OXIDES OF SULFUR ANNUAL EMISSION REPORT

Company Name Chevron Products CompanySite Name Salt Lake RefineryCompany ID - 95Site ID - 10119NOTE: Be aware that this report uses different methods of calculating emissions than are required for the 2006 Emissions Inventory.

A

1 1998 3874 1a-1 10200701 No 3084 

2

2006 (using 1998 method of calculation) 3874 1a-1 10200701 No 3084 

3

2006 (if method of calculation is different from 1998) 3874 1a-1 10200701 No 3084 

A

1 1998 3875 1a-2 10200701 No 3084 

2

2006 (using 1998 method of calculation) 3875 1a-2 10200701 No 3084 

3

2006 (if method of calculation is different from 1998) 3875 1a-2 10200701 No 3084 

2006 Calculations

Fuel oil

Year DAQ ID

Pt Source

ID SCC

Thro

4

2006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.

Boilers 1 & 2 Fuel GasBoilers 1 & 2 Fuel GasBoilers 1 & 2 Fuel Gas

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Thro

This form is to be used by sources that have emitted 100 tons or more of SOx in any calendar year after 1999, and that are not subject to acid rain cont

requirements (40CFR Part 75). Row 1 in the following table(s) contains historical inventory data for the listed component. Row 2 is used to calculate the 

the same method that was used in the historical data. The inputs required are in green font. To insert the new data you type over the top of the old data. 

show and calculate any changes in the method of calculation from 1998 to 2006 (i.g. emission factors, % of sulfur, heating value, controls, breakdowns, 

current method of calculating the SOx emissions does not work with the equation provided in row 3, the calculation should be provided in the row 4. Row

calculations as contained in the 2006 Emission Inventory.

Year DAQ ID

Pt Source

ID SCC

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Boilers #1 & 2Boilers #1 & 2Boilers #1 & 2

Fuel oilFuel oil #6

Chevr
A

1 1998 3876 1b-1 10200701 No 3085 

2

2006 (using 1998 method of calculation) 3876 1b-1 10200701 No 3085 

3

2006 (if method of calculation is different from 1998) 3876 1b-1 10200701 No 3085 

A

1 1998 3877 1b-2 10200701 No 3085 

2

2006 (using 1998 method of calculation) 3877 1b-2 10200701 No 3085 

3

2006 (if method of calculation is different from 1998) 3877 1b-2 10200701 No 3085 

Thro

Boilers #3 & 4 Fuel oil #6

Raw Material or Fuel 

used

Thro

Boilers #3 & 4 Fuel oil Boilers 3 & 4 Fuel Gas

Year DAQ ID

Pt Source

ID SCC Description of Process

NSPS 

(Yes/No)

Boilers 3 & 4 Fuel GasBoilers 3 & 4 Fuel Gas

Thro

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

4

Year DAQ ID

Pt Source

ID SCC

Raw Material or Fuel 

used

4

2006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.

Associated 

Stack ID

Boilers #3 & 4 Fuel oil

4

2006 Calculations

Chevr
A

1 1998 3878 2a-1 30600106 No 3086 

2

2006 (using 1998 method of calculation) 3878 2a-1 30600106 No 3086 

3

2006 (if method of calculation is different from 1998) 3878 2a-1 30600106 No 3086 

A

1 1998 3886 3a 30600106 No 3090 

2

2006 (using 1998 method of calculation) 3886 3a 30600106 No 3090 

3

2006 (if method of calculation is different from 1998) 3886 3a 30600106 No 3090 

A

1 1998 3887 3b 30600106 No 3091 

NSPS 

(Yes/No)

Associated 

Year DAQ ID Stack ID

Pt Source

ID

Crude F-1and F2

SCC Description of Process

Fuel GasFuel Gas

Year DAQ ID

Pt Source

ID SCC

Raw Material or Fuel 

used

Crude F-1and F2 Fuel Gas

Associated 

Stack ID

Crude F-1and F2 Fuel Gas

Description of Process

NSPS 

(Yes/No)

4

2006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.

Raw Material or Fuel 

used

Thro

FCC F-21 Fuel GasFCC F-21FCC F-21 Fuel Gas

Year DAQ ID

Pt Source

ID SCC

4

2006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

FCC F-23 Fuel Gas

Thro

Chevr
2

2006 (using 1998 method of calculation) 3887 3b 30600106 No 3091 

3

2006 (if method of calculation is different from 1998) 3887 3b 30600106 No 3091 

A

1 1998 3888 3c 30600201 No 3092 

2

2006 (using 1998 method of calculation) 3888 3c 30600201 No 3092 

3

2006 (if method of calculation is different from 1998) 3888 3c 30600201 No 3092 

A

1 1998 3889 3d 30600904 No 3093 4

2

2006 (using 1998 method of calculation) 3889 3d 30600904 No 3093 4

3

2006 (if method of calculation is different from 1998) 3889 3d 30600904 No 3093 1

FCC F-23 Fuel GasFCC F-23 Fuel Gas

Year DAQ ID

Pt Source

ID SCC

4

2006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

FCC Reg./CO Boiler Fuel Gas

Thro

FCC Reg./CO Boiler Fuel GasFCC Reg./CO Boiler Fuel Gas

Year DAQ ID

Pt Source

ID SCC

4

2006 Calculations: Stack Test changed drastically because of addition of VGO unit and additive to flue gas.

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Cracker Flare gas

Thro

Cracker Flare gasCracker Flare gas

2006 Calculations

Chevr
A

1 1998 3890 4 30600106 No 3094 

2

2006 (using 1998 method of calculation) 3890 4 30600106 No 3094 

3

2006 (if method of calculation is different from 1998) 3890 4 30600106 No 3094 

A

1 1998 3891 5a 30600106 No 3095 

2

2006 (using 1998 method of calculation) 3891 5a 30600106 No 3095 

3

2006 (if method of calculation is different from 1998) 3891 5a 30600106 No 3095 

Year DAQ ID

Pt Source

ID SCC

4

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

HDN F7110 & F-7130 Fuel Gas

Thro

HDN F7110 & F-7130 Fuel GasHDN F7110 & F-7130 Fuel Gas

Year DAQ ID

Pt Source

ID SCC

4

2006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Reformer F-1 Fuel Gas

Thro

Reformer F-1 Fuel GasReformer F-1 Fuel Gas

4

2006 Calculations

Thro

Chevr
A

1 1998 3892 5b 30600106 No 3096 

2

2006 (using 1998 method of calculation) 3892 5b 30600106 No 3096 

3

2006 (if method of calculation is different from 1998) 3892 5b 30600106 No 3096 

A

1 1998 3893 5c 30600106 No 3097 

2

2006 (using 1998 method of calculation) 3893 5c 30600106 No 3097 

3

2006 (if method of calculation is different from 1998) 3893 5c 30600106 No 3097 

A

1 1998 3894 6a-1 30600106 No 3098 

Year DAQ ID

Pt Source

ID SCC Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Reformer F-2 Fuel GasReformer F-2 Fuel GasReformer F-2 Fuel Gas

Year DAQ ID

Pt Source

ID SCC

4

2006 Calculations

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Reformer F-3 Fuel Gas

Thro

Reformer F-3 Fuel GasReformer F-3 Fuel Gas

Year DAQ ID

Pt Source

ID SCC

4

2006 Calculations

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Alkylation F-3617 (fuel gas) Fuel Gas

Thro

Chevr
2

2006 (using 1998 method of calculation) 3894 6a-1 30600106 No 3098 

3

2006 (if method of calculation is different from 1998) 3894 6a-1 30600106 No 3098 

A

1 1998 3895 6a-2 30600106 No 3098 

2

2006 (using 1998 method of calculation) 3895 6a-2 30600106 No 3098 

3

2006 (if method of calculation is different from 1998) 3895 6a-2 30600106 No 3098 

A

1 1998 3896 6b 30600904 No 3099 

2

2006 (using 1998 method of calculation) 3896 6b 30600904 No 3099 

3

2006 (if method of calculation is different from 1998) 3896 6b 30600904 No 3099 

Alkylation F-3617 (fuel gas) Fuel GasAlkylation F-3617 (fuel gas) Fuel Gas

Year DAQ ID

Pt Source

ID SCC

4

2006 Calculations: The heating value and percentage of sulfur changed in the fuel. This is not a change in method.

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Alkylation F-3617 (polymer fueled) Polymer

Th

Alkylation F-3617 (polymer fueled) PolymerAlkylation F-3617 (polymer fueled) Polymer

Year DAQ ID

Pt Source

ID SCC

4

2006 Calculations: The percentage of sulfur changed in the fuel. This is not a change in method.From 2006 AEI Spreadsheet calculations - Sox = %S*157*#of Polymer/2000/7.786/1000=0.266 ton

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Alky Flare Gas

Th

Alky Flare GasAlky Flare Gas

2006 Calculations

Chevr
A

1 1998 3897 7a 30600106 No 3100 

2

2006 (using 1998 method of calculation) 3897 7a 30600106 No 3100 

3

2006 (if method of calculation is different from 1998) 3897 7a 30600106 No 3100 

A

1 1998 3898 7b 30600904 No 3101 

2

method of calculation) 3898 7b 30600904 No 3101 

3

2006 (if method of calculation is different from 1998) 3898 7b 30600904 No 3101 

A

Year DAQ ID

Pt Source

ID SCC

4

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Coker F-7001 Fuel Gas

Th

Coker F-7001 Fuel GasCoker F-7001 Fuel Gas

Year DAQ ID

Pt Source

ID SCC

4

2006 Calculations: The percentage of sulfur changed in the fuel. This is not a change in method.

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Coker Flare Gas

Th

Coker Flare GasCoker Flare Gas

Year DAQ ID

Pt Source

ID SCC

4

2006 Calculations

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Th

Chevr
1 1998 3899 8a 30600106 No 3102 

2

2006 (using 1998 method of calculation) 3899 8a 30600106 No 3102 

3

2006 (if method of calculation is different from 1998) 3899 8a 30600106 No 3102 

A

1 1998 4333 8b 30600106 No 3103 

2

2006 (using 1998 method of calculation) 4333 8b 30600106 No 3103 

3

2006 (if method of calculation is different from 1998) 4333 8b 30600106 No 3103 

A

1 1998 4334 9 30609904 No 3104 

2

2006 (using 1998 method of calculation) 4334 9 30609904 No 3104 

HDS F-10 Fuel GasHDS F-10 Fuel GasHDS F-10 Fuel Gas

Year DAQ ID

Pt Source

ID SCC

4

2006 Calculations: The percentage of sulfur changed in the fuel. This is not a change in method.

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

HDS F-11 Fuel Gas

Th

HDS F-11 Fuel GasHDS F-11 Fuel Gas

Year DAQ ID

Pt Source

ID SCC

4

2006 Calculations: The percentage of sulfur changed in the fuel. This is not a change in method.

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Sulfur Plant Fuel Gas

Th

Sulfur Plant Fuel Gas

Chevr
3

2006 (if method of calculation is different from 1998) 4334 9 30609904 No 3104 

A

1 1998 5479 10 20200202 No 0 

2

2006 (using 1998 method of calculation) 5479 10 20200202 No 0 

3

2006 (if method of calculation is different from 1998) 5479 10 20200202 No 0 

EQUIPMENT NOT RUN IN 1998 THAT EMITS SOx

2006 SOx

How sulfur content was calculated Tons/year

171147 32033 0

22552 9.73514897 0

176662 0.0874

0

177029 0.005177030 0.007177032 10.651177033 2.282

TOTAL 22.7674

Tier 2 Diesel Eng. 100% Conversion of Fuel Sulfur

Sulfur Plant Fuel Gas

Year DAQ ID

Pt Source

ID SCC

4

2006 Calculations From 2006 AEI Spreadsheet calculations - Sox = CEM data (563,434 lb/yr)/2000 = 281.717 ton

Description of Process

NSPS 

(Yes/No)

Associated 

Stack ID

Raw Material or Fuel 

used

Reform. Comp. Drivers Natural Gas

Th

Reform. Comp. Drivers Natural GasReform. Comp. Drivers Natural Gas

DAQ ID

Point 

Source ID Description of Process

Temporary boiler

4

2006 Calculations

Boiler #5 Emission FactorsFCC Emergency Air Compressors Emission FactorsDiesel Generators Emission Factors

Boiler #5 Emission FactorsTier 1 Diesel Eng 100% Conversion of Fuel SulfurVGO Furnace F66100 Agreed per 1990 PM10 SIPVGO Furnace F66200 Agreed per 1990 PM10 SIP

Chevr
Chevr
OXIDES OF SULFUR ANNUAL EMISSION REPORT

111.6 mmbtu/hr 1253 btu/cf 0.0007 CEM

111.6 mmbtu/hr 1393 btu/cf 0.0003 CEM

111.6 mmbtu/hr btu/cf CEM

111.6 mmbtu/hr 6000000 btu/bbl 0.8028 Explain

111.6 mmbtu/hr 6000000 btu/bbl 1.0000 Explain111.6 mmbtu/hr 6000000 btu/bbl 0.0000 Explain

How Sulfur Content is 

calculated

%

Ash

Control 

Code (See 

List)

Heating

Value Units

%

Sulfur

Design 

Rate Units

Primary Control

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

Design 

Rate Units

If Throughput is a Fuel Primary Control

%

Ash

Name of

Primary Control

Control 

Code (See 

List)

If Throughput is a Fuel

Name of

Primary Control

Chevr
100.8 mmbtu/hr 1189 btu/cf 0.0007 CEM

100.8 mmbtu/hr 1393 btu/cf 0.0003 CEM

100.8 mmbtu/hr btu/cf 0.0000 CEM

108 mmbtu/hr 6000000 btu/bbl 0.8028 Explain108 mmbtu/hr 6000000 btu/bbl 0.9951 Explain

100.8 mmbtu/hr 6000000 btu/bbl 0.0000 Explain

Design 

Rate Units

Design 

Rate Units

If Throughput is a Fuel Primary Control

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Name of

Primary Control

Control 

Code (See 

List)

If Throughput is a Fuel Primary Control

Heating

Value Units

%

Sulfur

Control 

Code (See 

List)

Name of

Primary Control

How Sulfur Content is 

calculated

%

Ash

Control 

If Throughput is a Fuel Primary Control

Chevr
mmbtu/hr 1189 btu/cf 0.0014 CEM

159.3 mmbtu/hr 1393 btu/cf 0.0003 CEM

mmbtu/hr 0 btu/ct CEM

mmbtu/hr 1189 btu/cf 0.0014 CEM

50.3 mmbtu/hr 1393 btu/cf 0.0003 CEM

mmbtu/hr btu/cf 0.0003 CEM

mmbtu/hr 1189 btu/cf 0.0014 CEM

Units

%

Sulfur

Design 

Rate

How Sulfur Content is 

calculated

%

Ash

Name of

Primary Control

Control 

Code (See 

Units List)

Heating

Value

Design 

Rate Units

If Throughput is a Fuel Primary Control

Name of Primary Control

Control 

Code (See 

List)

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of Primary Control

Control 

Code (See 

List)

Design 

Rate Units

If Throughput is a Fuel

Chevr
50.3 mmbtu/hr 1393 btu/cf 0.0003 CEM

0 mmbtu/hr 0 btu/cf CEM

mmbtu/hr 1189 btu/cf 0.0014 CEM

97.3 mmbtu/hr 1393 btu/cf 0.0003 CEM

mmbtu/hr btu/cf CEM

mmbtu/hr 23mmbtu/hr 23

0 23

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of Primary Control

Control 

Code (See 

List)

Design 

Rate Units

If Throughput is a Fuel

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of Primary Control

Control 

Code (See 

List)

Flaring

Design 

Rate Units

If Throughput is a Fuel

FlaringFlaring

Chevr
mmbtu/hr 1189 btu/cf 0.0014 CEM

43.5 mmbtu/hr 1393 btu/cf 0.0003 CEM

mmbtu/hr btu/cf CEM

mmbtu/hr 1189 btu/cf 0.0014 CEM

52.3 mmbtu/hr 1393 btu/cf 0.0003 CEM

mmbtu/hr btu/cf CEM

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of

Primary Control

Control 

Code (See 

List)

Design 

Rate Units

If Throughput is a Fuel

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of

Primary Control

Control 

Code (See 

List)

Design 

Rate Units

If Throughput is a FuelIf Throughput is a Fuel Primary Control

Chevr
mmbtu/hr 1189 btu/cf 0.0014 CEM

45 mmbtu/hr 1393 btu/cf 0.0003 CEM

mmbtu/hr btu/cf CEM

mmbtu/hr 1189 btu/cf 0.0014 CEM

31.7 mmbtu/hr 1393 btu/cf 0.0003 CEM

mmbtu/hr btu/cf CEM

mmbtu/hr 1189 btu/cf 0.0014 CEM

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Name of

Primary Control

Control 

Code (See 

List)

Design 

Rate Units

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of

Primary Control

Control 

Code (See 

List)

Design 

Rate Units

If Throughput is a Fuel

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of

Primary Control

Control 

Code (See 

List)

Design 

Rate Units

If Throughput is a Fuel

Chevr
90 mmbtu/hr 1393 btu/cf 0.0003 CEM

mmbtu/hr btu/cf 0.0000 CEM

mmbtu/hr 6000000 btu/bbl 0.0014 lab analysis

90 mmbtu/hr 6000000 btu/bbl 0.0441 lab analysis90 mmbtu/hr 0 btu/bbl 0.0441 lab analysis

mmbtu/hr 23mmbtu/hr 23mmbtu/hr 23

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of

Primary Control

Control 

Code (See 

List)

Design 

Rate Units

If Throughput is a Fuel

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of Primary Control

Control 

Code (See 

List)

Flaring

Design 

Rate Units

If Throughput is a Fuel

FlaringFlaring

Chevr
mmbtu/hr 1189 btu/cf 0.0014 CEM

71.1 mmbtu/hr 1393 btu/cf 0.0003 CEM

mmbtu/hr btu/cf CEM

mmbtu/hr 23mmbtu/hr 23mmbtu/hr 23

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of

Primary Control

Control 

Code (See 

List)

Design 

Rate Units

If Throughput is a Fuel

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of

Primary Control

Control 

Code (See 

List)

Flaring

Design 

Rate Units

If Throughput is a Fuel

FlaringFlaring

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of

Primary Control

Control 

Code (See 

List)

Design 

Rate Units

If Throughput is a Fuel

Chevr
mmbtu/hr 1189 btu/cf 0.0014 CEM

13.8 mmbtu/hr 1393 btu/cf 0.0014 CEM13.8 mmbtu/hr 1393 btu/cf 0.0003 CEM

mmbtu/hr 1189 btu/cf 0.0014 CEM

20.6 mmbtu/hr 1393 btu/cf 0.0003 CEM20.6 mmbtu/hr 1393 btu/cf 0.0003 CEM

mmbtu/hr 1189 btu/cf 0.0014 CEM 45 Dir

4.5 mmbtu/hr 1393 btu/cf 0.0003 CEM 45 Dir

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of

Primary Control

Control 

Code (See 

List)

Design 

Rate Units

If Throughput is a Fuel

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of

Primary Control

Control 

Code (See 

List)

Sulfur Plant

Design 

Rate Units

If Throughput is a Fuel

Sulfur Plant

Chevr
4.5 mmbtu/hr 1393 btu/cf 0.0003 CEM 45 Dir

1035 mmbtu/hr 0 0 0.0010 From Natural Gas supplier

1035 mmbtu/hr 1060 btu/cf 0.0011 From Natural Gas supplier1035 mmbtu/hr 1060 btu/cf 0.0011 From Natural Gas supplier

Sulfur Plant

Heating

Value Units

%

Sulfur

How Sulfur Content is 

calculated

%

Ash

Primary Control

Name of

Primary Control

Control 

Code (See 

List)

Design 

Rate Units

If Throughput is a Fuel

Chevr
Chevr
6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.199 lbs/mm

0.00 6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 0.507 lbs/mm

0.00 6 lbs/mm

8 AP-42 5th Edition, Table 1.3-1 (9/98) EF = 157 X (.8028%) 126.040 lbs/mm

0.00 8 AP-42 5th Edition, Table 1.3-1 (9/98) EF = 157 X (.9951%) 156.230 lbs/mm0.00 0 AP-42 5th Edition, Section 1.3 lbs/10^3 ga

Emissions 

from 

Breakdown 

(tons/year)

Estimate 

Code Estimate Method

Emission 

Factor

Emissions

(tons/yr)

Emission 

Factor Units

Control 

Efficiency 

(%)

Emissions 

from 

Breakdown 

(tons/year)

Estimate 

Code

Emissions

(tons/yr) Estimate Method

0.62

0.38

0.116

0.00

Control 

Efficiency 

(%) Units

0.000.00

Chevr
6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.199 lbs/mm

0.00 6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 0.507 lbs/mm

0.00 6 lbs/mm

8 AP-42 5th Edition, Table 1.3-1, 9/98 EF = 157 x .8028% 126.040 lbs/mm

0.00 8 AP-42 5th Edition, Table 1.3-1, 9/98 EF = 157 x .8028% 156.231 lbs/mm0.00 8 lbs/10^3 ga

Control 

Emissions 

from 

0.62

Emission 

Factor Units

Control 

Efficiency 

(%)

Emissions

(tons/yr)

Emissions 

from 

Breakdown 

(tons/year)

Estimate 

Code Estimate Method

0.31

0.065

Control 

Efficiency 

(%)

Estimate 

Code Estimate Method

Emission 

Factor Units

0.00

Emissions

(tons/yr)

Emissions 

from 

Breakdown 

(tons/year)

0.000.00

Chevr
6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.199 lbs/mm

0.00 6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 0.507 lbs/mm

0.00 6 lbs/mm

6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.199 lbs/mm

0.00 6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 0.507 lbs/mm

0.00 6 lbs/mm

6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.199 lbs/mm

Control 

Efficiency 

(%)

Emissions

(tons/yr)

from 

Breakdown 

(tons/year)

0.58

Estimate 

Code Estimate Method

Emission 

Factor Units

0.242

0.00

Estimate Method

Emission 

Factor

Control 

Efficiency 

(%) Emissions (tons/year)

Emissions 

from 

Breakdown 

(tons/year)

Estimate 

Code

0.04

Units

0.035

0.00

Emission 

Factor Units

Control 

Efficiency 

(%) Emissions (tons/year)

Emissions 

from 

Breakdown 

(tons/year)

0.10

Estimate 

Code Estimate Method

Chevr
0.00 6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 0.507 lbs/mm

0.00 6 Agreed to per 1990 PM10 SIP lbs/mm

4 Source Test 77.1 lbs/

0.00 4 Source Test 18 lbs/0.00 4 Stack Test

8

AP-42 5th Edition, Table 5.1-1, 01/95, each flare is based on 1/3 of crude unit throughput 26.9 lbs/mbb

2.00 8

AP-42 5th Edition, Table 5.1-1, 01/95, each flare is based on 1/3 of crude unit throughput 26.9 lbs/mbb

2.00 8

Based on 2006 Engineering Data -Flowmeters; H2S Analysis 0.22 lbs/mbb

0.00

0.031

Emission 

Factor Units

Control 

Efficiency 

(%) Emissions (tons/year)

Emissions 

from 

Breakdown 

(tons/year)

337.70

Estimate 

Code Estimate Method

0.00

71.38

Emission 

Factor Units

Control 

Efficiency 

(%) Emissions (tons/year)

Emissions 

from 

Breakdown 

(tons/year)

64.78

Estimate 

Code Estimate Method

3.58

66.47

Chevr
6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mm

0.00 6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 0.50659631 lbs/mm

0.00 6 lbs/mm

6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mm

0.00 6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 0.50659631 lbs/mm

0.00 6 lbs/mm

Emission 

Factor Units

Control 

Efficiency 

(%) Emissions (tons/year)

Emissions 

from 

Breakdown 

(tons/year)

0.10

Estimate 

Code Estimate Method

0.00

0.046

Emission 

Factor Units

Control 

Efficiency 

(%) Emissions (tons/year)

Emissions 

from 

Breakdown 

(tons/year)

0.13

Estimate 

Code Estimate Method

0.00

0.043

Emissions 

Chevr
6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mm

0.00 6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 0.50659631 lbs/mm

0.00 6 lbs/mm

6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mm

0.00 6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 0.50659631 lbs/mm

0.00 6 lbs/mm

6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mm

Emission 

Factor Units

Control 

Efficiency 

(%) Emissions (tons/year)

Emissions 

from 

Breakdown 

(tons/year)

0.13

Estimate 

Code Estimate Method

0.00

0.044

Emission 

Factor Units

Control 

Efficiency 

(%) Emissions (tons/year)

Emissions 

from 

Breakdown 

(tons/year)

0.06

Estimate 

Code Estimate Method

0.00

0.022

Emission 

Factor Units

Control 

Efficiency 

(%)

Emissions

(tons/yr)

Emissions 

from 

Breakdown 

(tons/year)

0.31

Estimate 

Code Estimate Method

Chevr
0.00 6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 0.50659631 lbs/mm

0.00 6 lbs/mm

8 AP-42 5th Edition, Table 1.3-1, 9/98 EF = 157 x .10% 15.7 lbs/10^3 ga

0.00 8 AP-42 5th Edition, Table 1.3-1, 9/98 EF = 157 x .04% 6.9237 lbs/10^3 ga0.00 8 AP-42 5th Edition, Table 1.3-1, 9/98 EF = 157 x .04% lbs/10^3 ga

8 AP-42 5th Edition, Table 5.1-1, 01/95, each flare is based on 1/3 of crude unit throughput 26.9 lbs/mbb

0.00 8 AP-42 5th Edition, Table 5.1-1, 01/95, each flare is based on 1/3 of crude unit throughput 26.9 lbs/mbb0.00 8

Based on 2006 Engineering Data -Flowmeters; H2S Analysis 0.19 lbs/mbb

0.00

0.121

Emission 

Factor Units

Control 

Efficiency 

(%)

Emissions

(tons/yr)

Emissions 

from 

Breakdown 

(tons/year)

0.59

Estimate 

Code Estimate Method

0.000.27

Emission 

Factor Units

Control 

Efficiency 

(%)

Emissions

(tons/yr)

Emissions 

from 

Breakdown 

(tons/year)

64.78

Estimate 

Code Estimate Method

1.37

64.47

Chevr
6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mm

0.00 6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 0.50659631 lbs/mm

0.00 6 lbs/mm

8

AP-42 5th Edition, Table 5.1-1, 01/95, each flare is based on 1/3 of crude unit throughput 26.9 lbs/mbb

90.73 8

AP-42 5th Edition, Table 5.1-1, 01/95, each flare is based on 1/3 of crude unit throughput 26.9 lbs/mbb

90.73 8

Based on 2006 Engineering Data -Flowmeters; H2S Analysis 79.5 lbs/mbb

Emission 

Factor Units

Control 

Efficiency 

(%)

Emissions

(tons/yr)

Emissions 

from 

Breakdown 

(tons/year)

0.15

Estimate 

Code Estimate Method

0.000.10

Emission 

Factor Units

Control 

Efficiency 

(%)

Emissions

(tons/yr)

Emissions 

from 

Breakdown 

(tons/year)

64.78

Estimate 

Code Estimate Method

662.34155.20

Emission 

Factor Units

Control 

Efficiency 

(%)

Emissions

(tons/yr)

Emissions 

from 

Breakdown 

(tons/year)

Estimate 

Code Estimate Method

Chevr
6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mm

0.00 6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 0.50659631 lbs/mm

0.00 6 Agreed to per 1990 PM10 SIP lbs/mm

6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 1.19894459 lbs/mm

0.00 6

Agreed to per 1990 PM10 SIP EF(lb/mmscf) = ((% S/100) * (lb mole/379cf)*(32 lb/lb mole)*(2 SOx/S)*(1 *10^6 cf/mmcf 0.50659631 lbs/mm

0.00 6 Agreed to per 1990 PM10 SIP lbs/mm

1 CEM NA lbs/mm

129.57 1 CEM 563434 lbs/ye

0.025

0.00

0.014

Emission 

Factor Units

Control 

Efficiency 

(%)

Emissions

(tons/yr)

Emissions 

from 

Breakdown 

(tons/year)

0.05

Estimate 

Code Estimate Method

0.00

0.024

Emission 

Factor Units

Control 

Efficiency 

(%)

Emissions

(tons/yr)

Emissions 

from 

Breakdown 

(tons/year)

308.80

Estimate 

Code Estimate Method

411.29

Chevr
0.00 1 CEM lbs/mm

3 Agreed to per 1990 PM10 SIP EF = ((7.1 ppm*32*2)/379 1.19894459 lbs/mm

0.00 3 Agreed to per 1990 PM10 SIP EF = ((7.1 ppm*32*2)/379 1.19894459 lbs/mm0.00 3 AP-42 Table 3.2-2 0.000588 lbs/10^6 b

Component Amount 

3874 0.113875 0.03876 0.063877 0.03878 0.243886 0.033887 0.033888 71.33889 3.53890 0.043891 0.043892 0.03893 0.023894 0.13895 0.23896 1.33897 0.1

0.00

Emission 

Factor Units

Control 

Efficiency 

(%)

Emissions

(tons/yr)

Emissions 

from 

Breakdown 

(tons/year)

0.05

Estimate 

Code Estimate Method

0.026

0.05

Chevr
3898 662.3

3899 0.014333 0.024334 411.25479 0.0

After 1999 22.767TOTAL 1173.91

Chevr