 to 3 MeV. With use of relatively high energy, 4.5 MeV. high power electron beam machine sterilization of health care products are realized in the United States. It is not yet popular in the other countries due to small scale production of such products. The market size is smaller in Japan than the U.S. and it is not commercially feasible to do sterilization only for medical devices and health care products. We have to give contract irradiation to the other fields such as polymer application. It is assumed that the industrial infra-structures here are similar to Japan in this sense. Best way here might be construction of the dual purpose EB facility for sterilization and polymer applications.
- 138 -
jAERI -M 93-160
Bremsstrahlung Facility of RIC
Fig. 2 shows x-ray converter located below a beam window
of RIC's EB machine. 5 MeV. 30 mA electron beams are cαr ve~ted into x-ray in the high Z target made of tantal四 1. The
x-ray dose rate 40 cm belo¥,' the target is shown in Fig. 3
together with experimental llleasurement by CTA and computer simulation using APEX-P. Discrepancy in conveyor directiα1 between dosimetry and the calculation is due to shadowing to
diagonal x-ray by target structure. It is noteworthy that x-
ray by bremsstrahlung gives very high dose rate photon ir-
radiation than Co-60 gamma source. We started the co羽田ercialactivity of the new technology just this year
Conclusion
Many EB machines in the world are used for polymer processing
most of which generate medium energy electrα1 beam in the
range of 0.8 to 3 MeV. With use of relatively high energy.
4.5 MeV. high power electron beam machine sterilizatiα1 of
health care products are realized in the United States. It is
not yet popular in the other countries due to small scale
production of such products.τhe market size is smaller in
Japan than the U.S. and it is not cαllIDercially feasible to do
sterilization only for medical devices and health care
products. We have to give contract irradiation to the other fields such as polymer application. It is assumed that the
industrial infra-structures here are similar to Japan in this
sense. Best way here might be construction of the dual pur-
pose EB facility for sterilization and polymer applicatiα15.
-138一
JAERI-M 93-160
Discussion
Questions from Mrs. Nazly Hilmy, Director of PAIR
1) Method of validation in irradiation with use of electron beam machine.
2) How do you carried out dosimetric validation ?
Answers from Dr. Takehisa
1) Sterilization of medical devices and food irradiation are obligatrily to validate the routine processing. The validation include facility, and routine processing. Most important point is to deliver a correct dose to the product. In this sense, the difference of electron beam and gamma rays is that the gamma ray can be validated to dose distribution in the product box for bulk density. But in the case of electron beam overall bulk density can not validate a delivered dose to each product in the product box, and needs measuring dose distribution on/in a represented each product. Then the product configuration in a box should be determined in the electron beam application.
2) We use CTA dosimeter to find a detailed dose mapping in/on the each product in a carton box. (-'ith use of long strip of CTA dose distribution can be measured in detail and minimum and maximum dose points are obtained conveniently.
- 139 -
JAERI-M 93-160
Discussion
Questions from Mrs. Nazly Hilmy. Director of PAIR
1) Method of validatiα1 in irradiatiα1 with use of electrα1
beam machine.
2) How do you carried out dosimetric validation ?
Answers from Dr. Takehisa
1) Sterilization of medical devices and food irradiation are
obligatrily to validate the routine processing. 官1e valida-
tion include facility. and routine processing・Mostimportant
point is to deliver a correct dose to the product. In this sense, the difference of electron beam and gamma rays is that the gamma ray can be validated to dose distribution in は1e
product box for bulk density. But in the case of electron beam
overall bulk density can not validate a delivered dose to each product in the product box. and needs measuring dose distribu-
tion on/in a represented each product. Then the product con-
figuration in a box should be dete~mined in the electron beam
application.
2) We use CTA dosimeter to find a detailed dose mapping injon
the each product in a carton box. i.'午thuse of long strip of CTA dose distribution can be measured in detail and minimum and rnaximum dose points are obtained conveniently.
- 139-
JAERI-M 93-160
A: Electron Beam Generator B: EB Scan Horn C: Irradiation Conveyer D: Product E: Unloading from Conveyer F: Loading to Conveyer G: Shielding Door H: Slit for Long Object Note: X-ray Converter is not shown in Bird's Eye View
Fig. 1 Bi rd ' s eye view of RIC's EB and X-ray f a c i l i t y
- 140 -
]AERI-M 93ー160
A: Electron 8eam Generator 8: EB Scan Horn
C: Irradiation Conveyer 0: Product
E: Unloading from Convcyer F: Loading to Conveycr
G: Shielding Door H: Slit for Long Object
Note: X-ray Converter is not shown in 8ird's Eye View
Fig. 1 Bird's eye view of RIC's EB and X-ray facility
- 140 -
JAKKl-M 93-160
Fig. 2 Product under EB i r r a d i a t i o n
-~.s~z&srs
Fig. 3 Turn over machine for dual side irradiation
141 -
JEIH --¥1 93--160
Fig. 2 Product under EB irradiation
Fig. 3 Turn over machine for dual side irradiation
141
JAKRI--M 93-160
I I i? -'•
ui-sr
4«*
.«TS
Fig. 4 X-ray converter and product under x-ray irradiation
50
40"
•v 20-
10-
0-V
5MV,30fifl,140cm-S740cm UNDER THE WINDOW 10+2min IRRflD.
40 i
80 120
• PHHfl - - CTfl K=0.072
• «. ^~^ £
K J P ' '
• £ ;' • • \ •
i • •
\ '• V
i * • • i ; \
f ••• ••• • , „
• • • • V
160 200
Fig. 5 Dose d i s t r i b u t i o n of x-ray
142
JAERI--¥1 93 -160
X-ray converter and product under x-ray irradiation Fig. 4
5l-lVr3Or前:,140cm-S,4ocmUlDER mE ~m!IXX.J 10-泊ninIR問D.
50
40
30
20
10
h、v q嘘
札
wnaA
2伺160 120 8O 40 9
0
SC411 D/r.jsc-tiD U どど削J
ー-c丁目 K==0.0n
Dose distribution of x-ray
142
φ 門小泊
Fig. 5
JAERI-M 93-160
2.12. The Possibility of using Electron Beam Machine for Food Preservation in Indonesia
Nazly Hilmy
Center for the Application of Isotopes and Radiation, BATAN
INTRODUCTION
The first industrial-sized Electron Beam Machine was built by Raychem Company in March 1957. It was a 1 MeV 6 m A General Electric resonant transformer. The first three products of Raychem Company were miniature coaxial cable, heat-shrinkable tubing and high-performance hook-up wire. The total cost of the first beam cell was US $ 7.000. In 1976 the value of the company become US $ 175 million at a growth rate of 25 % per year (1).
At present Electron Beam Machine have also been used for sterilization of medical health care items.beside others technology such as Etylene oxyde gas and gamma radiation. The market share of the application can be seen in Fig. 1. From an estimated 10 million cubic meters of disposable medical products and related health care items currently being sterilized around the world Ethylene oxide gas (ETO) is used to treat approximately 7.1 million m 3, gamma radiation is used approximately 2.8 million m3, and EBM is used to treat on approximately 0.3 million m3 . The estimation future growth of EBM applications for sterilization of medical items is uncreasing as can be seen in Fig. 2 (2).
The Codex Alimentarius Commission's (1984) proposed international standard for irradiated foods, permits three types of ionizing radiation to be used i.e. gamma rays from the radionuclides Co-60 or Cs-137, electrons from EBM with energies of 10 MeV or less, and X-rays with energies of 5 MeV or less. On the molecular level, these three types of radiation have similar effects. The effects of electron beam and gamma rays on microbes and materials exposed are similar.but they have different properties that effects their technical, social and economic desirability such as energy efficiency, absorption efficiency, reliability and maintainability, cultural fit, product flow and dose quality assurance (3-4).
This paper will not be assessed in any detail of economic issues.
THE CHARACTERISTICS OF RADIATION
The characteristics of the three types of radiation can be seen at Table 1. The low penetration of electron particles in water compared to gamma -rays or X-rays can be seen in Fig. 3 and the penetration of 10 MeV electron in water can be seen in Fig. 4.Penetration of 5 Mev bremstrallung in water ( x-rays) can be seen in Fig.5.
RADIATION PENETRATION
One of the most important difference between the three types of radiation sources is penetration.Gamma rays from Co-60 and x-rays can penetrate pallet load of foods.Depending on foods density, 10 Mev electrons cannot penetrade more than 2.5 up to 8.0 cm when irradiated from one side ( Table 2 ).The calculation was based on the formula (5):
- 143 -
JAERI-M 93← 160
2.12. The Possibility of using Electron Beam Machine for Food Preservation in Indonesia
Nazly Hilmy
Center for the Application of Isotopes and Radiation, BATAN
INTRODUCTION
The first industrial-sized Electron Beam Machine was built by Raychem Company in March 1957. It was a 1 Me V 6 m A General Electric resonant transformer. The first three products of Raychem Company were miniature coaxi心cable,heat-shrinkable tubing and high-performance hook-up wire. The to凶 costof the first beam cell was US $ 7.000. In 1976 the va1ue of the company become US $ 175 miIIion at a growth rate of 25 % per year (1).
At present Electron Beam Machine have also been used for sterilization of medical hea1th care items,beside others technology such as Etylene oxyde gas and gamma radiation. The market share of the application can be seen in Fig. 1. From an estimated 10 million cubic meters of disposable medical products and related health care items currently being steriliz~ around the world Ethylene oxide gas (ETO) is used _to treat approximately 7.1 million m~ , gamma radiation is u~éd approximately 2.8 million m3, and EBNI is used to treat on approxi-mately 0.3 million mJ
• The estimation future growth of EBM applications for sterilization of medical items is uncreasing as can be seen in Fig. 2 (2).
The Codex Alimentarius Commission's (1984) proposed international standard for irradiated foods, permits three types of ionizing radiation to be used i.e. gamma rays from the radionuclides Co・60or Cs-137, electrons from EBM with energies of 10 MeV or less, and X-rays with energies of 5 MeV or less. On the molecular level, these three types of radiation have similar effects. The effects of electron beam and gamma rays on microbes and materia1s exposed are similar,but they have different properties that effects their technical, social and economic desirability such as energy efficiency, absorption efficiency, reliability and maintain-ability, cultural fit, product flow and dose quality assurance (3・4).
This paper will not be assessed in any detaiI of economic issues.
THE CHARACTERISTICS OF RADIATION
The characteristics of the three types of radiation can be seen at Table 1. The Iow penetration of electron particles in water compared to gamma -rays or X-rays can be seen in Fig・3and the penetration of 10 MeV electron in water can be seen in Fig. 4.Penetration of 5 M\~v bremstrallung in water ( x-rays) can be seen in Fig.5.
RADIATION PENETRATION
One of the most important difference between the three types of radiation sources is penetration.Gamma rays from Co・60and x-rays can penetrate pallet load of foods.Depending on foods density, 10 Mev electrons cannot penetrade more than 2.5 up to 8.0 cm when irradi-ated from one side (Table 2 ).The calculation was based on the formula (5):
143 -
JAERI-M 93-160
Voltage = 2.63 TD + 0.32 ( single sided treatment)
Voltage = 1.19 TD + 0,32 ( double sided treatment)
where: T = Thickness of product D = Density of product
Caused by the low penetration of electron particles,the calculation is based only on 5 up to 10 Mev EBM. The limited penetration of electron beams restricts their use only to treating food surface,thin packages or a shallow stream of grain,powder or liquids. A bulk irradiator using electron beams would need to be part of a processing or packing plant to treat the food before it is packed for shipping. One of the important advantages of EBM compared to gamma facilities is operation condition.The operation of the machine can be arranged based on the availability of materials to be irradiated.lt is very useful to be used to treat seasonal products which have peak season.
COMMODITIES TO BE IRRADIATED
Indonesia has approved the food irradiation technology for commercial purposes since December 1987,consisting of three kinds of food commodities i.e. spices,tubers and grains.The commercial application of radiation technology on spices and mixed herbs for local consumtion was increasing in Indonesia i.e. about 90 m in 1989 and 180 m3 in 1990.Spices are one of the important Indonesian export commodity where radiation technology can be used.Export of Indonesian black pepper, white pepper,nutmeg and cassia vera to countries that have accepted irradiated spices are increasing,but sometimes a part of the commodities was detained by the importing countries,since the quality did not meet the requirements in the importing countries.lt is hoped that in the future all important countries will accept irradiated spices from Indonesia (6).
MAINTENANCES AND POWER OF ELECTRICITY
In operating the EBM.maintenance and electricity are two main problems in developing countries like Indonesia. Spare-parts have to be imported and the facility has to have skill labours in handling and maintained the machine.The EMB need higher power of eiectricity compared to Co-60 facilities.If the problems of maintenance,electricity and skill-labours could be overcome,the EBM will be an alternative technology for food preservation in Indonesia.
CONCLUSIONS
It can be concluded that an EBM with energy between 5 to 10 Mev has a good prospect to be used for food preservation in Indonesia if problems on maintenance , electricity and human resources could be overcome.
- 144 -
JAERI -M 93-160
Voltage = 2.63 TD + 0.32 ( single sided tr回 tment)
Voltage = 1.19 TD + 0,32 (double sided treatment )
where: T = Thickness of product D = Density of product
Caused by the low penetration of electron p釘 tic1es,thecalculation is based only on 5 up to 10 恥1evEBM. The limited penetration of electron beams restricts their use only to treating food surface,thin packages or a shallow stream of grain,powder or liquids.A bulk irradiator using electron beams would need to be part of a processing or packing plant to treat the food before it is packed for shipping. One of the important advantages of EBM compared to gamma facilities is operation condition. The operation of the machine can be arranged based on the availability of materials to be irradiated.It is very useful to be used to treat seasonal products which have p飽 kseason.
COMMODlTIES ro BE IRRADlATED
Indonesia has approved the food irradiation technology for commercial pu中osessince December 1987,consisting of three kinds of food commodities i.e. spices,tubers and
~~~~~!.~:_c~~~::r:~~ ~I?~i~_at!~~ _o!_~~?i~~o~ ~~~n~~o!~ ~..n 1sR~~e~ ~~~ ~i:.~ : ~e~~~!o~~?~ consumtion was increasing in Indonesia i.e. about 90 in"J in 1989 and 180 m3 in 1990.Spices are one of the important Indonesian export commodity where radiation technology can be used.Export of Indonesian black pepper, white pepper,nutmeg and cassia vera to countries that have accepted irradiated spices are increasing,but sometimes a part of the commodities was detained by the importing countries,since the qua1ity did not meet the requirements in the importing countries.It is hoped that in the future all important countries wi11 accept irradiated spices from Indonesia (6).
MAINTENANCES AND POWER OF ELECTRICITY
In operating the EBM,maintenance and electricity are two main problems in developing countries like Indonesia. Spare-parts have to be imported and the facility has to have skill labours in handling and maintained the machine. The EMB need higher power oi ek~trícity compared to Co-60 facilities.If the problems of maintenance,electricity and skill-labours could be overcome, the EBM wi1l be an alternative technology for food preservation in Indonesia.
CONCLUSIONS
It can be concluded that an EBM with energy between 5 to 10 Mev has a good prosp配 tto be used for food preservation in Indonesia if problems on maintenance , electricity and human resources could be overcome.
1.COOK,P.M. (1990),Impact and Benefit of Radiation Technology.Radiat.Phys.Chem., Vol. 35,Nos 1-3, pp 7-8.
2.BRINSTON,R.M.(1990),Future Growth in the Gamma Sterilization of Disposable Medical Products,Radiat.Phys.Chem.,Vol.35,Nos 1-3, pp 390-392.
3.MORRISON,R.M.(1990),Economic of Food Irradiation Comparison Between Electron Accelerators and Co-60,Radiat.Phys.Chem.,Vol.35 Nos 4-6, pp 673-679.
4.ISHIGAKI,I.(1990),Electron Beam Sterilization of Medical Products.Proc.of The Workshops on The Utilization of Electron Beams,JAERI-M 90-194, JAERI,Japan,pp 102-108.
5.HENRY,G.TIMOTHY,(1990),Electron Beam A CaseHistory,Radiat.Phys.Chem., Vol.35,Nos 4-6, pp 528-533.
6.NAZLY HILMY,(1990),Prospect of Commercialization of Food Irradiation in Indonesia.Proc.of The Workshops on The Utilization of Electron Beams, JAERI-M 90-194,JAERI,Japan, pp 129-136.
- 145 -
]AERI-M 93-160
LIST OF REFERENCES
l.COOK,P.M. (1990),Impact and Benefit of Radiation Technology,Radiat.Phys.Chem., Vol. 35,Nos 1-3, pp 7-8.
2.BRINSTON,R.M.(l990),Future Growth in the Gamma Sterilization of Disposable Medical Products,Radiat.Phys.Chem., Vo1.35,Nos 1-3, pp 390-392.
3.MORRISON,R.M.(l990),Economic of Food Irradiation Comparison Between Electron Accelerators and Co・60,Radiat.Phys.Chem.,Vo1.35 Nos 4・6,pp 673・679.
4.ISHIGAKI,I.(1990),Electron Beam Steri1ization of Medical Products,Proc.of The Workshops on The Utilization of Electron Beams,JAERI-M 90-194, JAERI,Japan,pp 102-108.
5.HENRY,G.TIMarHY,(l990),Electron Beam A Case History,Radiat.Phys.Chem., Vo1.35,Nos 4・6,pp 528-533.
6.NAZLY HILMY,(1990),Prospect of Commercialization of Food Irradiation in Indonesia,Proc.of The Workshops on The Utilization of El田 tronB回 ms,JAERI-M 90-194,JAERI,Japan, pp 129・136.
-145-
JAERI-M 93-160
Table 1 Characteristics of Radiation
TYPE OF RADIATION CHARACTERISTICS Electron Beam (e-particle)
- Electrical Generation - Ease of Control - High Power & High Dose Rate - Quick Processing - Low Penetration
X-ray (electro magnetic) ray
- Electrical Generation - Ease of Control - High Power & High Dose Rate - Quick Processing - High Penetration
Gamma-rays (electro magnetic)ray
- High Penetration - Uniform Irradiation - Ease of Control
Table 2 Penetration of electron beam in several densities of packaged food and bulk
Energy of EBM
Density
5 MeV 10 MeV Energy of EBM
Density One side (bulk)
Two sides (packaged)
One side (bulk)
Two sides (packaged)
0,4 (spices)
0,8 (grains)
4.45 cm
2.28 cm
9.83 cm
4.91 cm
9.20 cm
4.60 cm
20.73 cm
10.17 cm
- 146 -
JAERI-M 93-160
Table 1 Characteristics of Radiation
TYPE OF RADIAT工ON CHARACTERIST工CS
Elec七ronBeam -Electrical Generation (e-particle) -Ease of Con七rol
-High Power & High Dose Ra七e-Quick Processing -Low Penetration
X四 ray -Elec七ricalGenera七ion(electro magne七ic) ray -Ease of Control
-High Power & High Dose Ra七e-Quick processing -High Penetration
Table 2 Penetration of electron beam in several densities of packaged food and bulk
Energy of 5 MeV 10 MeV EBM
One side Two sides One side Two sides Densi七y (bulk) (packaged) (bulk) (packaged)
0,4 4.45 cm 9.83 cm 9.20 cm 20.73 cm (spices)
0,8 2.28 cm 4.91 cm 4.60 cm 10.17 cm (grains)
146 -
JAERI-M 93-160
MARKET SHARE BY STERILIZATION METHOD
EIO 553
EIO 70S
E-b«om J.
Comma 27%
1988 1993
F i g . 1 Market s h a r e of ETO, Gamma-ray and E-beam, fo r s t e r i l i z a t i o n of med ica l p r o d u c t s (2)
- 147 -
jAERI-M 93-160
MARIくETSHARE 8Y STERILlZATION METHOD
[10 55:':
EIO 70%
E-b・om
Comrno ‘ Z~
1988 199.3
Ulh... 1):' E-t,e..'"
Fig. 1 Market share of ETO, Gamma-ray and E-beam, for sterilization of medical products (2)
- 147一
JAERI-M 93-160
FUTURE GROWTH DISPOSABLE MEDICAL PRODUCTS
700
600
500
400 -
300
200 -
100
1980 1984 1988 1992 1996 2000
ESS EIO Comma I •' I E-beam HH l Other
millions of cubic feet
Fig. 2 Future growth of appl ica t ion of E-beam, ETO, and Gamma-rays for s t e r i l i z a t i o n of medical item (2)
- 148 -
]AERI-孔193-160
FUTURE GROWTH DISPOSABLE MEDICAL PRODUCTS
700
600
Z 府
側邸側悶悶
悶州側[欄
500 --1
400→
員同間同阿国民単2
隣蜘醐醐…目
酬問問間関ー
同悶困問同回同悶H悶阿平
z
ョ鵬醐一醐一
J )1
O 1980
300 --1
100 -'
200 -.
露麹 Other仁ヨ E-beom国盟国 Gommom!I EtO
millions of cubic feet
Future growth of application of E-beam, ETO, and Gamma-rays for sterilization of medical item (2)
-148-
2 Fig.
JAERI-M 93-160
IOT I
a o • H •P <s u •p <u a <v &
o Cn C
•H in (!) 0) O a) D
7«
#
3 J
-, >oo
1 MeV Gamma.
i 1 MeV" E l e c t r o n
7*
SO
15"
o o.5 2,5 5 IS Water (cm)
ID 11,5"
F i g . 3 P e n e t r a t i o n of e l e c t r o n beam i n wa te r compared t o Gamma-rays
- 149 -
]AERI -M 93-160
tDD
lMeV
~ 1$' I
j mll←叩 ωrol'¥f;
-u口H 、何回rω d
白Uω 21十 E
o O.S l,S s 7.f Water (cm)
G Q. 1"1'¥ "'" Q.
.0
Fig. 3 Penetration of electron beam in water compared to Gamma-rays
- ::'49ー
ー。。
115'
15'0
115"
11.,5"
JAERI-M 93-160
TWO-SIDED IRRADIATION 10 MeV ELECTRONS IN WATER
3 U 5
DEPTH (cm)
Fig. 4 Penetration of 10 MeV electron beam in water
- 150 -
]AERI-M 93-160
TWO-SIDED IRRADIA TION
10 MeV ELECTRONS IN WATER
e-ー-
1.43 2.12
門AX/門IN
GAIN
--e
7
6
4
5
3
2
凶ωOD
凶〉一ト《」凶
α
8 7 6 5
DEPTH (cm)
ら3 2 。
Penetration of 10 MeV electron beam in water
- 150一
Fig. 4
JAERI-M 93-160
100 ~l I 1 —
5 MeV BREM. (Z = 74) WATER
o Q
>
< U_J
cr
10
10 20 30 DEPTH (cm)
40
Fig. 5 Penetration of X-rays (5 MeV Brem) in water
- 151 -
JAERI-M 93-160
100
5MeV BREM. (Z = 74) WATER
y---ー
/ /
/
民
J
叩
一011~
W
¥
T
¥
y
¥
一
¥
10
UωO口
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。 40 30 20
DEPTH (cm) 10
Penetration of X-rays (5 MeV Brem) in water
- 151 -
Fig. 5
JAERI-M 93-160
2.13. Application of Electron Accelerators to Bio-Resources T. Kume
Takasaki R a d i a t i o n Chemist ry Research E s t a b l i s h m e n t Japan Atomic Energy Research I n s t i t u t e
1 . I n t r o d u c t i o n
R a d i a t i o n p r o c e s s i n g on b i o l o g i c a l m a t e r i a l s h a s b e e n
deve loped and t h e commercial a p p l i c a t i o n i s s p e c i a l l y i n c r e a s i n g
i n t h e f i e l d of food i r r a d i a t i o n and s t e r i l i z a t i o n of m e d i c a l
s u p p l i e s . The r a d i a t i o n p r o c e s s i n g on b i o - r e s o u r c e s h a s b e e n
a p p l i e d f o r v a r i o u s p u r p o s e s , s u c h a s s p r o u t i n h i b i t i o n ,
d i s i n f e c t i o n of i n s e c t , d e c o n t a m i n a t i o n of m i c r o o r g a n i s m s ,
i n a c t i v a t i o n of v i r u s , enzymes and o t h e r b i o a c t i v e m a t e r i a l s , and
d e g r a d a t i o n of c e l l u l o s i c w a s t e s . The e f f e c t i v e d o s e s a r e v a r i e d
i n wide r ange of 0 .01 - 1000 kGy a c c o r d i n g t o t h e purpose (Tab le
1 ) .
Two t y p e s of r a d i a t i o n s o u r c e , y from Co-60 and e l e c t r o n
a c c e l e r a t o r , a r e commonly used f o r t h e r a d i a t i o n p r o c e s s i n g . The
r a d i a t i o n p r o c e s s i n g by EB c a n b e e x p e c t e d t o h a v e v a r i o u s
advan t ages a s shown i n Table 2 (h igh dose r a t e of 500,000 kGy/hr
c o m p a r e d t o 20 k G y / h r of y - r a y and p e n e t r a t i o n c o n t r o l by
changing ene rgy , 0 .2 - 50 mm i n w a t e r ) . R a d i a t i o n p r o c e s s i n g of
b i o - r e s o u r c e s i n t h e fo l lowing c a s e s can be performed e f f e c t i v e l y
- 152-
]AERI-M 93-160
2.13. Application of Electron Accelerators to Bio-Resources
T.Kume
Takasaki Radiation Chemis七ryResearch Es七ablishmen七Japan Atomic Energy Research工ns七itu七e
1. In七roduction
Radia七ion processing on biological ma七erials has been
developed and七hecommercial applica七ionis specially increasing
in 七he field of food irradia七ionand s七erilizationof medical
supplies. The radia七ionprocessing on bio-resources has been
applied for various purposes, such as sprout inhibition,
disinfection of insec七, decontamination of microorganisms,
inactiva七ionof virus, enzymes and other bioactive materials, and
degradation of cellulosic was七es. The effective doses are varied
in wide range of 0.01 -工000kGy according to the purpose (Table
1) .
Two 七ypes of radia七ion source, y from Co-60 and electron
accelera七or,are commonly used for the radia七ionprocessing. The
radia七ion processing by EB can be expected to have various
advan七ages as shown in Table 2 (high dose ra七e of 500,000 kGyjhr
compared 七o 20 kGyjhr of y-ray and pene七ra七ion control by
changing energy, 0.2 - 50 mm in wa七er). Radia七ionprocessing of
bio-resources in七hef0110wing cases can be performed effec七ively
152
JAERI-M 93-160
t o u t i l i z e t h e advan tages of EB t r e a t m e n t .
2. Faster Processing Faster processing is required for the irradiation of frozen
samples. EB processing avoids a long time exposure which causes the melting of samples. At SPI (Societe de Proteines Industrielles) in France (1), packed frozen boneless poultry meat (5.5 x 55 x 36.5 cm) has been commercially processed using 7 MeV Linear accelerator. For the elimination of salmonella, the samples are irradiated within 1 sec for 5 kGy irradiation whereas the processing by y-ray needs 30 min - 1 hr (Table 3). The treatment cycle of frozen meat by EB with both sides irradiation takes about 10 minutes. The facility has been operated for several years.
3. High Dose Processing As the bioactive materials such as virus and enzymes are
generally radioresistant, high dose processing up to 1000 kGy is required for their inactivation. Figure 1 shows the inactivation curves of various bioactive materials. The activity decreased exponentially and the higher doses were necessary for the inactivation of small molecules according to the following empirical equation
D 3 7 = 6.4 x 10 4 / Mr where D37 is the dose (kGy) necessary to inactivate an activity
- 153 -
jAERI-M 93-160
to utilize the advantages of EB treatrnent.
2. Faster Processing
Faster processing is required for the irradiation of frozen
sarnples. EB processing avoids a long七imeexposure which causes
七he mel ting of sarnples. At SP工 (Societe de Proteines
工ndus七rielles) in France (1), packed frozen boneless poultry rnea七
(5.5 x 55 x 36.5 crn) has been comrnercially processed using 7 MeV
Linear accelera七or. For 七he elirnina七ion of sa工rnonella,七he
samples are irradiated within 1 sec for 5 kGy irradia七ionwhereas
七he processing by y-ray needs 30 rnin - 1 hr (Table 3). The
trea七rnen七 cyc1eof frozen meat by EB with both sides irradia七ion
七akes abou七 10 minutes. The facility has been opera七ed for
several years.
3. High Oose Processing
As 七he bioactive rna七erials such as virus and enzymes are
genera11y radioresis七ant,high dose processing up to 1000 kGy is
curves of various bioac七ive ma七erials. The ac七ivity decreased
exponen七ially and 七he higher doses were necessary for the
inactivation of smal1 molecules according to the fo工lowing
empirical equa七ion
037 6.4 x 104 / Mr
where 037 is七hedose (kGy) necessary七o inactivate an activity
。JE-u
-eEe
JAERI-M 93-160
to 37% of its initial level, and Mr is the molecular size (2). As shown in Fig. 2, the molecular weight of ovomucoid is 28,000 but the D37 dose for inactivation is 627 kGy because ovomucoid consists of three domains with small molecular size (Mr = 10,200). This result shows that the long time irradiation of 50 - 100 hr is necessary for the inactivation of ovomucoid by Y - r ay with the dose rate of 10 - 20 kGy /hr whereas it can be inactivated within a few minutes by EB irradiation with high dose rate.
4. Large Scale Processing A huge amount of agro-resources such as cellulose, starches
are discarded or under-utilized. We have been studying the radiation processing on upgrading of these wastes into useful end-products not only to recycle the bio-resources but also to reduce pollution. Empty fruit bunch (EFB) and palm press fiber (PPF) are major cellulosic wastes of the palm oil industry. The current availability of EFB and PPF in Malaysia is estimated to be 3 million tones (dry weight bases) per year, respectively (Table 4). Animal feeds and mushrooms can be produced from oil palm cellulosic wastes by radiation and fermentation treatment. The process is as follows: decontamination of microorganisms in fermentation media of EFB by radiation, inoculation of useful fungi, and subsequently production of proteins and edible mushrooms. Table 5 shows the throughput capasity of EFB by EB and Y-ray. Maximum throughput capasity with 6 0Co (3.0 MCi) Y - r aY
— 154 —
]AERI -M 93-160
七o 37% of i七s ini七ial level, and Mr is 七hemolecular size (2).
As shown in Fig. 2, the molecular weight of ovomucoid is 28,000
bu七七heD37 dose for inactivation is 627 kGy because ovomucoid
consis七s of three domains with sma11 mo1ecular size (Mr
10,200). This result shows that the long七imeirradiation of 50
- 100 hr is necessary for the inactivation of ovomucoid by y-ray
wi七h the dose ra七e of 10 - 20 kGy /hr whereas it can be
inac七ivatedwithin a few minutes by EB irradiation with high dose
ra七e.
4. Large Scale Processing
A huge amount of agro-resources such as ce11u10se, starches
are discarded or under-u七i1ized. We have been s七udying the
radiation processing on upgrading of these wastes into usefu1
end-produc七s not on1y to recyc1e the bio-resources but a1so to
reauce pollution. Empty frui七 bunch (EFB) and palm press fiber
(PPF) are major ce11u1osic was七esof the pa1m oi1 industry. The
current availability of EFB and PPF in Malaysia is estimated to
be 3 million tones (dry weight bases) per year, respectively
(Table 4). Animal feeds and mushrooms can be produced from oil
palm cellulosic wastes by radiation and fermentation treatment.
The process is as follows: decontamination of microorganisms in
fermen七ationmedia of EFB by radia七ion, inoculation of useful
fungi, and subsequen七ly production of pro七eins and edib1e
mushrooms. Table 5 shows 七hethroughput capasity of EFB by EB
and y-ray. Maximum throughput capasity with 60Co (3.0 MCi) y-ray
-i54-
JAERI-M 93-160
is estimated as 6000 ton/year whtreas the thrhoughput capasity
with EB (3MeV, 25mA) is 100,000 ton/year. The estimation
suggests that EB irradiation is easier and cheeper to process
such a large amount of EFB as 100 thousand - 3 million ton/year.
5. Surface Disinfection EB with low energy can be utilized for disinfection of mold
on the surface of fruits. Organoleptic properties of mandarin orange was significantly changed by y _ r a y Du"fc "the hedonic score was not decrease by EB (Table 6). When the mandarin oranges were irradiated by EB of 0.2 - 1.5 MeV, 0.5 MeV was the best to prevent the spoilage. When the oranges were stored at 3°C for 3 months followed by storage at room temperature (16 - 25°C) for one week, fungal growth was effectively inhibited by irradiation of 5 kGy (Table 7 ) . However, if the oranges were irradiated by EB energy of more than 0.5 MeV, their browning of skin and rotting were increased.
For the engineering study of EB on the surface of mandarin orange, a conveyor system was installed (Fig. 3 ) . The dose uniformity ratio of overall samples at 0.5 MeV EB was best when the slope of the side of the sample pallet was 18° (Fig. 4) and the overall dose uniformity was less than 2.0 (Fig. 5).
6. Conclusion
Electron beam irradiation has various advantages for the
- 155 -
]AERI-M 93-160
is es七ima七ed as 6000 ton/year whc~eas 七he 七hrhoughpu七 capasi七Y
wi七h EB (3MeV, 25mA) is 100,000 七on/year. The es七imation
suggests tha七 EB irradia七ionis easier and cheeper to process
such a 1arge amount of EFB as 100七housand-3 mi11ion七on/year.
5. Surface Disinfection
EB with 10w energy can be u七i1ized for disinfec七ionof mo1d
on 七he surface of fruits. Organo1ep七ic proper七ies of mandarin
orange was significan七1ychanged by y-ray bu七 七hehedonic score
was no七 decreaseby EB (Tab1e 6). When七hemandarin oranges were
irradia七ed by EB of 0.2 - 1.5 MeV, 0.5 MeV was 七he bes七七o
prevent the spoi1age. When七heoranges were s七oreda七 30C for 3
mon七hs followed by s七orage a七 room 七emperature (16 - 250C) for
one week, fungal grow七h was effec七ive1y inhibited by irradia七ion
of 5 kGy (Table 7). However, if七heoranges were irradia七edby
EB energy of more 七han 0.5 MeV, their browning of skin and
ro七七ingwere increased.
For七heengineering study of EB on七hesurface of mandarin
orange, a conveyor system was insta11ed (Fig. 3). The dose
uniformi七y ra七ioof overa11 samp1es a七 0.5MeV EB was bes七 when
七heslope of七heside of七hesamp1e pal工etwas 180 (Fig. 4) and
七heovera11 dose uniformi七ywas 1ess than 2.0 (Fig. 5).
6. Conc1usion
E1ec七ronbeam irradia七ionhas various advantages for the
F同日w
pb
唱・A
JAERI-M 93-160
treatments of bio-resources specially in following cases; 1) Faster processing for the elimination of salmonella
(5 kGy) in frozen poultry meet EB: less than 1 second (5.5 x 55 x 36.5 cm, 10 kg) Y : 30 min - 1 hr (cooling system is necessary)
2) High dose processing ( - 1000 kGy) for the inactivation of bioactive materials
EB: within a few minutes y : 50 - 100 hr
3) Large scale processing for a huge amount of agricultural wastes such as EFB
3. T. Kume, H. Ito, I. Ishigaki, M. LebaiJuri, Z. Othman, F. Ali, H. H. Mutaat, M. R. Awang and A- S. Hashim: Effect of Gamma Irradiation on Microorganisms and Components in Empty Fruit Bunch and Palm Press Fiber of Oil Palm Wastes, J. Sci. Food
Agrlc, 52, 147 (1990).
4. M. R. Awang, H. H. Mutaat, R. M. Deres and T. Kume: Scale-up Fermentation of Oil Palm Empty Fruit Bunch to Produce Ruminant Feed by Radiation Processing, Proceedings of the International
Conference on Evolution of Beam Applications, Takasaki, Japan,
Nov. 1991, p.501.
5. H. Tachibana, H. Watanabe and S. Aoki: Dosimetry for Electron-Beam Irradiation on Citrus "Unshiu", Food Irrad. Japan, 13, 30 (1978).
- 157 -
]AERI-M 93ー 160
3. T. Kume, H. 工七0,工. 工shigaki,M. LebaiJuri, Z. Othman, F. Ali,
H. H. Mu七aat,M. R. Awang and A. S. Hashim: Effect of Gamma
工rradiationon Microorganisms and Componen七s in Empty Frui七
Bunch and palm Press Fiber of Oil Palm Wastes, J. Sci. Food
Agric., 52, 147 (1990).
4. M. R. Awang, H. H. Mu七aa七, R. M. Deres and T. Kume: Scale-up
Fermen七a七ionof Oi1 Palm Empty Fruit Bunch to Produce Ruminant
Feed by Radia七ionProcessing, proceedings of the International
Conference on Evolution of Beam Applications, Takasaki, Japan,
Nov. 1991, p.501.
5. H. Tachibana, H. Watanabe and S. Aoki: Dosimetry for Electron-
Sprou t i n h i b i t i o n D i s i n f e s t a t i o n of i n s e c t Decontaminat ion of microorganisms I n a c t i v a t i o n of v i r u s I n a c t i v a t i o n of enzymes Degrada t i on of c e l l u l o s i c was tes
0.01 - 0.1 0.1 - 1 1 - 30
10 - 500 50 - 1000
100 - 1000
Table 2 Advantages of rad ia t ion processing by e lectron beam to bio-resources
High dose r a t e s : 50 - 500,000 kGy/hr (Y : - 20 kGy/hr)
* Faster processing * High dose processing * Large scale processing
Penetration control: 0.2 - 50 mm in water * Surface disinfection
- 158 -
]AERI-M 93-160
Tab1e 1 Effective doses for bio-resources
Sprou七 inhibition
Disinfes七ationof insec七
Decon七aminationof microorganisms
工nactivationof virus
工nac七iva七ionof enzymes
Degradation of ce11u1osic wastes
Dose (kGy)
0.01 - 0.1
0.1 1
1 30
10 500
50 - 1000
100 - 1000
Tab1e 2 Advantages of radiation processing by e1ectron bearn to bio-resources
High dose ra七es: 50 - 500,000 kGyjhr
(y - 20 kGyjhr)
* Faster processing 合 Highdose processing
* Large sca1e processing Pene七ra七ioncontro1: 0.2 - 50 mm in water
骨 Surfacedisinfec七ion
-158-
JAERI-M 93-160
Table 3 I r r ad i a t i on conditions of frozen poultry meats by e lec t ron beam a t SPI (France)
A c c e l e r a t o r : Linac Energy: 7 MeV Power: 5 kW
Purpose: Decontamination of Salmonella Dose: 5 kGy
Conditions Sample size: 5.5(thick) x 55 x 36.5 cm Operation: 14 hr/day (2 shift) Production: 2,000 ton/year (Throughput: 5 packs/min)
Table 4 Oil palm production in Malaysia
Year Cultivated area Crude oil PPF* EFB** (x lOOOha) (x lOOOt) (x lOOOt) (x lOOOt)
Appearance and hardness were tested on peel of fruits, and odor and taste were judged as changes in flesh of fruits. Samples were judged by nineteen persons. a) The samples were irradiated with a surface dose of 1.5 kGy by
1.0 MeV electrons. * Significance from unirradiated fruits by 95% of probability. ** Significance from unirradiated fruits by 99% of probability.
- 160 -
JAERI-M 93-160
Tab1e 5 Irradiation of EFB by e1ectron beam and y-ray
EB (3 MeV)
60
Curren七 (mA)
Power (kW)
Throughpu七
Co y-ray
Ac七ivity (MCi)
Throughpu七 (ton)
Operation: 6,000 hrjyear
1
3
4,000
0.05
100
2.6
7.8
10,000
0.5
1,000
EFB package size: 16 x 53 x 43 cm, y=0.16 g/cm3
Moisture conten七 ofEFB: 60%.
25
75
100,000
3.0
6,000
Tab1e 6 Effect of y or e1ectron irradiation on organo1eptic properties of Citrus unshiu tested immediate1y after irradiation
Appearance and hardness were七es七edon pee1 of frui七s,and odor and taste were judged as changes in flesh of frui七s. Samples were judged by nine七eenpersons. a) The samples were irradia七edwith a surface dose of 1.5 kGy by
1.0 MeV elec七rons.大 Significancefrom unirradia七edfruits by 95告 ofprobabili七y.** Significance from unirradia七edfruits by 99号 ofprobabili七Y・
-160
JAERI-M 93-160
Table 7 Effect of e lec t ron energies on browning and r o t t i n g of f r u i t s Citrus unshiu s tored at room temperature (16 - 25°C) a f te r storage a t 3°C for 3 months
Percen t of browned and r o t t e d f r u i t s
Energy(MeV) T o t a l number S t o r a g e t ime (days) (Mev) of sample 3 7
browned r o t t e d browned r o t t e d
U n i r r a d i a t e d 40 3 20 5 48 0 .2 40 3 35 13 60 0 . 5 20 0 0 5 5 0 . 9 20 0 20 5 40 1 .5 20 5 25 15 55
- 161 -
jAERI -M 93-160
τable 7 Effect of electron energies on browning and rotting of fruits Citrus unshiu stored at room temperature (16 -2S
0C) after
storage at 30C for 3 months
Percen七 of browned and ro七七edfruits
Energy(MeV) To七al number Storage七ime (days) (Mev) of samp1e 3 7
browned ro七七ed browned ro七七ed
Unirradiated 40 3 20 5 48
0.2 40 3 35 13 60
0.5 20 O O 5 5
0.9 20 O 20 5 40
1.5 20 5 25 15 55
-161一
JAERI-M 93-160
1001 ,o
> S <
10
Ovomucoid Mr= 10,200
D
Pepsin Mr = 35,000
ADH Mr =164,000
•
100 200 300 400 500
Dose (kGy)
Fig. 1 Inactivation of bioactive materials by irradiation
Domain 2
Domain 1
Fig. 2 Structure of ovomucoid MW = 28,000 Mr(active domain 2) = 10,200 D 3 7 = 627 kGy
- 162 -
JAERIー乱if93-160
100
ADH Mr = 164.000
AW)去一〉一5《
10 o 100 200 300 400 500
Dose (kGy)
Fig. 1 Inactivation of bioactive materials by irradiation
Fixation of dosimeter X : scanning direction Y -.conveying direction
WOMO
Position of model surface
Pallet Side pallet o°
180°
Fig. 3 Geometry of irradiation apparatus and model samples
5 10 15 Slope of side pallet (degree)
Fig. 4 Surface dose uniformity on one side irradiation at various positions
- 163 -
Fig. 3
qJV
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ω
JAERI-M 93-160
Position of model surtace
噛 9ぴ
180・
Geometry of irradiation apparatus and model samples
5
、、、、
在、、、、、
、、南町、
H
、
a
崎、.
門
u
、、、、、
、
4
NO.1
10 15 20 O 5 Slope of side pal¥et (degree)
Fig. 4 Surface dose uniformity on one side irradiation at various positions
-163 -
JAERI-M 93-160
100r
I 50 01 o Q
0 180
\>J Energy: 500 keV, Slope of side pallet: 18°
90 0
/ / No. 3/
-No. 2
No. 4
-90 Position of surface (degree)
180
Fig. 5 Surface dose distribution on both side irradiation at various positions
- 164 -
JAERI-M 93-160
100
(hov
一)O凶00
Energy: 500 keV,
Slope of side pallet: 18。
180 O 100 -90
Position of surface (degree)
O 90
Surface dose distribution on both side irradiation at various positions
-164-
Fig. 5
JAERI-M 93-160
3. CLOSiNG
1(14
jP.ERI-M 93-160
3. CLOSING
ーヴ必
JAERI-M 93-160
3.1. Closing Remarks with Summary of the Workshop
Suchat Mongkolphantha
Secretary-General, OAEP
Dr. Sato, Mr. Takahashi, Honored Guests Ladies and Gentlemen,
The importance of electron accelerator utilization to the development of our countries and people hardly need emphasizing. I am very much pleased that the need to promote this technology has been acknowledged. And I trust that with this in mind, participation of experts, scientists and decision-makers from various government and private sectors will help satisfy the potential demands more effectively.
Although it is well aware that for their great advantages and effectiveness, electron accelerators have been widely accepted and utilized all over the world, the uses are still limited to only in the developed countries. It is in this light that we welcome the various initiatives to promote the transfer of this technology to the developing countries, such as Thailand.
- 167 -
JAERI -M 93-160
3.1. Closing Remarks with Summary ofthe "~"/orkshop
Dr. Sa七0,
Mr. Takahashi,
Honored Guests
Ladies and Gent1emen,
Suchat Mongkolphantha
Secre七ary-General,OAEP
The importance of e1ec七ronaccelera七oru七i1iza七ionto the
deve10pmen七 ofour coun七ries and peop1e hardly need ernphasizing.
1 am very much p1eased七hat七heneed to promo七e this technology
has been acknow1edged. And 1 trust that wi七h this in mind,
par七icipationof exper七s,scientis七s and decision-makers from
various government and private sec七ors wi11 he1p satisfy the
and effectiveness, e1ectron accelera七ors have been widely
accepted and uti1ized a11 over 七hewor1d,七he uses are sti11
1imited七oonly in the deve工opedcoun七ries. 工t is in this 1igh七
七hatwe we1come七hevarious initiatives to prorno七e the transfer
of this techn010gy to the developing countries, such as Thailand.
-167一
JAERI-M 93-160
My G o v e r n m e n t i s h o n o r e d a n d p l e a s e d t o h o s t t h i s w o r k s h o p
i n B a n g k o k . I b e l i e v e t h a t t h i s o p p o r t u n i t y p r o v i d e d a w e a l t h
o f e x p e r i e n c e a n d k n o w l e d g e f r o m w h i c h a l l o f u s c a n s h a r e .
W i t h m o s t s h a r i n g s i m i l a r p r o b l e m s a n d c o n s t r a i n t s , o n e c o u n t r y
c a n l e a r n f rom t h e e x p e r i e n c e s o f t h e o t h e r . T h i s w i l l h e l p
e a c h i n t h e s e a r c h f o r a p p r o p r i a t e way and means t o d e a l w i t h i t s
own i n t e r n a l s i t u a t i o n and r e q u i r e m e n t s .
I am, t h e r e f o r e , s u b m i t t i n g t h a t we m u s t c o n s t a n t l y p r o m o t e
a n d d e v e l o p t e c h n i c a l c o o p e r a t i o n b e t w e e n o u r c o u n t r i e s . I n
p a r t i c u l a r , we m u s t a im a t d o i n g t h e u t m o s t t o t a k e a d v a n t a g e s o f
e l e c t r o n a c c e l e r a t o r s . I n t h i s r e g a r d , we h o p e t h a t t h e
G o v e r n m e n t o f J a p a n w i l l b e a b l e t o a s s i s t T h a i l a n d i n h e r
i n d u s t r i a l i z a t i o n e f f o r t s b y a p p l y i n g t h i s h i g h e n e r g y t e c h n i q u e .
A t t h i s o p p o r t u n e m o m e n t , o n b e h a l f o f t h e R o y a l T h a i
G o v e r n m e n t , I w i s h t o e x p r e s s o u r d e e p a p p r e c i a t i o n t o t h e
G o v e r n m e n t of J a p a n , JAERI a n d J A I F f o r t h e i r k i n d c o n t r i b u t i o n
a n d e x c e l l e n t c o o p e r a t i o n e x t e n d e d t o o u r c o u n t r y a n d t o b e
e x t e n d e d i n t h e f u t u r e . And I would l i k e t o a s s u r e t h e m o f o u r
f u l l a n d c o n t i n u e d s u p p o r t i n g e n e r a t i n g v e r y a c t i v e i n p u t s t o
p r o m o t e t h e f u l l e s t p o s s i b l e o p p o r t u n i t y f o r t h e t r a n s f e r o f
e l e c t r o n a c c e l e r a t o r t e c h n o l o g y e n s u r i n g t h e p r o s p e r i t y o f o u r
n a t i o n s and t h e r e g i o n a s a w h o l e .
Thank y o u .
- 168 -
JAERI-M 93-160
My Government is honored and p1eased七ohost this workshop
in Bangkok. 工 be1ieve七ha七 thisoppor七unityprovided a wea1th
of experience and know1edge from which a11 of us can share.
With most sharing similar problems and constraints, one country
can 1earn from七heexperiences of the other. This wi11 he1p
each in the search for appropriate way and means七odeal with i七s
own interna1 si七ua七ionand requirements.
工 am,七herefore, submitting that we must constant1y promote
and deve10p technica1 coopera七ionbetween our coun七ries. 工n
particular, we must aim at doing the utmos七七o take advantagE:¥S of
e1ec七ron accelera七ors. 工n this regard, we hope 七ha七 the
Government of Japan will be able to assist Thailand in her
indus七rializa七ionefforts by applying this high energy七echnique.
A七七his opportune moment, on behalf of the Royal Thai
Governmen七 1 wish七o express our deep appreciation to 七he
Governmen七 ofJapan, JAERI and JAIF for their kind contribu七ion
and exce11en七 coopera七ionextended 七o our country and to be
ex七endedin七hefuture. And 1 would like to assure七hemof our
fu11 and con七inued support in genera七ingvery active inpu七s to
promote the fulles七 possible oppor七uni七y for the transfer of
electron accelerator technology ensuring 七heprosperity of our
na七ionsand七heregion as a who1e.
Thank you.
-168-
JAERI-M 93-160
3.2. Closing Remarks with Summary of the Workshop
Nazly Hilmy
Director, CAIR, BATAN
Ladies and Gentlemen,
We have discussed several aspects on the application of EB
Accelerators in Industry. From the discussions, we would like
to conclude as follows:
1. EB Accelerators have been widely used in Japanese industries, particularly to produce different kinds of high quality polymer cross-linked product, such as wire & cable insulations, heat-shrinkable tubing and films, PE foam and the treatment of parts of radial rubber tire. The application of EH Accelerators in the field of sterilization of medical products, food irradiation and flue gas treatment are under explored.
2. The potential application of EB Accelerators in Indonesia seems to be great, particularly when the Indonesian industrial society intends to introduce Radiation Technology in their industrial line to produce high quality and high performance products which is needed to fulfill the requirement of technology development.
- 169 -
]AERI-M 93-160
3.2. Closing Remarks with Summary of the Workshop
Nazly Hilmy
Direc七or,CA工R,BATAN
Ladies and Gen七lemen,
We have discussed several aspects on the application of EB
Accelera七orsin Industry. From the discussions, we would like
七o conclude as fo工lows:
1. EB Acce1erators have been widely used in Japanese industries,
particu1ar1y to produce differen七 kindsof high quality po工ymer
cross-1inked product, such as wire & cable insulations, heat-
shrinkab1e tubing and fi1ms, PE foam and the t:rea七mentof parts
of radia1 rubber tire. The app1ication of EH Accelerators in
七he fie1d of steri1iza七ionof medica1 products, food irradiation
and flue gas trea七百lentare under explored.
2. The po七en七ia1 app1ication of EB Accelerators in 工ndonesia
seems to be great, par七icular1ywhen the 工ndonesian indus七rial
socie七y in七ends to introduce Radia七ion Technology in their
indus七rial 1ine to produce high quali七y and high performance
products which is needed to fu1fill七herequirement of techno1ogy
deve10pmen七.
-169 -
JAERI -M 93-160
3. The present workshop is very useful to energize our idea to improve industrial capability in the production technology and also to invite our attention on a new production tool such as EB Accelerators.
4. BATAN is the only research institute who is doing a lot of
work on radiation processing in Indonesia, therefore BATAN is
ready to provide further information about the application of EB
Accelerators.
5. Bilateral cooperation between JAERI and BATAN is expected to maintain exchange information system, especially in the field of Radiation Technology such as the application of EB Accelerators by seminar, workshop and scientist exchange program.
Thank you to you all and on behalf of Organizing Committee I would like to express my gratitude to JAERI and JAIF for the nice cooperation and to all of participants for their attention. I hope such kind of workshop can be carried out regularly for every two years.
Thank you.
- 170 -
JAERI -M 93-160
3. The present workshop is very useful to energize our idea 七o
improve industrial capabili七y in七heproduction technology and
also to invi七eour a七七entionon a new produc七iontool such as EB
Accelera七ors.
4. BATAN is the only research institute who is doing a lot of
work on radia七ionprocessing in Indonesia, therefore BATAN is
ready七o provide further informa七ionabout七heapplication of EB
Accelerators.
5. Bilateral cooperation be七weenJAERI and BATAN is expected to
main七ainexchange information sys七em,especially in七he field of
Radiation Technology such as the applica七ionof EB Accelerators
by seminar, workshop and scientist exchange program.
Thank you to you all and on behalf of Organizing Committee I
would like七oexpress my gratitude to JAERI and JAIF for the nice
cooperation and 七o a工工 of par七icipants for their attention. I
hope such kind of workshop can be carried ou七 regularlyfor every
two years.
Thank you.
- 170 -
JAERI-M 93-160
SUPPLEMENT
{(11
]AERI-M 93-160
SUPPLEMENT
JAERI-M 93-160
S u p p l e m e n t 1 . A g e n d a ( 1 )
OAEP/JAERI/JAIF WORKSHOP ON INDUSTRIAL UTILIZATION
OF ELECTRON ACCELERATORS
9 July 1992 at Central Plaza Hotel. Bangkok, THAILAND
Opening Seession
9:40 Welcome Remarks by Mr. Suchat Mongkolphantha (Secretary-General, OAEP)
9:50 Opening Adress by Dr. S. Sato (Director General, TRCRE, JAERI)
10:00 Speech by Dr. Y. Sasaki (Advisor, Yazaki Co., JAIF Representive)
10:30 Coffee break
Session 1 Chairpersons: Mr. A. Kuroyanagi (Nisshin)
Dr. S. Chonkum (OAEP)
10:30 - 11:15 General View of Electron Accelerator Utilization Dr. S. Sato (JAERI)
11:15 - 12:00 Introduction to Industrial Electron Acceleratrors Mr. M. Suzuki (NHV)
12:00 - 13:30 Lunch
9:30 -
9:40 -
9:50 -
10:00 -
- 173 -
JAERI-M 93-160
Supp1ement 1. Agenda. ( 1 )
OAEP/JAERI/JAIF
WORKSHOP ON INDUSTRIAL UTILIZATION
OF ELECfRON ACCELERATORS
9 July 1992
at Centra1 P1aza Ho七e1. Bangkok, THA工LAND
Opening Seession
9:30 - 9:40 Welcorne Rernarks by
Mr. Suchat Mongkolphantha
(Secretary-General, OAEP)
9:40 - 9:50 Opening Adress by
Dr. S. Sato
(Director General, TRCRE, JAERI)
9:50 -10:00 Speech by
Dr. Y. Sasaki
(Advisor, Yazaki Co., JAIF Representive)
10:00 - 10:30 Coffee break
Session 1
Chairpersons: Mr. A. Kuroyanagi (Nisshin)
Dr. S. Chonkum (OAEP)
10:30 - 11:15 General View of Electron Accelerator U七iliza七ion
Dr. S. Sato (JAERI)
11:15 - 12:00 Introduc七ion七o Industrial Electron Accelera七rors
Mr. M. Suzuki (NHV)
12:00 - 13:30 Lunch
-173 -
JAERI-M 93-160
S e s s i o n 2 Chairpersons: Dr. Y. Sasaki (Yazaki)
Mr. T. Na Chieng Mai (STR GROUP)
13:30 - 14:00 Economical Aspects of Industrial Electron Accelerators
Mr. T. Doi (NKK) 14:00 - 14:30 Polymer Processing with Electron Accelerators
Dr. K. Makuuchi (JRERI) 14:30 - 15:00 Potential Application of Electron Accelerators in
Thailand Mr. C. Siri-upathum (Chulalongkorn Univ.)
15:00 - 15:30 Coffee break
Session 3 Chairpersons: Dr. S. Sato (JRERI)
Mr. S. P. Kasemsanta (Thai R.E.C. Commissioner)
15:30 - 16:00 Food Irradiation with Electron Accelerators Dr. C. Banditsing (OAEP)
16:00 - 16:30 EB Treatment of Wastewater and Sewage Sludge Dr. S. Hashimoto (JRERI)
16:30 - 17:00 Flue Gas Purification with Electron Accelerators Dr. W. Kawakami (JRERI)
17:00 - 17:15 Closing Remarks with Summary of the Workshop OREP
23. Mr. Ja】<rapopCharatsri N. S. Consu1七antCo., Ltd. 1131/318 20th F100r, Sahakorn B1dg., Terd Dumri Road, Nakornchaisri, Dusi七, Bangkok 10300
24. Mr. Jirawa七 KhengnukrohDry K1in and Wood Products Plant 146 Pracharach 1 Road, Dusit, Bangkok 10800
25. Mr. Kijja Chongkitivi七yaDivision of Radia七ionPro七ec七ionServices, Departmen七
-178 -
JAERI-M 93-160
of Medical Sciences, 693 Bamrungmuang Road, Mahanark, Pomprabsatrupai, Bangkok 10100
26. Mr. Kongsak Tatiyanukule Kongsak X-Ray Medical Industry Co., Ltd. 212/1 Soi Phaholyothin 55, Phahonyothin Road, Anusavaree, Bangkhen, Bangkok 10220
27. Mr. Korpong Sripawatakul Consultants of Technology Co., Ltd., 38-40 Soi Ladprao 130, Ladprao Road, Klongchan, Bangkapi, Bangkok 10240
28. Mr. Krisda Suchiva Faculty of Science, Mahidol University Rama VI Road, Phya Thai, Bangkok 10400
29. Ms. Kritsanaporn Tangkuptanon United Pharma Antibiotics Industries Co., Ltd. 101/52 Soi 5, Paholyothin Road, Klongneung, Klongluang, Pathun Thani 12120
30. FS.l La-Ong Maksri Technology Transfer Centre, Ministry of Science, Technology and Environment, Rama VI Road, Ratchathewi, Bangkok 10400
31. Ms. Mayuree Naovaratanophas Food Control Division, Food and Drug Administration 275 Samsen Road, Devaves Palace, Pranakorn, Bangkok 10200
35. Ms. Nualchavee Roongtanakiat Faculty of Sciences, Kasetsart University Pahol Yothin Road, Ladyoa, Bangkhen, Bangkok 10900
36. Ms. Nuanchan Terapat Department of Photographic Science and Printing Technology, Chulalongkorn University Phya Thai Road, Patumwan Road, Bangkok 10330
57. Mr. Sangchai Viriyaumpaiwong Siam Kraft Industry Co., Ltd. 19 Sang-Xuto Road, Tapah, Bang Pong, Ratchaburi 70110
58. Mr. Sangiam Pinprasurtsataya Kurusapa Business Organization 52 Ladprao Road, Bangkapi, Bangkok 10310
59. Mr. Siri Srimanoroth Division of Radiation Protection Services, Department of Medical Sciences, 693 Bamrungmuang Road, Mahanark, Pomprabsatrupai, Bangkok 10100
60. Ms. Sirinart Vasanavatana Technical Division, Food and Drug Administration 275 Samsen Road, Wat Sampraya, Pranakorn, Bangkok 10200
61. Ms. Siripan Eamroongroj Medical Device Control Div., Food and Drug Admnistation 275 Samsen Road, Wat Sampraya, Pranakorn, Bangkok 10200
57. Mr. Sangchai Viriyaumpaiwong Siam Kraft Industry Co., Ltd. 19 Sang-xu七oRoad, Tapah, Bang Pong, Ratchaburi 70110
58. Mr. Sangiam ~inprasurtsataya Kurusapa Business Organization 52 Ladprao Road, Bangkapi, Bangkok 10310
59. Mr. Siri Srimanoroth Division of Radiation Protec七ionServices, Depar七mentof Medical Sciences, 693 Bamrungmuang Road, Mahanark, Pomprabsatrupai, Bangkok 10100
60. Ms. Sirinart Vasanavatana Technical Division, Food and Drug Administration 275 Samsen Road, Wa七 Sampraya,Pranakorn, Bangkok 10200
61. Ms. Siripan Eamroongroj Medical Device Con七rolDiv., Food and Drug Admnistation 275 Samsen Road, Wat Sampraya, Pranakorn, Bangkok 10200
65. Mr. Sobhak P. Kasemsanta Thai AEC Commissioner, 1/498-1/499 Garden Home Village, Phahon Yothin Road, Km. 26, Bangkhen, Bangkok 12130
66. Mr. Somsak Chutanan General Electric International Operations Company, Inc. Unit 901, 9th Floor, Tower A, Diethelm Towers, at 9321 Wireless Road, Lumpinee, Patumwan, Bangkok 10300
67. Mr. Somsak Rapeepatana Safety and Environment Section, Electricity Generating Authority of Thailand 53 Charan Sanid Wong Road, Bang Kruay, Nonthaburi 11000
68. Mr. Sornsom Nawasalao Hiang Seng Fibre Container Co., Ltd. 110/4 Soi Wat Bang-pla, Setrakit Road, Ban-Koh, Muang, Samut Sakhon 74000
69. Ms. Sriutai Maorapong Industrial Development Division, Department of Industrial Promotion, Soi Trimitr, Rama IV Road, Kluaynamthai, Phra Khanong, Bangkok 10110
70. Ms. Suda Dilokphatanamongkol Drug Control Div., Food and Drug Administration, 275 Samsen Road, Wat Sampraya, Pranakorn, Bangkok 10200
71. Dr. Suda Kiatkamjornwong Faculty of Science, Chulalong University Phya Thai, Patumwan, Bangkok 10300
72. Ms. Sumalee Pornkitprasarn Medical Control Division, Food and Drug Administration 275 Samsen Road, Wat Sampraya, Pranakorn, Bangkok 10200
73. Mr. Supachai Phaiboon 74. Mr. Tawatchai Laprungsirat 75. Mr. Terdpong Prasertwigai
Environmental Development Section, ELlectricity Generaing Authority of Thailand 53 Charan Sanid Wong Road, Bang Kruai, Nonthaburi 11000
76. Mr. Surasak Suntipong Bangpoo Industrial Estate Office, Soi 1, Sukhumvit Road, Phraeksa, Muang, Samutprakarn 10280
77. Ms. Sutathip Promachotikool Forest Produts Research Division, Royal Forest Department 61 Phaholyothin Road, Ladyao, Bangkhen, Bangkok 10900
78. Mr. Thavitchai Saiyasombat Bangkok Cable Co., Ltd., 93 Soi Cable, Suksawad Road. Nai Klong Plakod, Prasamudjedee, Samut Prakan 10290
- 182-
JAERI-M 93-160
65. Mr. Sobhak P. Kasems己n七aThai AEC Commissioner, 1/498-1/499 Garden Home Vi11age, Phahon Yothin Road, Km. 26, Bangkhen, Bangkok 12130
67. Mr. Somsak Rapeepatana Safety and Environment Section, Electricity Generating Authori七y of Thai1and 53 Charan Sanid Wong Road, Bang Kruay, Nonthaburi 11000
68. Mr. Sornsom Nawasalao Hiang Seng Fibre Container Co., Ltd. 110/4 Soi Wat Bang-p1a, Setraki七 Road,Ban-Koh, Muang, Samut Sakhon 74000
69. Ms. Sriutai Maorapong 1ndustria1 Deve10pment Division, Department of Indus七ria1Promotion, Soi Trimitr, Rama IV Road, Kluaynamthai, Phra Khanong, Bangkok 10110
70. Ms. Suda Di10kpha七anamongko1Drug Control Div., Food and Drug Administration, 275 Samsen Road, Wat Sampraya, Pranakorn, Bangkok 10200
71. Dr. Suda Kiatkamjornwong Facu1ty of Science, Chulalong University Phya Thai, Patumwan, Bangkok 10300
72. Ms. Suma1ee Pornki七prasarnMedical Control Division, Food and Drug Administration 275 Samsen Road, Wa七 Sampraya,Pranakorn, Bangkok 10200
73. Mr. Supachai Phaiboon 74. Mr. Tawa七chaiLaprungsirat 75. Mr. Terdpong Praser七wigai
Environmental Development Section, ELlectricity Generaing Au七horityof Thailand 53 Charan Sanid Wong Road, Bang Kruai, Nonthaburi 11000
76. Mr. Surasak Sun七ipongBangpoo Industrial Estate Office, Soi 1, Sukhumvit Road, Phraeksa, Muang, Samutprakarn 10280
78. Mr. Thavi七chaiSaiyasombat Bangkok Cable Co., Ltd., 93 Soi Cable, Suksawad Road. Nai Klong P1akod, Prasamudjedee, Samut prakan 10290
-182 -
JAKRI-M 93 160
7 9 . Mr. Thaweesak Pramulwong BB Group Co., Ltd. 518/5 Maneeya Road, Patumwan, Bangkok 10330
80. Mr. Thipwan Tieocharoenkit Ladkrabang Industrial Estate Office, 94 Chalongkrung Road, Lamplatiew, Lat Krabang, Bangkok 10520
81. Mr. Trakulwattana Na Chieng Mai STA Group of Companies 2/3 Moo 14, Bangna Tower 9th Floor, Bangna-Trad (Km. 6.5), Bangkhaew, Bangplee, Samutprakarn 10540
83. Mr. Vichit Vaisayanunt Business Promotion Division, The Industrial Finance Corporation of Thailand 1770 New Petchburi Road, Huay Kwang, Bangkok 10310
85. Mr. Weera Chintongprasert Surabangyikhan II Factory, 82 Rasbumrung Road, Bangkoowad, Muang District, Pathumtani 12000
86. Mr. Wiboonkiet Moleeratanond Research, development and Engineering Center, Premier Global Co., Ltd., 1 Soi Premier, Srinakarin Road, Nongbon, Prawet, Bangkok 10260
87. Ms. Wimonwan Witayapiboon Medical Device Control Div., Food and Drug Administration 275 Samsen Road, Wat Sampraya, Pranakorn, Bangkok 10200
91. Mr. Anan Yuthamanop 92. Mr. Apichai Chvajarernpun 93. Ms. Archara Sangariyavanich
- 183 -
JAEI~I ~ ¥1 93--160
79. Mr. Thaweesak Pramuh-.1ong BB Group Co., Ltd. 518/5 Maneeya Road, Patumwan, Bangkok 10330
80. Mr. Thipwan Tieocharoenkit Ladkrabang Industria1 Estate Office, 94 Cha10ngkrung Road, Lamp1atiew, Lat Krabang, Bangkok 10520
81. Mr. Traku1wattana Na Chieng Mai STA Group of Companies 2/3 Moo 14, Bangna Tower 9th F1oor, Bangna-Trad (Km. 6.5), Bangkhaew, Bangp1ee, Samutprakarn 10540
91. Mr. Anan Yu七harnanop92. Mr. Apichai Chvajarernpun 93. Ms. Archara Sangariyavanich
-183
JAKRI-M 93-160
94. Mr. Chanchai Asvavijnijkulchai 95. Mr. Chouvana Rodthongkora 96. Mr. Manon Sutantawong 97. Mr. Pariwat Siangsanan 98. Ms. Pornsri Polphong 99. Ms. Saranya Piadang
100. Mr. Sirichai Keinmeesuke 101. Ms. Siriratana Biramorvtri 102. Mr. Sumran Songprasertchai 103. Ms. Sunanta Patrashakorn 104. Mr. Surachai Pongj arernsuk 105. Mr. Surapong Pimjun 106. Ms. Swimol Kaewpila 107. Mr. Udorn Youngchuy 108. Ms. Vachira Pringsulaka 109. Mr. Vichian Vongsmarn 110. Ms. Valailak Phadvibulya 111. Mr. Wanchai Dharmvanij 112. Ms. Warapon Wanitsuksombut 113. Ms. Yureeporn Panyatipsakul
- 184 -
JAERI-如I93-160
94. Mr. Chanchai Asvavijnijkulchai 95. Mr. Chouvana Rodthongkom 96. Mr. Manon Sutantawong 97. Mr. Pariwat Siangsanan 98. Ms. Pornsri Polphong 99. Ms. Saranya Piadang
100. Mr. Sirichai Keinmeesuke 101. Ms. Siriratana Biramontri 102. Mr. Sumran Songprasertchai 103. Ms. Sunanta Patrashakorn 104. Mr. Surachai pongjarernsuk 105. Mr. Surapong Pimjun 106. Ms. Swimol Kaewpila 107. Mr. Udorn Youngchuy 108. Ms. Vachira Pringsulaka 109. Mr. Vichian Vongsmarn 110. Ms. Valailak Phadvibulya 111. Mr. Wanchai Dharmvanij 112. Ms. Warapon Wanitsuksombut 113. Ms. Yureeporn panya七ipsaku1
-184-
JAERI-M 93-160
BATAN/JAERI/JAIF SECOND WORKSHOP
(1) Participants from Company
1. Mr. Alex B. Sumatrie 2. Mr. Sigit Sudarminto 3. Mr. Sastra Viqaya
PT. BIMACOM PERDANA RUBBER INDUSTRY, Wisma BCA 6th Floor Jl. Jend. Sudirman Kav. 22-23, Jakarta 122970
4. Mr. Haris Siswantoro PT. CYPRESS PLASTIC Ind. Ancol Barat III No.2 Jakarta 14430
5. Mr. Harry Tanugraha PT. YAKINDO Jl. Cideng Barat No. 49, Jakarta 10150
6. Ms. Galiah Seno Sastro PT. SKIGA ANANTA DHARMA, Jl. Pulo Gadung Kav. 11/11 Kawasan Industri Pulo Gadung, Jakarta Timur
7. Mr. Rusdy Harmayn 8. Mr. Mas Agoes Soeparto
PT. DIAN INDAH REKSA WOOD INDUSTRY Jl. Sutan Syahrir lc, 3-4, Jakarta 10350
9. Mr. Indrotomo Upoyo PT. SURYO INDO UPOYO Jl. Kramat VI/40, Jakarta 10430
10. Mr. Dody Budiaraan PT. ELWAN SEJATI Jl. Raya Bekasi Km 14.9, Jakarta Timur
11. Mr. Satria PT. FOODTECH UTAMA Jl. Ancol I No. 4-5, Ancol Barat, Jakarta 13430
12. Ms. Rosali Setiawan 13. Ms. Eviazizah 14. Mr. M. Soleh
PT. RISTRA INDOLAB Jl. Rajawali Selatan E5-6, Jakarta Pusat
15. Mr. D. Gustam 16. Mr. Tri Djoko
PT. INDOGAMA STERILIZATION/ PT. PERKASA STERILINDO Jl. KH. Hasyim Ashari 11A, Jakarta Pusat
17. Mr. Sadewa Eka Satria 18. Mr. A. Paryanto
PT. B0STINC0
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jAERI 加193-160
BATAN/JAERI/JAIF SECOND WORKSHOP
(1) Participants from Company
1. Mr. Alex B. Sumatrie 2. Mr. Sigit Sudarminto 3. Mr. Sastra Viqaya
PT. BlMACOM PERDANA RUBBER工NDUSTRY, Wisma BCA 6th Floor J1. Jend. Sudirman Kav. 22-23, Jakar七a 122970
4. Mr. Haris Siswantoro PT. CYPRESS PLASTIC 工nd. Ancol Bara七工II No.2 Jakarta 14430
5. Mr. Harry Tanugraha PT. YAKINDO J1. Cideng Barat No. 49, Jakarta 10150
6. Ms. Ga1iah Seno Sas七roPT. SKIGA ANANTA DHARMA, J1. Pu工o Gadung Kav. 工工/11Kawasan Industri Pulo Gadung, Jakarta Timur
7. Mr. Rusdy Harmayn 8. Mr. Mas Agoes Soepar七o
PT. D工AN INDAH REKSA WOOD INDUSTRY J1. Su七anSyahrir 1c, 3-4, Jakarta 10350
9. Mr. 工ndrotomoUpoyo PT. SURYO INDO UPOYO J1. Krama七 V工/40,Jakarta 10430
10. Mr. Dody Budiaman PT. ELWAN SEJAT工J1. Raya Bekasi Km 14.9, Jakarta Timur
11. Mr. Sa七riaPT. FOODTECH UTAMA J1. Anco1 1 No. 4-5, Ancol Barat, Jakarta 13430
12. Ms. Rosa工i Setiawan 13. Ms. Eviazizah 14. Mr. M. Soleh
PT. R工STRA 工NDOLABJ1. Rajawali Selatan E5-6, Jakar七a Pusa七
15. Mr. D. Gustam 16. Mr. Tri Djoko
PT. INDOGAMA STERIL工ZATION/ PT. PERKASA STERIL工NDOJ1. KH. Hasyim Ashari 11A, Jakarta Pusat
17. Mr. Sadewa Eka Satria 18. Mr. A. paryan七o
PT. BOSTINCO
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19. Mr. Nahrawi PT. KABELINDO MURNI, Jl. Rawa Girang, Kawasan Industri Pulo Gadung, Jakarta Timur
20. Mr. Agus Swasono 21. Mr. Moh. Sjaifuddin ZH. 22. Mr. Setiawan 23. Mr. Paribotro
PT. APKINDO, Gedung Manggala Wanabhakti Lt.9 Jl. Gatot Subroto P.O. Box 23 JKWB, Jakarta 10270
24. Mr. Moh. Natsir PT. WOOD INDUSTRY Jl. Raya Serang Km. 12 Cikupa, Tangerang
25. Ms. Ida Guntoro PT. INDONESIA DENTAL INDUSTRIES Jl. Pulo Buaran IV, No. Wl, Jakarta Timur
26. Mr. Taufik KPB PERKEBUNAN Jl. Cut Mutiah 11, Jakarta Pusat
27. Mr. .Oermawan Nur 28 . Mr. I r v a n Mansur
PT. SABIN ADI PERTAMA, Patra Build., 10th Floor Jl. Gatot Subroto Kav. 32-34, Jakarta
29. Mr. John Lean PT. ELWAN SEJATI Jl.Raya Bekasi Km. 14.9, Jakarta Timur
30. Dr. Moch. Sholichin PT. KIMIA FARMA, Jl. Rawagelam V Kawasan Industri Pulo Gadung, Jakarta Timur
(2) Participants from Governmental, Institute and University
31. Dr. Saifula 32. Mr. Setyadi
BALAI PENELITIAN AGRICULTURA, Dept. Pertanian Parsar Minggu, Jakarta Selatan
33. Dr. Mulyo Sidik 34. Dr. Haryadi Halid
KAPUSLITBANGSISLOG, Badan Usaha Logistik Jl. Gatot Subroto, Jakarta Selatan
35. Mr. Sunarto DEPARTMEN KESEHATAN RI, Direkt. Jend. Pengawasan Obat dan Makanan, Jl. Percetakan Negara No. 23, P.O. Box 1143, Jakarta 10011
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JAERI-M 93-160
19. Mr. Nahrawi PT. KABELINDO MURN工 J1. Rawa Girang, Kawasan Industri Pulo Gadung, Jakarta Timur
20. Mr. Agus Swasono 21. Mr. Moh. Sjaifuddin ZH. 22. Mr. Setiawan 23. Mr. Paribotro
PT. APK工NDO, Gedung Manggala Wanabhakti L七.9J1. Gatot Subroto P.O. Box 23 JKWB, Jakarta 10270
24. Mr. Moh. Natsir PT. WOOD INDUSTRY J1. Raya Serang Km. 12 Cikupa, Tangerang
25. Ms. 工daGun七oroPT. 工NDONES工A DENTAL INDUSTR工ESJl. Pulo Buaran IV, No. W工, Jakarta Timur
26. Mr. Taufik KPB PERKEBUNAN J1. Cut Mutiah 11, Jakarta Pusat
27. Mr • ,,~ermawan Nur 28. Mr. 工rvanMansur
PT. SAB工N ADI PERTAMA, Patra Build., 10七h Floor Jl. Gatot Subroto Kav. 32-34, Jakarta
29. Mr. John Lean PT. ELWAN SEJATI J1.Raya Bekasi Km. 14.9, Jakarta Timur
30. Dr. Moch. Sholichin PT. K工MIAFARMA, J1. Rawagelam V Kawasan工ndustri Pu工O
Gadung, Jakar七a Timur
(2) participants from Governmental, Institute and University
31. Dr. Saifula 32. Mr. Setyadi
BALAI PENEL工TIANAGR工CULTURA,Dep七. Pertanian Parsar Minggu, Jakarta Sela七an
33. Dr. Mulyo Sidik 34. Dr. Haryadi Halid
KAPUSLITBANGS工SLOG,Badan Usaha Logis七ikJ1. Gatot Subro七0,Jakar七a Selatan
35. Mr. Sunarto DEPARTMEN KESEHATAN RI, Direkt. Jend. Pengawasan Oba七 danMakanan, J1. percetakan Negara No. 23, P.O. Box 1143, Jakarta 10011
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JAERI-M 93-160
36. Mr. Sunit H. 37. Mr. Indratmoko
LIPI, P3 Fisika Terapan Jl. Cisitu 21, 154D, Bandung
38. Ms. Siti Nurhayati DIREKTORAT PENGAWASAN OBAT TRADISONAL Jl. Percetakan Negara No. 23, Jakarta 10011
39. Ms. Ellysabeth DEPARTMEN PERTANIAN Jl. Ragunan Pasar Minggu, Jakarta Selatan
40. Mr. Sudarto DEPARTEMEN PERINDUSTRIAN Jl. Gatot Subroto, Jakarta Selatan
41. Ms. Yanna H.lianawati S. 42. Asep Dedi Sutrisno
UNIVERSITY PASUNDAN (Fak. Teknik) Jl. Lengkong Besar 68, Bandung
43. Dr. Soleh Kosela 44. Dr. Agus Nurhadi 45. Dr. Nelly D. Leswara 46. Dr. Riwandi Sihombing
UNIVERSITY INDONESIA Kampus UI, Depok, Jakarta Selatan
(3) Participants from BATAN
BATAN HQ Jl. KH. Abd. Rohim, Mampang Prapatan, Jakarta Selatan
47. Dr. Nazir Abdullah 48. Mr. Iyos Subki 49. Dr. Hidjang Kerry Sisworo 50. Dr. Hasrul Thayib
PPNR-BATAN 51. Mr. Sunarmo 52. Mr. Sunarhadijoso
PPEN-BATAN 53. Mr. Sudijatmo PPR-BATAN 54. Mr. Hisyam Hubies PPNY-BATAN 55. Mr. Sudjatmoko 56. Mr. Darsono
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JAERI-M 93-160
36. l¥1r. Sunit H. 37. Mr.工ndra七moko
LIP工, P3 Fisika Terapan J1. Cisitu 21, 154D, Bandung
38. Ms. Si七i Nurhaya七1DIREKTORAT PENGAWASAN OBAT TRAD工SONALJ1. percetakan Negara No. 23, Jakarta 10011
39. Ms. Ellysabeth DEPARTMEN PERTANIAN J1. Ragunan Pasar Minggu, Jakarta Se1atan
40. Mr. Sudar七O
DEPARTEMEN PERINDUSTRIAN Jl. Gatot Subroto, Jakarta Selatan
41. Ms. Yanna li、lianawati S. 42. Asep Dedi Sutrisno
UN工VERS工TYPASUNDAN (Fak. Teknik) J1. Lengkong Besar 68, Bandung
43. Dr. Soleh Kosela 44. Dr. Agus Nurhadi 45. Dr. Nelly D. Leswara 46. Dr. Riwandi Sihombing
UN工VERS工TY INDONES工AKampus U工, Depok, Jakar七a Selatan
(3) participants from BATAN
BATAN HQ J1. KH. Abd. Rohim, Mampang Prapatan, Jakarta Selatan
47. Dr. Nazir Abdullah 48. Mr. 工yos Subki 49. Dr. Hidjang Herry Sisworo 50. Dr. Hasru1 Thayib
PPNR-BATAN 51. Mr. Sunarmo 52. Mr. Sunarhadijoso
PPEN-BATAN 53. Mr. Sudijatmo
PPR-BATAN 54. Mr. Hisyam Hubies
PPNY-BATAN 55. Mr. Sudja七moko56. Mr. Darsono
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JAERI
PAIR-BATAN 57. Ms. Nazly Hilmy 58. Dr. Mirzan T. Razzak 59. Mr. F. Sundardi 60. Dr. Moch. Ismachin 61. Ms. Munsiah Maha 62. Mr. Marga Utama 63. Mr. Sugiarto Danu 64. Mr. Ashar Waskito 65. Mr. Gatot Triraulyadi R. 66. Mr. Erizal 67. Mr. Zainuddin 68. Ms. Herwinami S. 69. Ms. Isni Marlijarrti 70. Ms. Kadarijah 71. Ms. Wiwik Sofiarti 72. Ms. Anik Sunarni 73. Ms. Dian Iramani 74. Mr. Sudradjat Iskandar 75. Mr. Darsono 76. Mr. Edih Suwadji 77. Mr. Nikham 78. Mr. Yahya 79. Mr. A. Sudrajat 80. Mr. Affandi Djamil 81. Mr. Basril Abbas 82. Ms. Rosalina Sinaga 83. Mr. Rindy PT. 84. Mr. Bilter Sinaga 85. Mr. Madrois 86. Jasin Hafif 87. Mr. Amin Nursodik 88. Mr. Sunardi
]AERI-M 93-160
PA工R-BATAN57. Ms. Nazly Hilmy 58. Dr. Mirzan T. Razzak 59. Mr. F. Sundardi 60. Dr. Moch. 王srnachin61. Ms. Munsiah Maha 62. Mr. Marga Utarna 63. Mr. Sugiar七o Danu 64. Mr. Ashar Waski七O
65. Mr. Ga七o七 TrirnulyadiR. 66. Mr. Erizal 67. Mr. Zainuddin 68. Ms. Herwinarni S. 69. Ms. Isni Marlijan七i70. Ms. Kadarijah 71. Ms. Wiwik Sofiarti 72. Ms. Anik Sunarni 73. Ms. Dian Irarnani 74. Mr. Sudradjat Iskandar 75. Mr. Darsono 76. Mr. Edih Suwadji 77. Mr. Nikharn 78. Mr. Yahya 79. Mr. A. Sudraja七80. Mr. Affandi Djarni工81. Mr. Basril Abbas 82. Ms. Rosalina Sinaga 83. Mr. Rindy PT. 84. Mr. Bilter Sinaga 85. Mr. Madrois 86. Jasin Hafif 87. Mr. Arnin Nursodik 88. Mr. Sunardi
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JAERI-M 93-160
Participants from Japan
TRCRE-JAERI 89. Dr. Soichi Sato 90. Dr. Waichiro Kawakami 91. Dr. Keizo Makuuchi 92. Dr. Shoji Hashimoto 93. Dr. Tamikazu Kume 94. Mr. Akio Kuroyanagi
Nissin Electric Co., Ltd. 95. Mr. Mitsuaki Suzuki
Nissin High Voltage Co., Ltd. 96. Mr. Takeshi Doi
NKK Co. 97. Mr. Keiichiro Tomita 98. Dr. Masaaki Takehisa
Radia Industry Co., Ltd.
99. Dr. Yasuichi Sasaki Yazaki Co.
100. Mr. Seiichiro Takahashi JAIF
101. Dr. Hiroshi Amano Expert PPR-BATAN, Serpong
102. Dr. Fumoto Expert BPPT, Serpong
103. Mr. Mitsugi Chiba Expert Indonesian Institute of Science
104. Mr. Takashi Bito Expert BPP Technology
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JAERI一如I93-160
Participants from Japan
TRCRE-JAERI 89. Dr. Soichi Sa七o90. Dr. Waichiro Kawakami 91. Dr. Keizo Makuuchi 92. Dr. Shoji Hashimoto 93. Dr. Tamikazu Kume
94. Mr. Akio Kuroyanagi Nissin E1ec七ricCo., Ltd.
95. Mr. Mitsuaki Suzuki Nissin High Vo1tage Co., Ltd.
96. Mr. Takeshi Doi NKK Co.
97. Mr. Keiichiro Tomita 98. Dr. Masaaki Takehisa
Radia Industry Co., Ltd.
99. Dr. Yasuichi Sasaki Yazaki Co.
100. Mr. Seiichiro Takahashi JA工F
101. Dr. Hiroshi Amano Expert PPR-BATAN, Serpong
102. Dr. Fumoto Expert BPPT, Scrpong
103. Mr. Mi七sugiChiba Expert Indonesian工nsti七U七e of Science
104. Mr. Takashi Bito Expert BPP Techno1ogy
-189-
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