calculation sheet2.xls

8/9/2019 calculation sheet2.xls

1/60

Select form type to navigate to the emission calculator for the source type:

Company Name: Note: Don't forget to enable macros.

Insert Company and/or site name here.

Choose form type:

Blodon and/or process vents !hroughout this or"boo":

Boilers and #eaters $Input variables into the blue bo%es.

Compressor engines $&missions ill be in the green bo%es.

lares

rac tan"s

(lycol dehydrators !o be notified of any updates to this or"boo"

)oading

*iping component fugitive areas

Separators

Condensate storage tan"s

Crude oil storage !an"s

*roduced ater storage tan"s

!urbines

+ther:

Non,flare combustive device

◊ Emitted 1 ton or more of volatile organic compounds (VOC), or

◊ Emitted 01 tons per year or more of a ha!ardous air pollutant ("#$)

◊ less than % tons of &O',

◊ less than % tons of VOC, and

◊ less than 1 ton of aggregate "#$s

The Barnett Shale Special Inventory list server hamessages about the agency’s special inventory ef

If you haven't already done so, we recommend yto receive any important updates concerning the iemission calculator. To do so, you will need to crTC!’s distribution service, "ov#elivery.com, smanage your subscriptions. To create a profile osubscriptions, please visit$ http$%%service.govdelivcodeT(TC!.

Complete a form for each piece of euipment (listed aove) that meets one of thefollo*ing criteria for +00:

◊ Emitted 1 ton or more of &O',

-f individual pieces of euipment do not meet the reuirements listed aove, theymay e omitted from the inventory provided that the total emissions from all suchunreported sources are:

-f the total emissions from the omitted pieces of euipment do not satisfy thesereuirements, report each source starting *ith the piece of euipment *ith thehighest emissions until the total emissions of the remaining omitted sourcessatisfy the aove reuirements


2/60

Barnett Shale *hase II Identification Information: $Input variables into the b

Company Name: Insert Company and/or site name here. $&missions ill be in the g

Blodon -:

mole . *eight .

(as nalysis: &itrogen +/01/ 0 23-V405

00% 0 23-V405 VO

0/1// 0 23-V405 VOC *eig

methane (C1) 180+8 0 23-V405

ethane (C+) 0080 0 23-V405

propane (C) 0%8+ 0 23-V405 "#$ content of g

i9utane (C) %/1+++ 0 23-V405 en!en

n9utane (C) %/1+++ 0 23-V405 ;oluen

i9pentane (C%)


3/60

#eater and Boiler &mission Calculations 0fueled by natural gas1


Company Name: Insert Company and/or site name here. $&missions ill be in the

#eater or Boiler -:

"eater4oiler rating (@@tu4hr):

pick from list

Operating hours4year:

uel "eat Value (tu4BC):

pollutant emission factor (l4@@C)? tpy

VOC %% 23-V405

2 23-V405

? Emission actors from #$9+, Chapter 1, ;ales 191 and 19+

Company's 5ni7ue IdentificationNumber:

6ating aove is 0select from list1:

&O=

Back to Workbook N


4/60

&ngine &mission Calculations 0fueled by natural gas1

Barnett Shale *hase II Identification Information:

Company Name: Insert Company and/or site name here. $

&ngine -: $

N

#orsepoer: !

uel consumption 0Btu/hp,hr1:9.

#ours of operation per year:

pick from list .

&ngine )oad: pick from list

units

+C 2.2 2.2 lb/44Btu 2.2222


5/60

lare


Company Name: Insert Company and/or site name here.

lare -:

(eneral Information &missioEmissio

non9steam assisted flare *ith high tu stream flared

Emission actors for aste Das Btream(s) (l4@@tu)

01/

Ies

Emission actors for $ilot Btream (l4@@scf)

100

&o

Enter !eros into the o'es in the column for Btream &o + elo*

Emission actors for #dded uel Btream (l4@@tu)

0

/

Stream Information

Stream Sent to lare No. 9 < ; ? >

$ilot(s) e': oil tanJ e': *ater tanJ

Company's 5ni7ueIdentification Number:

091 Fhat type of flare is

thisG *ic" from list.

&O'

0


6/60

rac Storage !an"



rac !an"-:

!an" emissions are made up of different components6 or"ing6 breathing and fl

5sing &* !NJS ;.2 Softare to calculate For"ing and Breathing losses

For"ing and Breathing )osses

E$# ;#&MB 0This softare is a!aila"le for donload at .epa.#o!$ttn$chief$softare$tanks$inde%.html

orJing reathing

VOCs, C>

en!ene

;oluene

E en!ene

=ylenes

n9he'ane+,+, 9 ;rimethylpentane

#ny #dditional "#$ (if applicale):

5sing &K* !NJS ;.2 Softare to calculate For"ing and Breathing losses

This softare can "e purchased from .#lo"al.ihs.com

Component Controlled Emissions Nton4yr

VOCs, C>

en!ene

;oluene

E en!ene

=ylenes

n9C8

++;rimethylp


EP$ ;anJs (accounts for *orJing, reathing and flash losses)


7/60


8/60

Notes:

$ &nter variables into blue bo%es

$ &missions ill be in green bo%es

ash losses.

lash losses !otal &missions

3irect @easurement of Emissions

$rocess Bimulator @odels

lash losses

VOCs, C> VOCs, C> 00000

en!ene en!ene 00000

;oluene ;oluene 00000

E en!ene E en!ene 00000

=ylenes =ylenes 00000

n9he'ane n9C8 00000+,+, 9 ;rimethylpentane +,+, 9 ;rimethylpentane 00000

#ny #dditional "#$ (if applicale): #ny #dditional "#$ (if applicale):

00000

00000

00000

00000

#nnual Emissions tons per year

VOCs, C> 00000

en!ene 00000

;oluene 00000

E en!ene 00000

=ylenes 00000

n9C8 00000

+,+, 9 ;rimethylpentane 00000

Valid @ethods for Condensate (Qse one of thefollo*ing accepted methods):

the gas4oil ratio (DO6) method

Back to Workbook NavigationTab.


9/60


10/60

6eport VOC emissions onrac ;anJ(s) ;a

6eport "#$ emissions on

rac ;anJ(s) ta or "#$speciation ta if the valuesare greater than or eualto 01 tpy

6eport VOC emissions onrac ;anJ(s) ;a

6eport "#$ emissions onrac ;anJ(s) ta or "#$speciation ta if the valuesare greater than or eualto 01 tpy


11/60


12/60

(lycol Dehydrator &mission Calculations


Still-:

Company's 5ni7ue Identification Number:

;here are t*o options that are used most commonly to determine the emissions from a glycol dehydr

$lease chose the option you prefer:

(I,()HCalc *rogram6un the soft*are program maJing sure to using a *et gas analysis for your input ;his analysis shou

5ncontrolled/ Controlled egenerator &missions lash (as &m

Component tpy Component

$ropane $ropane

-soutane -soutane

n9utane n9utane

-sopentane -sopentanen9pentane n9pentane

cyclopentane cyclopentane

n9he'ane n9he'ane

cyclohe'ane cyclohe'ane

other he'anes other he'anes

heptanes heptanes

methylcyclohe'ane methylcyclohe'ane

+,+, ;rimethylpentane +,+, ;rimethylpentane

en!ene en!ene

;oluene ;oluene

Ethylen!ene Ethylen!ene

=ylene(s) =ylene(s)C/> "eavies C/> "eavies

;otal VOC ;otal VOC

ich/)ean nalysis

R D6-9DAICalc Boft*are $rogram

R 6ich4Aean #nalysis

;he total emissions for a glycol dehydrator should include oth the KControlled 6egenerator Emissionpresent and if the flash tanJ is not 100. controlled *ith the recycled4recompression option) y revie

emissionsClicJ to see e'ample reports:

Controlled regenerator *ith flash tanJ

Qncontrolled regenerator *ith flash tanJ

Qncontrolled regenerator vent *ith a flash tanJ *ith recycle4recompressi


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Dlycol recirculation rate (gal4min)

#nnual hour of operation (hr)

Component ich 0mg/)1 )ean 0mg/)1 tpy

;otal VOC 000n9he'ane 000

+,+, ;rimethylpentane 000

en!ene 000

;oluene 000

Ethylen!ene 000

=ylene(s) 000

#dditional "#$s

000

000

000

000

Euation used in 6ich4Aean #nalysis:

here:

t 7 annual hours of operation

5sing a laboratory analysis of enriched and lean glycol samples that includes benAene6 toluefolloing information.

(Crich

9 Clean

) ? Hrecirc

? t ?


14/60

Notes:



$ Instructions for using this form.

ator

ld include an e'tended gas analysis that includes ut not limited to ;E=

issions !otal (lycol Still &missions

tpy Component tpy

;otal VOC 0

en!ene 0

;oluene 0

Ethylen!ene 0=ylene(s) 0

+,+, ;rimethylpentane 0

n9he'ane 0

sK or KQncontrolled 6egenerator EmissionsK and the Klash Das EmissionsK (if the flash tanJ is*ing the D6-9DAICalc #ggregate Calculations report you *ill e ale to determine your total

n option

Back to Workbook NavigationTab.


15/60

e6 ethylbenAene and %ylene0s16 complete the


16/60

Calculations

n Information: Notes:

Insert Company and/or site name here. $ &nter va

$ &missio

$ 5se thes

0completion is optional1

;?=.> 2

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0 1

0 1

tpy

00000 6eport VOC emissions on KAoadingK ;a

00000

00000

00000

00000

00000

00000

00000 eport any dditional #*s if they are greater than or e7ual to 2.9 tpy.00000

Can assume /


17/60

ugitives &mission Calculations

Complete this form for each type of each stream type.

Barnett Shale *hase II Identification Information: Notes:

Company Name: Insert Company and/or site name here. $Input variables int

ugitive rea -: $&missions ill be

(as nalysis:

mole . *eight .

&itrogen +/01/ 0 23-V405 VO

00% 0 23-V405 VOC

0/1// 0 23-V405 VOC *eig

methane (C1) 180+8 0 23-V405

ethane (C+) 0080 0 23-V405

propane (C) 0%8+ 0 23-V405 "#$ content of

i9utane (C) %/1+++ 0 23-V405 en!ene

n9utane (C) %/1+++ 0 23-V405 ;oluenei9pentane (C%)


18/60

'ylenes (@, $, O) 10818 0 23-V405

undecanes (C11>)? 1%81 0 23-V405

;O;#AB: 00000 0 23-V405

? -f the @olecular eight is availale on the gas analysis, enter it aove, other*ise, can use the default value

ugitives &mission Calculations

$lease choose from the follo*ing:

(as (as

numer component l4hr tpy

Valve 000% 000+ 0 0 23-V405

$ump Beal 000+ 000%+ 0 0 23-V405

Connector 0000+ 0000 0 0 23-V405

lange 0000 0000/8 0 0 23-V405

Open9ended Aine 000+ 0001 0 0 23-V405

Other 000// 0010 0 0 23-V405

;otal: 0 0

)ight +il )ight +il

numer component l4hr tpy

Valve 000+% 000%%1 0 0 23-V405

$ump Beal 001 00+/88 0 0 23-V405

Connector 0000+1 00008 0 0 23-V405

lange 000011 0000+ 0 0 23-V405

Open9ended Aine 0001 0000 0 0 23-V405

Other 000


19/60

;oluene 23-V405

Ethylen!ene 23-V405

=ylene(s) 23-V405

n9"e'ane 23-V405

? or fugitive calculations, VOC content should e VOC content of total hydrocarons, not of total sample

6eport en!ene, Ethylen!ene, ;oluene,=ylene, and n9he'ane on the $hase --calculator if they are greater than 01 tpy onthe Kugitive(s)K ta

Emission factors are for oil and gas production facilities (not refineries), and come from the E$#Ss K$rotocol for Euipment AeaJ Emission Estimate69%901


20/60


21/60

+C en!ene ;oluene Ethylen!ene =ylene n9he'ane

tpy tpy tpy tpy tpy tpy

23-V405 23-V405 23-V405 23-V405 23-V405 23-V405

23-V405 23-V405 23-V405 23-V405 23-V405 23-V405

23-V405 23-V405 23-V405 23-V405 23-V405 23-V405

23-V405 23-V405 23-V405 23-V405 23-V405 23-V405

23-V405 23-V405 23-V405 23-V405 23-V405 23-V405

23-V405 23-V405 23-V405 23-V405 23-V405 23-V405

23-V405 23-V405 23-V405 23-V405 23-V405 23-V405


23-V405 23-V405 23-V405 23-V405 23-V405 23-V405

23-V405 23-V405 23-V405 23-V405 23-V405 23-V405

23-V405 23-V405 23-V405 23-V405 23-V405 23-V405

23-V405 23-V405 23-V405 23-V405 23-V405 23-V405

23-V405 23-V405 23-V405 23-V405 23-V405 23-V405

23-V405 23-V405 23-V405 23-V405 23-V405 23-V405

23-V405 23-V405 23-V405 23-V405 23-V405 23-V405


0000 0000 0000 0000 0000 0000

0000 0000 0000 0000 0000 00000000 0000 0000 0000 0000 0000

0000 0000 0000 0000 0000 0000

0000 0000 0000 0000 0000 0000

0000 0000 0000 0000 0000 0000

0 0 0 0 0 0


0000 0000 0000 0000 0000 0000

0000 0000 0000 0000 0000 0000

0000 0000 0000 0000 0000 0000

0000 0000 0000 0000 0000 0000

0000 0000 0000 0000 0000 0000

0000 0000 0000 0000 0000 0000

0000 0000 0000 0000 0000 0000


22/60


23/60

&N!&D S&*!+ &4ISSI+N C)C5)!I+N

Barnett Shale *hase II Identification Information: $Input variables into the


Separators -:

(as nalysis of separator vent gas:

mole . *eight .

&itrogen +/01/ 0 23-V405 VOC

CO+ 00% 0 23-V405 V

"+B 0/1// 0 23-V405 VOC *e

methane (C1) 180+8 0 23-V405

ethane (C+) 0080 0 23-V405

propane (C) 0%8+ 0 23-V405 "#$ content of

i9utane (C) %/1+++ 0 23-V405 en!e

n9utane (C) %/1+++ 0 23-V405 ;oluei9pentane (C%)


24/60

Condensate Storage !an"



Condensate !an"-:




E$# ;#&MB 0

This softare is a!aila"le for donload at .epa.#o!$ttn$chief$softare$tanks$inde%.html

orJing reathing

VOCs, C>

en!ene

;oluene

E en!ene

=ylenes

n9he'ane+,+, 9 ;rimethylpentane





VOCs, C>

en!ene

;oluene

E en!ene

=ylenes

n9C8

++;rimethylp

Das condensate is defined as a liuid hydrocaron *ith an #$- gravity greater than 0° at 80° (a




25/60

Notes:



ash losses.


3irect @easurement of Emissions$rocess Bimulator @odels

lash losses

VOCs, C> VOCs, C>

en!ene en!ene

;oluene ;oluene

E en!ene E en!ene

=ylenes =ylenes

n9he'ane n9C8+,+, 9 ;rimethylpentane +,+, 9 ;rimethylpentane

#ny #dditional "#$ (if applicale): #ny #dditional "#$ (if app

#nnual Emissions

VOCs, C>

en!ene

;oluene

E en!ene

=ylenes

n9C8

+,+, 9 ;rimethylpentane

nd a specific gravity less than 0/+%+)

Valid @ethods for Condensate (Qse one of the follo*ingaccepted methods):


Back to Workbook NavTab.


26/60

00000

00000

00000

00000

00000

0000000000

licale):

00000

00000

00000

00000

tons per year

00000

00000

00000

00000

00000

00000

00000

6eport VOC emissions onCondensate ;anJ(s) ;a

6eport "#$ emissions onCondensate ;anJ(s) ta or

"#$ speciation ta if thevalues are greater than oreual to 01 tpy

6eport VOC emissions onCondensate ;anJ(s) ;a

6eport "#$ emissions onCondensate ;anJ(s) ta or"#$ speciation ta if thevalues are greater than oreual to 01 tpy

gation


27/60

Crude +il Storage !an"



Crude +il !an"-:

!an" emissions are made up of different components6 or"ing6 breathing and flash l



E$# ;#&MB 0This softare is a!aila"le for donload at .epa.#o!$ttn$chief$softare$tanks$inde%.html

orJing reathing

VOCs, C>

en!ene

;oluene

E en!ene

=ylenes

n9he'ane






VOCs, C>

en!ene

;oluene

E en!ene

=ylenes

Crude oil is defined as heavy, lo* volatility oil appro'imated y a DO6 less than 1,


28/60

n9C8

++;rimethylp


29/60

Notes:



sses.




6ollins, @cCain, and Creeger correlations

lash losses

VOCs, C> VOCs, C>

en!ene en!ene

;oluene ;oluene

E en!ene E en!ene

=ylenes =ylenes

n9he'ane n9C8

+,+, 9 ;rimethylpentane +,+, 9 ;rimethylpentane

#ny #dditional "#$ (if applicale): #ny #dditional "#$ (if app

#nnual Emissions

VOCs, C>

en!ene

;oluene

E en!ene

=ylenes

arrel and an #$- gravity less than 0°

Valid @ethods for Crude Oil (Qse one of the follo*ing

accepted methods):

Vasue!9eggs correlation


Back to Wo


30/60

n9C8



31/60

00000

00000

00000

00000

00000

00000

00000

licale):

00000

00000

00000

00000

tons per year

00000

00000

00000

00000

00000

6eport VOC emissions on CrudeOil ;anJ(s) ;a

6eport "#$ emissions on CrudeOil ;anJ(s) ta or "#$ speciationta if the values are greater thanor eual to 01 tpy

6eport VOC emissions on CrudeOil ;anJ(s) ;a

6eport "#$ emissions on CrudeOil ;anJ(s) ta or "#$ speciationta if the values are greater than

kbook NavigationTab.


32/60


33/60

*roduced Fater Storage !an"



*roduced Fater !an"-:

Company's 5ni7ue Identification Number:




E$# ;#&MB 0?This softare is a!aila"le for donload at .epa.#o!$ttn$chief$softare$tanks$inde%.html

orJing reathing

VOCs, C>

en!ene

;oluene

E en!ene

=ylenes

n9he'ane






VOCs, C>

en!ene;oluene

E en!ene

=ylenes

n9C8

++;rimethylp

?-t is possile to create a mi'ture in the E$# ;#&MB program similar to the composition of the produced*ater stored in the tanJs (eg, a mi'ture of . *ater and 1. condensate) to determine the emissions



34/60

Notes:



sh losses.




lash losses

VOCs, C> VOCs, C>

en!ene en!ene

;oluene ;oluene

E en!ene E en!ene

=ylenes =ylenes

n9he'ane n9C8

+,+, 9 ;rimethylpentane +,+, 9 ;rimethylpentane

#ny #dditional "#$ (if applicale): #ny #dditional "#$ (if appli

#nnual Emissions

VOCs, C>

en!ene;oluene

E en!ene

=ylenes

n9C8



Vasue!9eggs correlation

Back to Workbook NavigaTab.


35/60

00000

00000

00000

00000

00000

00000

00000

cale):

00000

00000

00000

00000

tons per year

00000

0000000000

00000

00000

00000

00000

6eport VOC emissions on

$roduced ater ;anJ(s);a

6eport "#$ emissions on$roduced ater ;anJ(s)ta or "#$ speciation ta ifthe values are greater thanor eual to 01 tpy

6eport VOC emissions on$roduced ater ;anJ(s);a

6eport "#$ emissions on$roduced ater ;anJ(s)ta or "#$ speciation ta ifthe values are greater thanor eual to 01 tpy

tion


36/60

!urbine &mission Calculations 0fueled by natural gas1



!urbine -:

;urine rating (@@tu4hr):

Operating hours4year:

pollutant emission factor (l4@@tu)? tpy

VOC 000+1 0000

0+ 0000

? Emission actors from #$9+, Chapter , ;ales 191 and 19+a

Company's 5ni7ue IdentificationNumber:

&O=

Back to Workbook Navigation T


37/60

Non,lare Combustive Devices



+ther -:

(eneral Information &missi

Emission actors for aste Das Btream(s) (l4@@scf)

&O' 100

Ies

Emission actors for $ilot Btream (l4@@scf)

&O' 100

Ies

Emission actors for #dded uel Btream (l4@@scf)

&O' 100

/

Stream Information

Stream Sent to lare No. 9 < ; ? >

$ilot(s) e': oil tanJ e': *ater tanJ

$il t( ) il t J t t J


091 Fhat "ind of device isthisG &nter a shortdescription of the devicetype.

Emissio(l4@@s

0


38/60


39/60

(+ 4ethod for &stimating lash &missions



!an"-:

$ &nter variables into

$ &missions ill be in

Das Oil 6atio: in standard cuic feet of flash gas per arrel (BC4l) of oil4condensate pro

arrels of Oil or Condensate per day:

!his information is based on an analysis submitted by the applicant. lash Das @

lash Das Bpeciation:

mole . *eight . ;otal

&itrogen +/01/ 0 23-V405

CO+ 00% 0 23-V405

"+B 0/1// 0 23-V405

methane (C1) 180+8 0 23-V405 VOC *

ethane (C+) 0080 0 23-V405 en!ene *eig

propane (C) 0%8+ 0 23-V405 ;oluene *eig

i9utane (C) %/1+++ 0 23-V405 Ethylen!ene *eig

n9utane (C) %/1+++ 0 23-V405 =ylene *eig

i9pentane (C%) )? 11+ 0 23-V405

nonane (C>)? 1+/+8 0 23-V405

decane (C10>)? 1++ 0 23-V405 Contaminant !

en!ene


40/60

'ylenes (@, $, O) 10818 0 23-V405 ethylen!ene 23

undecanes (C11>)? 1%81 0 23-V405 'ylene 23

;O;#AB: 00000 0 23-V405 n9he'ane (C8) 23

? -f @ of heptanes plus is given, you can change the value in the tale aove

? -f the @ of the total sample is given, you can adFust the @ of heptanes> until the Klash Das @K value aove euals the value on the la rep


41/60

o%es

bo%es

0

mitted:

0

23-V405

23-V405

23-V405

23-V405

23-V405

23-V405

6eport ;otal VOC emissions on theappropriate tanJ ta

Back to WorkbookTab.


42/60

6eport "#$ emissions on theappropriate tanJ ta or "#$speciation ta if the values aregreater than or eual to 01 tpy


43/60

&%ample irst page of a (I,()HCalc eport:

Controlled egenerator ith lash !an"


44/60

Controlled egenerator &missions section e%ample:

lash (as &missions section e%ample:

5ncontrolled egenerator ith lash !an"

5ncontrolled egenerator &missions section e%ample:

6eport these emissions asthe uncontrolled4controlledregenerator emissions

;otal VOC is 1+/8 tpy forthis e'ample for the

uncontrolled 4controlledregenerator emissions

6eport these emissions as

the flash tanJ emissions

;otal VOC is 0018/ tpy forthe flash tanJ emissions forthis e'ample


45/60


5ncontrolled egenerator ith lash !an" ith recycle/recompression option

5ncontrolled egenerator &missions section e%ample:

6eport these emissions asthe Kuncontrolled4controlledregenerator emissionsK

;otal VOC is +1+%1 tpy forthis e'ample for theuncontrolled 4controlledregenerator emissions

6eport these emissions asthe flash tanJ emissions

;otal VOC is 0018/ tpy forthe flash tanJ emissions forthis e'ample


46/60


6eport these emissions asthe Kuncontrolled4controlledregenerator emissionsK

;otal VOC is +1+%1 tpy forthis e'ample for theuncontrolled 4controlledregenerator emissions

&o emissions to report for flashtanJ that isrecycled4recompressed Ioumay leave this section lanJ orenter !eros


47/60

Back to Glycol Dehydrator Tab.


48/60




49/60



50/60


51/60

&K* !an" &%ample


52/60

AooJ for the KCalculation 6esultsK Bection ofthe EP$ ;anJ printout for emissions data

rom the KControlled Nton4yrK column, readthe VOCs, C> emissions ;his is your;otal VOC emissions (or this e'ample


53/60

-C Engines Aist of ;ypes

+ BtroJe Aean

BtroJe Aean

BtroJe 6ich

+ BtroJe Aean BtroJe Aean BtroJe 6ich

&o' (0910%. Aoad) 1< 0/ ++1

&o' (W0. Aoad) 1 0/< ++<

CO (0910% Aoad) 0/8 01<


54/60

luorene 1


55/60

O-AE6

&O= CO

)arge Fall ired 0922 44Btu/hr1 , 100 /



)arge Fall ired 0922 44Btu/hr1 , +/0 /

esidential urnaces , 0 2.1 5nco 0Small Boilers 0922 44Btu/hr1 , Co %0 /

Small Boilers 0922 44Btu/hr1 , Co + /

Small Boilers 0922 44Btu/hr1 , 5n 100 /

!angential ired Boilers 0ll1 , )o


56/60

Caron ;etrachloride

Chloroen!e

Chloroform

Chrysene

Cyclohe'ane

cyclopentane

Ethylen!eneEthylene 3iromide

luoranthene

luorene

ormaldehyde +/0E90

-soutane

@ethanol

@ethylcyclohe'ane

@ethylene Chloride

n9"e'ane

n9&onane

n9Octane

n9$entane&aphthalene %0E90%

$henanthrene

$henol

$ropane

$yrene

Btyrene

;oluene

Vinyl Chloride

=ylene9u


57/60

Distillate +il , Fater,Steam InTec)andfill (as , 5ncontrolled

+0E901 10E901


58/60

+/0E90

%0E90%

110E90

10E90%


59/60

Natural (as , )ean *remi% Natural (as , 5ncontrolled Natural (as , Fater,Steam InTection

0E90+ +0E901 10E901

1%0E90+ /+0E90+ 00E90+

0E90

+10E90 +10E90 +10E90

880E90 880E90 880E90

10E90 10E90 10E90

00E90% 00E90% 00E90%

80E908 80E908 80E908

1+0E90% 1+0E90% 1+0E90%


60/60

+0E90% +0E90% +0E90%

calculation sheet2.xls

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