Air Emissions Summary Existing Equipment

Transcription

1 Air Emissions Summary Existing Equipment

2 Air Emissions Summary - Existing Equipment Lease Name Permit Equipment Name Device ID Equipment Tag Description Air Emissions NOx lb/day NOx ton/yr ROC lb/day ROC ton/yr CO lb/day CO ton/yr SOx lb/day SOx ton/yr PM lb/day PM ton/yr GHG (MTCO 2 e) Bonetti PTO Oil & Gas Well Cantin PTO R3 Loading Rack M Cantin PTO R3 LCO Unloading Rack M Cantin PTO R3 Wash Tank T BBL Cantin PTO R3 Crude Tank T BBL Cantin PTO R3 Crude Tank T BBL Cantin PTO R3 LCO Tank T BBL Cantin PTO R3 LCO Tank T BBL Cantin PTO R3 Heater Treater H MMBTu/hr , Cantin PTO R3 Boiler H MMBTu/hr , Cantin PTO R3 Fugitives , , Fleisher PTO Oil & Gas Wells Fulger 80 PTO Oil & Gas Wells GWP PTO R8 Produced Water Tank T-03M01T BBL Emissions included in Device ID , Fugitive Emissions Components for the GWP lease. GWP PTO R8 Produced Water Tank T-03M01U BBL Emissions included in Device ID , Fugitive Emissions Components for the GWP lease. GWP PTO R8 Process Heater CHF MMBtu/hr , GWP PTO R8 Process Heater CHF MMBtu/hr , GWP PTO R8 LCO Tank BBL GWP PTO R8 Tank Heater # PH MMBtu/hr GWP PTO R8 Tank Heater # PH MMBtu/hr GWP PTO R8 Retention (Wash) Tank South T-03M01R BBL GWP PTO R8 Retention (Wash) Tank North T-03M01Q BBL GWP PTO R8 Standby/Reject Tank T-02M01V BBL GWP PTO R8 Ground Level Loading Rack M GWP ATC Steam Generator 3 pending SG MMBTU/hr , GWP PTO R8 LACT Tank T-05C01S GWP PTO R8 Crude Oil Storage Tank # T-25C01Z BBL GWP ATC Crude Oil Storage Tank # T-25C01Y BBL GWP ATC Fugitive Components for Dev GWP PTO R8 Heater PH MMBtu/hr GWP PTO R8 Heater PH MMBtu/hr GWP PTO R8 Fugitive Emissions Components Los Alamos PTO R9 Test Tank T BBL Los Alamos PTO R9 Fugitive Hydrocarbons Los Alamos PTO R9 Wash Tank T BBL Los Alamos PTO R9 Test Tank # T BBL Los Alamos PTO R9 Fugitive Hydrocarbon Components Los Alamos PTO R9 Heater H MMBtu/hr Recruit PTO R9 Line Heater MMBTu/hr Recruit PTO R9 Fugitive Valves and Fittings Recruit ATC LCO Tank T BBL Recruit ATC LCO Tank T BBL Recruit ATC Fugitive Hydrocarbon CLPs West PTO Oil & Gas Wells Williams B PTO R6 O&G Wellheads Williams B PTO R6 Well Cellars Williams B PTO R6 Valves & Fittings Williams Fee PTO R7 Fugitives: Valves & Fittings Williams Fee PTO R7 Fugitives: Wellheads Williams Fee PTO R7 Fugitives: Well Cellars Williams Holding PTO R9 Steam Generator SG-100A MMBTu/hr , Williams Holding PTO R9 Steam Generator SG-100B MMBTu/hr , Williams Holding PTO R9 Fugitive Hydrocarbon CLPs ATCs 13500, Williams Holding PTO R9 Flare # FL MMBTu/hr , Williams Holding PTO R9 LCO Tank East T BBL Williams Holding PTO R9 LCO Tank West T BBL Williams Holding PTO R9 LCO Unloading Rack M Williams Holding PTO R9 Fugitives: Valves & Fittings Page 1 of 2

3 Air Emissions Summary - Existing Equipment Lease Name Permit Equipment Name Device ID Equipment Tag Description Air Emissions NOx lb/day NOx ton/yr ROC lb/day ROC ton/yr CO lb/day CO ton/yr SOx lb/day SOx ton/yr PM lb/day PM ton/yr GHG (MTCO 2 e) Williams Holding PTO R9 Fugitives: Wellheads Williams Holding PTO R9 Fugitives: Well Cellars Williams Holding ATC H2S System V-30-02/V Williams Holding 303 PTO R10 Oil & Gas Wellheads Williams Holding 303 PTO R10 Well Cellars Williams Holding 303 PTO R10 Valves & Fittings Williams Holding 303 PTO R10 Crude Oil Storage Tank T BBL Williams Holding 303 PTO R10 Crude Oil Storage Tank T BBL Williams Holding 303 PTO R10 Wash Tank T BBL Williams Holding 303 PTO R10 Test Tank T BBL Williams Holding 303 PTO R10 Truck Loading Rack M Williams Holding Long Canyon PTO R5 Oil & Gas Wells Williams Holding Long Canyon PTO R5 Oil & Gas Well Cellars Williams Holding Long Canyon PTO R5 Valves & Fittings Williams Holding Long Canyon PTO R5 Wash Tank T BBL Williams Holding Long Canyon ATC Heater Treater H MMBtu/hr , Williams Holding Long Canyon PTO R5 Crude Tank T BBL Williams Holding Long Canyon PTO R5 Crude Tank T BBL Williams Holding Long Canyon PTO R5 LCO Tank V BBL Williams Holding Long Canyon PTO R5 Loading Rack (Crude Oil Truck Loading) M Williams Holding Long Canyon PTO R5 LCO Unloading Rack M BBL Williams Holding Long Canyon PTO R5 LCO Tank (#502) T BBL Williams Holding Long Canyon ATC Tank Heater (Boiler) MMBtu/hr Various Locations PTO Portable Vapor Recovery Compressor PK Various Locations ATC Tank Heater #1- At Los Alamos H MMBtu/hr Various Locations ATC Tank Heater #2- At Los Alamos H MMBtu/hr Total , Page 2 of 2

4 Air Emissions Summary New Equipment for WCCPP

5 Equipment Description Air Emissions NOx lb/day NOx ton/yr ROC lb/day ROC ton/yr CO lb/day CO ton/yr SOx lb/day SOx ton/yr PM lb/day PM ton/yr GHG (MTCO 2 e) 233 Thermal Wells Cantin Compressor Plant 350 Fugitives Cantin Steam Generator Fugivites Cantin Steam Generator 501, 85 MMBtu/hr - Combustion , GWP Dehy Plant Fugitives GWP Retention Tank, 5000 BBL GWP Treater Boiler 1, 4.9 MMBtu/hr , GWP Treater Boiler 2, 4.9 MMBtu/hr , PUC Gas Pipeline Fugitives PUC Gas Pipeline Pig Receiver Recruit Fugitive Components Recruit Slop Oil Tank, 1000 BBL Recruit Steam Generator Fugitives Recruit Steam Generator 401, 85 MMBtu/hr - Combustion , Williams Holding Compressor Plant 150 Fugitives Williams Holding Compressor Plant 250 Fugitives Williams Holding Steam Generator Fugitives Williams Holding Steam Generator 201, 85 MMBtu/hr - Combustion , Williams Holding Steam Generator Fugitives Williams Holding Steam Generator 601, 85 MMBtu/hr - Combustion , Passenger Vehicles Total , Page 1 of 16

6 ADMINISTRATIVE INFORMATION Attachment: Company: ERG Facility: Cat Canyon, 233 New Wells Processed by: BAM Date: 2/24/2014 Path & File Name: Santa Barbara County APCD Fugitive s Calculation - CLP Method Facility Type: (Choose one facility type by marking the box to the right of the facility type with an "x") Production Field x Gas Processing Plant Refinery Offshore Platform Component: Count THC 1 Emission Factor (lb/day-clp) ROC/THC Ratio Uncontrolled Control 2,3 Efficiency (lb/hr) (Tons/Qtr) (Tons/Yr) Gas Condensate Service Valves - Accessible/Inaccessible Valves - Unsafe Valves - Bellows Valves - Bellows / Background ppmv Valves - Category A Valves - Category B Valves - Category C Valves - Category D Valves - Category E Valves - Category F Valves - Category G 1, Flanges/Connections - Accessible/Inaccessible Flanges/Connections - Unsafe Flanges/Connections - Category A Flanges/Connections - Category B Flanges/Connections - Category C Flanges/Connections - Category D Flanges/Connections - Category E Flanges/Connections - Category F Flanges/Connections - Category G 9, Compressor Seals - To Atm Compressor Seals - To VRS PSV - To Atm/Flare PSV - To VRS Pump Seals - Single Pump Seals - Dual/Tandem Sub Total 10, Oil Service Valves - Accessible/Inaccessible Valves - Unsafe Valves - Bellows Valves - Bellows / Background ppmv Valves - Category A Valves - Category B Valves - Category C Valves - Category D Valves - Category E Valves - Category F Valves - Category G 4, Flanges/Connections - Accessible/Inaccessible Flanges/Connections - Unsafe Flanges/Connections - Category A Flanges/Connections - Category B Flanges/Connections - Category C Flanges/Connections - Category D Flanges/Connections - Category E Flanges/Connections - Category F Flanges/Connections - Category G 39, PSV - To Atm/Flare PSV - To VRS Pump Seals - Single Pump Seals - Dual/Tandem Sub Total 44, Total 55, Notes: 1 APCD P&P # A 80% efficiency is assigned to fugitive components Rule 331 implementation. 3 Emission Control efficiencies for the "category x" components are identified in "FHC Control Factors (ver 2.0)" Page 2 of 16

7 Santa Barbara County APCD Fugitive s Calculation - CLP Method ADMINISTRATIVE INFORMATION Company: ERG Facility: Each Compressor Plant Processed by: ERG Date: 4/7/14 NOTE: Facilities are not built yet. CLP count is estimated based on similar existing facilities. Facility Type: (Choose one facility type by marking the box to the right of the facility type with an "x") Production Field x Gas Processing Plant Refinery Offshore Platform Component: Count THC 1 Emission Factor (lb/dayclp) ROC/THC Ratio Uncontrolled Control 2,3 Efficiency (lb/hr) (Tons/Qtr) (Tons/Yr) Gas Condensate Service Valves - Accessible/Inaccessible Valves - Unsafe Valves - Bellows Valves - Bellows / Background ppmv Valves - Category A Valves - Category B Valves - Category C Valves - Category D Valves - Category E Valves - Category F Valves - Category G Flanges/Connections - Accessible/Inaccessible Flanges/Connections - Unsafe Flanges/Connections - Category A Flanges/Connections - Category B Flanges/Connections - Category C Flanges/Connections - Category D Flanges/Connections - Category E Flanges/Connections - Category F Flanges/Connections - Category G 2, Compressor Seals - To Atm Compressor Seals - To VRS PSV - To Atm/Flare PSV - To VRS Pump Seals - Single Pump Seals - Dual/Tandem Sub Total 2, Oil Service Valves - Accessible/Inaccessible Valves - Unsafe Valves - Bellows Valves - Bellows / Background ppmv Valves - Category A Valves - Category B Valves - Category C Valves - Category D Valves - Category E Valves - Category F Valves - Category G Flanges/Connections - Accessible/Inaccessible Flanges/Connections - Unsafe Flanges/Connections - Category A Flanges/Connections - Category B Flanges/Connections - Category C Flanges/Connections - Category D Flanges/Connections - Category E Flanges/Connections - Category F Flanges/Connections - Category G PSV - To Atm/Flare PSV - To VRS Pump Seals - Single Pump Seals - Dual/Tandem Sub Total Total 2, Notes: 1 APCD P&P # A 80% efficiency is assigned to fugitive components Rule 331 implementation. 3 Emission Control efficiencies for the "category x" components are identified in "FHC Control Factors (ver 2.0)" Page 3 of 16

8 Santa Barbara County APCD Fugitive s Calculation - CLP Method ADMINISTRATIVE INFORMATION Company: ERG Facility: Steam Generator Processed by: ERG Date: 2/20/14 NOTE: SG is not built yet. CLP count is estimated based on similar existing SGs. Facility Type: (Choose one facility type by marking the box to the right of the facility type with an "x") Production Field x Gas Processing Plant Refinery Offshore Platform Component: Count THC 1 Emission Factor (lb/dayclp) ROC/THC Ratio Uncontrolled Control 2,3 Efficiency (lb/hr) (Tons/Qtr) (Tons/Yr) Gas Condensate Service Valves - Accessible/Inaccessible Valves - Unsafe Valves - Bellows Valves - Bellows / Background ppmv Valves - Category A Valves - Category B Valves - Category C Valves - Category D Valves - Category E Valves - Category F Valves - Category G Flanges/Connections - Accessible/Inaccessible Flanges/Connections - Unsafe Flanges/Connections - Category A Flanges/Connections - Category B Flanges/Connections - Category C Flanges/Connections - Category D Flanges/Connections - Category E Flanges/Connections - Category F Flanges/Connections - Category G Compressor Seals - To Atm Compressor Seals - To VRS PSV - To Atm/Flare PSV - To VRS Pump Seals - Single Pump Seals - Dual/Tandem Sub Total Oil Service Valves - Accessible/Inaccessible Valves - Unsafe Valves - Bellows Valves - Bellows / Background ppmv Valves - Category A Valves - Category B Valves - Category C Valves - Category D Valves - Category E Valves - Category F Valves - Category G Flanges/Connections - Accessible/Inaccessible Flanges/Connections - Unsafe Flanges/Connections - Category A Flanges/Connections - Category B Flanges/Connections - Category C Flanges/Connections - Category D Flanges/Connections - Category E Flanges/Connections - Category F Flanges/Connections - Category G PSV - To Atm/Flare PSV - To VRS Pump Seals - Single Pump Seals - Dual/Tandem Sub Total Total Notes: 1 APCD P&P # A 80% efficiency is assigned to fugitive components Rule 331 implementation. 3 Emission Control efficiencies for the "category x" components are identified in "FHC Control Factors (ver 2.0)" Page 4 of 16

9 Attachment: A-1 Date: 04/14/14 BOILER / STEAM GENERATOR CALCULATION WORKSHEET (ver. 6.0) DATA Permit No.... Owner/Operator...ERG Facility/Lease...Steam Generator Boiler Type... Firetube Boiler Mfg.... PLC Industrial Boiler Model No.... Boiler Serial/ID No.... Boiler Horsepower... no data Bhp Burner Type... Gas Burner Mfg.... COEN Burner Model No.... QLN-II Max. Firing Rate of Burner MMBtu/hr Max. Annual Heat Input , MMBtu/yr Daily Operating schedule hrs/day Yearly Load factor (%) % Fuel Type... Field Gas High Heating Value... 1,050 Btu/scf Sulfur Content of Fuel ppmvd as H2S Nitrogen Content of Fuel... - wt. % N Boiler Classification... Firing Type... PM Emission Factor... PM 10 Emission Factor... NO x Emission Factor... SO x Emission Factor... CO Emission Factor... Factor... Industrial Other Type lb/mmbtu lb/mmbtu lb/mmbtu lb/mmbtu lb/mmbtu lb/mmbtu RESULTS lb/hr lb/day TPY Nitrogen Oxides (as NO 2 ) Sulfur Oxides (as SO 2 ) PM Total Suspended Particulate (PM) Carbon Monoxide Reactive Organic Compounds (ROC) Hourly Heat Release... Daily Heat Release... Annual Heat Release... Rule 342 Applicability MMBtu/hr 2, MMBtu/day 744, MMBtu/yr Billion Btu/yr Page 5 of 16

10 Santa Barbara County APCD Fugitive s Calculation - CLP Method ADMINISTRATIVE INFORMATION Company: ERG Facility: GWP RT Tank and 2 Treater Boilers Processed by: ERG Date: 2/20/14 NOTE: Tank is not built yet. CLP count is estimated based on similar existing equipment. Facility Type: (Choose one facility type by marking the box to the right of the facility type with an "x") Production Field x Gas Processing Plant Refinery Offshore Platform Component: Count THC 1 Emission Factor (lb/dayclp) ROC/THC Ratio Uncontrolled Control 2,3 Efficiency (lb/hr) (Tons/Qtr) (Tons/Yr) Gas Condensate Service Valves - Accessible/Inaccessible Valves - Unsafe Valves - Bellows Valves - Bellows / Background ppmv Valves - Category A Valves - Category B Valves - Category C Valves - Category D Valves - Category E Valves - Category F Valves - Category G Flanges/Connections - Accessible/Inaccessible Flanges/Connections - Unsafe Flanges/Connections - Category A Flanges/Connections - Category B Flanges/Connections - Category C Flanges/Connections - Category D Flanges/Connections - Category E Flanges/Connections - Category F Flanges/Connections - Category G 1, Compressor Seals - To Atm Compressor Seals - To VRS PSV - To Atm/Flare PSV - To VRS Pump Seals - Single Pump Seals - Dual/Tandem Sub Total 1, Oil Service Valves - Accessible/Inaccessible Valves - Unsafe Valves - Bellows Valves - Bellows / Background ppmv Valves - Category A Valves - Category B Valves - Category C Valves - Category D Valves - Category E Valves - Category F Valves - Category G Flanges/Connections - Accessible/Inaccessible Flanges/Connections - Unsafe Flanges/Connections - Category A Flanges/Connections - Category B Flanges/Connections - Category C Flanges/Connections - Category D Flanges/Connections - Category E Flanges/Connections - Category F Flanges/Connections - Category G 1, PSV - To Atm/Flare PSV - To VRS Pump Seals - Single Pump Seals - Dual/Tandem Sub Total 1, Total 2, Notes: 1 APCD P&P # A 80% efficiency is assigned to fugitive components Rule 331 implementation. 3 Emission Control efficiencies for the "category x" components are identified in "FHC Control Factors (ver 2.0)" Page 6 of 16

11 FIXED ROOF TANK CALCULATION (AP-42: Chapter 7 Method) 5,000 BBL Crude Oil Tank Basic Input Data Attachment: A-1 Permit: GWP liquid {1:G13, 2:G10, 3:G7, 4:C, 5:JP, 6:ker, 7:O2, 8:O6} = 4 Date: 04/14/14 liquid TVP = 1.4 Tank: ew Crude Tanks if TVP is entered, enter TVP temperature ( F) = 192 Name: name tank heated {yes, no} = yes Filename: if tank is heated, enter temp ( F) = 180 Distrcit: Santa Barbara vapor recovery system present? {yes, no} = yes Version: Tank-2b.xls is this a wash tank? {yes, no} = no will flashing losses occur in this tank? {yes, no} = no breather vent pressure setting range (psi) (def = 0.06): 0.06 Tank Data diameter (feet) = 38 capacity (enter barrels in first col, gals will compute) = 5, ,000 conical or dome roof? {c, d} = c shell height (feet) = 24 roof height (def = 1): 1 ave liq height (feet): 12 Paint Factor Matrix Molecular Weight Matrix color {1:Spec Al, 2:Diff Al, 3:Lite, 4:Med, 5:Rd, 6:Wh} = 4 paint condition liquid mol wt condition {1: Good, 2: Poor} = 1 paint color good poor gas rvp upstream pressure (psig) (def = 0 when no flashing occurs): 0 spec alum gas rvp diff alum gas rvp 7 68 Liquid Data lite grey crude oil 50 A B med grey JP maximum daily throughput (bopd) = 5,000 red jet kerosene 130 Ann thruput (gal): (enter value in Column A if not max PTE) 7.665E+07 white fuel oil RVP (psia): fuel oil API gravity = 16 Computed Values roof outage 1 (feet): 0.3 vapor space volume 2 (cubic feet): 13,950 turnovers 3 : 365 turnover factor 4 : 0.25 paint factor 5 : 0.68 Adjusted TVP Matrix RVP Matrix surface temperatures ( R, F) liquid TVP value liquid RVP value average 6 : gas rvp gas rvp maximum 7 : gas rvp gas rvp minimum 8 : gas rvp gas rvp 7 7 product factor 9 : 0.75 crude oil crude oil diurnal vapor ranges JP JP temperature 10 (fahrenheit degrees): 5 jet kerosene jet kerosene vapor pressure 11 (psia): fuel oil fuel oil molecular weight 12 (lb/lb-mol): 50 fuel oil fuel oil TVP 13 (psia) [adjusted for ave liquid surface temp]: vapor density 14 (lb/cubic foot): vapor expansion factor 15 : Long-Term vapor saturation factor 16 : VRU_Eff = 95.00% vented vapor volume (scf/bbl): 8 fraction ROG - flashing losses: Short-Term fraction ROG - evaporative losses: VRU_Eff = 95.00% Emissions Uncontrolled ROC emissions ROC emissions lb/hr lb/day ton/year lb/hr lb/day ton/year breathing loss 17 = working loss 18 = flashing loss 19 = TOTALS = NOTES: see attachment for explanation of notes (1 through 19) Page 7 of 16

12 GWP Dehy Plant - Level 1 Treater Boilers Date: 01/14/13 HEATER CALCULATION WORKSHEET (ver. 6.0) DATA Permit No.... Owner/Operator... ERG Operating Company Facility/Lease... Boiler Type... NA Boiler Mfg.... NA Boiler Model No.... NA Boiler Serial/ID No.... NA Boiler Horsepower... no data Bhp Burner Type... Gas Burner Mfg.... Ame Burner Model No ew Max. Firing Rate of Burner MMBtu/hr Max. Annual Heat Input... 42, MMBtu/yr Daily Operating schedule hrs/day Yearly Load factor (%) % Fuel Type... Produced gas High Heating Value... 1,050 Btu/scf Sulfur Content of Fuel ppmvd as H2S Nitrogen Content of Fuel... - wt. % N Boiler Classification... Industrial Firing Type... Other Type PM Emission Factor lb/mmbtu PM 10 Emission Factor lb/mmbtu NO x Emission Factor lb/mmbtu SO x Emission Factor lb/mmbtu CO Emission Factor lb/mmbtu Factor lb/mmbtu RESULTS lb/hr lb/day TPY Nitrogen Oxides (as NO 2 ) Sulfur Oxides (as SO 2 ) PM Total Suspended Particulate (PM) Carbon Monoxide Reactive Organic Compounds (ROC) Page 8 of 16

13 Santa Barbara County APCD Fugitive s Calculation - CLP Method ADMINISTRATIVE INFORMATION Company: ERG Facility: PUC Gas Line Processed by: ERG Date: 2/20/14 NOTE: Line is not built yet. CLP count is estimated based on design documents. Facility Type: (Choose one facility type by marking the box to the right of the facility type with an "x") Production Field x Gas Processing Plant Refinery Offshore Platform Component: Count THC 1 Emission Factor (lb/dayclp) ROC/THC Ratio PUC Gas Only Uncontrolled Control 2,3 Efficiency (lb/hr) (Tons/Qtr) (Tons/Yr) Gas Condensate Service Valves - Accessible/Inaccessible Valves - Unsafe Valves - Bellows Valves - Bellows / Background ppmv Valves - Category A Valves - Category B Valves - Category C Valves - Category D Valves - Category E Valves - Category F Valves - Category G Flanges/Connections - Accessible/Inaccessible Flanges/Connections - Unsafe Flanges/Connections - Category A Flanges/Connections - Category B Flanges/Connections - Category C Flanges/Connections - Category D Flanges/Connections - Category E Flanges/Connections - Category F Flanges/Connections - Category G Compressor Seals - To Atm Compressor Seals - To VRS PSV - To Atm/Flare PSV - To VRS Pump Seals - Single Pump Seals - Dual/Tandem Sub Total Oil Service Valves - Accessible/Inaccessible Valves - Unsafe Valves - Bellows Valves - Bellows / Background ppmv Valves - Category A Valves - Category B Valves - Category C Valves - Category D Valves - Category E Valves - Category F Valves - Category G Flanges/Connections - Accessible/Inaccessible Flanges/Connections - Unsafe Flanges/Connections - Category A Flanges/Connections - Category B Flanges/Connections - Category C Flanges/Connections - Category D Flanges/Connections - Category E Flanges/Connections - Category F Flanges/Connections - Category G PSV - To Atm/Flare PSV - To VRS Pump Seals - Single Pump Seals - Dual/Tandem Sub Total Total Notes: 1 APCD P&P # A 80% efficiency is assigned to fugitive components Rule 331 implementation. 3 Emission Control efficiencies for the "category x" components are identified in "FHC Control Factors (ver 2.0)" Page 9 of 16

14 PUC GAS LINE Gas Release Volume from Pigging Operation Length (in) Length (ft) Diameter (in)diameter (ft) Radius (ft) Volume (ft 3 ) pig receiver TOTAL per pigging event Density of TOC in Vessel density = P x MW / R x T Pressure (psig psi), Depressurize Launch to 5 psig psig Molecular Weight Gas lb/lb-mole R Universal Gas Constant Temperature R Calculated Density lb/ft3 ROC per Cubic Foot of Volume ROC = density x s from Pigging Events lb ROC/ft3 = s per pigging event 0.11 lb TOTAL s from Pigging Events Assume two pigging operations max occur in one day lbs/day Assume 4 pigging operations max per year tons/year Page 10 of 16

15 Santa Barbara County APCD Fugitive s Calculation - CLP Method ADMINISTRATIVE INFORMATION Company: ERG Facility: Recruit Slop Oil Tank and Pump Processed by: ERG Date: 3/7/14 NOTE: Tank is not built yet. CLP count is estimated based on similar existing tanks. Facility Type: (Choose one facility type by marking the box to the right of the facility type with an "x") Production Field x Gas Processing Plant Refinery Offshore Platform Component: Count THC 1 Emission Factor (lb/dayclp) ROC/THC Ratio Uncontrolled Control 2,3 Efficiency (lb/hr) (Tons/Qtr) (Tons/Yr) Gas Condensate Service Valves - Accessible/Inaccessible Valves - Unsafe Valves - Bellows Valves - Bellows / Background ppmv Valves - Category A Valves - Category B Valves - Category C Valves - Category D Valves - Category E Valves - Category F Valves - Category G Flanges/Connections - Accessible/Inaccessible Flanges/Connections - Unsafe Flanges/Connections - Category A Flanges/Connections - Category B Flanges/Connections - Category C Flanges/Connections - Category D Flanges/Connections - Category E Flanges/Connections - Category F Flanges/Connections - Category G Compressor Seals - To Atm Compressor Seals - To VRS PSV - To Atm/Flare PSV - To VRS Pump Seals - Single Pump Seals - Dual/Tandem Sub Total Oil Service Valves - Accessible/Inaccessible Valves - Unsafe Valves - Bellows Valves - Bellows / Background ppmv Valves - Category A Valves - Category B Valves - Category C Valves - Category D Valves - Category E Valves - Category F Valves - Category G Flanges/Connections - Accessible/Inaccessible Flanges/Connections - Unsafe Flanges/Connections - Category A Flanges/Connections - Category B Flanges/Connections - Category C Flanges/Connections - Category D Flanges/Connections - Category E Flanges/Connections - Category F Flanges/Connections - Category G PSV - To Atm/Flare PSV - To VRS Pump Seals - Single Pump Seals - Dual/Tandem Sub Total Total Notes: 1 APCD P&P # A 80% efficiency is assigned to fugitive components Rule 331 implementation. 3 Emission Control efficiencies for the "category x" components are identified in "FHC Control Factors (ver 2.0)" Page 11 of 16

16 FIXED ROOF TANK CALCULATION (AP-42: Chapter 7 Method) 1,000 BBL Slop Oil Tank Basic Input Data Attachment: A-1 Permit: Recruit liquid {1:G13, 2:G10, 3:G7, 4:C, 5:JP, 6:ker, 7:O2, 8:O6} = 4 Date: 04/14/14 liquid TVP = 1.4 Tank: New Crude Tank if TVP is entered, enter TVP temperature ( F) = 192 Name: name tank heated {yes, no} = yes Filename: if tank is heated, enter temp ( F) = 180 Distrcit: Santa Barbara vapor recovery system present? {yes, no} = yes Version: Tank-2b.xls is this a wash tank? {yes, no} = no will flashing losses occur in this tank? {yes, no} = no breather vent pressure setting range (psi) (def = 0.06): 0.06 Tank Data diameter (feet) = 21.5 capacity (enter barrels in first col, gals will compute) = 1,000 42,000 conical or dome roof? {c, d} = c shell height (feet) = 16 roof height (def = 1): 1 ave liq height (feet): 12 Paint Factor Matrix Molecular Weight Matrix color {1:Spec Al, 2:Diff Al, 3:Lite, 4:Med, 5:Rd, 6:Wh} = 4 paint condition liquid mol wt condition {1: Good, 2: Poor} = 1 paint color good poor gas rvp upstream pressure (psig) (def = 0 when no flashing occurs): 0 spec alum gas rvp diff alum gas rvp 7 68 Liquid Data lite grey crude oil 50 A B med grey JP maximum daily throughput (bopd) = 500 red jet kerosene 130 Ann thruput (gal): (enter value in Column A if not max PTE) 7.665E+06 white fuel oil RVP (psia): fuel oil API gravity = 16 Computed Values roof outage 1 (feet): 0.3 vapor space volume 2 (cubic feet): 1,561 turnovers 3 : turnover factor 4 : 0.33 paint factor 5 : 0.68 Adjusted TVP Matrix RVP Matrix surface temperatures ( R, F) liquid TVP value liquid RVP value average 6 : gas rvp gas rvp maximum 7 : gas rvp gas rvp minimum 8 : gas rvp gas rvp 7 7 product factor 9 : 0.75 crude oil crude oil diurnal vapor ranges JP JP temperature 10 (fahrenheit degrees): 5 jet kerosene jet kerosene vapor pressure 11 (psia): fuel oil fuel oil molecular weight 12 (lb/lb-mol): 50 fuel oil fuel oil TVP 13 (psia) [adjusted for ave liquid surface temp]: vapor density 14 (lb/cubic foot): vapor expansion factor 15 : Long-Term vapor saturation factor 16 : VRU_Eff = 95.00% vented vapor volume (scf/bbl): 8 fraction ROG - flashing losses: Short-Term fraction ROG - evaporative losses: VRU_Eff = 95.00% Emissions Uncontrolled ROC emissions ROC emissions lb/hr lb/day ton/year lb/hr lb/day ton/year breathing loss 17 = working loss 18 = flashing loss 19 = TOTALS = NOTES: see attachment for explanation of notes (1 through 19) Page 12 of 16

17 COMBUSTION GREENHOUSE GAS EMISSIONS Emission Factors Pollutant EF (lb/mmscf)* EF (lb/mmbtu) CO 2 120, CH N 2 O *AP-42, 1998 HHV 1,050 Btu/scf Global Warming Potential CO 2 GWP 1 CH 4 GWP 25 N 2 O GWP 298 Unit Conversions lb/kg 1000 kg/mt Equipment Capacity (MMBtu/hr) CO 2 Emissions (MTCO 2 ) CH 4 Emissions (MTCH 4 ) N 2 O Emissions (MTN 2 O) GHG Emissions (MTCO 2 e) Each Steam Generator 85 38, ,679.7 Each GWP Treater Boiler 4.9 2, ,229.8 Page 13 of 16

18 On-Road Passenger Vehicle Emissions Average Trip Distance (Miles) Daily Trips New Employee Trips Proposed Increase in Emissions NOX ROC CO SOX PM10 CO2 CH4 CO2e (MT) Emission Factor (lb/mile)* 6.55E E E E E E E-05 - Trip Emissions (lb/trip) 9.17E E E E E E E-04 - Maximum Daily Emissions (lbs/day) Annual Emissions** (tons/year) *Emission factors taken from CARB 2007EMFAC model (Passenger Vehicles, Scenario Year 2014) **Assumes 250 working days per year Page 14 of 16

19 Table 2 Fugitive Emission Factors for Oil and Gas Facilities Using the Component Count Method (P&P ) FACILITY TYPE Production Field 1 Gas Processing Plant 2 Refinery 3 Offshore Platform 4 THC EF 5 ROC/THC THC EF ROC/THC THC EF ROC/THC THC EF ROC/THC Component Type lb/day-comp-lp Ratio lb/day-comp-lp Ratio lb/day-comp-lp Ratio lb/day-comp-lp Ratio Gas/Condensate Service Valve Connection Compressor Seal Pump Seal Pressure Relief Oil Service 6 Valve Connection Pump Seal Pressure Relief NOTES: (1) (2) (3) (4) Eaton, W.S. et al., "Fugitive Hydrocarbon Emissions From Petroleum Operations", American Petroleum Insttitute, Rockwell International, March 1980, See Attachment 1 for tehmethodology used to consolidate the API emission factors. Harris, G.E. et al., "Frequency of Leak Occurence and Emission Factors for Natural Gas Factors for Natural Gas Liquid Plants", EPA DCN , July 1982 For oil service components, see page 3 of Attachment 1. United States Environmental Protection Agency, Assessment of Atmospheric Emissions from Petroleum Refining, EPA-600/ a through -075d, U.S. Environmental Protection Agency, Research Triangle Park, NC, Santa Barbara County APCD, "Modeling of Fugitive Hydrocarbon Emissions", Tecolote Research Inc., January Assumes the facility is primarily a crude oil site with a significant portion of gas components. For ROC/THC ratios for other facility types, please see page 63. (5) "lb/day-clp" = pound of pollutant per day for each component CLP. "THC" = total hydrocarbons (includes methane and ethane) "ROC" = reactive organic compounds (non-methane, non-ethane) (6) Oil service includes water, oil and gas emulsions. Page 15 of 16

20 Table 3 Fugitive Hydrocarbon Control Factors Using the Component Count Method (P&P ) Item Description Notes BACT Vapor Recovery Monthly Inspections LDAR 100 ppmv LDAR 500 ppmv Control Efficiency % 1 Valves - Accessible/Inaccessible 1 80% 2 Valves - Unsafe 0% 3 Valves - Bellows x x 90% 4 Valves - Bellows / Background ppmv 2 x 100% 5 Valves - Category A 3 x 84% 6 Valves - Category B 3 x 85% 7 Valves - Category C 3 x 87% 8 Valves - Category D 3 x x 87% 9 Valves - Category E 3 x x 88% 10 Valves - Category F 4 x x 90% 11 Valves - Category G 4 x x x 92% 12 Flanges/Connections - Accessible/Inaccessible 80% 13 Flanges/Connections - Unsafe 0% 14 Flanges/Connections - Category A 3 x 84% 15 Flanges/Connections - Category B 3 x 85% 16 Flanges/Connections - Category C 3 x 87% 17 Flanges/Connections - Category D 3 x x 87% 18 Flanges/Connections - Category E 3 x x 88% 19 Flanges/Connections - Category F 4 x x 90% 20 Flanges/Connections - Category G 4 x x x 92% 21 Compressor Seals - To Atm 80% 22 Compressor Seals - To VRS x 100% 23 PSV - To Atm/Flare 80% 24 PSV - To VRS x 100% 25 Pump Seals - Single 80% 26 Pump Seals - Dual/Tandem 100% Notes: 1 "Standard" valves and connections/flanges subject to R331 (1000 ppmv/quarterly inspection) = 80% control 2 Bellows valves with 100% control have a minor leak threshold of any OVA reading above background. 3 Categories A through E are defined by lower leak threshold limits and/or increased monitoring frequency of standard components. 4 Categories F and G are BACT approved components that have been designed to perform at a lower leak threshold. Page 16 of 16