Jou rn al of Scientifi c & Industrial Research Vol.60, January 200 I, pp 52-59 Pyrolysis of Solid Wastes A N E Rahman, M A Khaleel Akmal and K B S Prasad Indian Institute of Che mi c al Tec hn ology, Hyderabad 500 007, India Received: 19 June 2000; accepted: 18 Se ptemb er 2000 Pyro lysis of solid was tes lik e papers , rags, ga rd en wastes. used tea leaves and mun ic ip al solid waste (MSWJ is ca rri ed o ut in a fix ed bed reactor for stud yin g distri but io n or energy in pyrolytic products a nd th eir poss ibl e ap pli ca ti ons as fuel. Pyro lys is is conducted between 450°C to 650°C and at different react ion tim es. The temperature of 600°C is foun d to be good forgett in g max imum yie ld or tar and is enh anced from 16 per ce nt to 27.6 pe r cen t as th e pyrolysi s tim e redu ces fr om 35 min to 5 min. The average yield of char and gas is found between 30-34 per cent and 16-20 per ce nt respectively, irrespective of reaction time. The ca lori fic va lu es or so lid , liquid and gaseous prod cts o r pyro lysis of· all the wastes show a good fuel po tential. The ta r can be used as furn ace o il , char ca n be utili zed as a feedstock for prod uc in g ac ti ve carbon and gas as a fu el for indu s tr ia l fu rnaces or internal co mbu st ion engine s. Introduction The rapid growth of industria li za ti on a nd urban- ization culminated the problem of waste di sposa l. Th e co ll ec ti o n, transport and disposal of sol id wastes, th ough an important step and also a serv ice, to be rendered by any municipality, less attentic.. n is be in g paid s in ce it in - vo lves hu ge expenditure. Municipal so lid waste is th e cheapest and abu ndantly avai lable renewa bl e source of energy. Wa stes in India are cons id erably diffe rent from those produced in adva nc ed cou ntri es du e to food hab- it s, cu lture and trad ition . The annual o ut put of garbage in Indi a is estimated at 20 million tonnes equivalent to I 0 million me tri c tonnes of coal replaceme nt 1 • Th e main ener gy compone nt in th e so lid waste with an average of 8000 Btu/lb ( 18 mJ/kg) is its cellul os ic content. The usual method of wastes disposal as lan d fi !l - in g causes land and a ir pollution. In th e process of in - c in erat ion th e heat re le as ed by co mpl ete combusti on can generate steam a nd powe r. Pyrolysis of waste materials yie ld s so li d, liquid and gaseous fu els and also minimizes atmosphe ri c pollution . Variou s typ es of processes of py rolys is for mu- ni c ipal r efuse main ly emp loy fix ed beds viz., th e Uni on Carbide Purox Process 1 . The Andco Torrax fluidized bed process' and th e Occidental Flash pyro lys is in e n- trained bed are report ed fr om Jap an and th eUS .The o b- jective of these processes is to produce fu el gas exce pt for th e Occidental Flash Pyrolysis process of th e US wh ich produces fuel oi l. In the prese nt invest igation, laboratory sca le results ar e reporte d on both norma l and rapid pyr o ly ti c behaviour of some common wastes li ke paper, rags. gar- den wast e, us ed tea leaves and municipal sol id was tes , which mainly constitute th e municipal wastes. Materials and Methods The laboratory set up for norma l pyrolysis studies is shown in Figure I. The reactor was made of pyrex glas s (50 mm ID X 750 mm long). It was in se rt ed into a horizontal elec tri c furnac e to maintain th e required te m- perature. The volatile products (moisture, o il va pours and gas) were led to a U-tube kept i the ice ba th for affect in g condensation. The 1 ixture of non-condens- ab le gas and res idu al oil vapours was scrubbed counter curre ntl y with acetone in a tower packed with g lass rin gs . Acetone was found to be a be tt er sol ve nt t ha n benzene or tol uene as it le ft no trac es of o il · nd th e surface co n- tain e r. For th e co ll ection of gas, a calibrated gas holder was prov id ed. An open tube manometer, to ind icate the sy stem pressure as th e pyrolysis proceeded, was al so attached. The apparat us us ed fo r th e rapid pyrol ys is was a standard Gra y- King Assay as sembl y. Experimental Procedure (i) Preparation of Feed Stock (i) Wa ste pape r. (ii) Ga rd en wast e. (iii ) Muni ci pal so li d wast e.
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Journal of Scientific & Industrial Research Vol.60, January 200 I, pp 52-59
Pyrolysis of Solid Wastes
A N E Rahman, M A Khaleel Akmal and K B S Prasad
Indian Institute o f Chemical Technology, Hyderabad 500 007 , India
Rece ived: 19 June 2000; accepted : 18 September 2000
Pyro lysis of solid wastes like papers , rags, garden wastes. used tea leaves and mun icipal solid waste (MSWJ is carried out in a fix ed bed reactor for stud ying distri but ion or energy in pyrolytic products and their possibl e applicati ons as fuel. Pyrolysis is conducted between 450°C to 650°C and at different react ion times. The temperature of 600°C is found to be good forgett ing max imum yield or tar and is enhanced from 16 per cent to 27.6 per cent as the pyrolysi s time reduces from 35 min to 5 min. The average yield of cha r and gas is found between 30-34 per cent and 16-20 per cent respectively, irrespect ive of reaction time. The ca lori fic values or so lid , liquid and gaseous prod cts o r pyro lysis of· all the wastes show a good fuel potential. The ta r can be used as furnace oil , char can be utili zed as a feedstock for prod ucing ac ti ve carbon and gas as a fu el for industria l fu rnaces or internal combust ion engines.
Introduction
The rapid growth of industria li zati on and urbanization culminated the problem of waste di sposal. The co llec ti on, transport and disposal of sol id wastes, th ough an important step and also a serv ice, to be rendered by any municipality, less attent ic.. n is being paid since it invo lves huge expenditure. Municipal so lid waste is the cheapest and abu ndantly avai lable renewable source of energy. Wastes in India are considerabl y diffe rent from those produced in advanced cou ntries due to food habits, cu lture and trad ition . The annual output of garbage in India is estimated at 20 million tonnes equivalent to I 0 million metric tonnes of coa l replacement 1
• The main energy component in the so lid waste with an average of 8000 Btu/lb ( 18 mJ/kg) is its cellulos ic content.
The usual method of wastes disposal as land fi !l ing causes land and air pollution. In the process of incinerat ion the heat re leased by complete combusti on can generate steam and power. Pyrolysis of waste materials yields so li d, liquid and gaseous fuels and also minimizes atmospheric pollution .
Various types of processes of pyrolys is for municipal refuse main ly employ fix ed beds viz., the Union Carbide Purox Process1
. The Andco Torrax fluidized bed process' and the Occidental Flash pyro lys is in entrained bed are reported from Japan and theUS .The object ive of these processes is to produce fu el gas except for the Occidental Flash Pyrolysis process of the US wh ich produces fuel oi l.
In the present invest igation, laboratory sca le results are reported on both norma l and rapid pyro lyti c behaviour of some common wastes li ke paper, rags. garden wast e, used tea leaves and municipal sol id was tes, which mainly constitute the municipal wastes.
Materials and Methods
The laboratory set up for norma l pyrolys is studies is shown in Figure I. The reactor was made of pyrex glass (50 mm ID X 750 mm long). It was in serted into a horizontal electric furnace to maintain the required temperature. The volatile products (moisture, oil vapours and gas) were led to a U-tube kept i the ice bath for affecting condensat ion. The 1 ixture of non-condensab le gas and res idual oil vapours was scrubbed counter currentl y with acetone in a tower packed with glass rings . Acetone was found to be a better sol vent than benzene or tol uene as it left no traces of oil · nd the surface container. For the co llection of gas, a calibrated gas holder was prov ided. An open tube manometer, to ind icate the system pressure as the pyrolysis proceeded, was al so attached. The apparatus used fo r the rapid pyrol ys is was a standard Gray-King Assay assembl y.
Experimental Procedure
( i) Preparation of Feed Stock
(i) Waste paper. (i i ) Garden waste. (iii ) Munici pal so lid waste.
RAHMA et a/..·PYROLYS IS OF SOLID WASTES 53
Acetone
To Atmosphere --~
Stop Cock -.-\-~
Manometer
Furnace
Ice bath
Gas holder
Fi gure 1 -A lahoratory set- up for conducting pyrolysis or so li d wastes
(iv ) Rags. (v) Used tea leaves.
The first three materia ls were crushed in a mirac le mill to a s ize between I to 2 mm. The rags co ll ected from a tail or 's shop, compri sing most ly of sy ntheti c fibres , were cut w ith scissors to 2 mm. The muni c ipa l so lid waste was a sy nth e ti c bl e nd of 80 per ce nt compostab le matter (grass, garden waste and vegetables),
8 per cent waste paper, 8 per cent rags and 4 per cent plastics . The composi tion of blend was similar to that
of Hyderabad C ity refuse.
Waste mate ri a l (70 g) was taken in the g lass reactor and it was inserted into the e lectri c furnace. The
furnace was heated to 650°C at the rate of 20°C/mi n. The time, system pressure and vo lume of gas evo lved
were noted at inte rva ls of 25°C pyrolysis. As the pyro lys is of pure cellul os ic materia l yie ld s carbon dioxide upto 3 10°C(ref. 4) the gas up to 250°C was let out into atmosphere for avoiding di luti on of pyro lytic gas . (The 250°C is assumed to be the safest temperature for the materia ls which are not cellul os ic). The assumpti on was va lid as indicated by the gas collected separatel y up to 250°C , contained up to 2 pe r cent carbon diox ide. Gas rate vs temperature and system pressure vs time (Figure 2 and 3) be long to a ll the mate rials under stud y. Acetone from the sc rubbin g tower was collec ted and distilled. The tar thus recovered and co llected from the Utubc trap was accounted for the total quantity produced
54 J SCIIND RES VOL.60 JAN UARY 2001
for each ex periment. The quantity of liquor from Utube trap and char from the reactor were accounted fo r material balance.
In conducting rapid pyrolysis, about 5 g of material was filled in the si lica tube of standard Gray King appara tu s. The sliding electric furnace after gett ing heated at 450°C, 550°C or 650°C was moved /mounted over the sili ca tube and retained for 2.5, 5 an I 0 min durat ion, and then qu ickly withdrawn. The products of pyrolysis evolved du ring the reaction time were recovered and materi al balance drawn.
Results and Discussion
Proximate and ultimate analyses of the materials used in the present studies are presented in Tabl I. The data is in agreement with the values reported in the lit erature for waste material s, indicating a typical characteri st ics of cellulose material hav ing hi gh vo latile matter and oxygen with low sulphur content. The materi als used in this stud y have a hi gh elemental carbon. The Gray King assay results are presented in Table 2. The feed materials yielded an average of 20 per cent tar, 28 per cent aqueous I iquor, 33 per cent char and 19 per cent gas by Gray King assay. In fact the yields are dependent upon the size of feed, rate of heating, pressure and temperature of pyrolysis5.
3 C/H ratio 7.7 9.5 4 Ca lorifi c value( k cal/kg) 4444 4743
Pyrolysis
In the present study the pyrolysis us ing the reactor described, was carried out at 650°C and at atmo.-pheric pressure with 20°C/min rate of heati ng us ing feed size of 1-2 mm. It can be seen from the data on pyro lysis (Tab le 3) that the yield of product is in agreement with that generally reported values in literature for biomass and waste materi alr'. The low yie .i d of l< r, as compared to Gray King assay is due to the di fficul [y in its recovery from the reactor surface. The quantity of carbon dioxide let out into the atmosphere up to 250°C caused a loss in gas balance. However the compos ition of gas is similar to that of Gray-King assay.
The rate of gas evo lution (Figure 2) for the ce llulos ic materials ranged from 440 to 500 rnl/min but for rags of synthetic fibres, it dropped to 250 ml/min thereby shift ing the peak temperature of pyrolysis from 325°C to 425°C. The active pyro lys is ti me fo r cellulos ic materi als was 5 to 8 min whereas for rags 12 min (Figure 3) . This indicates that pyrolysis of plastic or sy nthetic fibre requ ires higher duration and temperature than for cellulos ic materials.
The characteristics of char and tar oi Is covering proximate and ultimate analyses, calorific va lue. etc., are presented in Table 4 and 5. It i~ evident that the chars have an average heating va lue equal to that of charcoal so it can be converted to shaped fue l by briquetting.
Table :\ - Data on pyro ly> is of solid wastes at 650°C Waste Rags Used tea leaves Garden waste MSW
Product yields
(wt per cen t)
Char
Tar
Li quor
Gas
Losscs
2 Gas compos i li on
(vo l per cent)
Carbon d iox idc
Unsa turatt:s
Oxygen
Carbon monoxide
Hydrogen
Mcthane
Nitrogen
paper
:\4.4
10
28.6
14.0
8.7
46.5
1.4
0.6
27.4
8. 1
8.5
7.5
28 .6 :\4 .:\
20.7 17 .1
28. 6 21.4
14 .6 16.7
7.5 10.5
"i i.O 51.7
0.6 2. 1
O.X 1.0
25 .7 14.4
7.8 10.1
5.7 11.5
.4 9.2
:\ Ca lorilic va lue of gas
(k caVNnr1
)
1953 1537 2005
4 Time of pyrolysis 30 :\8 34
min
The chars from MSW and garden waste are a good feedstock for active carbon as indicated by their methylene
blue absorption test. T he test has the same va lu ~ for the c har obtained by low te mperature ca rboni za ti o n of Rama g undam coal in Lurgi Squel gas p lant. Ramagundam char is being used in India as a raw mate
ria l fo r the produc ti on of active carbon. The tar oil obtained by pyrol ys is of wastes con
tains I 0 pe r cent oxygen (except rags and paper) whereas that got by flash pyrolysis of American MSW con tained 33 per cent which leads to corrosion of burners. The calorifi c value of tar is more than that obtained by flash pyrolysis. Hence, it can be used as a fue l o il o r alternate ly it can be thermally cracked for getting low mo
lecul ar hydrocarbons.
Rapid Pyrolysis The effect s of time and temperature on pyro lysis
of MSW is presented in Figure 4 a and band S a and b and Tab les 6-8. It can be seen that 5 min and 550°C are the I imiting conditions for achieving 27 per cent tar, 32
:\0.0 :\0.0
15 .7 14.3
28.6 30 .0
16.0 14.6
9.7 I 1.1
53.7 48 .5
1.6 1. 8
0.8 0.7
15 .7 18.8
9.7 10.3
13.4 12.6
5.1 n
2 11 5 2191
34 34
pe r cent char and 22 per cent gas . Further inc rease in e ithe r time and temperature does not have any sig nifi
cant effect on products yield, but with the inc rease in time (more than 5 min ) the calorifi c va lue of gas dec reases and with the increase in tempe rature (above 550°C) the calorific value o f gas increa. es. This study forms a basis for the se lect ion and design o f an efficient pyro lysis r actor.
Overall the energy distribution in the products of solid wastes was found to be 5, 22 and 7 per cent in char, tar o il and gas respectively the re ma in ing 20 per cen t be ing the losses in the system . Thi s di st ribu tion pattern is in agreement with that of biomass and wastes generally reported except losses of gas in our system which are at a hi gher s ide which presumabl y due to the un accountability of gas formed during py ro lysis up to 250 oc. Conclusions
Figun: :; - Temperawrc or pyro ly, is v, y ield or product caloriric va lue or gas
T ah le o - Ellec l llr dural ion on pyrol y, is or MSW al 600°C
Dural ion
2.5 :1.0 I 0 .ll
Yi elds o r prnducl s (W I per ccn l )
Char 3(L2 32.9 32 .::.
T ar 25.2 27.6 27.7
Liquor 17.2 17. 1 17 .7
Gas 2 1A 22.4 22.-+
--1 I 0.0 -- I 00.0 - I 00.0
V ol orgas (inl/ 100 g or ICed! 1-LRo 15.0 15 .2
Composi1 ion or gas (l'n l per ccnl )
Carbon diox ide 52.0 :10.0 51.2
Okrins .l .X -Ul 3. ()
Oxygens 0.6 0.2 0.-+
Carbon mnnox ide: 22 .0 21.0 20.2
Hydrogen 6 .0 5.-+ :1.6
i\'kthanc X.X 12.6 IUl
N i1 rogc n 6.X 7.2 7.2
Caloriric va lue or gas (k c.t i/Nm1
) 2 I I 0 2-l 2X 2:?X)
•
•
RAHM AN et a/.: PYROLYSlS OF SOLID WASTES 59
Tab le 7 - Effect or temperature on rapid pyro lys is of MSW, 5mi n
Details Temperatureoc
450 550 600 650 Product yields (wt per cent) Char 43.4 33.2 33.0 32.6 T ar 2 1.4 27.1 27.6 27.5 Liquor 17 .8 17.5 17.1 17.4 Gas 17.4 22.2 22 .3 22.5 Vol or gas ( in Ill 00 g of Iced) 9.8 14.2 1 15.0 1-U::
2 Composi ti on or gas (vo l per cent ) Carbon 73.0 54.0 50.0 46.6 Unsaturates 2.4 4.0 4.0 -Ul Oxygen 0.2 0.4 0.2 0. -1-Carbon monoxide 20.0 25.6 2 1.0 24.4 Hydrogen 0.4 4.0 5.4 5.0 M ethane 0.8 6.0 12.6 12.4
3 Calorili c va lue or gas (kca i/Nm') 982 1925 2420 251-1-
T ab le 8- Comparison or pyro lyti c yields and gas composi ti on Pyrolysis at 550°C and 5 min W aste paper Rags Garden waste MSW
Product y ields (wt per cent ) Char 34.8 Tar 22.7 Liquor 27.2 Gas 16.3
2 Compositi on or gas (vo l per cent ) Carbon dioxide 52.0 Unsaturates 2.6 Oxygen 1.6 Carbon monox id.:: 29.6 Hydrogen 6. -1-M eth ane 3.X Nitrogen -1- .0
3 Calori l:c ~a lu e or gas 17 17 (k cai/Nm')
similar materials can be pyrolysed to yield gas and tar of moderate heat ing va lue suitabl e for power generation or fu el for internal combusti on eng me.
It can be concluded th at tar obtained by normal pyrolysi s under reduced time is useful as fu el oil.
The presence of syn thetic fibres or plasti cs in wastes needs shift in the pyrolysis reaction time and temperatu re to a littl e hi gher side. This study forms a basis for the des ign of an effici ent reactor whi ch is under progress.
25.2 35. 1 26.9 24.6 28.7 18.0 19.2 2 1.9
59 0 5 1.0 3.0 4.0 0.6 1.2
23.2 23.8 4.8 3.8 5.2 9.4 4.2 6.8
1670 2 169
Acknowledgement
33.2 27.1 17.5 22.2
5-1-.0 4.0 0.-1-
25.6 -1- .0 6.0 6.0
1925
The authors thank Dr K V Raghavan, Direc tor. Indian Institute of Chemical Technology, Hyderabad for giving permi ss ion to publish thi s paper. Thank s are also clue to Mr A P Rudradas for hi s assistance in anal yzi ng raw waste material and the char.
References Manject Kumar & Pande GN. U1ju. l ( I 985) 32
2 Mech Cug. 99 (December 1977 ) 22. 2-1-
3 M cG rowin R. Chc111 D1g Prog. (March I 9!:>5) 57
4 Graham R G . .I Au a/ Af'f' Prml. (September 6. 198-1- l 12 5 I S Method oJTestiug r!f'Coal aud Coke. IS 1353 ( I <J<J .~ ) (J
6 Pul z W & Chartie r K. l:·ucrgv.fiwu bit•111ass iul~·llmfJI ' . ( I') ' 7)