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ERG Operating Company Foxen Petroleum Pipeline Volume 2: Appendices September 2014
Appendix 4
Air Quality
Air Emissions Calculations
FOXEN PETROLEUM PIPELINE PROJECT - ATC 14067 June 2013
OPERATIONAL EMISSIONS - Proposed Pipeline and Facility Emissions
Equipment Category Capacity ea. NOX ROC CO SOX PM10
Sales Oil Tanks (2) 10,000 BBL
lbs/day 10.38
tons/year 1.90
Reject Tank 3,000 BBL
lbs/day 0.75
tons/year 0.14
LCO Tank - Contingency Use 3,000 BBL
lbs/day 2400 BBL/day 3.64
tons/year 20 days/year 0.66
Pigging Operations
lbs/day 2 per day max 1.34
tons/year 4 per year max 0.001
Fugitive Component Emissions
lbs/day 8.63
tons/year 1.57
TOTAL
lbs/day 0.00 24.74 0.00 0.00 0.00
tons/year 0.00 4.276 0.00 0.00 0.00
Page 1 of 1
FOXEN PETROLEUM PIPELINE PROJECT
Gas Release Volume from Pigging Operation
Length (in) Length (ft) Diameter (in) Diameter (ft) Radius (ft) Volume (ft3)
391.2 32.6 12.75 1.0625 0.53125 28.904 pig receiver
TOTAL 28.904 per pigging event
Density of TOC in Vessel density = P x MW / R x T
Pressure (psig + 14.7 psi), Depressurize Launch to 5 psig 19.700 psig
Molecular Weight Gas 23.000 lb/lb-mole
R Universal Gas Constant 10.730
Temperature 560.000 R
Calculated Density 0.075 lb/ft3
ROC per Cubic Foot of Volume
ROC = density x 0.308 0.023
ROC Emissions from Pigging Events
lb ROC/ft3 = 0.02322507
Lb ROC Emissions per day 0.67 lb/day
TOTAL ROC Emissions from Pigging Events
Assume a pigging operation occurs in one day 1 0.67 lbs/day
Assume one pigging operation per year 1 0.000335654 tons/year
Page 1 of 12
FIXED ROOF TANK CALCULATION (AP-42: Chapter 7 Method)
10,000 BBL Sales Oil Tanks
Basic Input Data Attachment: A-1
Permit: Foxen Pipeline
liquid {1:G13, 2:G10, 3:G7, 4:C, 5:JP, 6:ker, 7:O2, 8:O6} = 4 Date: 08/30/12
liquid TVP = 3.9 lab data Tank: T-1
if TVP is entered, enter TVP temperature (°F) = 192 lab data 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) = 55
capacity (enter barrels in first col, gals will compute) = 10,000 420,000
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 13 62
upstream pressure (psig) (def = 0 when no flashing occurs): 0 spec alum 0.39 0.49 gas rvp 10 66
diff alum 0.60 0.68 gas rvp 7 68
Liquid Data lite grey 0.54 0.63 crude oil 50
A B med grey 0.68 0.74 JP -4 80
maximum daily throughput (bopd) = 12,500 red 0.89 0.91 jet kerosene 130
Ann thruput (gal): (enter value in Column A if not max PTE) 1.916E+08 white 0.17 0.34 fuel oil 2 130
RVP (psia): 0.69822 fuel oil 6 190
°API gravity = 18
Computed Values
roof outage 1 (feet): 0.3
vapor space volume 2 (cubic feet): 29,223
turnovers 3 : 456.25
turnover factor 4 : 0.23
paint factor 5 : 0.68 Adjusted TVP Matrix RVP Matrix
surface temperatures (°R, °F) liquid TVP value liquid RVP value
average 6 : 640 180 gas rvp 13 23.7 gas rvp 13 13
maximum 7 : 641.25 181.25 gas rvp 10 11.2 gas rvp 10 10
minimum 8 : 638.75 178.75 gas rvp 7 10.7 gas rvp 7 7
product factor 9 : 0.75 crude oil 3.12554 crude oil 0.6982194
diurnal vapor ranges JP -4 4.9 JP -4 2.7
temperature 10
(fahrenheit degrees): 5 jet kerosene 0.0385 jet kerosene 0.029
vapor pressure 11 (psia): 0.146849 fuel oil 2 0.0422 fuel oil 2 0.022
molecular weight 12 (lb/lb-mol): 50 fuel oil 6 0.00016 fuel oil 6 0.00019
TVP 13 (psia) [adjusted for ave liquid surface temp]: 3.12554
vapor density 14 (lb/cubic foot): 0.022755
vapor expansion factor 15 : 0.015 Long-Term
vapor saturation factor 16 : 0.329214 VRU_Eff = 99.00%
vented vapor volume (scf/bbl): 8
fraction ROG - flashing losses: 0.308 Short-Term
fraction ROG - evaporative losses: 0.885 VRU_Eff = 99.00%
Emissions Uncontrolled ROC emissions Controlled ROC emissionslb/hr lb/day ton/year lb/hr lb/day ton/year
breathing loss 17 = 0.12 2.91 0.53 0.00 0.03 0.01
working loss 18 = 12.43 298.22 54.43 0.12 2.98 0.54
flashing loss 19 = 0.00 0.00 0.00 0.00 0.00 0.00
TOTALS = 12.55 301.13 54.96 0.13 3.01 0.55
25.1 602.26 109.92 0.26 6.02 1.1
NOTES: see attachment for explanation of notes (1 through 19)
For Two (2) 10,000 BBL Tanks
Page 2 of 12
FIXED ROOF TANK CALCULATION (AP-42: Chapter 7 Method)
3000 BBL Reject Tank
Basic Input Data Attachment: A-1
Permit: Foxen Pipeline
liquid {1:G13, 2:G10, 3:G7, 4:C, 5:JP, 6:ker, 7:O2, 8:O6} = 4 Date: 08/30/12
liquid TVP = 3.9 Tank: T-1
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) = 30
capacity (enter barrels in first col, gals will compute) = 3,000 126,000
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 13 62
upstream pressure (psig) (def = 0 when no flashing occurs): 0 spec alum 0.39 0.49 gas rvp 10 66
diff alum 0.60 0.68 gas rvp 7 68
Liquid Data lite grey 0.54 0.63 crude oil 50
A B med grey 0.68 0.74 JP -4 80
maximum daily throughput (bopd) = 1,000 red 0.89 0.91 jet kerosene 130
Ann thruput (gal): (enter value in Column A if not max PTE) 1.533E+07 white 0.17 0.34 fuel oil 2 130
RVP (psia): 0.69822 fuel oil 6 190
°API gravity = 18
Computed Values
roof outage 1 (feet): 0.3
vapor space volume 2 (cubic feet): 8,694
turnovers 3 : 121.67
turnover factor 4 : 0.41
paint factor 5 : 0.68 Adjusted TVP Matrix RVP Matrix
surface temperatures (°R, °F) liquid TVP value liquid RVP value
average 6 : 640 180 gas rvp 13 23.7 gas rvp 13 13
maximum 7 : 641.25 181.25 gas rvp 10 11.2 gas rvp 10 10
minimum 8 : 638.75 178.75 gas rvp 7 10.7 gas rvp 7 7
product factor 9 : 0.75 crude oil 3.12554 crude oil 0.6982194
diurnal vapor ranges JP -4 4.9 JP -4 2.7
temperature 10 (fahrenheit degrees): 5 jet kerosene 0.0385 jet kerosene 0.029
vapor pressure 11 (psia): 0.146849 fuel oil 2 0.0422 fuel oil 2 0.022
molecular weight 12
(lb/lb-mol): 50 fuel oil 6 0.00016 fuel oil 6 0.00019
TVP 13 (psia) [adjusted for ave liquid surface temp]: 3.12554
vapor density 14 (lb/cubic foot): 0.022755
vapor expansion factor 15 : 0.015 Long-Term
vapor saturation factor 16 : 0.329214 VRU_Eff = 99.00%
vented vapor volume (scf/bbl): 8
fraction ROG - flashing losses: 0.308 Short-Term
fraction ROG - evaporative losses: 0.885 VRU_Eff = 99.00%
Emissions Uncontrolled ROC emissions Controlled ROC emissionslb/hr lb/day ton/year lb/hr lb/day ton/year
breathing loss 17 = 0.04 0.86 0.16 0.00 0.01 0.00
working loss 18 = 1.77 42.53 7.76 0.02 0.43 0.08
flashing loss 19 = 0.00 0.00 0.00 0.00 0.00 0.00
TOTALS = 1.81 43.39 7.92 0.02 0.43 0.08
Page 3 of 12
FIXED ROOF TANK CALCULATION (AP-42: Chapter 7 Method)
10,000 BBL Emergency Storage Oil Tanks
Basic Input Data Attachment: A-1
Permit: Foxen Pipeline
liquid {1:G13, 2:G10, 3:G7, 4:C, 5:JP, 6:ker, 7:O2, 8:O6} = 4 Date: 08/30/12
liquid TVP = 3.9 lab data Tank: T-1
if TVP is entered, enter TVP temperature (°F) = 192 lab data 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) = 55
capacity (enter barrels in first col, gals will compute) = 10,000 420,000
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 13 62
upstream pressure (psig) (def = 0 when no flashing occurs): 0 spec alum 0.39 0.49 gas rvp 10 66
diff alum 0.60 0.68 gas rvp 7 68
Liquid Data lite grey 0.54 0.63 crude oil 50
A B med grey 0.68 0.74 JP -4 80
maximum daily throughput (bopd) = 3,333.33 red 0.89 0.91 jet kerosene 130
Ann thruput (gal): (enter value in Column A if not max PTE) 5.110E+07 white 0.17 0.34 fuel oil 2 130
RVP (psia): 0.69822 fuel oil 6 190
°API gravity = 18
Computed Values
roof outage 1 (feet): 0.3
vapor space volume 2 (cubic feet): 29,223
turnovers 3 : 121.67
turnover factor 4 : 0.41
paint factor 5 : 0.68 Adjusted TVP Matrix RVP Matrix
surface temperatures (°R, °F) liquid TVP value liquid RVP value
average 6 : 640 180 gas rvp 13 23.7 gas rvp 13 13
maximum 7 : 641.25 181.25 gas rvp 10 11.2 gas rvp 10 10
minimum 8 : 638.75 178.75 gas rvp 7 10.7 gas rvp 7 7
product factor 9 : 0.75 crude oil 3.12554 crude oil 0.6982194
diurnal vapor ranges JP -4 4.9 JP -4 2.7
temperature 10
(fahrenheit degrees): 5 jet kerosene 0.0385 jet kerosene 0.029
vapor pressure 11 (psia): 0.146849 fuel oil 2 0.0422 fuel oil 2 0.022
molecular weight 12 (lb/lb-mol): 50 fuel oil 6 0.00016 fuel oil 6 0.00019
TVP 13 (psia) [adjusted for ave liquid surface temp]: 3.12554
vapor density 14 (lb/cubic foot): 0.022755
vapor expansion factor 15 : 0.015 Long-Term
vapor saturation factor 16 : 0.329214 VRU_Eff = 99.00%
vented vapor volume (scf/bbl): 8
fraction ROG - flashing losses: 0.308 Short-Term
fraction ROG - evaporative losses: 0.885 VRU_Eff = 99.00%
Emissions Uncontrolled ROC emissions Controlled ROC emissionslb/hr lb/day ton/year lb/hr lb/day ton/year
breathing loss 17 = 0.12 2.91 0.53 0.00 0.03 0.01
working loss 18 = 5.91 141.76 25.87 0.06 1.42 0.26
flashing loss 19 = 0.00 0.00 0.00 0.00 0.00 0.00
TOTALS = 6.03 144.67 26.40 0.06 1.45 0.26
12.06 289.34 52.8 0.12 2.9 0.52For Two (2) 10,000 BBL Tanks
Page 4 of 12
FOXEN PETROLEUM PIPELINE PROJECT
Date: 06/14/12
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. ................................................23ew
Max. Firing Rate of Burner .....................................5.000 MMBtu/hr
Max. Annual Heat Input ......................................43,800.000 MMBtu/yr
Daily Operating schedule .................................... 24 hrs/day
Yearly Load factor (%) .......................................... 100 %
Fuel Type ...........................................................Produced gas
High Heating Value ......................................... 1,050 Btu/scf
Sulfur Content of Fuel .................................... 80.00 ppmvd as H2S
Nitrogen Content of Fuel ........................................ - wt. % N
Boiler Classification ........................................Industrial
Firing Type ............................................ Other Type
PM Emission Factor ...........................................0.0075 lb/MMBtu
PM10 Emission Factor ...........................................0.0075 lb/MMBtu
NOx Emission Factor ...................................... 0.0360 lb/MMBtu
SOx Emission Factor ..................................... 0.0137 lb/MMBtu
CO Emission Factor ............................................0.2970 lb/MMBtu
ROC Emission Factor .................................. 0.0054 lb/MMBtu
RESULTS lb/hr lb/day TPY
Nitrogen Oxides (as NO2) ......................................0.18 4.3 0.79
Sulfur Oxides (as SO2) ........................................0.07 1.6 0.30
PM10 .....................................................................0.04 0.9 0.16
Total Suspended Particulate (PM) ..................................0.04 0.9 0.16
Carbon Monoxide ...............................................1.49 35.6 6.50
Reactive Organic Compounds (ROC) ..............................0.03 0.6 0.12
Page 5 of 12
FOXEN PETROLEUM PIPELINE PROJECT
Heater GHG Emission Calculations
Heater Parameters - Primary and Back Up GHG Emission Factors
Rated Capacity 5 MMBtu/hr 53.02 kg CO2/MMBtu
Load Factor 100 % 0.0009 kg CH4/MMBtu
CO2 Emissions 584.55 lbs/hr 0.0001 kg N₂O/MMBtu
14,029.08 lbs/day Emission Calculation Assumptions
2,560.31 tons/year 2.205 lbs/kg
2,322.27 metric tonnes/year 116.909 lbs in 53.02 kg
24 hours/day
Total GHG Emissions 365 days/year
14,029.08 lbs/day 2,205 lbs/metric tonne
2,322.27 MT/year 2,000 lbs/US short ton
0.238 lbs/day
0.0394 MT/year
0.026 lbs/day
0.0044 MT/year
Notes:
CO2 EF Source AB32: Appendix A, Table 4
CH4 EF Source AB32: App. A Table 6
Table: "Default Carbon Content, Heat Content, and Carbon Dioxide Emission Factors from
Stationary Combustion by Fuel Type"
(unspecified weighted US avergae Natural Gas Higher Heating Value)
CO2
CH4
N2O
Page 6 of 12
FUGITIVE ROC EMISSIONS CALCULATION
ADMINISTRATIVE INFORMATION
Enhanced Fugitive I&M Program
Company: ERB
Facility: Foxen Petroleum Pipeline
Processed by: LMN
Date: 8/20/2012
Facility Type: (Choose one)
Production Field x
Gas Processing Plant ROC(2)
Uncontrolled Controlled Controlled Controlled Controlled
Refinery Emission ROC/THC ROC ROC ROC ROC ROC ROC
Offshore Platform Factor Ratio Emission Control Emission Emission Emission Emission
Component Count(1)
(lbs/day-clp) (lbs/day) Eff (lbs/hr) (lbs/day) (Tons/Qtr) (Tons/year)
Gas Condensate Service
Valves - Acc/Inacc 4 0.295 0.31 0.37 0.92 0.00 0.03 0.00 0.01
Valves - Bellows 0.295 0.31 0.00 1.00 0.00 0.00 0.00 0.00
Valves - Unsafe 0.295 0.31 0.00 0.00 0.00 0.00 0.00 0.00
Valves - Low Emitting 0.295 0.31 0.00 0.00 0.00 0.00 0.00 0.00
Valves - E-500 0.295 0.31 0.00 0.85 0.00 0.00 0.00 0.00
Valves - E-100 0.295 0.31 0.00 0.90 0.00 0.00 0.00 0.00
Flanges - Acc/Inacc 30 0.070 0.31 0.65 0.92 0.00 0.05 0.00 0.01
Flanges - Unsafe 0.070 0.31 0.00 0.00 0.00 0.00 0.00 0.00
Flanges - E-500 0.070 0.31 0.00 0.85 0.00 0.00 0.00 0.00
Flanges - E-100 0.070 0.31 0.00 0.90 0.00 0.00 0.00 0.00
Compressor Seals - To Atm 2.143 0.31 0.00 0.80 0.00 0.00 0.00 0.00
Compressor Seals - To VRS 4 2.143 0.31 2.66 1.00 0.00 0.00 0.00 0.00
Compressor Seals - E-500 2.143 0.31 0.00 0.85 0.00 0.00 0.00 0.00
Compressor seals - E-100 2.143 0.31 0.00 0.90 0.00 0.00 0.00 0.00
PSV - To Atm 6.670 0.31 0.00 0.80 0.00 0.00 0.00 0.00
PSV - To VRS 4 6.670 0.31 8.27 1.00 0.00 0.00 0.00 0.00
PSV - E-500 6.670 0.31 0.00 0.85 0.00 0.00 0.00 0.00
PSV - E-100 6.670 0.31 0.00 0.90 0.00 0.00 0.00 0.00
Pump Seals 1.123 0.31 0.00 0.80 0.00 0.00 0.00 0.00
Pump Seals - E-500 1.123 0.31 0.00 0.85 0.00 0.00 0.00 0.00
Pump Seals - E-100 1.123 0.31 0.00 0.90 0.00 0.00 0.00 0.00
Sub Total 42 11.94 0.00 0.08 0.00 0.01
Oil Service
Valves - Acc/Inacc 324 0.0041 0.56 0.74 0.92 0.00 0.06 0.00 0.01
Valves - Unsafe 0.0041 0.56 0.00 0.00 0.00 0.00 0.00 0.00
Valves - E-500 0.0041 0.56 0.00 0.85 0.00 0.00 0.00 0.00
Valves - E-100 0.0041 0.56 0.00 0.90 0.00 0.00 0.00 0.00
Flanges - Acc/Inacc 888 0.0020 0.56 0.99 0.92 0.00 0.08 0.00 0.01
Flanges - Unsafe 0.0020 0.56 0.00 0.00 0.00 0.00 0.00 0.00
Flanges - E-500 0.0020 0.56 0.00 0.85 0.00 0.00 0.00 0.00
Flanges - E-100 0.0020 0.56 0.00 0.90 0.00 0.00 0.00 0.00
Pump Seals - Single 13 0.0039 0.56 0.03 0.80 0.00 0.01 0.00 0.00
Pump Seals - E-500 0.0039 0.56 0.00 0.85 0.00 0.00 0.00 0.00
Pump Seals - E-100 0.0039 0.56 0.00 0.90 0.00 0.00 0.00 0.00
PSV - To Atm 8 0.2670 0.56 1.20 0.80 0.01 0.24 0.01 0.04
PSV - To VRS 0.2670 0.56 0.00 1.00 0.00 0.00 0.00 0.00
PSV - E-500 0.2670 0.56 0.00 0.85 0.00 0.00 0.00 0.00
PSV - E-100 0.2670 0.56 0.00 0.00 0.00 0.00 0.00 0.00
Sub Total 1233 2.963 0.02 0.38 0.02 0.07
Total 1275 14.91 0.02 0.47 0.02 0.08
TOTAL for (4) 10,000 BBL Tanks plus Other Equipment 24.85 0.03 0.78 0.04 0.14
Notes:
1. Source:
2. APCD P&P # 6100.060.1998.
3. APCD P&P # 6100.061.1998
4. A 80% efficiency is assigned to fugitive components Rule 331 implementation.
Page 7 of 12
LOADING RACK EMISSION CALCULATION (ver 3.0)
Attachment: A Reference: Loading Rack
Company: ERG Foxen Canyon Pipeline Rack Type: Enter X as Appropriate S Factor
Facility: Emergency Trucking ScenarioSubmerged loading of a clean cargo tank
0.50
File Name: Submerged loading: Dedicated normal servicex 0.60
Submerged loading: Dedicated vapor balance
service 1.00
Splash loading of a clean cargo tank1.45
Splash loading: Dedicated normal service1.45
Splash loading: Dedicated vapor balance
service 1.00
Input data Reference
S = Saturation Factor 0.60 See AP-42 Table 4.4-1 2
M = Molecular Weight 50 Crude Oil: Default = 50 lb/lb-mole 3
P = True Vapor Pressure (psia) 3.900 See AP-42 Table 12.3-5 1T = Liquid Temperature 0R 640 180
0F + 460 =
0R 5
R = Loading Rate (bbl/hr) 417.00 17,514 gallons (42 gallons = 1 bbl) 1
C = Storage Capacity (bbl) 25,000 1,050,000 gallons (42 gallons = 1 bbl) 1
D = Daily Production (bbl) 10,000 420,000 gallons (42 gallons = 1 bbl)
A = Annual Production (bbl) 100,000 4,200,000 gallons (42 gallons = 1 bbl) 1
eff = Vapor Recovery Efficiency 0.99 Default = 0.95 1
ROC/THC = Reactivity Crude Oil: Default = 0.885
HLPD = hours loading per day = (C/R) if < 24 = 24.00 hours/day
HLPY = hours loading per year = (A/R) = 239.81 hours/year
LL = Loading loss (lb/1000 gal) = 12.46 (S)(P)(M)/T = 2.2778 lb/1000 gal
Total Uncontrolled Hydrocarbon Losses:
Hourly
THLH = (R)(42 gal/bbl)(LL/1000) = 39.89 lbs/hr
Daily
THLD = (THLH)(HLPD) = 957.46 lbs/day
Annual
THLA = (HLPY)((THLH)(1/2000) = 4.78 TPY
Total Controlled Hydrocarbon Losses:
Hourly
THLHC = (THLH)(1-eff) = 0.40 lbs/hr
Daily
THLDC = (THLD)(1-eff) = 9.57 lbs/day
Annual
THLAC = (THLA)(1-eff) = 0.05 TPY
Processed by: Name Date: August 30, 2012
Notes:
1. Data provided by the applicant
2. AP-42, (Chapter 5, 5th Edition, January 1995), Table 5.2-1
3. If not otherwise provided, crude oil is assumed to be 50 lb/lb-mole.
4. If not otherwise provided, vapor pressure is calculated from CARB AB-2588 Guidelines, page 103, eq. 25
5. R is calculated by adding 460 to 0F.
Revised: October 8, 2007
Page 8 of 12
FOXEN PETROLEUM PIPELINE PROJECT
OPERATIONAL EMISSIONS - Proposed Pipeline and Facility Emissions
Equipment Category Capacity ea. NOX ROC CO SOX PM10 CO2 CH4 N2O CO2e*
Sales Oil Tanks (2) 10,000 BBL
lbs/day 6.02
tons/year 1.10
Reject Tank 3,000 BBL
lbs/day 0.43
tons/year 0.08
Heaters (Primary and Back Up) 5 MMBTU/hr
lbs/day 4.32 0.65 35.64 1.64 0.90 14,029 0.24 0.03 14,042
tons/year 0.79 0.12 6.50 0.30 0.16 2,322 0.04 0.004 2,324
Emergency Oil Tanks (2) 10,000 BBL
lbs/day 2.9
tons/year 0.52
Loading Rack - Emergency Trucking
lbs/day 9.57
tons/year (10 days loading per year) 0.05
Pigging Operations
lbs/day 0.67
tons/year 0.00
Fugitive Component Emissions
lbs/day 0.78
tons/year 0.14
TOTAL
lbs/day 4.32 21.02 35.64 1.64 0.90 14,029 0.24 0.03 14,042
tons/year or MT*/year 0.79 2.01 6.50 0.30 0.16 2,322 0.04 0.004 2,324
CEQA Thresholds (lbs/day) 55.00 55.00 240.00 55.00 80.00 - - - 10,000 MT/yr
*CO₂, CH4, and N2O annual emissions are in Metric Tonnes (MT)
CH4 and N2O emissions are converted to CO2 equivalents by multiplying their emissions by their global warming potential (21 for CH4, 310 for N2O)
SBCAPCD BACT and Offsets Thresholds Comparison
Threshold Units NOX ROC CO SOX PM10
BACTlbs/day per
project25 25 550 25 25
Offsetslbs/day per
project55 55 240 55 80
Page 9 of 12
FOXEN PETROLEUM PIPELINE PROJECT
Trucking Emissions
Baseline Increase New Proposed
Trucking Rate (BBL/day) 3,100 6,800 9,900
Trip Distance (Miles) 21 0 21
Daily Trips 19 42 61
Oil Storage Capacity per
Truck (BBL)160
Proposed Increase in Emissions
NOX ROC CO SOX PM10 CO2 CH4 CO2e (MT)
Emission Factor (lb/mile)* 0.027 0.002 0.009 0.00004 0.001 4.215 0.0001 -
Trip Emissions (lb/trip) 0.587 0.048 0.199 0.001 0.029 90.205 0.002 -Maximum Daily Emissions
(lbs/day)24.653 2.034 8.375 0.037 1.202 3,789 0.094 -
Annual Emissions**
(tons/year)0.370 0.031 0.126 0.001 0.018 51.555 0.001 51.582
*Emission factors taken from CARB 2007EMFAC model (2013 heavy-duty diesel truck)
**Calculated based on estimated annual trips needed to transport oil
Page 10 of 12
FOXEN PETROLEUM PIPELINE PROJECT
Stationary and Mobile Emissions Summary
NOX ROC CO SOX PM10 CO2* CH4* N2O* NOX ROC CO SOX PM10 CO2* CH4* N2O*
Stationary Emissions 4.320 21.019 35.640 1.644 0.900 14,029 0.238 0.026 0.788 2.008 6.504 0.300 0.164 2,322 0.039 0.004 2,324
Mobile Emissions 24.653 2.034 8.375 0.037 1.202 3,789 0.094 0.000 0.370 0.031 0.126 0.001 0.018 52 0.001 0.000 52
Total Emissions 28.973 23.054 44.015 1.681 2.102 17,818 0.332 0.026 1.158 2.038 6.630 0.301 0.182 2,374 0.041 0.004 2,376
CEQA Thresholds 55 55 240 55 80 - - - 10 10 25 15 10 - - - 10,000
Above Threshold? No No No No No No No No No No No No No No No No No
* CO2, CH4, and N2O annual emissions are in Metric Tonnes (MT)
CH4 and N2O emissions are converted to CO2 equivalents by multiplying their emissions by their global warming potential (21 for CH4, 310 for N2O)
Daily Emissions (lbs/day) Annual Emissions (tons/year)CO2e*
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FOXEN PETROLEUM PIPELINE PROJECT
Construction Emissions
ROC CO NOX SOX PM10 CO2 CH4 ROC CO NOX SOX PM10 CO2 CH4
Backhoe 1 40 101 0.069 0.353 0.457 0.001 0.038 51.700 0.006 5 35 0.139 0.706 0.913 0.001 0.077 103.400 0.013
Steel Drum Roll 1 60 150 0.147 0.735 1.119 0.001 0.063 124.000 0.013 4 35 0.352 1.763 2.686 0.003 0.151 297.600 0.032
Crane 1 40 250 0.104 0.295 0.995 0.001 0.035 112.000 0.009 1 5 0.042 0.118 0.398 0.001 0.014 44.800 0.004
Water Truck 1 40 190 0.144 0.758 1.031 0.001 0.060 125.000 0.013 2 35 0.115 0.606 0.824 0.001 0.048 100.000 0.010
Delivery Truck & Trailer 1 20 450 0.217 0.636 1.672 0.003 0.063 272.000 0.020 2 4 0.087 0.254 0.669 0.001 0.025 108.800 0.008
Pick-Ups 2 50 185 0.144 0.758 1.031 0.001 0.060 125.000 0.013 2 35 0.288 1.516 2.061 0.003 0.120 250.000 0.026
TOTAL 1.023 4.963 7.551 0.010 0.436 904.600 0.092
ROC CO NOX SOX PM10 CO2 CH4 ROC CO NOX SOX PM10 CO2 CH4
Dump Truck 1 40 487 0.217 0.636 1.787 0.003 0.063 272.000 0.020 3 60 0.260 0.763 2.144 0.003 0.076 326.400 0.024
Water Truck 1 40 190 0.144 0.758 1.031 0.001 0.060 125.000 0.013 2 60 0.115 0.606 0.824 0.001 0.048 100.000 0.010
Welding Machine 3 60 50 0.098 0.275 0.254 0.000 0.024 26.000 0.009 6 60 1.057 2.973 2.738 0.003 0.259 280.800 0.095
Compactor 1 40 240 0.149 0.433 1.418 0.002 0.049 172.000 0.014 7 60 0.418 1.213 3.972 0.005 0.138 481.600 0.038
Backhoe 1 40 101 0.069 0.353 0.457 0.001 0.038 51.700 0.006 6 60 0.167 0.847 1.096 0.001 0.092 124.080 0.015
Excavator 1 40 125 0.109 0.518 0.679 0.001 0.059 73.600 0.010 6 60 0.261 1.242 1.630 0.002 0.141 176.640 0.024
A-Frame 1 40 330 0.155 0.529 1.132 0.002 0.052 180.000 0.014 6 60 0.372 1.270 2.716 0.004 0.124 432.000 0.034
Pavement Saw 1 20 60 0.070 0.754 0.249 0.002 0.030 141.000 0.006 1 5 0.014 0.151 0.050 0.000 0.006 28.200 0.001
Road Boring Machine 1 80 30 0.012 0.063 0.125 0.000 0.003 10.300 0.001 1 10 0.010 0.051 0.100 0.000 0.002 8.240 0.001
Delivery Truck & Trailer 1 20 450 0.217 0.636 1.672 0.003 0.063 272.000 0.020 2 10 0.087 0.254 0.669 0.001 0.025 108.800 0.008
Pick-Ups 3 50 185 0.144 0.758 1.031 0.001 0.060 125.000 0.013 3 60 0.648 3.411 4.637 0.006 0.271 562.500 0.059
TOTAL 3.409 12.782 20.575 0.029 1.183 2,629.260 0.307
ROC CO NOX SOX PM10 CO2 CH4 ROC CO NOX SOX PM10 CO2 CH4
Backhoe 1 40 101 0.069 0.353 0.457 0.001 0.038 51.700 0.006 5 20 0.139 0.706 0.913 0.001 0.077 103.400 0.013
Crane 1 40 250 0.104 0.295 0.995 0.001 0.035 112.000 0.009 1 5 0.042 0.118 0.398 0.001 0.014 44.800 0.004
Dump Truck 1 40 487 0.217 0.636 1.787 0.003 0.063 272.000 0.020 2 20 0.174 0.509 1.429 0.002 0.051 217.600 0.016
Welding Machine 1 60 50 0.098 0.275 0.254 0.000 0.024 26.000 0.009 6 60 0.352 0.991 0.913 0.001 0.086 93.600 0.032
Pick-Ups 2 50 185 0.144 0.758 1.031 0.001 0.060 125.000 0.013 2 20 0.288 1.516 2.061 0.003 0.120 250.000 0.026
TOTAL 0.995 3.840 5.714 0.008 0.348 709.400 0.090
ROC CO NOX SOX PM10 CO2 CH4
5.43 21.59 33.84 0.05 1.97 4,243.26 0.49
Daily Emissions (lb/day)
Daily Emissions (lb/day)
ConocoPhillips Tie-In
Equipment No. Each Load % HP
AGGREGATE TOTALS
Emission Factors (lb/hr) Hours per
Peak Day
Days per
Project
Year
Hours per
Peak Day
Days per
Project
Year
Daily Emissions (lb/day)
Installation of Cantin Facility
Equipment No. Each Load % HPHours per
Peak Day
Days per
Project
Year
Daily Emissions (lb/day)
8" Pipeline Installation
Equipment No. Each Load % HPEmission Factors (lb/hr)
Emission Factors (lb/hr)