P.1 

RCRA Box 1883 

Prepped by Ollie Stewart 

Document Number: 

96) ll-B-258 

Docket Number: 

A-90-19 

Printed 12/3/200810:42:16 AM Sheet 96 of 171 
P.2 

RADIAN 

CORPORATIO N 

MEMORANDUM 

A-90-19 

ll-B-258 

DATE: December 22, 1991 

TO: HON Project File 

FROM: Bart Ferrero 

SUBJECT: Baseline Emissions Methodolog. 

jj)ILLLLU1ljj] 

!Fi'' SEP I 41992 ;iA' 

CKET j 

rocess** Vents 

The purpose of this memorandum is to describe the 

methodology used to estimate process vent emissions from U.S. 

facilities in the "baseline case" (prior to the enactment of the 

HON regulations) and to present the total industry baseline 

emission estimates. The control status of process vents 

throughout the country varies considerably. Some process vent 

sources are totally uncontrolled where others have varying 

degrees of control as a result of Federal, State or local 

regulations. Calculations are illustrated by the example 

presented in Attachment A. 

Model process vent streams were assigned to represent the 

uncontrolled emissions from a process unit. The model assigned 

to each process vent stream had an associated production capacity 

(Gg/yr), uncontrolled HAP emission rate (Mg/yr), and VOC 

uncontrolled emission rate (Mg/yr). These uncontrolled emission 

rate factors were derived based on previous EPA studies, 

questionnaire responses under Section 114 of the Clean Air Act 

and testing data and were expressed on a mass of pollutant per 

production basis (i.e., Kg VOC/Gg of product). The emission 

factors of a HON vent stream were developed as the ratio of the 

model HAP emission rate to the model production capacity. 

Process unit specific production capacity data were multiplied by 

the appropriate model vent stream emission factor to derive 

uncontrolled VOC and HAP emission estimates from each vent. 

bemethod(htm OD(ts) 

Progress Center/3200 E. Chapel Hill Rd./Nelson Hwy./P.O. Box 13000/Research Triangle Park, N.C. 27709/(919)541-9100 
P.3 

Uncontrolled HAP Emissions = cap * Ehap 

M, cap 

Where:

 scap = Stream Production Capacity 

Mcap = Model Production Capacity 

Ehap = Model HAP Emissions Rate 

Uncontrolled VOC Emissions = CAP * E 

M, cap 

voc 

Where:

 scap = Stream Production Capacity 

Mcap = Model Production Capacity 

EVoc = Model VOC Emission Rate 

An example of an uncontrolled emissions calculation is presented 

in Attachment A. 

Adjustments were made to the uncontrolled emission estimates 

where appropriate to reflect emission controls required by the 

vinyl chloride NESHAP and State regulations. The regulations 

were evaluated to develop estimates of the required control 

efficiency based on equipment or emission limit requirements. 

The control efficiency applied for VOC was assumed to apply to 

4 .. . 

HAP as well . The controlled or baseline emissions were 

estimated by applying the level of control required by the 

regulation to the calculated uncontrolled emissions: 

Baseline Uncontrollled 

Emissions = Emissions * 

Estimates Estimate 

(100 - % Control) 

100 

An example of a baseline emissions calculation is presented in 

Attachment A. For vent streams that were not assumed to have 

emission or control requirements at the State or federal level, 

baseline emissions were equal to the uncontrolled emissions. 

Using the described methodology, the total baseline 

emissions for each product process were then calculated by 

bemethod(htm 01)(ls) 
P.4 

summing the individual vent emissions at every process vent using 

a specific product process. Attachment B contains the 1989 VOC 

and HAP baseline emission estimates for each of the 13 6 Category 

A product processes. As described in previous submittals, 

Category A product processes are those where available 

information is judged to be of sufficient quality for regulatory 

decision making. The emission values presented in Attachment B 

reflect combined totals for air oxidation vents, reactor vents, 

and distillation vents from all process units. The columns 

titled minimum and maximum show the range of emissions from the 

individual process units using the product process. Attachment C 

presents the emissions distributed between vent types for each 

product process. 

Attachment A contains an example calculation presenting the 

baseline emissions calculation for the product process 

chloronitrobenzene production via nitration of chlorobenzene. 

cc: Project File 6.1 (M. Haley) 

Thomas R. Olsen, Radian 

bemethod(htm OD(ls) 
REFERENCES 

1. Memorandum from Ferrero, B. J., Radian Corporation, to HON 

Project File. "HON Process Vents Model Assignment." 

December 17, 1991. 

2. Memorandum from Olsen, T. R., Radian Corporation, to 

Evans, L., EPA/CPB. "Development of Model Emission Source 

Characteristics for SOCMI Process Vents." 

September 17, 1991. 

3. Memorandum from Olsen, T. R., Radian Corporation, to 

King, B., Radian Corporation, "Vinyl Chloride NESHAP 

Interpretation into the Process Vents Framework." 

October 11, 1991. 

4. Memorandum from Ferrero, B., Radian Corporation, to 

Evans, L., EPA/CPB. "HON Control Technology for HON Process 

Vents." November 19, 1991. 

bemethod(htm OD(ls) 
P.6 

ATTACHMENT A 

EXAMPLE BASELINE EMISSIONS CALCULATION 

FOR 

CHLORONITROBENZENE PRODUCTION VIA NITRATION OF CHLOROBENZENE 
P.7 

Example Baseline Emissions Calculation 

PURPOSE: 

The purpose of this attachment is to present an example of 

calculating the baseline HAP and VOC emissions for a product 

process. The product process selected as the example is 

chloronitrobenzene production via nitration of chlorobenzene 

(product process number 100005A). 

APPROACH: 

As identified by the SOCMI characterization, this product 

process is classified as having a reactor and a distillation 

vent. The process reaction is nitration and the distillation 

column was classified as a vacuum operation. Two process units 

have been identified as producers of chloronitrobenzene by the 

nitration of chlorobenzene. The process unit specifications are: 

Process Unit 1 has a capacity of 38.6 gigagrams and is located in 

St. Clair County Illinois, and Process Unit 2 has a capacity of 

27.3 gigagrams and is located in Salem County, New Jersey. 

Model process vent streams are assigned to each facility. 

For this example process unit, two model vent streams are 

assigned based upon the classification of the process vents as 

determined by the SOCMI characterization. Since there is not a 

compound-specific model available for chloronitrobenzene 

production by nitration of chlorobenzene, the generic nitration 

model and the generic vacuum distillation model are assigned. 

Shown below is the methodology for developing the uncontrolled 

and baseline emissions for each vent for each of the facilities. 

bemethodChtm OD(ls) 
P.8 

Emissions Calculations for Process Unit Number 1 

Reactor Model Description: 

The generic nitratio n model has the following 

characteristics: 

Nitration Model Production Capacity: 48.12 Gg/yr; 

Nitration Model Uncontrolled HAP Emission: 38.16 Mg/yr; 

Nitration Model Uncontrolled VOC Emission: 38.16 Mg/yr. 

Uncontrolled Reactor Emissions Calculation: 

The uncontrolled emissions are calculated for the 

chloronitrobenzene product process by scaling the reactor 

emissions by the nitratio n model and the process unit capacities, 

The uncontrolled emissions are : 

Uncontrolled HAP Emission = Model HAP Emission * Process Unit Capacity 

Model Capacity 

Uncontrolled HAP Emission - 38.16 Mg/yr * (38.6 Gg/48.12 Gg) 

Uncontrolled HAP Emission = 30.61 Mg/yr 

Uncontrolled VOC Emission - Model VOC Emission * Process Unit Capacity 

Model Capacity 

Uncontrolled VOC Emission - 38.16 Mg/yr * (38.6 Gg/48.12 Gg) 

Uncontrolled VOC Emission = 30.61 Mg/yr 

bemethodChtm OD(ls) 
P.9 

Baseline Reactor Emissions Calculation: 

Since Process Unit Number 1 is located in St. Clair County, 

Illinois, the State regulation requires reactor emissions to be 

controlled if the emission cap of 31 Mg/yr is exceeded. Since 

the HAP and VOC emissions are both less than the emission cap, no 

emission control is required by the State of Illinois. 

Reactor Baseline HAP Emission = 30.61 Mg/yr 

Reactor Baseline VOC Emission = 30.61 Mg/yr 

Vacuum Distillation Generic Model Description: 

Vacuum Distillation Model Production Capacity: 85.35 Gg/yr; 

Vacuum Distillation Model Uncontrolled HAP Emission: 6.62 Mg/yr; 

Vacuum Distillation Model Uncontrolled VOC Emission: 12.71 

Mg/yr. 

Uncontrolled Vacuum Distillation Emissions Calculation: 

The uncontrolled emissions are calculated for the 

chloronitrobenzene product process by scaling the vacuum 

distillation emissions by the vacuum distillation model and the 

process unit capacities. The uncontrolled emissions are: 

Uncontrolled HAP Emission «• Model HAP Emission * Process Unit Capacity 

Model Capacity 

Uncontrolled HAP Emission » 6.62 Mg/yr * (38.6 Gg/85.35 Gg) 

Uncontrolled HAP Emission =2.99 Mg/yr 

Uncontrolled VOC Emission = Model VOC Emission * Process Unit Capacity 

Model Capacity 

Uncontrolled VOC Emission = 6.62 Mg/yr * (38.6 Gg/85.35 Gg) 

Uncontrolled VOC Emission * 5.75 Mg/yr 

bemathod(htm 01)(Ls) 
P.10 

Baseline Vacuum Distillation Emissions Calculation 

Since Process Unit Number 1 is located.in St. Clair County, 

Illinois, the State regulation requires reactor emissions to be 

controlled if the emission cap of 31 Mg/yr is exceeded. Since 

the HAP and VOC emissions are both less than the emission cap, no 

emission control is required by the State of Illinois. 

Vacuum Distillation =2.99 Mg/yr 

Baseline HAP Emission 

Vacuum Distillation =5.78 Mg/yr 

Baseline VOC Emission 

betnethod(htn) 01) (ls) 
P.11 

Emissions Calculations for Process Unit Number 2 

Reactor Model Description: 

The generic nitration model has the following 

characteristics: 

Nitration Model Production Capacity: 48.12 Mg/yr; 

Nitration Model Uncontrolled HAP Emission: 38.16 Mg/yr; 

Nitration Model Uncontrolled VOC Emission: 38.16 Mg/yr. 

Uncontrolled Reactor Emissions Calculation: 

The uncontrolled emissions are calculated for the 

chloronitrobenzene product process by scaling the reactor 

emissions by the nitration model and the facility capacities. 

The uncontrolled emissions are: 

Uncontrolled HAP Emission = Model HAP Emission * process unit capacity 

model capacity 

Uncontrolled HAP Emission = 21.65 Mg/yr 

Uncontrolled VOC Emission = Model VOC Emission * process unit capacity 

model capacity 

Uncontrolled VOC Emission = 38.16 Mg/yr * (27.3 Gg/48.12 Gg) 

Uncontrolled VOC Emission = 21.65 Mg/yr 

bemethod(htm 01)(ls) 
Baseline Reactor Emissions Calculation: 

Since Process Unit Number 2 is located in Salem County, New 

Jersey, the State regulation is based on vapor pressure and the 

weight percent. Using the HAP/VOC weight percent and 

chloronitrobenzene vapor pressure, the State required a minimum 

control efficiency of 83 percent. No control device is 

specified. 

Reactor Baseline HAP Emission = Uncontrolled HAP * (1 - 0.83) 

Reactor Baseline HAP Emission = (21.65 Mg/yr) * (1 - 0.83) 

Reactor Baseline HAP Emission =3.6 8 Mg/yr 

Vacuum Distillation Generic Model Description: 

Vacuum Distillatio n Model Production Capacity: 85.35 Gg/yr; 

Vacuum Distillatio n Model Uncontrolled HAP Emission: 6.62 Mg/yr; 

Vacuum Distillatio n Model Uncontrolled VOC Emission: 12.71 Mg/yr. 

Uncontrolled Vacuum Distillation Emissions Calculation: 

The uncontrolled emissions are calculated for the 

chloronitrobenzene product process by scaling the vacuum 

distillatio n emissions by the vacuum distillatio n model and the 

facilit y capacities. The uncontrolled emissions are : 

Uncontrolled HAP Emission = Model HAP Emission * process unit capacity 

model capacity 

Uncontrolled HAP Emission = 6.62 Mg/yr * (27.3 Gg/85.35 Gg) 

Uncontrolled HAP Emission » 2.12 Mg/yr 

Uncontrolled VOC Emission = Model VOC Emission * process unit capacity 

model capacity 

Uncontrolled VOC Emission = 12.71 Mg/yr * (27.3 Gg/85.35 Gg) 

Uncontrolled VOC Emission =4.0 6 Mg/yr 

bamethod(htm OD(ls) 
P.13 

Baseline Vacuum Distillation Emissions Calculation: 

Since Process Unit Number 2 is located in Salem County, New 

Jersey, the State regulation is based on vapor pressure and the 

weight percent. Using the HAP/VOC weight percent and 

chloronitrobenzene vapor pressure, the State requires a minimum 

control efficiency of 83 percent. No control device is 

specified. 

Vacuum Distillation = Uncontrolled Emission * (1 -Efficiency) 

Baseline HAP Emission 

Vacuum Distillation =2.12 Mg/yr * (1 - 0.83) = 0.36 Mg/yr 

Baseline HAP Emission 

Vacuum Distillation = Uncontrolled Emission * (1 - Efficiency) 

Baseline VOC Emission 

Vacuum Distillation =4.06 Mg/yr * (1 - 0.83) = 0.69 Mg/yr 

Baseline VOC Emission 

b method (htm 01) (ls) 
P.14 

Total Product Process Baseline Emissions 

The total product process emissions are determined by adding 

the baseline HAP and VOC emissions for each vent for the two 

process units. The total product process baseline emissions are: 

Total Baseline Reactor Emissions: 

Total Reactor = Process Unit 1 Emissions + Process Unit 2 Emissions 

Total Reactor HAP = 30.61 Mg/yr +3.68 Mg/yr = 34.29 Mg/yr 

Total Reactor VOC = 30.61 Mg/yr +3.68 Mg/yr = 34.29 Mg/yr 

Total Baseline Distillation Emissions: 

Total Distillation = Process Unit 1 Emissions + Process Unit 2 Emissions 

Total Distillation HAP =2.99 Mg/yr + 0.36 Mg/yr =3.35 Mg/yr 

Total Distillation VOC =5.75 Mg/yr +0.69 Mg/yr =6.44 Mg/yr 

Total Product Process Emissions: 

Total Emissions = Total Reactor + Total Distillation 

Total Emissions HAP = 34.29 Mg/yr +3.35 Mg/yr = 37.64 Mg/yr 

Total Emissions VOC = 34.29 Mg/yr +6.44 Mg/yr = 40.73 Mg/yr 

b«n«thod(htm 01 His) 
ATTACHMENT B 

CATEGORY A PRODUCT PROCESS BASELINE EMISSIONS 
Product-Procoaa (P-PI Raaallm 

(•lation Sourc* Tvaa 

Cal ••Ions Sourca Tvo* 

Procaaa Vanta 

Paaa I e« S 

r-r is 

IOOOOSA 

108210*. 

1002108 

180414* 

1*04 M S 

1004 258 

I00447A 

I00SI4A 

100*70* 

I0I488A 

10177**. . 

101848* 

I0SS77A 

I0S4OM 

10*4 tM 

I0444S8 

1048*8* 

I04»*0* 

to***os 

107028* 

1070SIA 

I07O42A 

I07ISI* 

I07IS1A 

107184* 

I07I848 

1*721IA 

187222* 

107880* 

1081*1* 

188247* 

toni M 

108441* 

I08VO7A 

I0*»I8* 

•00*4IA 

icmu 

IMtM * 

P-P DaacrlaMva HW I 

CM.OMWITMMtMICNI <P-IS0nC*l VIA NITRATION OF CNLOKOSCHIEMt 

TCRCPHTMALIC AC IS VIA 011 DAI I OH OP MIU M 

TCRSPMTHALIC AC IP VIA HYSROLYStt OF DMT 

CTMVLSCNICNC VIA ALKYL*! ION OF BCN2CIC Ml TO CTMYLCMC 

STYMNC PM8UCTI0N VIA MMTOHOCSNATIOM OF CTNYLSCMfMt 

STTCCMC VIA SCHYRRATIOH OF HCTHYL BCNIYL ALCOHOL 

RCMIYL CM.0MIRC VI A CMLORINATION OF TOLUEMI 

StHIYl ALCOHOL VIA HYDROLYSIS OF SCNIVL CM.0MIK 

NCIAMTMYLCNCTCTRAHIIaT. VIA AOOITIOM OF AflNMIA TO FOMMLKMTK 

HSI VIA WACTIMS 4.4 ACTMVlf MEOIAMILINC MITM PHDS6CISI 

4.4-nCTMVLCNCBIANILINC VIA COMCNSATION OF ANILINC MITM FORHALSCMYSC 

8IPHSNVL 01 IOC VIA HVBMLYS1S OF CMLOHOOCHICMC 

ACCTAL VIA COHOCHSATIOH OF CTHANOL AHO ACCTALRCMYR 

CAPMLACTAtl PMOUCTIOM VIA SCASMAHSCICMT OF CYCLOMMMMC 

•YLCHC IP-I VIA PURIFICATION OF III II R ITLCIC 

CRSSOLS/CMSYLIC ACISS (P-ltOflCRI VIA ALKALI FUSION OF TOLIKMC SULPOMATCS 

CPICMLOMHYMIM VIA CMLOMHYDRATIOH OF ALLYL CHtOAIDS 

OUTASICMC VIA CATALYTIC SSFOOIMTIOH OF C4 STACMTS 

SUTAOICMC VIA KMYWOSCNATIOH OF C4 COHPOUMS 

ACMLCIN VIA OIIDATIOH OF PROPVLCNC 

ALLYL CMLOMIDI VIA MALOCCMATIOH OF POOPCMC 

CTMYLCMI *ICML0*IK VIA CM.OHIHATIOH/OIYCMLOAIMATIOH OF CTMYLCMC 

ACRVLOHITRILC VIA AIR 011 OAT I OH OF PROPYLCM 

CtHYLCNCSIAnlNC VIA KHTSROHALOCCNATIOH OF CTNYLCM SICM.ORIOE 

ALLYL ALCOHOL VIA HYMOLYSIS OF ALLYL CMLORIM 

ALLYL ALCOHOL VIA ISOnCRIIATION OF PROPCMC 01 ISC 

CTMYLCM CLVCOL VIA HYSROLYSIS OF CTNYLCMS OII K 

SLYOIAL VIA AIR OIISATIOM OF CTMVLM SLYCOL 

SUTTLCMC SLYCOL (I.S- 1 VIA NYMOSCNATIOR SF ACCTALOOL 

PMPYLCMC GLYCOL nOHOHCTNYL CTICR VIA ALCOHOLY. PROPYLCM OII K OY IKTHAHOL 

VIHYL ACCTATC VIA OIYACSTYLATI OH OF CTMYLCMC 

HCSITYL OII M VIA KHYSRAIIOM OF SIACtTOJC AHS MYSROGCMATIOH OF DOURLC OOMO 

ACCTIC AAMYSOIK VIA AIR OIIRATIOM OF ACCTALBCHYK 

IMLSIC AHMT—IK VIA AIR OIIBATIOH OF RUTINS 

RCSOHCIMOL VIA SULFOHATI FUSIOH PROCCSS 

CMLOMOSCMtCHC VIA MALOSCMTION OF KNIb C 

CYCLOMITLAfllNC VIA NYSROSSHATIOH OF AHILIMC 

CVCLOHCIAHOW VIA HYMNCCMATIOH OF PHtMOL 

PWHOL VIA ACI* CLCAVAC* OF CUTKW HYOROPCROIIK 

CTRYLOC SLYCOL IKMVSTM. CTWIR VIA ALCOOLYSIS OF CTHTLCIC OII K RY IKTHA. 

U.S. 

p-p 

Capacity 

<«• / Vr> 

*S.* 0 

2*54.50 

IU.I O 

4215.00 

1405.00 

S44.00 

40.7» 

L I S 

40.1 J 

4IS.IS 

141.SS 

11.40 

0.00 

401.00 

1*40.00 

11.40 

210.2V 

11*0.00 

M l . 00 

11.SO 

2O4.0O 

•242.00 

I2OS.00 

20.00 

21.24 

22.24 

2*14.00 

2.SO 

11.40 

41.00 

I2SS.00 

04.40 

114.74 

202.00 

l». M 

140.20 

• .00 

272.00 

1414.00 

II.SO 

—~ 

•4 

Facllttla a 

2 

4 

1 

• 

S 

1 

I 

1 

4 

5 

S 

17 

1 

1 

S 

1 

2 

10 

1 

1 

2 

1 * 

4 

1 

1 

1 

I I 

1 

1 

4 

S 

1 

1 

s 

• 

1 

2 

1 

* 

7 

•Uxlaua 

NAP 

120.57 

4105.40 

2.4J 

12.1 * 

4444.5* 

1204.54 

17.14 

7.42 

40.17 

1M.* I 

204.17 

0.00 

0.00 

0.00 

1174.OS 

41.04 

411.40 

240.02 

1740.04 

2.41 

0.00 

S2.7S 

11*7.10 

I . M 

0.07 

40.42 

0.00 

21.SS 

S.24 

47.74 

2.74 

SO. 71 

27*7.44 

8110.48 

44.10 

440.40 

S7.SI 

• 471*.OS 

0.00 

20.47 

Baaallna Caiaalana <lta / Yrl 

VOC 

IIS.2 7 

4107.SI 

2.41 

12.24 

7001.77 

1535.45 

45.17 

S.SS 

S I . 17 

410.77 

251. » l 

0.00 

0.00 

0.00 

1444.44 

74.12 

540.12 

107. SJ 

2154.IR 

4.S7 

0.00 

101.22 

274S1.2S 

2.0 * 

0.07 

74.8* 

0.00 

S*.47 

4.4 * 

58. *2 

1.04 

102.74 

75IS.02 

8248.24 

57.15 

1007.41 

111.45 

4044.45 

0.00 

25.25 

Procaaa Unit 

Mal i 

HAP 

2 *. 28 

I17S.7* 

2.41 

l.»7 

»4».17 

1204.54 

7.04 

7.41 

8.01 

4.1 * 

S.S7 

0.00 

o.os 

0.00 

1.27 

41.8* 

225.48 

4.8 * 

17*8.0* 

2.41 

0.00 

5.40 

20.01 

1.40 

0.07 

40.42 

0.0 * 

21.SS 

5.2* 

21.78 

2.I I 

40.17 

27*7.44 

41.05 

44.10 

255.41 

87.81 

471*.05 

0.00 

20.47 

Solaalona 

VOC 

10.7 * 

1174.14 

2.* 1 

l.» 7 

1157.18 

1515.45 

8.80 

a.aa 

10.22 

7.41 

4.* I 

0.00 

0.00 

0.00 

1.52 

74.12 

287.21 

5.44 

2154.18 

4.57 

0.00 

4.40 

144.11 

2.0 * 

0.07 

74.8* 

0.00 

54.47 

4.4 * 

10.22 

2.5 * 

51.17 

7515.02 

41.75 

57.15 

257.54 

111.45 

4044.45 

0.00 

25.25 

Avar*** 

HAP 

74. »1 

1*40.17 

l.» l 

11.41 

4041.42 

1204.54 

22.41 

7.42 

24.48 

140.81 

47.04 

0.00 

0.00 

0.00 

251.51 

41.84 

128.4* 

•0.7 8 

1748.04 

2.41 

0.00 

14.74 

457.44 

I.VO 

0.07 

40.42 

0.00 

21.85 

5.24 

I * . 74 

2.55 

41.88 

2747.44 

2414.22 

44.10 

701.44 

87.81 

4714.05 

0.00 

20.47 

VOC 

84.51 

14*1.10 

2.* 1 

11.44 

4424.11 

1515.45 

27.77 

8.88 

11.45 

202.42 

58.51 

0.00 

0.00 

0.00 

M l . 02 

7*. 12 

417.77 

115.40 

2154.18 

4.57 

0.00 

42.50 

1)012.00 

2.0 * 

- 0.07 

74.8* 

0.00 

5*. 47 

4.4 * 

44.14 

2.82 

81.2 * 

7515.02 

2412.21 

57.15 

707.-07 

111.45 

4044.45 

0.00 

25.25 

Total 

CalaaIon* 

HAT 

14*.85 

21*42.1 * 

I . M 

104.47 

12112. M 

1204.54 

47.82 

7.42 

104.71 

804.10 

21S.12 

O.OS 

0.00 

0.00 

2012.21 

41.8 * 

457.18 

»07.7» 

1748.0* 

2.41 

0.00 

555.85 

1444.41 

I.VO 

0.07 

40.42 

0.00 

ii.as 

S.24 

218.5* 

12.75 

1*1.41 

2747.»4 

11081.10 

44.10 

2105.81 

175.41 

471*.05 

0.00 

141.28 

VOC 

1*4.0* 

214*7.70 

2.41 

104.78 

1*40*.84 

1515.45 

81.11 

8.88 

IIS.8 2 

1011.11 

2*2.45 

0.01 

0.0 0 

OOO 

24081.1* 

74.12 

815.54 

IIS*.0 1 

2154.18 

4.57 

0.00 

47*. »4 

7807*.81 

2.0 * 

0.07 

74.a * 

0.00 

5 *. 47 

«.«* 

2*4.11 

14.14 

241.87 

7515.02 

110*1.05 

57.15 

2121. «0 

221. M 

•0*4.45 

0.00 

17*.77 
P-P IS 

I0*«*7A 

II0IS4R 

II0I78A 

HOBOS* 

IIOMI* 

110877* 

111*418 

III441C 

1117*2* 

111*44* 

112872* 

IISIOM 

IISII7B 

IIS77SA 

1170*8* 

IIMI** 

11*414* 

120*14* 

120*14* 

121142* 

I2II42B 

121**7* 

121*15* 

I2S0I2* 

I21M8A 

12111** 

12111*8 

121*11* 

121*118 

121*1IC 

I24110* 

124*48* 

I27IS4* 

1271848 

111*771* 

114814* 

1151*1* 

1108814. 

I4I122A 

I4I41SA 

P-P Daacrlatlva Naaa 

Product-Procaaa (P-P) Baaalln 

Ealaalon Sourc* Tvaa 

U.S. 

lalaalona Sourca Tvaa 

Procaaa Vont* 

12/20/*! • Pova 1« H 

Saaalina lalaalona (It* / Yrl 

Procaaa Unit Calaatona 

BICTMVLAMNS VIA CTMVLATION OF AIRSMIA 

SUCCINIC ACIB VI * NVOMOLYSIS OF CTMYLSNS RICYANIDC 

FISMBIC ACIB VIA NYBNATION OF MLSIC ANHYMIK 

CTHYLCM SLYCOL MHOCTM. CTHCR VI * ALCOHOLYSIS OF CTHYLOSI OII K SY CTNAMOL 

PYRIBIW VI * CONDSHSATIOM OF ACSTALRCMVK AMB POBnRLSCMYK 

CYCLOMIAMC VI* HTSMtCHATIOH OF SCHICK 

ABIP0HIT8ILS VI* ASOIIIOM OF HVSMSSN CYAHIR TO BUTABICK 

ABIPONITMILS VI* UICIMMYRKOSIMSIIATlaN OF ACRYLONITRILC 

CTMYLCW SLYCOL HSH08. CTHCR VI * ALCOHOLYSIS OF CTHYLCM OII K BY BUTANOL 

DICTNVLtW SLYCOL RI M THYL CTMCB VI * MVBBOCCNATIOH OF BCSHH CTHCR 

•TMYLSK SLYCOL IWM08UTYL CTMCB ACCTATC VI* CSTCRIFICATIOH OF C.S.M.CTMCB 

OinCTMYL CTMCB (M.M-I VI * CATALYTIC BCHYRaATION OF HCTHAHOL 

ISOOUTYLCM VIA CRACK INC OF HTK 

PCNTACRYTMIITPL VIA ABBITION OF FOMIALKHYK TO ACCTALSCHYK 

TCTRACM.OMPMTMALIC ARMVBBIK VIA HALOCCNATIOH OF PHTHALIC ANMYBRIK 

BSMIOIN VIA CSTCRIFICATIOH OF SCHIALBCMYK 

BCHtOPMCNOM VI* ACYLAT10H OF KHICMC « BCNIOVL CM.ORIB 

BCNIYL BCMIOATS VIA CSTCRIFICATIOM OF SKNIYL ALIOH 

DIHCTHYL TCRCPMTHALATC VI * CSTCRIFICATIOH OF TPA 

OINITN0T0LUCJSI 12.4-t VI * NITB*TION OF NITBOTOLUCW MITU M 

BIHITBOTOLUDC 12.4-1 VI * NITRATION OF MITROT0LUCMCIP-) 

DIMSTMVLANILIM VI * ALKYLATIOH OF ANILIK 

ISOPHTHALIC ACIB VI* AI* 011 BAT I ON OF H-IYLIHC 

LIMA * ALKYLKMKRC VIA ALKYLATIOH OF N-CMLOMPMRAFFINS 

MIIMPMM L «P-> VIA HVRNOSCNATION OF MITNOFMCMOL 

HYOHOOUIMDMC VI* SUINONS RC8UCTISN 

HYSROQUINOM VI * RIISOPDOPYL-RCMICNI HYBROPCMIIK CLCAVAtC 

BIOIAtRl <l.4-» VIA CYCLIC RCHYSKATION OF B1SLYC0L 

BIOIAM U.4- 1 VI * CTNYLSM OII K MYO*MinCRIlATIOH 

BIOIAHC II.4- 1 VIA •CHYOKMALOSCMATIOH OF CM.OROHYORI* 

SULFSLAM VI * AS8III0H OF SULFUN SIOII K TO BUTABICK 

acoagpasK vi* RCMYD*OIIALOMHATION OF I.4-BIOCOBO-I-BUTCK 

PCRCHLOMCTMYLCM VI * CMABIH*TIM OF CTMYLCMC BICM.MIK 

PMCNLONOCTMYICHI VI* OIVCMLOBIMATION OF CIMYLCK 8ICW.0BIK 

CMSOLS/CKSYLIC ACIDS (Mill VIA KCOVCRY FROH fPCMT RCFIMCRY CAUSTICS 

KM1IL VIA CAMONYLATIOH OF CHL0BO8CN1CM 

HAPMTHOL IR-IIOKR) VIA OIIOATIOM ILCAMACC OF ISOPROPYL NAPMTHALCK 

•THYL aCBYLATC VI * CSTCRIFICATIOH OF ACRYLIC ACID RY CTHYL ALCOHOL 

BUTYL ACBYLATC IH-ISOnCR> VIA CSTCRIFICATIOH OF ACRYLIC AC 10 

STHAMLAMM VIA AHMMOLYSIS OF CTHYLCK OII K 

Capacity af Haxlaai 

<C« / Yr) Facllttla a HAP 

57. M 

1.18 

18.00 

41.40 

27.20 

884.45 

272.00 

40.00 

1*1. M 

0.2 * 

2.50 

27.20 

ISO. 00 

71.00 

2.SO 

O.OS 1 

0.7S 

O . M 

128*. M 

171.00 

57.00 

1.00 

124.70 

SS4.S4 < 

0.00 

5.40 

10.70 1 

1.80 

1.80 

1.80 

7 . M : 

22.50 

2M. M 9 

•O. M 

71.70 1 

0.01 3 

IB.10 1 

111.00 1 

125.04 J 

IM.4 0 9 

1 57. M 

1 O. M 

I 5*.1 1 

F 20.0* 

1 01.24 

1 O. M 

1 204.OS 

1 »2.2I 

1 SI.4 * 

1 2.12 

1 7.44 

1 121.72 

1 *2.* 2 

1 7S.4I 

1 1.01 

1 0.01 

1 1.4* 

r o.u 

1 1054.44 

1 111.41 

111.41 

1 S. M 

21.7* 

1 275.42 

O . M 

12.42 

1 12.44 

1.* * 

1.84 

4.17 

1 8.18 

54. M 

t 1». M 

208. M 

1 11.4* 

1 O. M 

51.4* 

12.41 

1.01 

O . M 

VOC 

71.44 

O . M 

72. M 

14.7* 

•01.05 

O . M 

25*.47 

118.2* 

*».2 1 

2.BS 

* . M 

152.44 

117.72 

M.* 7 

1.12 

0.01 

2.12 

0.04 

4245.12 

154.55 

IS*. 55 

7.07 

5*. 11 

12*. 41 

0.01 

15.81 

14.0* 

S . M 

2.17 

4.17 

10.BS 

54.40 

4 *. 14 

2*1.25 

17. M 

O . M 

42. J * 

11*4.18 

4.«S 

O . M 

ninlaua 

HAP 

1.1 * 

O . M 

22.74 

0.S4 

SB.41 

O . M 

!.•» 

42.21 

45.»l 

2.22 

7.44 

121.72 

*.* 2 

.5.1 2 

I.OI 

0.01 

I . M 

0.01 

1011.18 

1.21 

III.4 1 

S.*2 

21.7* 

1.40 

O . M 

12.42 

11.04 

1.* * 

1.84 

4.17 

8.18 

54.40 

I.S* 

2M. M 

2.54 

0.00 

51.44 

0.45 

i.ai 

0.00 

VOC 

I . M 

O . M 

28.04 

0.70 

72.41 

O . M 

S . M 

IIS.24 

S*.4 I 

2.85 

• .10 

152.44 

12.24 

4.77 

1.12 

0.01 

2.12 

0.04 

1404.71 

1.75 

154.55 

7.07 

5*. 11 

4.11 

0.01 

15.81 

14.11 

S . M 

2.17 

4.17 

10.B5 

54.40 

1.41 

241.25 

1.04 

O . M 

42.10 

21.41 

4.45 

O . M 

Avaraaa 

HAP 

14. *4 

O . M 

40.44 

20.21 

44. *4 

0.00 

115.a* 

*2.2 I 

44.8* 

2.22 

7.44 

121.72 

51.27 

41.42 

1.01 

0.01 

1.44 

0.01 

2214.04 

44.42 

111.41 

S . M 

21.7* 

B4.5* 

O . M 

12.42 

I I . B7 

!.»» 

1.S4 

4.17 

S.1B 

54.40 

21.14 

2M. M 

14.21 

0.00 

51.44 

11.15 

1.01 

0.00 

VOC 

42.4* 

O . M 

50.50 

25.05 

04. M 

O . M 

172.41 

IIB.2 * 

40.45 

2.85 

*.» 

152.44 

44. M 

55. R* 

1.12 

0.01 

2.12 

0.04 

1102. M 

55.48 

IS*.55 

7.07 

S». 11 

101.21 

0.01 

15.81 

15.10 

S . M 

2.17 

4.17 

10.85 

54. M 

24.15 

241.25 

17. M 

O . M 

42.18 

442.41 

4.«S 

O . M 

Ealaal 

HAP 

104.52 

O . M 

81.87 

141.40 

11*.aa 

O . M 

407.44 

•2.2 1 

174.8 * 

4.44 

7.44 

121.72 

102.54 

111.75 

1.01 

0.04 

1.4* 

0.2 1 

4702.11 

11*.04 

111.41 

11.as 

21.7 * 

118.15 

O . M 

12.42 

21.71 

1.* * 

1.84 

4.17 

14.7* 

S4. M 

105.7* 

2M. M 

42.41 

0.01 

51.44 

44.74 

7.4 * 

O . M 

•na 

VOC 

128.** 

O . M 

101.01 

ITS. IS 

171.* * 

O . M 

510.70 

110.2* 

485.2 1 

S.71 

* . M 

152.44 

12*. *7 

147.4* 

1.12 

O . M 

2.12 

0.28 

•M8.« 5 

1*7.05 

IS*.5 5 

• 4.14 

S*.l l 

404. M 

O.OI 

IS.BI 

M.2 0 

S . M 

2.17 

4.17 

21.4 * 

S4.40 

IM.7 4 

241.25 

SI.0 1 

0.01 

42. M 

2444.55 

» . M 

O . M 
Product- ion* Sourc* Tyaa 

P-P Daacrlatlva Naaa 

I414044A 

I414044C 

I742M4 * 

2SIS4SIM 

ISI47800* 

28122481* 

28122**4* 

254*72*4* 

2*471425* 

2*741400* 

274*7814* 

27SS424M 

SI2 

84*841* 

S42IS* 

S42I5S 

S4aisc 

57554 * 

5*4421* 

MISS * 

«24S14* 

42*11 * 

42511B 

441*7* 

441*7* 

47*41 * 

47441* 

•74418 

Mill * 

M l 228 

4*727* 

7I2S8* 

71412* 

714128 

7I4I2C 

MTHYL TSRT BUTYL CTHCR VI* CTHCRIFICATION OF ISOSUTYLCK AMI KTMAMOL 

MTMYL TCBT BUTYL CYWB VI* ISOKRIIATION OF BUTAMS . 

ATRWHIUH THIOCYAHATC VIA PVROYSIS OF AMMlU n OITHIOCARBOHATC 

NONVLPMNOL VIA ALKYLATIOH OF PHCMOL 

OA.0H0PMH0L5 VIA MYSMLYSIS OF CHLOMMNICM 

POLYCTMYLCM SLYCOL VI * POLYM* I IAT IOH OF CTHYLCM SLYCOL • CTHYLCM OII K 

POLYP80PVLCM SLYCOL VI* POLYMR OF PROPVLCM OII K AM PHOPYLCM SLYCOL 

CFC-22 VI * HALOSCMATIOH OF CHLOROFORM 

TOLUCM BI1S0CYAHATIS VIA OINITMTION OF TOLUCM MITM PHOSCtCHATtOH 

BIISOKCYL PHTHALATC VIA CSTCRIFICATIOH H/PHTHALIC MBTYMIK A*8 KCAMOL 

SNOHONAPHTHALCM VI* HALOSCMATIOH OF NAPHTHALAN 

SI ISOOCTYL PHTHALATC VI* CSTCRIFICATIOH Itl PHTHALIC AMHYSBIM 4 OCTYL ALCOH 

FOaHALKHYK FROH RCHYBMSSMATIM OF WTHAHOL 

BIHITHOPMCHOL 12.4-1 VIA HYBMLVSIS OF 2.4-BIMITR0CML0*0BSMlCM 

TRIMTHYLPCMTAM 12.2.4-1 (•-> VI* ALKYLATIOH OF ISOSUTYLSM AMB IS0-8UTANI 

CAHROH TCTMOCORIH VIA CMLMIHATION OF CARBON BISULFIK 

CARBON TSTBHCIB.OBIK VI* CMLO*IN*TION OF HVBBOCAMBOMS 

SLYCIM VI * AHHONOLYSIS OF CMLOAOACSTIC ACIS 

SLYCSBOL VI * MYSNOLYSIS OF CPICM.0MOHVMIH 

PHOPYIIM SLYCOL VI* HYSN0LYS1S OF FROPYLCM OII K 

PCNCMLOaOHCTHYL KBCAPT M VIA NALOGCMATION OF CAMBON BISULFIK 

HCSTMIIK VI * RISTILLATIOH OF AmOHIUH ACCTATC 

MTHYL ISOCYAHATC VIA PHOSCINATIOH OF MTHYLAHIM 

MHILIM VI * HYRN0CCNAT10H OF NITBOBCNICW 

AHILIM VIA AfllHOLYSIS OF FMHOL 

ACCTIC ACIS VI * C*SSONYL*TIM OF MTHAHOL 

ACSTIC ACIS VIA 01 IBM ION OF *CSTALBCMYK MITH CATALYST 

BIOIOLAHS VI * COMCMSAIIOH OF SLYCOL AHO FOrUMLDCMYM 

KMIOIC ACIB VIA 011 BAT I OM OF TOLUCM 

HCTMAHOL VI * NYRaOSCMRTIOM SF CAMOH ItOHOIIDS 

CMLoaoFoan VI A HALOKMATION OF H I THYL CHLMI K 

CMLONOFORn VI * HMLOSCNATIOM OF MTHAM 

BIMTMY L Foan*niM VI A CARBOHTLATIOH OF OIMTNYLAHI M 

BIMSTMYL FORI WHIM VIA AnlMOLYSIS OF MTHYL F0MMTC 

SALICYLIC ACIB VIA HVSNOFISNIYLATION OF SOQlUr) PMHATC 

HYSaOFOaRYLATIOH SF CTHYLCM TMM KVBROCCHATIOH OF FROPIONALSCNYK/OIO PROC 

RCHICM VIA CATALYTIC RCFOMIM OF NAPHTHA 

KNIC M VIA MTSNOKALKYLATIOH/IRAHSALKYLATIOM OF TOLUCM 

RCMCM VIA HTSMSCNATIOH OF PYROLYSIS SAS 

Ea!aalon Sour 

U.S. 

P-P 

Capacity 

( 6* / Yrl F 

1101.07 

SIS. 70 

7.74 

1*1. M 

17. M 

241.20 

120.40 

142.17 

151.15 

704.40 

O . M 

704.40 

1I7B. M 

1I11. M 

O . M 

0.25 

na. M 

14*. M 

I . M 

IS. M 

422.10 

11.42 

0.50 

ia. ia 

171.07 

M.7 2 

IISS. M 

1M. M 

2.50 

•7.40 

4IB4. M 

200.50 

14.50 

4.50 

• .20 

24. M 

•1.10 

2M1. M 

20)0.00 

ISS4.M 

Miiatar 

o l 

•Cllltl l 

17 

1 

1 

I I 

2 

I S 

10 

12 

* 

I I 

2 

I I 

28 

1 * 

1 

1 

1 

4 

1 

1 

5 

2 

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2 

I 

1 

4 

2 

1 

I 

10 

4 

1 

1 

2 

4 

1 

14 

17 

12 

Baaolln* Caiaalana (IH / Yr) 

Proc*** Unit Cal**!on* 

Hintaua 

VOC HAP VOC 

12/20/4! • Paa* 1 o« 5 

Total 

Ca!a*lon* 

241.47 

1144.5* 

11.71 

2.44 

20. IS 

204.50 

54.40 

O . M 

I7M.S4 

S2*.l » 

O . M 

52*.1 * 

1101.48 

ISM . 40 

0.00 

0.5 * 

2*1.72 

»*.BI 

1.44 

0.7S 

IOS. M 

IB. 48 

1.14 

41.15 

1.28 

412.41 

21* . 44 

1512.41 

12.84 

554.21 

27157.45 

24.4* 

S . M 

12.04 

20. »2 

1027* 2 

415.01 

258.44 

47*.47 

281*.45 

2B*.21 

1457.11 

14.1 * 

5.04 

24.15 

254.77 

4».sa 

O . M 

2172.51 

442.12 

O . M 

442.12 

1144*4 

151*. M 

0.00 

0.71 

111.0* 

127.01 

2.02 

O . M 

124.42 

21. M 

1.40 

SI.01 

I.2B 

S04. M 

275.** 

1004.70 

15.4* 

ISM . 72 

12*44.40 

M.4 4 

M.I * 

14.54 

25.01 

1118.20 

702.04 

HI.* * 

B7V.S4 

M22.I 5 

2.75 

1144.5* 

11.71 

0.1 * 

20. IB 

4.14 

B.l* 

O . M 

21.01 

27. M 

O . M 

27. M 

B.24 

7.24 

O . M 

0.5 * 

2*1.72 

I . M 

1.44 

0.70 

1.17 

S.I * 

1.14 

20. SB 

1.07 

412.41 

1*.*4 

57.40 

12. S4 

1*.5* 

242.41 

4.87 

8.0 * 

12.04 

20. M 

42.05 

11.41 

4.25 

48.71 

11.74 

1.2* 

I4S7.I I 

14.48 

0.74 

24.15 

7.SS 

10.10 

O . M 

2 *. 74 

11.84 

O . M 

11.84 

10. M 

7.25 

O . M 

0.71 

III . 04 

2.01 

2.02 

O . M 

1.7* 

4.44 

1.40 

24.14 

1.07 

SO*. M 

50.2 1 

72.84 

IS.* * 

107.77 

111.41 

.•.SO 

II.1 * 

14.54 

25.81 

Sl. M 

14.51 

B.S7 

127.77 

l*.) 0 

M.7 * 

1144.54 

11.71 

1.15 

20.18 

42.48 

44.44 

O . M 

774.07 

14*.84 

O . M 

14*.84 

2*4.45 

555.7* 

O . M 

0.5 * 

2*1.72 

M.O* 

1.44 

0.78 

14.20 

11.44 

1.14 

M.* 7 

1.17 

412.41 

127.05 

7*5.11 

12. B4 

281.72 

5758. M 

14.1 * 

8.0 * 

12.04" 

20. *2 

501.11 

212. • ! 

77.74 

272.24 

274.44 

70.14 

1457.11 

14.4* 

2.5* 

24.15 

7R.24 

55.2 * 

O . M 

*04.28 

204.51 

O . M 

204.51 

141.52 

554.14 

O . M 

0.71 

111.04 

M.2 4 

2.02 

O . M 

44. * l 

14.51 

1.40 

M.S4 

1.17 

SO*.M 

IS*. 78 

•M.7 7 

IS. M 

772.M 

4471.24 

22.47 

11.14 

14.54 

25.01 

442.42 

270.71 

102.20 

ISO.54 

154.4* 

»**.47 

1144.5* 

15.20 

14.81 

40. M 

»44.70 

444.42 

O . M 

4444.44 

1848.2* 

O . M 

1848.2* 

SM4. M 

10540.04 

O . M 

0.5 * 

2*1.72 

252.22 

4.41 

0.78 

IM. M 

2I. M 

2.27 

4 1 . M 

1.51 

412.41 

5M.2 2 

15*0.22 

12.8* 

051.14 

S75M.5 I 

M . M 

a.o* 

12.04 

4i.as 

2004.45 

4M.7 4 

2441.11 

4420.M 

1114.07 

11*4.15 

1457.11 

41.4 1 

28.44 

48.2 * 

1171.54 

552.00 

O . M 

5*05.4 8 

2271. as 

0.0 0 

2271.88 

10122.41 

10544.72 

0.0 0 

0.71 

111.0 * 

120.* 8 

4.0 4 

O . M 

114.54 

M.O * 

2.81 

77.17 

1.51 

SO*.08 

41*.1 1 

1877.51 

IS.* * 

2117. M 

40712.1 * 

IM.0 1 

I I . 1 * 

14.54 

SI.4 1 

2570.SO 

812.20 

1474.72 

SM4.4S 

4280. M 

_V 

a> 
Product -Procaaa IP-PI Saaallna lalaalona Sour.. Ty»a 

Calaalon Sourca Tyaa * Procaaa Vanta 

12/20/*! Paaa 4 o< 5 

P-P IS P-P Daacrlatlva Haa* 

7ISS4A 

7I8S4S 

7481** 

74871* 

W I M 

TRICMLOROCTMAM (I.I.I- I VI * HYOROHALOMMATION OF VINYL CHLOR I U 

TRICHLOMCTHAM II.I.I- I VI * HALOSCHATIW OF STHAM 

MTHYL BROniK VI * HALOSCMATIOH OF MTHAHOL 

MTMYL CMMI K VI * MVBROHALOSCNATION OF MTHAHOL 

MTMYLAMMS VIA MTHYLAtlOH OF MVBHIA 

CTHYL aUaiH i VI* HY**OCHL0*INATI0H OF CHTYLCM 

CTHYl CMMI K VI * HYSMCHLMINATIOH OF CTHAHOL 

VINYL CHLSMIK VIA KMYBBOrM* OMBATIOH OF CTHYLCM BICHOBIK BY TMRnAL 

7SOI4B 

7*070* 

7*1278 

7*1*0 * 

7*218* 

7SJS4* 

7S44S* 

.2-TRICML0MSTHAM 

7**44* 

7SS4M 

7*4»4A 

7*72*A 

74111* 

77781* 

7B»HA 

7 * 

7*014* 

7*0*1 * 

7*0*4B 

7*1*7* 

7*118* 

7*IIB 8 

7*18** 

7»S4*A 

7*S4SB 

8MS7A 

•BIS** 

8*42*A 

B44S1A 

VINYL CMLOMIK VI * HYBMMALOCCHAT MH OF ACCTYLCM 

*CSTAL*CMTM VIA AIR SUMMON OF CTHYLCM 

PORHMIK Ml* *MnONOLVSIS OF MTMYL FONHATS 

CAMOH BISULFIK VIA SULFOHATION OF MTHAM 

CTHYLCM OII K VI * Al* OIIBATIOH OF CTHYLCM 

VINYLIK M CMOBIK VIA MHYBROCM.MINATIOH OF I.I . 

Fl—CCM VI * HALOSCHATIM OF CARBON HOHOIIM 

CFC-142 VI * HALOECHATIOH OF M.O M COMPOUNDS 

PMPVLSM eiiK vi* KMYKOTIALOSCMAT ION OF PROPVLCM OCONOHYMIH 

PHSPTLSM OII K VI * CPOIIBATIOH OF T-BUTYL HYRROPCMIIK 

CFC VI* LIOUIB PHMS CATALYTIC MACIIOH 

CMSMT8IFUMI0MTM M VI* FLUOalMTIOM SF CHLOM COMPOUNM 

TaiCta^NOTRIPLUOMCTHAM VIA HALOCCHATIOH OF FCBCM.OBHTHYLSM 

BIMTNYL SULFATC VI * CSTCRIFICMTION OF MTHYLC.S. S SI-H.S. 

TCTMSTMYL LCA* VI * AMIIIOH OF CTNYL CM.08IM TO LSA8-SMIUH ALLOY 

MTMYL CTNYL KCTOal VI* MHYSaOSCHATIOH OF S-BUTYL ALCOHOL 

T*ICMLSMCTM*M (1.1.2-1 VIA HALOECHATIOH OF VINYL OLO*I K 

TRIOCBMSTMAM U.I.2- 1 VI * NAL06SNATI0N OF CTHYLCM 

TRICMJMCTMVLCM VI * CM.OBIMRTIM OF CTHYLCM BICMOBIK 

•orvuwiK VIA in—LYSIS OF ACRYLMITAILS 

FMFIONIC ACIB VI* Al* SIIBATION OF PHOPIOHALKHYK 

ACRYLIC ACIB VI* OIIBATIOH OF ACMLCIN. ACBOLSIN FBin OIIBATIOH OF PMPYLSN 

CW.OROACTTIC ACIB VIA HALOSCMATIOH OF ACCTIC ACIS 

OCOROACCTIC ACIB VI * MYSNOLVSIS OF CM.ORJMCSTVL CM.MI K 

MTMYL ACSTATC VI * MYBRSLYSIS OF POLYVINYL ACC1AU BV MTHAHOL 

TSTHACMLSBOCTHMM (1.1.2.2- 1 VI* HALOSCHATIW OF ACCTYLCM 

TSTMCMONMTMAM II.1.2.2- 1 VI* HALOSCMATIOH OF CTHYLCM 

BIIPMHDL • VI * COMKHIATIOH OF FMMOL A M ACCTOM 

CUMM NYMOPCRO^IK VI* OIIBATIOH OF CUM M 

MTHYL MTMRCaYLATC VI* HYSMLYSIS AH* ALKYLATIOH OF ACCTOM CTAMOHYMIH 

• VIA BSHTBROLYSIS OF 0CH2OYLBEN2OIC ACIB 

U.S. 

P-P ftnatii 

Capacity o4 llaalau 

I S* • Yr) Facllltla a HAP 

IB5. M 

M . M 

l*. M 

SM. M 

144. M 

178. M 

S . M 

404*. M 1 

471. M 

3M. M 

I . M 

117. M 

MM. M 1 

122. M 

1114.41 1 

M.2 4 1 

4S4. M 

S22. M 

101.42 

41.72 

S3. M 

27.20 

M . M 

241. M 

104. M 

104. M 

IS4.S0 

to.00 

•1.1 0 

544.12 

• . M 

14. M 

4.S4 

M.7 5 

M.7S 

514. M 

2414. M 

S24. M 

0.21 

2 5.54 

1 17. M 

2 41.IS 

• 4.11 

4 172.»7 

4 IS. M 

1 7.41 

0 S4.l l 

2 10.11 

2 O. M 

1 4.1 * 

* O. M 

1 40.47 

2 M. M 

7 82.12 

0 O. M 

I 41.1 * 

1 1182.10 

4 42.47 

1 O. M 

1 O. M 

2 41.47 

1 M.7 0 

I 4*.25 

1 41.12 

1 41.11 

1 41. M 

1 1M. M 

1 SM.I 1 

4 IIS*.1 8 

1 24.4* 

1 12.44 

1 S. M 

I 12.70 

1 12.70 

• 11.01 

* 4114.47 

1 1724.2* 

1 1.05 

Saaallna Calaalono 

VOC 

7.10 

M . M 

S2.41 

*.l l 

4M.I S 

l*. M 

*.S2 

41.S4 

11.20 

7*4. M 

7.41 

O . M 

172*0.17 

84.40 

IM.5 5 

O . M 

47. M 

IM2.4 7 

54. M 

O . M 

O . M 

M.5 7 

17. M 

210.15 

S5.24 

S5.2* 

52.** 

124.74 

1420.09 

1217.24 

2*.87 

1*. M 

4.14 

14.2* 

•4.28 

25.02 

117*4.4* 

20*0.S* 

1.2* 

(Ha / Vr) 

Proca** Unit Ca|aal*n* 

Hlaloua 

MAP 

I.B * 

17. M 

S.7S 

l.l l 

IS.l * 

4. IS 

7.41 

IB.17 

1.20 

O . M 

4.1 * 

O . M 

0.42 

8.17 

0.44 

O . M 

l*.OI 

IIS2.I 0 

O . M 

O . M 

O . M 

14.71 

M.7 0 

0.11 

41.12 

41.12 

22.51 

21. M 

2IB.47 

14.27 

24.4* 

12.44 

S . M 

12.70 

12.70 

0.25 

77. M 

77. M 

I.OS 

VOC 

4.»7 

4B. M 

10.42 

1 1 1 

22.45 

5. IS 

».S2 

l».»2 

I.S1 

174.51 

7.41 

O . M 

181.87 

».IB 

1.20 

O . M 

20.84 

1502.47 

I . M 

O . M 

O . M 

18.12 

17. M 

1.11 

SS.2* 

SS.2* 

28.8* 

25.12 

5*4.71 

H.S * 

2 *. 07 

S*. M 

4.14 

14.2a 

14.20 

0.47 

20*.B2 

•1.44 

1.2* 

*varaaa 

HAP 

4.72 

17.50 

24.04 

4.12 

1*4.4* 

10.2* 

7.41 

M.5 2 

5.77 

O . M 

4.1 * 

O . M 

7.54 

44.21 

27.07 

O . M 

11.11 

1102.10 

25.28 

O . M 

O . M 

20.20 

M.7 0 

M . M 

41.12 

41.12 

11. M 

52. M 

404.7* 

115.I I 

24.4* 

12.44 

S . M 

12.70 

12.70 

4.48 

1S47.04 

4*7.** 

1.05 

VOC 

4.04 

M . M 

.:' n.si 

4.12 

2M. M 

12.4* 

*.S2 

42.24 

7.17 

5*4.44 

7.41 

O . M 

1201.02 

44.7* 

14.71 

O . M 

14.11 

1502.47 

12.17 

O . M 

O . M 

14.45 

17. M 

140.55 

55.2 * 

55.2 * 

40.41 

' 41.28 

1107. I * 

857.S7 

2 *. 87 

M . M 

4.14 

14.28 

14.28 

11.41 

4240.01 

1147.02 

1.2* 

Total 

Calaalaa 

HAP 

4.45 

17.SO 

52.1 1 

14.58 

745. *4 

41.04 

7.4 1 

MS.2 2 

II.S S 

O . M 

4.1 * 

0.0 0 

M . M 

M . M 

4M.2 4 

0.00 

42.22 

1102.10 

151.45 

O . M 

0.00 

54.41 

M.7 0 

M.B 2 

41.12 

41.12 

•1.8 1 

IS8.44 

811.* • 

I2M.SS 

14.4 * 

12.44 

10.S* 

12.70 

12.70 

27. »4 

I41I0.S4 

2M1. M 

I . M 

-

a 

VOC 

12.07 

48.08) 

41.05 

14.58 

MO. M 

4».»7 

• .52 

422. M 

14.7 1 

1112.4) 

7.4 1 

0.0 0 

41411.24 

•i.sa 

S M . IS 

O . M 

48.2 2 

IS02.47 

• M. M 

0.0 0 

O.OO 

48.8 * 

17. M 

421.44 

SS.2 * 

SS.2 * 

81.82 

18*.8 1 

2214.78 

1411.48 

2*.8 7 

M . M 

12.47 

14.28 

14.28 

SS.44 

M4I2.1 I 

SSM . 44 

1.2* 

TJ 

CO 
Product -Procaaa (P-P) Saaallna Calsalon* Sourca Typa 

Cataalon Sourca Typ* • Procaaa Vanta 

12/20/41 r Paaa S o« 5 

P-P IB P-P Daacrlatlva Haa* 

A M SUTABICM 

! M M 

UIHOM VI * COM8CNSATI0H SF NAPMTHASUIN 

WHOM VI * HYBRMIMRIIATIOH OF STYACM 

PHTHALIC AAMVMIK VI * Al* OIIBATIOH OF O-IYLCM 

PHTHALIC AHMTMIM VI * Al* SIIMTION SF NAPHTHALSM 

PSHTACMLRMPMMOL VI * H4LRSCHATI0H OF PMMOL 

CTHYL TH I I*8 W VI * STNVLATIM OF fTIIULMC 

HAPTHALCM F80N PtTBOLSWI BCALKVLATION 

MPNTMALSM FMOTI COAL TA* BIST ILLATION 

BIPMHTL VI * BSMVSaaSCMTION OF B8MICM 

IVLSM (•-) VI * FMCTIOHAL SISTILLATION SF HI ICO IVLSM 

CM.0MTOLUCM (B-l VI * HALOSCHATIM OF TOLUCM 

RCHICM SULFONIC ACIS VI* COHTIMUOUS SULFONATION M/ OLCUM 

BSN2CM SULFONIC ACIB VI* SULFONATIOH S COHTIMUOUS CITRACTION 

RCHICM SULFONIC ACIS VIA SULFONATION S RCHOHAL OF I M 

TOLUCM SULFONYL CMLMIK VIA MAC! I OH OF TOLMM M/ CMLOSOSULFONIC ACIB 

CUMM VI * ALKYLATItN OF BSNICM MITM PMPVLCM 

BBM18VL OCOBIK VI * MACT ION OF KNIOIC ACIB « M SCMOTRICM.ORIK 

HITMSSMISM VIA MITBATIM OF RCHICM 

U.S. 

p-p 

Capacity 

<6* / Yr) 

0.12 

0.11 

424. M 

102. M 

IS. M 

1.44 

M . M 

102. M 

4.47 

421.84 

12.20 

70. M 

15.15 

IS. M 

2.72 

214S.M 

4.10 

444. M 

Nuofcor 

o4 

Facllltl* * 

1 

1 

S 

1 

1 

1 

2 

2 

1 

4 

I I 

2 

4 

rlaalau*) 

HAP 

0.42 

0.17 

71*4.1 * 

17. M 

8.81 

14.** 

122.81 

1*8.47 

7.24 

141.84 

11. M 

144. M 

81.42 

82.S* 

O . M 

• .12 

M4.2S 

Saaallna Cala*lona 

VOC 

0.77 

0.4 * 

7SSS.M 

40.51 

12.21 

20.41 

151.51 

184.44 

B.S2 

144.10 

17. M 

IM.2 8 

M.4 1 

M.4S 

O . M 

I I . M 

M4.2 * 

(It* / Vr) 

Procaaa Unit Caiaalana 

Hlataua 

HAP 

0.42 

0.17 

140.4* 

17.81 

a.ai 

I4.S4 

20. S* 

7*. 24 

7.24 

.

 s-** 

11. M 

144.02 

83.42 

82.S* 

O . M 

4.12 

II. M 

VOC 

0.77 

0.4S 

140.11 

4B.S1 

12.21 

20.41 

24.11 

M.B 1 

B.B2 

0.41 

17. M 

IM.2 B 

M.4 1 

M.4 5 

0.00 

II.so 

11.04 

Avara** 

HAP 

0.42 

0.17 

1M».»7 

17.01 

0.01 

l*.S* 

71.40 

IIR.05 

7.24 

M.0 4 

II. M 

1*4.02 

81.42 

82.5 * 

O . M 

4.12 

I7».* 7 

VOC 

0.77 

0.45 

1425.41 

48.51 

12.21 

20.41 

M . U 

142.24 

8.S2 

15. M 

17. M 

IM.2 S 

M.4 1 

M.4 5 

O . M 

II. M 

17*.47 

Total 

Calaaloma 

HAP 

0.42 

0.17 

1*44*.01 

17.81 

a. ss 

14.54 

141.17 

117.71 

21.71 

IM.2 4 

II. M 

144.02 

81.42 

82. S» 

O . M 

IS.4S 

718.44 

VOC 

0.77 

0.4S 

IM27.I I 

M.SS 

12.21 

M.4 I 

177.45 

284.4 * 

24.4 7 

2IS.7 I 

17. M 

IM.2 8 

M.4 I 

M.4 S 

O . M 

21.01 

718.44 
P.21 

ATTACHMENT C 

CATEGORY A PRODUCT PROCESS BASELINE EMISSIONS BY VENT TYPE 

b*m*thod(hta 01)(ls) 
chlor obansana 

cklarooaazana 

CT PRODUCT PROCESS MAM 

PROCESS 

I00005A Ckloronltrobaniana l*-l*eaar) via nitratio n ol 

1000O5A Cklaraaltrakaniana (p-laoaar) via nitratio n af 

I002I0A Tarapktkallc acid via oaldatlon af p-aylana 

IM2I M Tarapktkallc acid via kvdralv*!* *f OHl 

IOMI M Tarapktkallc acid via kydralyala •« SHT 

I004I4A Ctkylfcaaiana vl * alkvlatlaa al kaaxana ulth atkylana 

•004I4A Itkylkaaiaaa via alkvlatlaa af fcaaiaaa ult k atkylana 

I0O42S* Styr ana araductlan via dakydraaaaatlaa *4 atkylbanian* 

100425A Styr ana araductlan vi a aaki * aianatlan *• atkylkanaana 

I00425B Styr ana vi a dakvdratiaa a< aatkyl fcaniyl aicahol 

I00447A Baaxyl cklarlda wl* cfclarlnatlaa af taluon* 

100447* Baasvl cklarlda vi a cklarlaatla * af taluana 

I005I4A aaaiyl alcakal vi a kyaY-alyala af kaaxyl cklarlda 

I005I4A Bansvl alcakal vi a kvdralyal* af aaaiyl cklarlda 

I0M7 M Maaaaatkylaaatatraaiaa vl * addi 11 a* *4 unni i ta laraald*kyd* 

101408* M l VI * RCACTIM 4.4 MTMVLSMCSIAHILIM MITM FMOSSCM 

I0I488A M l VI * MACTI M 4.4 MTKYLCMBIANILIM MITM PMMSCM 

I0I77 M 4.4-Hatkylaaadlaalllna via ciidamatla a a4 anlllna alt k faraaldakyda 

I0I77 M 4.4-natkylanadlaalllaa vta caadaaaatlaa a4 anlllna alt k (araaldafcyda 

I0IB48* BIPMMYL OII K VI * HVSMLMIS SF CHLOROMHICM 

IMS77A Acatal vi a cmMaaatla a af atfcaaal and acataldakvd 

IOS402A Ctpralactaa pradactlan vl * raarraaaaaaat a l crclokamaaaaa 

I05M2A C**r*l*ct* a araductlan vl * raarraaaaaaat al cy*la*ia»anana 

I0442M lylaaa (*-> via auriflcatla a af al»ad aylaaa 

1044458 Craaala/craayllc acid* (p-laaaar) via alkal i fualaa *4 taluana aulfaa*t*a 

I0444SS Craaala/craayllc act da (*-l**aar> via alkal i tualaa al taluana aullanata* 

10I8IBA Eplcklarakydrla via cklar*ky*-atl* a af ally l cklarlda 

I04BMA Cplchlarakydrln via ckl*r*kyar*tl* a a l ally l cklarlda 

I04M0A Rutadlaaa via catalyti c rafaraatlaa af C4 atraaaa 

IMM M Batadlaaa vi a catalyti c rafaraatlaa af C4 atraaaa 

IM** M Batadlaaa vt* dakydraaaaatlaa af C4 caapaunda 

IMM M Batadlaaa vl * aaknara»anatlaa af C4 caaaauada 

107028* Acralala vi a aaldatlaa df praavlaaa 

•07051A Ally l cklarlda via kalaaaaatlaa af praaaaa 

I07MI * Ally l cklarlda vi a kalaaaaatlaa a* praaaaa 

107042* Etkylaa* Blcklarlda via cklarlaatlaa/aaycklarlaatlaa af atkylana 

1*70*2* Ctkylana Mcklarld a via cklarlaatlaa/aaycklarlaatlaa af atkylana 

187111* AC*YLOHIT*ILC VI * *I B 011 BAT I M OF PMPYLSM 

I07IS M Ctkylaaadlaalaa vi a dakyarakalaaaaattan af atkylana dlcklarlda 

I07IS M Ctkylaaadlaalaa via dak»«r*kalaaaa«tlaa af atkylaaa dlcklarlda 

107IMA ALLYL ALCOHOL VI * KYBROLVSIS SF ALLYL CMLMIK 

I071B4A ALLYL ALCOHOL VI * HYBROLVSIS OF ALLYL CMLMIK 

•07IBM ALLYL ALCOHOL VI * ISOMRIIATIOH OF PMPCM OII K 

1071*4* ALLTL ALCOHOL VI * ISOMRIIATIM OF PMFCM OII K 

107211A Ctkylaaa alycal via ky*V*lv*l« af atkylaaa aald* 

1*7211* Ctkylaaa alycal via kydraly*!* af atkylaaa aalaa 

•07222* SLV01M. VIA AIR SIISATION OF CTHYLCM SLYCOL 

107880* Butylaaa alycal ll.l- l vt* kyaraaanatlaa af acataldol 

I078B0A Bvtylaaa alycal (I.l- l vl * kvdraaanatlaa af acataldal 

107*02* Praavlaaa «lyc*l aoaaaatkyl alkar via *lc*H*ly . praavlaaa aald* ky aatfcanal 

P-P U.S. 

CAPACITY 

45. M 

45. M 

245*.SO 

114.10 

114.10 

42IS. M 

42IS. M 

S4M. M 

14M. M 

544. M 

40.7 * 

40.7 * 

1.18 

1.18 

M . M 

415.15 

411. IS 

142. n 

142.SS 

11. M 

O . M 

MI. M 

MI. M 

IM8. M 

IS. M 

11. M 

2*0.2 * 

2*0.2 * 

I1M. M 

I1M. M 

MI. M 

MI. M 

11. M 

204. M 

2M. M 

8242. M 

B242.M 

I2M. M 

M . M 

M . M 

27.24 

27.24 

27.24 

27.24 

281*. M 

281*. M 

2 . M 

11.40 

11. M 

41. M 

UCHT 

TYM 

0 

R 

A 

0 

R 

8 

a 

B 

R 

R 

0 

R 

B 

R 

R 

B 

a 

B 

R 

B 

R 

B 

B 

B 

8 

B 

B 

B 

B 

a 

B 

a 

A 

B 

a 

B 

B 

• 

B 

a 

B 

B 

B 

B 

B 

* 

« 

* 

* 

* 

nOSCL HAM 

DISTILLATION NV 

HITRATIM 

100210* 

IM2I M 

HYDROLYSIS 

100414* . 

100414* 

1004 25* 

100425A 

SCMCRIC MACTIOH 

OISTILLATIM NV 

HALOSSMATIM 

OISTILLATIM MV 

MYMOLYSIS 

SSMBIC MACTIM 

BISTILLATIOM MV 

SCMMIC MACTIM 

BISTILLATIOM MV 

COMCMSAIIOH 

HYBROLVSIS 

COMBSNMTIM 

105*02* 

10*402* 

BISTILLATIOM MV 

BISTILLATIOM NV 

SCMCRIC RCACTIM 

BISTILLATIOM MV 

SCMCRIC RCACTIM 

IMM M 

CATALYTIC REFORM* 

IMM M 

BSNVBB06CIMTIM 

A1B OIIMTI M 

I0703IA 

107051A 

OISTILLATIM MV 

107042* 

107111* 

BISTILLATIOM NV 

BSMYBaONALOSCMTiaN 

107184* 

HYBROLVSIS 

107184* 

SCMMIC *(ACT1M 

10721IA 

107211* 

AIA OIIMTI M 

BISTILLATIOM NV 

HYSHOSCNATIOH 

BIST1LLATIM MV 

HAP 

Hussions 

»7.5» 

52.24 

21*42.1* 

2.41 

0.2* 

15.22 

4*. 44 

OOO 

12112.M 

I2M.54 

42.71 

25.11 

7.41 

0.01 

IM.71 

114.21 

44*.S* 

IM.44 

128.M 

0.01 

0.00 

O . M 

0.00 

2011.11 

II.4 * 

M.I4 

11.51 

441.85 

18.14 

RS*.45 

4.74 

1741.M 

1.41 

O . M 

O . M 

M4.I4 

171.4* 

1*44.41 

O . M 

O . M 

O . M 

0.07 

O . M 

40.42 

O . M 

0.00 

21.85 

0.41 

4.41 

M . M 

VOC 

cm ssi OMS 

114.M 

52.24 

2IM7.78 

2.41 

0.2* 

15.21 

4*. 55 

O . M 

)*4M. M 

15)5.45 

51.12 

12.1* 

0.07 

0.01 

115.02 

1*0.42 

052.4* 

127.42 

145.01 

0.01 

0.00 

O . M 

0.00 

24M.I* 

17. M 

M.l* 

14.1* 

014.15 

18.14 

1140.4* 

4.74 

2144.42 

4.57 

O . M 

0.00 

454.7* 

220.1* 

7M74.8S 

1.12 

0.47 

0.00 

0.07 

O . M 

74.8* 

O . M 

O . M 

5*. 47 

0.74 

S . M 

110.11 

Want Typ* Kay, * • Air Oxidation. S • Slatlllatlan. R • Raactor 
pmouci 

PMCCSS 

I0O054A 

IMIOIA 

1MIOIA 

I0O247A 

1081148 

I0844M 

I0844M 

100*07 A 

I0BM7* 

I084I M 

I08*I M 

100*41* 

108*41* 

IOBMM 

IMM M 

I0M*7* 

I040*7A 

1101*48 

II0I7M 

II0I7B* 

110 

110 

110841* 

110*41* 

IIM77* 

IIM77* 

1114MB 

III4* » 

III44IC 

III44JC 

III7«2A 

III7A M 

111*44* 

111*44* 

II2072A 

112*72* 

IISI04 * 

IISIS4* 

IISII7S 

1151178 

IIS77S* 

II78BS* 

11 MM* 

11*41** 

I2MI4A 

120414* 

PRODUCT PROCESS NAM 

Proavlana slycol aonoaathyl athar vl * alcokoly. propylon* oatd* by aathanol 

Vlayl acatata via *xv*c*tyl*tlan of atkylana 

Vlayl atatat* vl * *>v*c*tyl«tl* n af atkylana 

naaltyl aald* via dakvdratiaa af diacatana aad hydraaanatlon af uoufcla kaad 

llaaltyl aalda vl * dahydratlan af diacatana aad kydraaanaliaa af daukia Band 

ACCTIC AkMVMIK VIA Al* OIIMTI M OF ACSTALSCHYK 

Halalc aakyarld* vl * air aaldatlaa af kut* 

•thyl* 

•thyla 

i anlda ay aatk*. 

i aalda by aatk*. 

claat via aulfaaata fu*l* n procaaa 

Cklarabaatana via kalaaanatlon af banian* 

CklaraBaaxaaa vl * kalaaaaatlaa af banaaaa 

Cyclakaiylaalaa vi a fcvdraaanatlan af anllla a 

Cycl*k»iiylaalaa via fcvdraaanatlan af anllla a 

Cvcl«fcaa*a*aa via ky*raaan*tlaa af pfcanal 

Cycl«k»naaa** via kydraaanatlara af phanal 

Pk*a*l via acid c I aavao* af caaaaa kydra**r*«lda 

Pkaaal vi a acid claavaa* af cuaana kydraparanlda 

Ctavlaaa alycal ai Ik . atfcar via alcakalyala • 

Ctkylaaa alycal aaaaaatk. atkar via alcakalyala a 

Bl*tkvl*al* a via atkylatla a af aaaanla 

Blatkvlaat M via atkvlatla a af aaaanla 

Succinic Acid VI * NVBBOLVSIS OF CTHYLCM SICVAHIK 

Fuaarlc acid via fcvdratlan af aalalc aakydrld* 

Fuaartc acid via kyaratlaa af aalalc aakydrlda 

Ctkylaaa alycal aaaaatk. atkar vl * alcakalyala af atkylaaa aalda by atkaaal 

Ctkylaaa alycal aaaaatk. atkar vl * alcakalyala at atkylana aalda ky atkaaal 

Pyrldlaa vl * caadaaaatlaa af acataldafcyda *ad faraaldakyda 

Pvrldtaa vl * c*ad*a**tlan af acataldahyd* and faraaldakyda 

Cycle*aaaaa vl * fcyaVaaanatlaa af fcaniana 

Cyclafcanaaa vl * kydraaaaatlan af banaaaa 

ASIPMITRILC VI* M8ITI M OF HVMOSCH CYAHI* TO BUT AO IS M 

MIPONIIBILS VI * AMITI M OF MYBROSSH CYAN IB TO 8UTMICM 

MIFONITBILS VI * CLCCT*OHY**MIMRIIATIM OF ACRVLMITRILC 

MIPWITBILC VI * CLCCT*OHVBM*IMRIIAIIM OF ACRYLMITRILC 

Ctkylaaa alycal aaaafc. atkar via alcakalyala af atkylaaa aalda ky butanol 

Ctkylaaa alycal aanab. atkar via alcakalyala af atkylana aald* by butanol 

• I atkylana Slvcal dl ant ay I atkar vl * hydraaanatlaa af daaaa atfcar 

BlatkylMd Slvcal alaatfcyl atkar via kydraaanallan af daaaa atkar 

Ctkylaaa alycal ••••Butyl atkar acatata VIA CSTCRIFICATIM OF a.*.a*.atfcar 

Ctkylaaa alycal aanabutvl atfcar acatata VI * CSTCRIFICAIIM OF a.a.afc.atfcar 

Rlaatkyl Ctkar (n.a-) VI * CATALYTIC BSMYSMTIM OF MTHAHOL 

Blaatkyl Ctkar (n.n-l VI* CATALYTIC SSNVSMTIM OF MTHAHOL 

laafcutylana vl * crackla* af MTK 

laofcutylana vl * crackla* af NI K 

Paataarytfcrltal vt* addltlaa af faraaldakyda l a acataldafcyda 

Tatracfcl*r*pfctk*llc Aakydrld* VIA HALOCCMATIM OF PHTHALIC AMHYMIK 

SCBIOIM VI * CSTCBIFICATIM.SF SCNIALSCNVK 

Baasaafcaaaaa VIA ACYLATION OF KN1CM S CCMIOYL CM.ORI* 

BSM1YL BDUOATE VIA CSTCRIFICATIM OF BCMIYL ALCOH 

Slaathvl taraafctkalata vl * aitarlfIcatla a af TPA 

P-P U.S. 

CAPACITY 

4 1 . M 

I2S5. M 

I2SS. M 

M . M 

M . M 

SI*. 74 

M2. M 

IS. M 

l*. M 

IM.2 8 

IM.2 8 

* . M 

» . M 

272. M 

272. M 

1*14. M 

1414.M 

II. M 

11. M 

S7. M 

57. M 

I . M 

IS. M 

IS. M 

41. M 

41. M 

27. M 

27.20 

M4.4S 

SB4.4S 

272. M 

272. M 

M . M 

M . M 

1*1. M 

1*1. M 

0.2 * 

0.2 * 

2 . M 

2 . M 

27.20 

27.20 

IM. M 

150. M 

71. M 

2.50 

O . M 

0.75 

O . M 

I2B*. M 

VENT 

TYM 

R 

B 

R 

B 

a 

A 

A 

B 

* 

B 

« 

B 

* 

B 

* 

B 

* 

8 

a 

B 

a 

a 

a 

a 

a 

a 

a 

a 

a 

B 

B 

a 

B 

a 

s 

a 

a 

a 

B 

a 

a 

a 

a 

a 

a 

a 

R 

R 

R 

a 

MOOCL HAM 

SCMCRIC REACTION 

10OO54A 

I080S4A 

IMIOI A 

SCMRIC REACTION 

AIR OIIMTI M 

1083148 

OISTILLATIM V 

SCMCRIC RCACTIM 

I0BM7A 

I0BM7* 

DISTILLATION NV 

HVMOSCHATIM 

IOBMIA 

HVMOSCHATIM 

IOBMM 

IOBMM 

OISTILLATIM NV 

SCMNIC MACTIM 

SISTILLATIM NV 

CSMRIC RCACTIM 

MYMOLVSIS 

SISTILLATIM MV 

SCMNIC MACTIM 

SISTILLATIM NV 

110805* 

SISTILLATIM NV 

CONKMIATIM 

110877* 

IIM77A 

II14M B 

SCMCNIC MACTIM 

III4M C 

III4M C 

SISTILLATIM V 

SCMCNIC RCACTIM 

SISTILLATIM V 

MYSaOSCNATIM 

SISTILLATIM NM 

CSTCRIFICATIM 

SISTILLATIM NV 

SCMNIC MACTIM 

SISTILLATIM MV 

SCmi C MACTIM 

SCMNIC MACTIM 

HALOCCMATIM 

CSTCRIFICATIM 

SSMRIC MACTIM 

CSTCRIFICATIM 

120*14* 

HAP 

EHISSIONS 

l)».7 ) 

11.14 

1.1 * 

O . M 

1*1.41 

2747. M 

IMSI.I O 

I . M 

42.01 

2042.01 

41.02 

21.14 

154.45 

M . U 

4424.71 

O . M 

O . M 

71.41 

4 *. 07 

SI.54 

M . M 

O . M 

41. M 

J». M 

72.82 

M . M 

41.1 * 

74. M 

O . M 

O . M 

O . M 

407.44 

O . M 

•2.21 

12.47 

M2.1 * 

• 02 

4.42 

S.81 

I . M 

41.1» 

M.I I 

4 . M 

M . M 

111.75 

1.01 

0.04 

1.44 

0.22 

4702.11 

VOC 

enISSIONS 

177.42 

11.14 

2. 78 

O . M 

241.87 

7515.02 

11041.M 

2.07 

54.47 

2042.01 

00.7* 

25.12 

IM. M 

Ill.B * 

54)0.54 

O . M 

O . M 

07.04 

M.4 1 

44. Ot 

44.04 

O . M 

50.20 

M.B1 

S7.I5 

M . M 

M . M 

M.I O 

O . M 

O . M 

O . M 

510.70 

O . M 

110.24 

24.12 

440. M 

0.04 

5.47 

4 . M 

2.12 

M . M 

74.77 

0.17 

121.40 

147.44 

1.12 

O . M 

2.12 

O . M 

4U8.4S 

Want Typa Kayi • • Air Onldatlan. 0 • Blatlllatlan . * • Raactor 
120414* 

121142* 

I2II42A 

1211428 

I21I42S 

I2I4MA 

121**7* 

I2I*I M 

I2MI1A 

I2MIM 

I21MM 

I211I M 

I21SI M 

121*11* 

121*11* 

121*1 IC 

I241M * 

I MIM A 

IMMM 

I27IB4* 

I27IB4* 

1271*4*' 

I27IBM 

111*771* 

ISMI M 

IMIM* 

IMMM 

14 

141122* 

I4II22* 

I4I41M 

I4I4IS* 

I4I4044A 

I414044A 

I4MM4C 

I414044C 

I742M4A 

I742M4A 

2SIS4U M 

2SIS4U M 

2SI47SBM 

MI4780 M 

2S12248M 

2S12248M 

2*1224*4* 

2*122444* 

2*4*72*4* 

2*47142** 

2447I42SA 

PR00UCT PROCESS MAM 

Olaatfcvl laraphtkaUt* via aatarlf Icatlon of TPA 

Blaltrataluana 12.4-1 via altratla a af altrataluana alatur* 

Blaltrataluana 12.4-1 via altratla a mt altrataluana alatura 

Blaltrataluana (2.4-1 vl * altratla a af altrataluaaa(p-) 

Blaltrataluana (2.4-1 vl * altratla a af altrataluana(p-l 

Maatfcvlaalllaa via alkyl«tl* a af aalltna 

Btaatkylaalltna vl * alkylattaa af aatlla a 

laaafctfcallc acid vl * air aalaatla * af a-ay I ana 

Llaaar altylfcaaaaaa via alkylatla * af N-ckl*rap*ra<fSaa 

Llnaar *ltylfcanaana vl * altylatla n af H-cklarapar*fflaa 

AfllMOFIKMBL Ip-I VI * MVSMCCMSTIM OF HITROPMMOL 

ilaaaa via aulaaaa raductlan 

ilaana vt* dUaaarapvl-baaaaaa fcvdraaaroalaa claavaaa 

(1.4-) via CYCLIC BSMYBMVIM OF BISLYCOL 

II.4- 1 VI * CTHYLCM MI K HYSNMIMRIIATIM 

II.4- 1 VI * aSMYSNONALMSNATIM SF OCOMNYMIH 

Sulfalana vi a adaltlaa af aalfur dl aalda t a kutadlaaa 

Sulfalana vi a addttla* af aalfur dlaalda t a Butadlaaa 

Chlaraaraaa via dak»dr«»alnaaitlan a l S.4-d!cklara-l-fcutaa* 

Parcfclaraatfcvlaaa vi a cfclarlaatlaa af atkylaaa dlcklarlda 

Parcklaraatkvlana vi a cfclarlaatlaa af atkylaaa dlcklarlda 

Parcfclaraatfcylaaa via aavcfclarlaatla* af atkylaaa dlcklarlda 

Parcfclaraatfcvlaaa via aaycfclarlaatlaa af atkylaaa dlcklarlda 

Craaala/craayllc acid* tola) via racavary 

SCNIIL VI * CAABONVLATIM OF CNLOROSCMICM 

Naafctfcal (fc-l*aaar) via aa I dat I an claavaaa af laapraarl naphthalan* 

Mapfctkal Ua-laaaar) vl * aalaatla * claavaaa of laaaraavl naphthalan* 

Ctkvl acrvlata via a*t*r!fIcatla a of acrylic acid by atayl alcafcal 

Cthyl acrylata vl * aatarlf Icatlaa af acrylic acid by atayl alcafcal 

Butyl acrvlata ta-laaaarl vl * aatarlf Icatla a af acrylic acid 

fra a opant raflaar y cauatlc* 

Butyl acrvlata tnCthaaalaalna vl * 

Ctfcaaalaalaa via aaaai 

Hatbyl tart butyl atfc 

r) vl * aatarlflcatl m af acrylic acid 

alvala af atkylaaa aalda 

•lyal a af atkylaaa aal M 

r vl * atfcarlflcatlaa af I utyl* 

utyla 

aad aatfcaaal 

Natfcyl tart butyl atfcar ul * atfcarlflcatlaa af I M and aatfcaaal 

Hatfcvl tart butyl athar vl * loaaarliatla a af bata 

Hatfcvl tart butyl atfcar vl * Imarliatla a af bata 

•Ion Thtacvaaata VI * PYBOMIS OF MHHMIiat BITHIO 

Hun Thlacyaaata VI * PYBBMIS OF aMBHIUTI BITMIS 

rlahaaal vl * altylatla n af ah anal 

•aal vl * alkylattaa af pfcanal 

Cfclaraafcaaal • vl * hydralval* af cfclarabaniana 

Cklaraafcaaala via hyaralyala af cklarak—nn * 

Palvatfcylaaa slvcal via palvaar Ha t I aa af atkylaaa alycal • atkylaaa aaW 

Palyatkylaaa alycal via aalyaarliatla a af atkylaaa alycal * atkylaaa aald 

Palvaraavlana (lycal vl * palvaar af praavlaaa aalda aad praavlaaa alycal 

Palyvraaylana alycal vl * palvaar af praavlaaa aalda and pr aay I ana alycal 

CFC-22 via fcalg—nllaa af cklarafara 

Taluana allaacyaaataa vl * dlaltr*tl* a af taluana ultfc aaaaaaaaatlaa 

Taluana allaacyaaataa vl * dlaltrctla a af taluana utt k phaaaaaaatlaa 

P-P U.S. 

CAPACITY 

I2S4. M 

171. M 

171. M 

S7. M 

S7. M 

S . M 

S . M 

124.70 

1*4.54 

1*4.54 

O . M 

5.40 

10.70 

I . M 

I . M 

I . M 

7 . M 

7 . M 

22. M 

2M. M 

2M. M 

M . M 

M . M 

71.70 

0.0 1 

18.10 

18.10 

lll. M 

lll. M 

I2S. M 

IIS. M 

IM. M 

IM. M 

1101.07 

1181.07 

SIS. M 

SIS. M 

7.74 

7.74 

IM. M 

MI. M 

M . M 

M . M 

241.20 

2*1 . M 

IM. M 

IM. M 

142.17 

151. M 

SSI.IS 

VCNT 

TYM 

R 

B 

a 

B 

a 

6 

R 

A 

B 

a 

a 

a 

a 

a 

a 

B 

a 

a 

a 

a 

a 

s 

B 

s 

* 

B 

B 

B 

a 

B 

R 

B 

B 

B 

a 

a 

a 

a 

a 

a 

B 

B 

a 

a 

a 

B 

a 

B 

B 

a 

KIK L NAM 

120414* 

SISTILLATIM NV 

I2II42A 

BISTILLATIM NM 

121142* 

SISTILLATIM MV 

ALKVLATIM 

AIM OIIMTI M 

BISTILLATIM MM 

I2MI M 

MVBBOSCIMTIM 

SCMRIC MACTIM 

SCMRIC RCACTIM 

SSMRIC MACTIM 

MY*RMIM*I!ATI « 

BCHYOMHALOtSNATII 

BISTILLATIM V 

SCMCRIC MACTIM 

BCHVBROMALOCCMATH 

I27IB4A 

HAL06CHSTIM 

1271*4* 

SCMCRIC MACTIM 

BISTILLATIM BV 

CARSOMYLATIM 

BISTILLATIM MV 

OIIMTI M 

IMS85A 

CSTCRIFICATIM 

BISTILLATIM NV 

CSTCRIFICATIM 

I4I419A 

I4I41SA 

BISTILLATIM MV 

141404 4A 

BISTILLATIM V 

SCMRIC MACTIM 

BISTILLATIM M 

SCMRIC RCACTIM 

BISTILLATIM V 

2SI5M2 M 

BISTILLATIM MV 

HYBROLMIS 

BISTILLATIM HV 

SCMRIC MACTIM 

BISTILLATIM MV 

SCMCRIC MACTIM 

254*72*4* 

BISTILLATIM MV 

HYB*OSCH*TIM 

HAP 

MISSIONS 

O . M 

IM.I S 

1.71 

IM. M 

0.S7 

11.45 

O . M 

21.7* 

1M.1 5 

O . M 

O . M 

12.42 

22.71 

I . M 

1.84 

4.17 

0.S7 

14.1 * 

S4. M 

17. M 

M . M 

*.«• 

Ml.4 1 

42.42 

0.01 

42.18 

* . M 

17.14 

14.40 

S.81 

1.84 

O . M 

O . M 

•M.4 7 

0.00 

O . M 

1141.7* 

IB. M 

17.17 

14.81 

O . M 

M . U 

0.04 

177. * 0 

SM. M 

Ml.0 1 

144.41 

0.00 

55*.44 

4084.74 

VOC 

EHISSIOHS 

0.00 

145.14 

1.71 

IM. M 

0.57 

11. M 

O . M 

S».l l 

404.*) 

O . M 

0.01 

15.01 

M . M 

S . M 

1.17 

4.17 

I . M 

M . M 

M . M 

17. M 

•11.IS 

4.4 * 

2S4.S7 

SI.01 

0.01 

M . M 

II. M 

2414.41 

M . M 

4 . M 

2.11 

O . M 

O . M 

11*4.15 

O . M 

1.54 

I4M.S7 

2 1 . S* 

21.8 * 

M.4 4 

0.00 

M . M 

O . M 

452.27 

721. M 

241.74 

111.04 

O . M 

44*.77 

52M.* I 

Want Typa «*v. A • Air Oald*tlon. 0 • Slatl I lation . A • Ructor 
CT 

PMCCSS 

Bllaaa 

Bllaaa 

Faraal 

PRODUCT PROCESS HAM 

Bllaadacyl phthalata vl * aatarlficatla n u/pfctkaltc anhydrld* and dacaaal 

Sllaadacvl phthalata vl * aatarlf Icatlan u/pat Dalle aafcvdrlde and dacaaal 

Rraaanap*thaiana vl * kalaaanatlaa af aaahtfcalana 

thai ana via kalaaanatlaa af aaahtfcalana 

t y l afctfcalata vl * aatarlf Icatla a ml pfctfcallc ankydrld* S actyl alcah 

t y l phthalata vl * aatarlflcatla a ml phthalic ankydrld* S actyl *lc*fc 

•hvda fra a dahyavaaanatlaa af aatkanal 

Foroaldafcyda fra a ««*i * imiHla a af aatfcaaal 

Faraal *•>)« • vi a air aal dat I aa af aatfcaaal 

Blaltraafcanal 12.4-1 VI * HYDROLYSIS OF 2.4-SINITROCM.OROSCMItM 

Blnltraafcaaal 12.4-1 VI * MYSROLMIS OF 2.4-BIHITMCMLOaOMHZIM 

Trlaathvlpaatana 12.2.4-1 (a-) VI * ALKVLATIM OF ISOSUTYLSM « M IM-BUTMC 

Trlaathylpaataaa (2.2.4- 1 (a-l VI * ALKYLATIM OF ISOMTYLCM A M IM-8UTAM 

Ctrbaa tatracfclarlda vl * chlarlaatlau af carban dlaulfl M 

Carta* tatrachlarlda vl * cklarlaatlan a l carbaa dlaulflda 

Carban tatrachlarlda vi a cfclarlaatlaa af fcy*-acartaa* 

Carta* tatracfclarlda vl * cfcl*rla*tlaa af fcyaVacartam 

SLVCIM VI * BIBMTII I 8F CIS.0MACBIIC *CIB 

SLVCIM VI * WSWNPLMI* SF CH.OHMCCIIC ACIB 

SLTCSML VI * HYBBOLMIS SF CPICHLOROHVMIH 

SLYCSML VI * HYSMLMIS SF CPIOCONOMYMIN ' 

Praavlaaa alycal via fcydralyal* mt praavlaaa aalda 

Parchlaraaatfcyl Karcaptaa VI * laV-OCCMATIM SF CAM M BISULFIK 

Parcfclaraaatkvl Harcaptan VI * MALOSCMATIOW SF CAM M BISULFIK 

MSTMI K VI * BISTILLATIM OF MOSMIUH *CST*TS 

MCCTAMIK VI * BISTILLATIM SF AMMIUN «CST*TS 

Hatfcvl laacyanata vi a afcaaaaaatla* mt aathylaalaa 

Matfcyl laacvaaat* vl * pfcaaaanatiaa mt aathylaalaa 

MILI M VIA IIYBB8CIMRTIM SF MITBOBSWSM 

AMILIM VIA IIISMfCMATIM SF NIT808B1UM 

MILI M VI * AHIHOLMIS 8F PNSNBL 

MILI M VIA MIMLMI S SF PMBMOL 

ACCTIC MI B VIA CAMONVLATIM OF MTHAML 

ACCTIC ACIB VI * CARSOMVLATIM OF MTHAHOL 

ACCTIC ACIB VI * MIMTI M SF ACSTALSSMVM MITM CATALMT 

ACSTIC ACIB VI * OIIMTI M SF *CST«LKMTK WI N CATALMT 

Btaaalaaa VI * COMCMMTIM OF SLYCOL A M FO 

Maaalaaa VI * COMCMMTIM SF SLVCSL M B FO 

v l * kvdraaanatlaa mt carbaa aanaaid* 

v i a fcvdraaan«tl*a a l carbaa aanaalda 

Cklarafara vi a fc*lai«aitlaa af aatfcvl cklarlda 

Cklarafara vl * balaoaaatlaa af aatfcvl cklarlda 

Cklarafara vi a kalaaanatlaa af aatk ana 

Cklarafara vl * kalaaanatlaa al aatfcaaa 

•4aatkvt farai*ld a via cartaaylatla * af dlaatfcylaalaa 

Blaatkyl faraaalda vl * carbaavlatlaa mt dlaatfcylaalaa 

Maatfcyl faraaalda vl * aalaalyal* mt aatfcvl faraata 

Blaatkyl faraaafda vl * aalaalyal* af aatfcvl faraata 

Salicylic acid vl * avarafaravMtl** a l aadlua ah an it * 

P-P U.S. 

CAPACITY 

704. M 

7M. M 

O . M 

O . M 

7M. M 

704. M 

IIM. M 

1178. M 

I1I1. M 

O . M 

O . M 

0.28 

0.2S 

118. M 

118. M 

IM. M 

I4*. M 

I . M 

I . M 

IS. M 

IS. M 

422.10 

11.42 

IS. M 

O . M 

O . M 

18.18 

IB. 18 

171.87 

271.87 

M.7 2 

M.7 2 

IIM. M 

IIM. M 

IM. M 

MO. M 

2 . M 

2 . M 

M . M 

4184. M 

4184. M 

2M. M 

2M. M 

M . M 

14. M 

4 . M 

4 . M 

* . M 

» . M 

M . M 

MCNT 

TYM 

* 

B 

B 

a 

B 

a 

8 

a 

A 

a 

a 

B 

a 

a 

a 

B 

a 

a 

a 

B 

a 

8 

B 

a 

B 

a 

B 

a 

a 

B 

B 

B 

B 

a 

B 

a 

B 

a 

A 

B 

a 

B 

a 

a 

a 

a 

B 

a 

a 

a 

HOKL NAM 

BISTILLATIM MV 

CSTCRIFICATIM 

BISTILLATIM NV 

HALOUMAIIM 

BISTILLATIM NV 

CSTCRIFICATIM 

SOOOM 

BEMYBAOCCMTIM 

SOOOM 

BISTILLATIM MV 

HYBROLVSIS 

BISTILLATIM NV 

ALKYLATIM 

S42SM 

SSMBIC RCACTIM 

SMS M 

SSMBIC RCACTIM 

BISTILLATIM M 

SSMBIC MACTIM 

BISTILLATIM NV 

HYSMLMIS 

BISTILLATIM NV 

BISTILLATIM NV 

N*LOCCN*TIM 

BISTILLATIM M 

SSMBIC RCACTIM 

BISTILLATIM M 

SCMCBIC RCACTIM 

42S1M 

•2SSM 

BISTILLATIM MV 

SCMCBIC BCACTIM 

MIM A 

CARMNYLATIM 

441*7* 

OIIMTI M 

BISTILLATIM NV 

COMCMMTIM 

• I B MIMTI M 

ATMI* 

NYSaaSSMTIM 

BISTILLATIM V 

HALOCCMATIM 

BISTILLATIM V 

HALSSCMIIM 

BISTILLATIM NV 

CAMONVLATIM 

BISTILLATIM MV 

SCMRIC MACTIM 

NYSaOFOBMYLATIM 

MAF 

cnissiOHs 

USI . 12 

SI4.V7 

O . M 

O . M 

USI . 12 

Sl*.» 7 

11.11 

B2M.72 

10540.04 

O . M 

O . M 

O . M 

0.01 

O . M 

241.72 

O . M 

M2.2 2 

2.52 

2 . M 

0.74 

O . M 

IM. M 

IS. M 

S.42 

1.17 

l.l l 

21.41 

M.S2 

L S I 

O . M 

211.42 

M l . 21 

IM.4 S 

1M.7 7 

DM.2 4 

IM. M 

S.S1 

7 . M 

01.1 4 

MIS4. M 

I14M.4 7 

IS. M 

82. M 

I . M 

4.81 

10.4* 

I . M 

21.44 

M.4 1 

2004. M 

VOC 

EMISSIONS 

1417.24 

454.42 

O . M 

O.M 

1417.24 

4S4.42 

11.13 

I01II. M 

10544.72 

O . M 

O . M 

0.70 

o.qi 

o.Oo 

lll. M 

O . M 

IM. M 

1.01 

I . M 

O . M 

O . M 

2M. M 

21.M 

7.21 

I . M 

1.41 

M . M 

SI. 11 

L S I 

O . M 

2*1.01 

2M. M 

124. M 

•12.47 

1421.11 

2*4.42 

4.»7 

*-M 

2117.M. 

SIMS. I I 

I72M.M 

M . M 

104.1* 

2 . M 

a. 74 

M . M 

I . M 

M . M 

25.47 

2570. M 

Vaat Tvaa Kavi * • Mr Oaldatlaa. * • Slatlllatlan. a • Raactar 
7I2MA 

7I2MA 

71412A 

7I412A 

7I4S M 

7I412B 

7I412C 

7I4S2C 

7ISS4A 

7IM M 

7ISSM 

7ISMS 

74S1M 

74S1M 

7487M 

7S08M 

7S0I M 

7S0IM 

7S0I M 

7MI M 

7S87M 

M U M 

M U M 

MIS M 

MIS M 

M2I M 

MIS M 

M M M 

7SS4M 

7M4 M 

M M M 

MS4 M 

7MM * 

7*4*4* 

M72 M 

M7M * 

74IS M 

74111* 

777*1* 

77MIA 

7B002A 

PRODUCT PROCSSS NAM 

Hydrofaraylatlaa af atfcylaaa tfcaa hydraaaaattaa af praalaaaldafcyd*/*** pro 

•Vayafaravlatl M af atkylaaa tfcaa hv*>»aaa*tlta af araplaaaldahyda/aaa pra 

IIMII I via catalytic rafarala * af aaaktha 

Bi«ik*k vi a catalvti c rafarala * af aaaktha 

> vi a fcy*r****lkylatlaa/traaaalkylrtlaa af taluana 

v l * fcy*V*da*lkyl*tla*/tr****ltrlotl** af taluana 

v i a *> • noaillo a af pyralyala s*a 

v l * fcvdraaaaatlaa a l pyralyal* a** 

Trlcklaraathana (1.1.l- l vl * fcydr*fc*laaaa*tl*a mt vlayl cklarlda 

Trlcklar•atktaa (I.I.I- ) vl * fcy+'afcal mmtla a a l vlayl cfclarlda 

Trlcklareattaa* (1.1.I- I vl * talaaaaatlaa af atktaa 

Trickier******* (I.I.I- ) vt* talaaaaatlaa af atfcaaa 

tatkvl fcraalda via fcalaaaaatiaa af aatkanal 

tathvl kraald* W * talaaaaatlaa af aatfcaaal 

Hatfcvl cklarlda vi a fcvdrafcalataaatlaa a f aatfcaaal 

aatfcvlaalaa* via aatfcvl*tI*a mt aaaaai* 

Natbylaalna* via aatfcyl*tl*a a l (aaaal* 

Stfcyl cklarlda vi a byarachlarltatlaa a l aktvlan* 

Ctfcvl cklarlda vi a fcydracfclf laatlt a •* aktvlaaa 

Stfcyl cfclarlda vi a hv*-achlarla«tlaa mt atkantl 

Vlayl cfclarlda vi a dahydr»htH*«aillt a a l atkylaaa dtcklarld* by tfcaraal 

cracklAO 

Vlayl cfclarlda via dahvdrafc*la*aa*t!*a a l atkylana dtcklarld* ky tfcaraal 

cractlao 

Vlayl cfclarlda vi a bydraa*l*aaa*tl*a a l acatvlana 

Vlayl cfclarlda vi a fcvar afc«l*a*aatlaa mt acatylaaa 

ACCTALBSNYM VI * *l * MIMTI M OF CTHYLCM 

FSaMBIH VI * (MOM-MI * SF MTHYL FSSMTC 

FSMMI K VI * (8SSMSLMIS SF MTMYL FSMttTS 

Carbaa alaulfld * vl * aulf*a*tia a a* aatk an* 

Carbaa dlavlllda ut* aallamtla a af tatkan* 

Ctkylaaa aalda vi a air wldatla a af atkylaaa 

Vtavlldaaa cfclarld* vl * dafcvdracfclarlaatlaa af 1.1.2-trlcklaraatfcaaa 

Vlayllataa cfclarlda vi a aaki *f acfclarlaatlaa af 1.1.2-trlcfclara 

Magna** vl * tataowatlaa a l carbaa aaaaai* 

CFC-142 via talaaaaatlaa a* cklara ca 

CFC-142 vl * talaaaaatlaa af cklara ca 

Praavlan* aalda via **fci • akil umitla a a l *r*ayl*a a cklarafcydrla 

Praavlaaa aalda via Baku* •*•)••—itl* a af ar aay I ana chlarafcraY-1* 

Pr*avl*aa aalda via apaaldatlaa af t-fcutyl kvaVaparaalaa 

Praavlan* aalda vl * apaalaatlaa af t-fcutyl hvdraaaraalta 

Cfc vl * liaui d **** * catalyti c raacll w 

Cfc vl * liaui d afcaaa catalyti c raactlaa 

Cklaratrlfluaraaattaaa vt* tluarlaatla a *f chlor* coapounda 

Chlaratrif luaraaatkaaa vl * tluarlaatla a af cklara caaaauad* 

Trlchlaratrlfluaraatfcan* vl * kalaaanatlaa af parcalaraathylaoa 

. frlcfclaratrlf luaraattaaar vl * talaaaaatlaa at *arcfcl*r**tfcyl*aa 

Slaathvl *ulf*t a VI* SSTU1FIC*TIM OF MTHYLC.S. S *I-*.S . 

Blaathvl *ulf*t a VI* CSTUIFICATIM OF MTHYLC.S. S DIHI.S. 

Tatraathvl land vt* addltlaa af athyl chl arid * t * la*d-**dlua alloy 

P-P U.S. 

CAPACITY 

•1.1 0 

•LI O 

2MI. M 

2MI. M 

2018. M 

MM. M 

ISM. M 

IMV. M 

IM. M 

IM. M 

M . M 

M . M 

M . M 

M . M 

IM. M 

IM. M 

IM. M 

IM. M 

IM. M 

S . M 

4»I*. M 

MCMT 

TYM 

8 

S 

B 

B 

B 

R 

B 

* 

a 

a 

B 

a 

a 

a 

a 

a 

a 

a 

-a 

a 

B 

MODEL NA M 

OISTILLATI M NV 

NTSaSSSNATIM 

BISTILLATIM V 

71412* 

BISTILLATIM V 

SCMRIC RCACTIM 

BISTILLATIM V 

MYMOGCMAIIM 

7ISSM 

HTS80HAL0SCMT1M 

7ISSM 

HALOCCMATIM 

SISTILLATIM NV 

NALOSCHAIIM 

7M7 M 

BISTILLATIM NV 

SCMNIC MACTIM 

BISTILLATIM NV 

75M M 

7SM M 

BISTILLATIM NV 

HAP 

STIIMIO M 

7*.»7 

541.77 

111.07 

2910.24 

107.*l 

M M . 17 

M . M 

1280. M 

O . M 

*.4S 

O . M 

M . M 

44. M 

7 . M 

M . M 

SS2.M 

141.74 

11.07 

*.* 7 

7.41 

IM.7 2 

VOC 

inISSIONS 

42.11 

7M. M 

MS.* * 

121*.21 

207.17 

S7S2.M 

74. M 

42M.44 

O . M 

12.07 

O . M 

M . M 

52. M 

10. M 

M . M 

457.41 

442. M 

17. IS 

12.7* 

*.S2 

225.04 

BCMva •TI M 

471 . M 

471. M 

IM. M 

I . M 

I . M 

117. M 

117. M 

MM. M 

122. M 

122. M 

1114.41 

M . M 

M.2 4 

4M. M 

4S4. M 

S22. M 

S22. M 

101.42 

101.42 

41.72 

41.72 

M . M 

B L M 

27.20 

27. M 

45. M 

B 

a 

* 

a 

a 

B 

a 

• 

a 

a 

a 

a 

B 

B 

a 

B 

a 

B 

a 

B 

a 

s 

B 

a 

R 

B 

7MI M 

HVBBOHHLOSSHATIM 

7M7 M 

BISTILLATIM MV 

SCMBIC BCACIIM 

MIS M 

MIS M 

M2I M 

BISTILLATIM MM 

M U M 

HALOEMATIM 

7*4*4* 

7*454* 

BISTILLATIM NV 

BCHVSROHALSSSNATIM 

BISTILLATIM MV 

SCMCBIC MACTIM 

7*4*4* 

SCMRIC MACTIM 

M72 M 

M72 M 

74111* 

74111* 

OISIILLAII0N NV 

flllRIFICATIOM 

BISTILLATIM *V 

O .M 

II.SS 

O .M 

1.17 

1.02 

O .M 

O .M 

M.O* 

5.** 

M.77 

440.24 

O .M 

O .M 

M . M 

11.74 

24.11 

1157.77 

0.00 

151.45 

O .M 

O .M 

O .M 

O .M 

14.45 

l».»4 

IS.71 

O .M 

14.71 

IIM.M 

1.7* 

L M 

O .M 

O .M 

41411.24 

4.SI 

M.77 

SM.IS 

O.M 

O .M 

M . M 

11.74 

M . U 

1471.TS 

O .M 

1*2.M 

O.M 

O.M 

O.M 

0.00 

41.42 

25.27 

IS.SI 

Mat Tvaa *«v. • • *lr Oaldatlaa. S • SlatllUtlea. • • Raactar 
78M2A 

78*31* 

7M1 M 

7M0 M 

7*00M 

7MIM 

7MIM 

7*041* 

7M4IA 

7MM* 

MI07A 

M UM 

MUM 

M UM 

M UM 

MMM 

MS4 M 

7*I4 M 

BBM7A 

B0M7A 

MIS M 

8M2 M 

0M2 M 

84451* 

B44SI* 

BMSIB 

S4MIB 

B4MIC 

BMSIC 

SSMM 

87M M 

M0I17 M 

•ISOM 

•IMM 

•I MM 

MS2M 

M47M 

MIMA 

M UM 

M UM 

M UM 

MUM 

M U X 

M U X 

PRODUCT PROCESS HAM 

Tatraathyl I aad vl * addition of ethyl cklarlda to la*d-*adlua alla y 

Itathvl *tky l katena via dofcydraaaaatlaa af *-fcutyl *lc*hal 

Hathvl athyl tatana vl * d*h>dr«aan«tl*a af a-hutyl *lc*k*l 

Trlchlaraatkana (1.1.2-) vl * HALOCCMATIM OF VINYL CMLMIK 

Trlchlaraatkana (1.I.2- ) vl * HALOCCMATIM OF VINYL CHLMIK 

Trlcklaraatkana II.1.2- 1 VI * HALOCCMATIM OF CTHYLCM 

Trlchlaraatkana (1.1.2- 1 VI * HALOCCMATIM OF CTHYLCM 

Irlcklaraatkylana via cfclarlaatlaa af atkylaaa dl chl arid * 

Trlchlcraatfcvlam via chlarlaatlaa af athyl ana dlchlarld* 

ACAVLAIIIK VIA HYSMLMIS OF ACRVLMITRILC 

ACRVUMIIK VI * HYSMLMIS OF ACRVLMITRILC 

Praplantc acid vl * air aalaatla * af pra»l*n*ldahyda 

ACRYLIC ACIB VI * OIIMTI M OF ACMLSIH. ACBOLCIN FBM OIIMTI M OF PROPYLS* 

Cklaraacatlc acid via kalaaanatlaa af acattc acid 

Chlaraacatlc acid via talaaaaatlaa af acatlc acid 

CklaraacMIc *cld wl* kvdralyala af cfclaraacatyl cklarlda 

Cklaraacatlc acid via bydralv*!* af cfclaraacatyl cfclarlda 

Hatfcvl acatata vi a fcvar al ral * mt palmlay l acatata bv aatfcaaal 

Natkyl acatata vi a fcvdraly*!* a l aalwlay l acatata by aatfcaaal 

Tatracklaraatfcam (1.1.2.2-) vi a kalaaanatlaa af acatvlaaa 

Tatr*chl*r*atk*n* II.1.2.2- 1 VI * NALSSCHATIM OF CTHYLCM 

Blspkaaal * via caadaaaatlaa mt ataaal aad acataaa 

Blaphanal • vl * caadaaaatlaa af pfcanal and acataaa 

C u m Hydraparaalda vi a aaldatiaa af cuaana 

Natfcyl aatkacrylat* vi * kvdralyal* *n * alkvlstlaa af acataaa cyaaafcydrla 

Matfcyl aatkacrylat* vi a fcvdraly*!* aad alkvlatla a af acataaa cvaaahydria 

Anthraaulnan* VI * SCHYSNOLMIS SF SSMIOYLDCMIOIC ACIS 

Aatfcraauiaana VIA SCHYSNOLMIS OF SCHI0YLICH20IC ACIB 

Aathraaulaaaa vi a c*nd*n**tl*u af aapktfcaauiaaaa aad fcutadlan* 

antfcrxulnan* vi a csadanoatlaa af aapfctfcaaulaan* and butadiana 

katbraaulnan* vl * hydradlaarlaatlaa af atyraaa 

Aathraaulaaaa vl * kvdradtaarlsatlaa mt atyraaa 

Pktkallc anhydrld* via air aalaatla * af a-aylana 

Phthalic anfcvdrlda via air aaldatiaa af aaakttalana 

Paatacfclaraafcaaal via fcalaaaaatiaa mt ataaal 

Paatacfclaraafcaaal via fcalaaaaatiaa mt pfcanal 

Cthvl callulaaa vi a athvlatlaa a l callalaaa 

Cthyl callulaaa via athvlatlaa af callulaaa 

Ma* thai an* Iran aatralaua daalkylatlaa 

Mapttalaaa fraa aatralaua daalkylatlaa 

Mapktfcalan* fra a caal ta r di*tlll*tl* a 

Bl phonyI vl * dahvdraaatatla* af fcaaiaaa 

•ylaaa la-l vl * fractlaa*! alatllUtla a af alaad avian* 

CNMOTOLUCM (a-l VIM HALOSCMTIM OF TOLUCM 

Banian* Sulfaalc Acid VIA CMTINUSUS SULFOHATIM HI DLCM 

INIM I Sulfaalc (acid VI * CMTIHUOUS SULFOHATIM HI OLCUH 

Sim** ! Sulfaalc Acid VI * MLFSMTI M * CONTINUOUS CITBACTIM 

*•»!•• • Sulfaalc *cl d VI * SULFRHATIM S CONTINUOUS CITBACTIM 

Damana Sulfaal c Acid VIA SULFSNATIM • BCMOVAL OF I M 

Sulfaalc Acid VI * SULFOHATIM S RMMAL OF I M 

P-P U.S. 

CAPACITY 

45. M 

241. M 

241. M 

IM. M 

IM. M 

IM. M 

IM. M 

IM. M 

IM. M 

M . M 

M . M 

M.I O 

SM.1 2 

* . M 

» . M 

M . M 

M . M 

4 . M 

4 . M 

M . M 

M . M 

SM. M 

SI4. M 

2414. M 

S24. M 

SM. M 

0.21 

0.21 

* . 12 

0.12 

*.l l 

0.11 

4M. M 

IM. M 

I8. M 

IS. M 

S . M 

S . M 

M . M 

M . M 

102. M 

4.47 

421.84 

M . M 

M . M 

70. M 

M . M 

M . M 

M . M 

M . M 

VENT 

TYM 

R 

B 

R 

B 

B 

8 

a 

a 

a 

a 

a 

'A 

* 

B 

a 

a 

a 

a 

a 

a 

a 

B 

a 

* 

B 

a 

B 

a 

8 

a 

a 

a 

* 

* 

B 

a 

B 

a 

B 

a 

B 

a 

a 

a 

B 

a 

a 

a 

a 

a 

noon, MAM 

UNCAIC MACTIM 

7MS M 

7B41IA 

7 MO M 

MALOSCNATIM 

7M0 M 

NALSSCHATIM 

74*14* 

HALOSCHATIM 

BISTILLATIM MV 

NYSNOLMIS 

AIR OIIMTI M 

• 1 * OIIMTI M 

BISTILLATIM NV 

HALOSCHATIM 

BISTILLATIM M 

HYSBOLMIS 

BISTILLATIM NV 

HMHOLMIS 

HALOSCHATIM 

HALOSCMTIM 

BISTILLATIM V 

w i n 

AIB OIIMTI M 

M424A 

MVMOLVSIS 

BISTILLATIM NV 

SCMRIC MACTIM 

BISTILLATIM NV 

COMCMMTIM 

BISTILLATIM M 

MVBAMlnUIIATIM 

M44 M 

AIB OIIMTI M 

BISTILLATIM V 

HALOSCHATIM 

BISTILLATIM M 

SCMNIC MACTIM 

BISTILLATIM M 

SCMRIC MACTIM 

SISTILLATIM MV 

BCHYSaOSCMATIM 

BISTILLATIM M 

HALOSCHATIM 

BISTILLATIM NV 

SULFOHATIM 

SISTILLATIM NV 

SULFOHATIM 

BISTILLATIM HV 

SULFOHATIM 

MAP 

CMSSIONS 

14. »7 

M.B 2 

O . M 

O . M 

41.12 

O . M 

41.12 

O . M 

41.SI 

•M.4 7 

0.17 

OILS * 

I2M.S 1 

M . M 

1.72 

12.41 

O . M 

10. M 

0.01 

12.70 

12.70 

27. M 

O . M 

14110.*4 

2M2.4 4 

1.12 

0.54 

O.SI 

0.2 8 

0.14 

0.24 

0.11 

1*444.81 

17.81 

I . M 

7.41 

8 . M 

8.07 

* L M 

M.0 2 

217.71 

21.71 

• M.2 4 

11. M 

1*1. M 

2.07 

82. M 

1.04 

S I . 57 

1.01 

VOC 

cnissioM 

It.OS 

421.44 

O.M 

O.M 

5S. M 

O.M 

M . M 

O.M 

S I . 02 

IM. M 

0.17 

2214. M 

1411.4* 

25.10 

4.77 

M . M 

O.M 

• I. M 

0.01 

M . M 

M . M 

51.44 

* . M 

M4I1.1 I 

1S»2.I) 

1.12 

O . M 

* . M 

*.l ) 

• .41 

• .I I 

• .14 

1*427.1) 

M.S1 

2 . M 

• .1 ) 

10. IS 

10.27 

75.01 

101. M 

284. M 

M.4 7 

215.71 

17. M 

IM.2 I 

2.07 

M.S * 

I . M 

•7.42 

i.es 

Want lyaa Kavi * • Air Oaldatlaa. 0 • Slatlllatlan . R • Raactar 
PRODUCT 

PROCESS 

PRODUCT PROCESS HAM 

Taluana aulfonyl cklorld* wl* raactl*n af teluan 

Taluana aulfaayl cklarlda via raactlaa af taluan 

Cu**aa vl * altylatla n af b*»»**a ultk prapylan* 

Cuaaaa vl * altylatla n af hoaaaaa altfc praavlana 

Baniavl cfclarlda via raactlaa tt baaaalc acid an 

Baaiovl chlarla * vl * raactlaa af baaaalc acid an 

Hitrabaaiana via altratla a af baaiana 

Hltrabaaiaa* vi a altratla a of baaiana 

u/ chlorooulfonlc *cld 

ml chloroaulIonic acid 

niatrlchlorlda 

niotrlchlarld * 

P-P U.S. 

CAPACITY 

2.72 

2.72 

2145. M 

21M. M 

4.18 

4.10 

4M. M 

M4. M 

VCHT 

TYM 

B 

a 

a 

a 

a 

a 

B 

a 

HOOCL HAM 

BISTILLATIM V 

MMRI C MACTIM 

MB2 M 

M82 M 

BISTILLATIM NV 

SCMCBIC MACTI M 

M M M 

M M M 

HAP 

EMISSIONS 

0.21 

4.01 

O . M 

O . M 

• M 

* . M 

M.S I 

4M.1 5 

VOC 

Itl ISS IONS 

0.41 

7.40 

O . M 

O . M 

11.44 

11.57 

M.I I 

4M.1 5 

H*nt Typ* Kay• * • Otr Oaldatlaa. B • Btallllatlaa . • • Raactar 

oo