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Facility Information

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-

16HW, 21-16HX, 21-16HZ Name of the facility and the well number.

Not Producing Yet Approximate first date of production or the date of modification of the facility.

Production Data Description

BOPD 5783 Average daily production in barrels of oil per day (BOPD), based on the predicted first 30 days of production.

Mscfd 4019 Average daily production of gas in Mscf per day, based on the predicted first 30 days of production.

Decline Factor 0.505 Expected decline factor for the first year of operation. Based on data from previously producing wells in the same field and formation.

Adjusted BOPD 2922 This is the calculated BOPD expected to be produced using the above entered decline factor.

Adjusted Produced Gas (Mscfd) 2031 This is the calculated mcfd of gas the well is expected to produce using the above entered decline factor.

Oil/Condensate Tank Data Description

Flash Gas Method: Process Simulator Use the drop down menu to choose the appropriate flash gas method.

Process Simulator Estimated scf/bbl 39.1 The scf/bbl from direct measurement or representative sample. Based on representative E&P Tank Emission Summary Output.

Estimated Tank Vapors (scfd) 114264.75 This is the estimated scfd of tank vapors based on the following: adjusted BOPD multiplied by the scf/bbl entered on Line 9.

Lower Heating Value 2338.03 Lower heating value (Btu/scf) of tank vapors. Based on representative E&P Tank Emission Summary Output.

Molecular Weight 40.93 Molecular weight of the tank vapors in pounds per pound-mole (lb/lb-mole). Based on representative E&P Tank Emission Summary Output.

VOC% 73.87712 VOC weight fraction of the tank vapor gas (C3+). Based on representative E&P Tank Emission Summary Output.

VOC TPY/BOPD Emission Factor 0.6514 Based on representative E&P Tank Emission Summary Output. (Summary Output creates a linear relationship between TPY and BOPD) 

HAP% 0.7286263 HAP weight fraction of the tank vapor gas. Based on representative E&P Tank Emission Summary Output.

HAP TPY/BOPD Emission Factor 0.0056 Based on representative E&P Tank Emission Summary Output. (Summary Output creates a linear relationship between TPY and BOPD) 

CO2% 0.29% CO2 weight fraction of the tank vapor gas. Based on representative E&P Tank Emission Summary Output.

CH4% 2.15% CH4 weight fraction of the tank vapor gas. Based on representative E&P Tank Emission Summary Output.

H2S weight % 0.09% H2S weight percent of the tank vapor gas. Based on representative E&P Tank Emission Summary Output.

H2S mole % 0.11% H2S mole percent of the tank vapor gas. Based on representative E&P Tank Emission Summary Output.

Enclosed Smokeless Combustor Use the drop down menu to choose the appropriate emission control type.

Control Destruction Efficiency 98% Control efficiency of any applicable controls. This is a fixed number based on control type.

RED = No input required. This is a calculated value.

Input Data

Dakota-3 E&P Company, LLC

GREEN = Requires input
Facility Information

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-

16HW, 21-16HX, 21-16HZ Name of the facility and the well number.

RED = No input required. This is a calculated value.

Input Data

Dakota-3 E&P Company, LLC

GREEN = Requires input

Treater Gas Data Description

Btu/scf 1700.3866 Btu/scf of wellstream gas. (From representative field gas analysis)

Molecular Weight 29.646857 Average molecular weight of the wellstream gas in lb/lb-mole. (From representative field gas analysis)

Specific Gravity 1.0236429 If necessary to convert specific gravity to molecular weight, enter the specific gravity of the wellstream gas. (From representative field gas analysis)

Average Molecular Weight 29.647 (From representative field gas analyses)

VOC% 45.94% VOC weight fraction of the wellstream gas (Note: Weight%, not Mole%). (From representative field gas analysis)

HAP% 1.28% HAP weight fraction of the wellstream gas. (Note: Weight%, not Mole%). (From representative field gas analysis)

CO2% 0.863% CO2 weight fraction of the wellstream gas. (Note: Weight%, not Mole%). (From representative field gas analysis)

CH4% 25.747% CH4 weight fraction of the wellstream gas. (Note: Weight%, not Mole%). (From representative field gas analysis)

H2S weight % 0.000% H2S weight percent of the wellstream gas. (From representative field gas analysis)

H2S mole % 0.000% H2S mole percent of the wellstream gas. (From representative field gas analysis)

Connected to sales line Use the drop down menu to choose the appropriate emission control type.

Control/Capture Efficiency 100% If routed to pipeline, assumed 100% capture of gas. If flared, control efficiency of any applicable controls (combustor, pit flare, utility flare, etc).

Treater Burner(s) Description

Total Btu/hr 5250000 Total burner rating for the heater treater burner(s) in btu/hr. If there are multiple burners, add the total heat input together.

Hours of Operation 8,760 The burner(s) is/are assumed to operate 8,760 hours per year.

Truck Loading Description

Oil is sold through LACT Use the drop down menu to choose the appropriate oil sales method. If oil is sold through a LACT, no input values are required in Lines 30-35.

Submerged loading: dedicated normal service 0.6 Use the drop down list to choose the appropriate mode of operation. The saturation factor will automatically be selected based on mode of operation.

Molecular Weight 40.93 Molecular weight of tank vapors in lb/lb-mole. Assumed same molecular weight as flashing emissions from representative E&P Tanks data.

Vapor Pressure 2.30 True vapor pressure of liquid loaded, pounds per square inch absolute (psia) If no site specific data is available, please refer to Table 2 on Truck Loading tab.

Temperature 50.00 Temperature of bulk liquid loaded in Fahrenheit. If no site specific data is available, use an estimated average annual temperature.

Load Rate (bbl/hr) 180 Load rate of liquid loaded in barrels per hour.

Load Time (hrs) 1.00 The time it takes to loadout one load (hrs).

Pneumatic Pumps and Contollers (None) Description

Glycol Dehydrator (None) Description
Facility:

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-

16HB, 21-16HC 21-16HD, 21-

16HW, 21-16HX, 21-16HZ

VOC HAP NOx PM PM10 PM2.5 CO H2S SO2 HCHO

Oil/Condensate Tanks 1903.63 16.41 N/A N/A N/A N/A N/A N/A N/A Negligible

Casing Head Gas 26.64 0.74 4.29 0.28 0.28 0.28 23.32 NA 0.00 0.00

Treater Burner 0.12 0.04 2.25 0.17 0.17 0.17 1.89 N/A 0.01 Negligible

RICE Engine 7.93 1.19E-01 30.44 0.18 0.18 0.18 50.26 N/A 1.45E-01 0.12

Truck Loading N/A N/A N/A N/A N/A N/A N/A N/A N/A Negligible

Fuel Storage Tank Negligible Negligible N/A N/A N/A N/A N/A N/A N/A N/A

Pneumatic Pump N/A N/A N/A N/A N/A N/A N/A N/A N/A Negligible

Pneumatic Controllers N/A N/A N/A N/A N/A N/A N/A N/A N/A Negligible

Glycol Dehydrator N/A N/A N/A N/A N/A N/A N/A N/A N/A Negligible

Totals (TPY) 1938.33 17.31 36.98 0.63 0.63 0.63 75.47 0.00 0.16 0.12

VOC HAP NOx PM PM10 PM2.5 CO H2S SO2 HCHO

Oil/Condensate Tanks 38.07 0.33 3.32 0.16 0.16 0.16 18.04 N/A N/A Negligible

Casing Head Gas 26.64 0.74 4.29 0.28 0.28 0.28 23.32 0.00 0.00 0.00

Treater Burner 0.12 0.04 2.25 0.17 0.17 0.17 1.89 N/A 0.01 Negligible

RICE Engine 7.93 1.19E-01 30.44 0.18 0.18 0.18 50.26 N/A 1.45E-01 0.12

Truck Loading N/A N/A N/A N/A N/A N/A N/A N/A N/A Negligible

Fuel Storage Tank Negligible Negligible N/A N/A N/A N/A N/A N/A N/A N/A

Pneumatic Pump N/A N/A N/A N/A N/A N/A N/A N/A N/A Negligible

Pneumatic Controllers N/A N/A N/A N/A N/A N/A N/A N/A N/A Negligible

Glycol Dehydrator N/A N/A N/A N/A N/A N/A N/A N/A N/A Negligible

Totals (TPY) 72.77 1.23 40.30 0.79 0.79 0.79 93.51 0.00 0.16 0.12

a

Emissions of lead and lead compounds, fluorides, sulfuric acid mist, total reduced sulfur, and reduced sulfur compounds are assumed to be negiligable for upstream oil & gas operations on the FBIR.

Criteria Pollutants

Criteria Pollutantsa

Dakota-3 E&P Company, LLC

Allowable Potential to Emit

Emission Summary

Uncontrolled Potential to Emit
Facility:

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-

16HB, 21-16HC 21-16HD, 21-

16HW, 21-16HX, 21-16HZ

Dakota-3 E&P Company, LLC

CO2 CH4 N2O CO2 CH4 N2O

Oil/Condensate Tanks N/A 48.40 N/A 2508.83 0.00 0.05

Casing Head Gas 4473.01 14.93 0.00 4473.01 14.93 0.00

Treater Burner 2705.29 0.15 0.03 2705.29 0.15 0.03

RICE Engine 2.65E+02 0.40 0.08 2.65E+02 0.40 0.08

Truck Loading 0.00 0.00 N/A 0.00 0.00 N/A

Fuel Storage Tank N/A N/A N/A N/A N/A N/A

Pneumatic Pump N/A N/A N/A N/A N/A N/A

Pneumatic Controllers N/A N/A N/A N/A N/A N/A

Glycol Dehydrator N/A N/A N/A N/A N/A N/A

Totals (TPY) 7443.25 63.88 0.12 9952.07 15.48 0.16

GHG Mass Emissions (tpy): 7507.25 GHG Mass Emissions (tpy): 9967.72

CO2e (tpy): 8820.53 CO2e (tpy): 10327.90

Applicable to the Tailoring Rule?: No

b Hydrofluorocarbons (HFCs), Perfluorocarbons (PFCs), and Sulfur Hexafluorides (SF6) emissions are not created from O&G production operations.

Actual

Greenhouse Gasesb

Potential To Emit

Greenhouse Gasesb
BOPD

scf/day

Btu/scf

lb/lb-mole

tpy/bopd

HAPs:

Benzene wt Fraction

Toluene wt Fraction

E-Benzene wt Fraction

Xylene wt Fraction

n-Hexane wt Fraction

2,2,4-Trimethylpentane

wt Fraction

HAP Emission Factor tpy/bopd

98% destruction efficiency of the VOC gas.

0.0203%

0.0021%

0.0110%

0.6343%

0.0116%

0.0493%

CH4 wt Fraction

0.006

Controlled emissions are calculated based on a 

0.29%

2.15%

CO2 wt Fraction

Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Tanks

Flare Gas Volume 114,265

Oil Production 2922

0.651

Lower Heating Value 2338.03

Molecular Weight 40.93

VOC wt Fraction 73.88%

VOC Emission Factor
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Tanks

Uncontrolled VOCs (PTE):

DRE

Using E&P Tanks Run: 0.651 x 2922.37 x 0% = 1903.63 TPY

Controlled VOCs (Allowable):

DRE

Using E&P Tanks Run: 0.651 x 2922.37 x 98% = 38.07 TPY

Uncontrolled HAPs (PTE):

Using E&P Tanks Run: wt% DRE TPY

Benzene 4,761 scf/hr x x 1/379 scf/lb-mole x 40.93 lb/lb-mol x 0.02% x 0% = 0.10 lb/hr 0.46

E-Benzene 4,761 scf/hr x x 1/379 scf/lb-mole x 40.93 lb/lb-mol x 0.00% x 0% = 0.01 lb/hr 0.05

Toluene 4,761 scf/hr x x 1/379 scf/lb-mole x 40.93 lb/lb-mol x 0.01% x 0% = 0.06 lb/hr 0.25

n-Hexane 4,761 scf/hr x x 1/379 scf/lb-mole x 40.93 lb/lb-mol x 0.63% x 0% = 3.26 lb/hr 14.29

Xylene 4,761 scf/hr x x 1/379 scf/lb-mole x 40.93 lb/lb-mol x 0.01% x 0% = 0.06 lb/hr 0.26

2,2,4-Trimethylpentane 4,761 scf/hr x x 1/379 scf/lb-mole x 40.93 lb/lb-mol x 0.05% x 0% = 0.25 lb/hr 1.11

Uncontrolled TOTAL HAPS (TPY) 16.41

Controlled HAPs (Allowable):

Benzene 4,761 scf/hr x x 1/379 scf/lb-mole x 40.93 lb/lb-mol x 0.02% x 98% = 0.00 lb/hr 0.01

E-Benzene 4,761 scf/hr x x 1/379 scf/lb-mole x 40.93 lb/lb-mol x 0.00% x 98% = 0.00 lb/hr 0.00

Toluene 4,761 scf/hr x x 1/379 scf/lb-mole x 40.93 lb/lb-mol x 0.01% x 98% = 0.00 lb/hr 0.00

n-Hexane 4,761 scf/hr x x 1/379 scf/lb-mole x 40.93 lb/lb-mol x 0.63% x 98% = 0.07 lb/hr 0.29

Xylene 4,761 scf/hr x x 1/379 scf/lb-mole x 40.93 lb/lb-mol x 0.01% x 98% = 0.00 lb/hr 0.01

2,2,4-Trimethylpentane 4,761 scf/hr x x 1/379 scf/lb-mole x 40.93 lb/lb-mol x 0.05% x 98% = 0.01 lb/hr 0.02

Controlled TOTAL HAPS (TPY) 0.33

BOPD

TPY VOC/BOPD

TPY VOC/BOPD

CRITERIA POLLUTANT EMISSIONSa

BOPD

=

=

=

=

=

=

=

=

=

=

=

=

=

=
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Tanks

Uncontrolled NOx:

NOx: 0 scf/hr x 2,338 Btu/scf x x 0.068 lb/MMBtu = 0.00 lb/hr

0.00 lb/hr x x 0.00 TPY

NOx Created by Combustion (Actual)

NOx: 4,761 scf/hr x 2,338 Btu/scf x x 0.068 lb/MMBtu = 0.76 lb/hr

0.76 lb/hr x x 3.32 TPY

Uncontrolled PM:

PM: 0 scf/hr x 7.6 lb/1,000,000 scf = 0.00 lb/hr

0.00 lb/hr x 8760 hr/yr x 0.00 TPY

PM Created by Combustion (Actual)

PM: 4,761 scf/hr x 7.6 lb/1,000,000 scf = 0.04 lb/hr

0.04 lb/hr x 8760 hr/yr x 0.16 TPY

1 MMBtu/1,000,000 Btu

8760 hr/yr

1 ton/2000 lb =

=

1 ton/2000 lb =

1 ton/2000 lb =

1 ton/2000 lb

1 MMBtu/1,000,000 Btu

8760 hr/yr
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Tanks

Uncontrolled CO:

CO: 0 scf/hr x 2,338 Btu/scf x x 0.370 lb/MMBtu = 0.00 lb/hr

0.00 lb/hr x x 0.00 TPY

CO Created by Combustion (Actual)

CO: 4,761 scf/hr x 2,338 Btu/scf x x 0.370 lb/MMBtu = 4.12 lb/hr

4.12 lb/hr x x 18.04 TPY

a

NOx, SO2, and CO emission factors are from AP-42 Table 13.5-1

(Emission Factors for Flare Operations).

=

1 MMBtu/1,000,000 Btu

8760 hr/yr 1 ton/2000 lb

1 MMBtu/1,000,000 Btu

8760 hr/yr 1 ton/2000 lb =
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Tanks

Uncombusted CO2:

wt DRE

CO2: 4,761 scf/hr x x 40.93 lb/lb-mole 0.29% x 0% = lb/hr

lb/hr x 8760 hr/yr x = TPY

CO2 Created by Combustion (Actual)

CO2: 4,761 scf/hr x 120,000.0 lb/1,000,000 scf = lb/hr

571.32 lb/hr x 8760 hr/yr x = 1 ton/2000 lb 2502.40 TPY

1/379 scf/lb-mole x

1 ton/2000 lb

1.47

6.43

571.32

REGULATED GREENHOUSE GAS EMISSIONSb

1.47
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Tanks

Uncontrolled CH4:

wt DRE

CH4: 4,761 scf/hr x x 40.93 lb/lb-mole 2.15% x 0% = lb/hr

lb/hr x 8760 hr/yr x = TPY

Controlled CH4: (Actual)

wt% DRE

CH4: 4,761 scf/hr x x 40.93 lb/lb-mole 2.15% x 98% = lb/hr

lb/hr x 8760 hr/yr x = TPY

x 0.22

0.22 0.97

1/379 scf/lb-mole

1 ton/2000 lb

x 11.05

11.05 48.40

1/379 scf/lb-mole

1 ton/2000 lb
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Tanks

Uncontrolled N2O:

wt% DRE

CH4: 4,761 scf/hr x x 40.93 lb/lb-mole 0.00% x 0% = lb/hr

lb/hr x 8760 hr/yr x = TPY

N2O Created by Combustion:

CH4: 4,761 scf/hr x 2.3 lb/1,000,000 scf = lb/hr

0.01 lb/hr x 8760 hr/yr x = 0.05 TPY

b

CO2 and N2O emission factors are from AP-42 Table 1.4-2

(Emission Factors for Natural Gas Combustion).

0.00 0.00

0.01

1 ton/2000 lb

1/379 scf/lb-mole x 0.00

1 ton/2000 lb
scf/hr (Takes into account the 10% of the total

produced gas volume that is not being sold.)

Btu/scf

lb/lb-mole

HAP wt fraction

Benzene wt fraction

E-Benzene wt fraction

Toluene wt fraction

n-Hexane wt fraction

Xylene wt fraction

2,2,4-Trimethylpentane

wt fraction

CO2 wt fraction

CH4 wt fraction

hours/yr

DRE

Dakota-3 E&P Company, LLC

8760 Hours of Flaring for 

PTE:

Control Effiiciency

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Casing Head Gas

Flare Gas Volume 8,463

Lower Heating Value 1700.386571

Avg. Molecular Weight 29.65

VOC wt fraction 45.94%

1.28%

0.15%

0.01%

0.18%

0.84%

0.10%

0.00%

0.86%

25.75%

98%
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Casing Head Gas

Controlled VOCs (PTE):

wt% Control %

VOC: 8,463 scf/hr x 1/379 scf/lb-mole x 29.64686 lb/lb-mole 45.94% x 98% = lb/hr

6.08 lb/hr x 8760 hr/yr x 1 ton/2000 lb = TPY

Controlled VOCs (Allowable):

wt% Control %

VOC: 8,463 scf/hr x 1/379 scf/lb-mole x 29.64686 lb/lb-mole 45.94% x 98% = lb/hr

6.08 lb/hr x 8760 hr/yr x 1 ton/2000 lb = TPY

26.64

6.08

26.64

x

CRITERIA POLLUTANT EMISSIONSa

x 6.08
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Casing Head Gas

Controlled HAPs (PTE):

Using E&P Tanks Run: wt% Control % TPY

Benzene 8,463 scf/hr x x 1/379 scf/lb-mole x 29.64686 lb/lb-mol x 0.15% x 98% = 0.02 lb/hr 0.09

E-Benzene 8,463 scf/hr x x 1/379 scf/lb-mole x 29.64686 lb/lb-mol x 0.01% x 98% = 0.00 lb/hr 0.01

Toluene 8,463 scf/hr x x 1/379 scf/lb-mole x 29.64686 lb/lb-mol x 0.18% x 98% = 0.02 lb/hr 0.10

n-Hexane 8,463 scf/hr x x 1/379 scf/lb-mole x 29.64686 lb/lb-mol x 0.84% x 98% = 0.11 lb/hr 0.49

Xylene 8,463 scf/hr x x 1/379 scf/lb-mole x 29.64686 lb/lb-mol x 0.10% x 98% = 0.01 lb/hr 0.06

2,2,4-Trimethylpentane 8,463 scf/hr x x 1/379 scf/lb-mole x 29.64686 lb/lb-mol x 0.00% x 98% = 0.00 lb/hr 0.00

Formaldehyde 8,463 scf/hr 7.50E-02 lb/MMscf = 0.00 lb/hr 0.00

` 0.17 lb/hr x 8760 hr/yr x 1 ton/2000 lb = TPY

Controlled HAPs (Allowable):

Using E&P Tanks Run: wt% Control % TPY

Benzene 8,463 scf/hr x x 1/379 scf/lb-mole x 29.64686 lb/lb-mol x 0.15% x 98% = 0.02 lb/hr 0.09

E-Benzene 8,463 scf/hr x x 1/379 scf/lb-mole x 29.64686 lb/lb-mol x 0.01% x 98% = 0.00 lb/hr 0.01

Toluene 8,463 scf/hr x x 1/379 scf/lb-mole x 29.64686 lb/lb-mol x 0.18% x 98% = 0.02 lb/hr 0.10

n-Hexane 8,463 scf/hr x x 1/379 scf/lb-mole x 29.64686 lb/lb-mol x 0.84% x 98% = 0.11 lb/hr 0.49

Xylene 8,463 scf/hr x x 1/379 scf/lb-mole x 29.64686 lb/lb-mol x 0.10% x 98% = 0.01 lb/hr 0.06

2,2,4-Trimethylpentane 8,463 scf/hr x x 1/379 scf/lb-mole x 29.64686 lb/lb-mol x 0.00% x 98% = 0.00 lb/hr 0.00

Formaldehyde 8,463 scf/hr x 7.50E-02 lb/MMscf x 1000000 scf/MMscf = 0.00 lb/hr 0.00

` 0.17 lb/hr x 8760 hr/yr x 1 ton/2000 lb = TPY

=

=

=

=

0.74

=

=

=

=

=

=

=

=

=

=

0.74
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Casing Head Gas

Uncontrolled NOx (PTE):

NOx: 8,463 scf/hr x 1,700 Btu/scf x x 0.068 lb/MMBtu = 0.98 lb/hr

0.98 lb/hr x 8760 hr/yr x 4.29 TPY

NOx Created by Combustion (Actual):

NOx: 8,463 scf/hr x 1,700 Btu/scf x x 0.068 lb/MMBtu = 0.98 lb/hr

0.98 lb/hr x 8760 hr/yr x 4.29 TPY

Controlled H2S (PTE):

wt% Control %

H2S: 8,463 scf/hr x 1/379 scf/lb-mole x 29.64686 lb/lb-mole 0.00% x 98% = lb/hr

0.00 lb/hr x 8760 hr/yr x 1 ton/2000 lb = TPY

Controlled H2S (Actual):

wt% Control %

H2S: 8,463 scf/hr x 1/379 scf/lb-mole x 29.64686 lb/lb-mole 0.00% x 98% = lb/hr

0.00 lb/hr x 8760 hr/yr x 1 ton/2000 lb = TPY

x

0.00

=

1 Mmbtu/1,000,000 Btu

1 ton/2000 lb =

x 0.00

0.00

1 ton/2000 lb

1 Mmbtu/1,000,000 Btu

0.00
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Casing Head Gas

SO2 Created by Combustion (PTE):

wt% Control %

SO2 8,463 scf/hr x 1/379 scf/lb-mole x 29.64686 lb/lb-mole 0.00% x 98% = lb/hr

0.00 lb/hr x 8760 hr/yr x 1 ton/2000 lb = TPY

SO2 Created by Combustion (Actual):

wt% Control %

SO2 8,463 scf/hr x 1/379 scf/lb-mole x 29.64686 lb/lb-mole 0.00% x 98% = lb/hr

0.00 lb/hr x 8760 hr/yr x 1 ton/2000 lb = TPY

CO Created by Combustion (PTE):

CO: 8,463 scf/hr x 1,700 Btu/scf x x 0.370 lb/MMBtu = 5.32 lb/hr

5.32 lb/hr x 8760 hr/yr x 23.32 TPY

CO Created by Combustion (Actual):

CO: 8,463 scf/hr x 1,700 Btu/scf x x 0.370 lb/MMBtu = 5.32 lb/hr

5.32 lb/hr x 8760 hr/yr x 23.32 TPY

0.00

0.00

0.00

=

0.00

=

1 ton/2000 lb

x

1 Mmbtu/1,000,000 Btu

1 ton/2000 lb

x

1 Mmbtu/1,000,000 Btu
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Casing Head Gas

PM Created by Combustion (PTE):

PM: 8,463 scf/hr x 7.6 = 0.06 lb/hr

0.06 lb/hr x 8760 hr/yr x 0.28 TPY

PM Created by Combustion (Actual):

PM: 8,463 scf/hr x 7.6 = 0.06 lb/hr

0.06 lb/hr x 8760 hr/yr x 0.28 TPY

=

 lb/1,000,000 scf

(Emission Factors for Flare Operations and Natural Gas Combustion).

 lb/1,000,000 scf

1 ton/2000 lb =

1 ton/2000 lb

a

NOx, SO2, PM, & CO emission factors are from AP-42 Table 13.5-1 and Table 1.4-2
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Casing Head Gas

CO2 (PTE):

CO2 Entrained in the Produced Gas:

Control %

CO2: 8,463 scf/hr x 1/379 scf/lb-mole x 29.64686 lb/lb-mole 0.86% x 98% = lb/hr

5.71 lb/hr x 8760 hr/yr x 1 ton/2000 lb = 25.01 TPY

CO2 Created by Combustion:

CO2: 8,463 scf/hr x 120,000.0 = 1015.52 lb/hr

`

1015.52 lb/hr x 8760 hr/yr x 4448.00 TPY

4473.01 TPY

REGULATED GREENHOUSE GAS EMISSIONSb

1 ton/2000 lb =

x 5.71

 lb/1,000,000 scf

Total CO2 Emitted (PTE):
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Casing Head Gas

CO2 (Actual):

CO2 Entrained in the Produced Gas:

wt% Control %

CO2: 8,463 scf/hr x 1/379 scf/lb-mole x 29.64686 lb/lb-mole 0.86% x 98% = lb/hr

5.71 lb/hr x 8760 hr/yr x 1 ton/2000 lb = 25.01 TPY

CO2 Created by Combustion: `

CO2: 8,463 scf/hr x 120,000.0 = 1015.52 lb/hr

`

1015.52 lb/hr x 8760 hr/yr x 4448.00 TPY

4473.01 TPY

Controlled CH4 (PTE):

wt% Control %

CH4: 8,463 scf/hr x 1/379 scf/lb-mole x 29.64686 lb/lb-mole 25.75% x 98% = lb/hr

3.41 lb/hr x 8760 hr/yr x 1 ton/2000 lb = TPY

Controlled CH4 (Actual):

wt% Control %

CH4: 8,463 scf/hr x 1/379 scf/lb-mole x 29.64686 lb/lb-mole 25.75% x 98% = lb/hr

3.41 lb/hr x 8760 hr/yr x 1 ton/2000 lb = TPY

x 3.41

14.93

Total CO2 Emitted (Allowable):

1 ton/2000 lb =

 lb/1,000,000 scf

x

3.41

14.93

x

5.71
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Casing Head Gas

N2O Created by Combustion (PTE):

N2O: 8,463 scf/hr x 2.2 = 1.86E-02 lb/hr

1.86E-02 lb/hr x 8760 hr/yr x 4.65E-03 TPY

N2O Created by Combustion (Actual):

N2O: 8,463 scf/hr x 2.2 = 1.86E-02 lb/hr

1.86E-02 lb/hr x 8760 hr/yr x 4.65E-03 TPY

(Emission Factors for Natural Gas Combustion).

1 ton/2000 lb =

 lb/1,000,000 scf

 lb/1,000,000 scf

b

CO2 and N2O emission factors are from AP-42 Table 1.4-2

1 ton/2000 lb =
5,250,000 Btu/hr This burner rating reflects the combined size of all of the proposed heater treater burners at the facility.

NOx: 0.10 lb/MMBtu x 5.25 MMBtu/hr = 0.515 lb/hr

0.5147 lb/hr x 8,760 hr/yr x 1 ton / 2000 lb = 2.254 TPY

CO: 0.08 lb/MMBtu x 5.25 MMBtu/hr = 0.432 lb/hr

0.43 lb/hr x 8,760 hr/yr x 1 ton / 2000 lb = 1.894 TPY

SO2: 5.88E-04 lb/MMBtu x 5.25 MMBtu/hr = 0.003 lb/hr

3.09E-03 lb/hr x 8,760 hr/yr x 1 ton / 2000 lb = 0.014 TPY

PM: 0.01 lb/MMBtu x 5.25 MMBtu/hr = 0.039 lb/hr

0.04 lb/hr x 8,760 hr/yr x 1 ton / 2000 lb = 0.171 TPY

Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Heater Treater Burnera

Burner Rating
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Heater Treater Burnera

VOC: 0.01 lb/MMBtu x 5.25 MMBtu/hr = 0.028 lb/hr

0.03 lb/hr x 8,760 hr/yr x 1 ton / 2000 lb = 0.124 TPY

HAP: 0.002 lb/MMBtu x 5.25 MMBtu/hr = 0.010 lb/hr

9.73E-03 lb/hr x 8,760 hr/yr x 1 ton / 2000 lb = 0.043 TPY

CO2 117.647 lb/MMBtu x 5.25 MMBtu/hr = 617.647 lb/hr

6.18E+02 lb/hr x 8,760 hr/yr x 1 ton / 2000 lb = 2,705.294 TPY
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Heater Treater Burnera

CH4: 0.007 lb/MMBtu x 5.25 MMBtu/hr = 0.035 lb/hr

3.47E-02 lb/hr x 8,760 hr/yr x 1 ton / 2000 lb = 0.152 TPY

N2O: 0.001 lb/MMBtu x 5.25 MMBtu/hr = 0.007 lb/hr

6.94E-03 lb/hr x 8,760 hr/yr x 1 ton / 2000 lb = 0.030 TPY

NOx TPY

CO TPY

SO2 TPY

PM TPY

VOC TPY

HAP TPY

CO2 TPY

CH4 TPY

N2O TPY

2705.29

0.15

0.03

1.89

0.12

0.04

0.01

0.17

a

NOx, CO, CO2, & VOC Emission Factors are from AP-42 Table 1.4-1 and 1.4-2 (Emission Factors for

Nitrogen Oxides (N2O) and Methane come from Table C-1 of Subpart W).

2.25
Saturation Vapor Molecular Temp + Load Loss

Factor (S) Pressure (P) Weight (MW) 460 lb/1000 gal

12.46 x 0.60 x 2.30 x 40.93 / 510.00 = 1.38

LL Truck Load Load Time

lb/1,000 gal Rate bbl/hr hrs gal/bbl

1.38 x 180.00 / 1.00 x 42.00 = 10.43

LL Annual Emissions

lb/1,000 gal bbl/yr gal/bbl lb/ton TPY 

1.38 x 1066665.82 x 42.00 / 2000.00 = 30.91 22.84

VOC

Emissions

Uncontrolled Control % TPY

22.84 100% 0.00 0.00

Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Truck Loadout Emission Calculation

Total Gas 

Emissions lb/hr

Uncontrolled 

C3+ VOC tpy
LL Annual Emissions

lb/1,000 gal bbl/yr gal/bbl lb/ton TPY 

1.38 x 1066665.82 x 42.00 / 2000.00 = 30.91 0.23

HAPs

Emissions

Uncontrolled Control % TPY

0.23 100% 0.00 0.00

LL Annual Emissions

lb/1,000 gal bbl/yr gal/bbl lb/ton TPY 

1.38 x 1066665.82 x 42.00 / 2000.00 = 30.91 0.09

CO2

Emissions

Uncontrolled Control % TPY

0.09 100% 0.00 0.00

LL Annual Emissions

lb/1,000 gal bbl/yr gal/bbl lb/ton TPY 

1.38 x 1066665.82 x 42.00 / 2000.00 = 30.91 0.66

CH4

Emissions

Uncontrolled Control % TPY

0.66 100% 0.00 0.00

Uncontrolled 

HAPs tpy

Uncontrolled 

CO2 tpy

Uncontrolled 

CH4 tpy
Combined Diesel Engines

Hours of Operation 8760

Maximum HP Rating 1925

NOx g/hp-hr 1.49E+00

CO g/hp-hr 2.61E+00

SO2 g/hp-hr 4.52E-06

PM g/hp-hr 4.85E-06

VOC g/hp-hr 1.42E-01

HAP g/bh-hr 1.02E-06

CO2 g/bh-hr 2.54E-03

CH4 g/bh-hr 2.10E-02

N2O g/hp-hr 4.20E-03

Recycle Pump

Hours of Operation 8760

Maximum HP Rating 56

NOx g/hp-hr 4.99E+00

CO g/hp-hr 3.16E+00

SO2 g/hp-hr 2.68E-01

PM g/hp-hr 3.27E-01

VOC g/hp-hr 9.80E+00

HAP g/hp-hr 2.20E-01

CO2 g/bh-hr 4.90E+02

CH4 g/hp-hr 2.10E-02

N2O g/hp-hr 4.20E-03

Description

Engine is assumed to operate 8,760 hours per year.

Manufacturer's maximum hp rating.

AP-42 Table 3.3-1

AP-42 Table 3.3-1

AP-42 Table 3.3-1

AP-42 Table 3.3-1

AP-42 Table 3.3-1

40 CFR 98 Subpart C, Table C-2

40 CFR 98 Subpart C, Table C-2

AP-42 Table 3.3-1

AP-42 Table 3.3-1

AP-42 Table 3.3-1

AP-42 Table 3.3-1

Manufacturer Guarantee (40 CFR 63 Subpart IIII requirements), see Attachment F

AP-42 Table 3.3-1

AP-42 Table 3.3-1

40 CFR 98 Subpart C, Table C-2

40 CFR 98 Subpart C, Table C-2

Dakota-3 E&P Company, LLC

RICE Input Data

Description

Engine is assumed to operate 8,760 hours per year.

Manufacturer's maximum hp rating.

Manufacturer Guarantee (40 CFR 63 Subpart IIII requirements), see Attachment F

Manufacturer Guarantee (40 CFR 63 Subpart IIII requirements), see Attachment F
ENGINE #1

1925 MAX HP 0% NOx DRE 0% CO DRE 0% VOC DRE 0% SO2 DRE 0% HAP DRE 0% PM DRE

##### #### ##### #### ### 100.00%

NOx: 1.49E+00 g/HP-HR 1925 HP x 1 lb / 453.6 grams = 6.33E+00 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 2.77E+01 NOx TPY 

CO: 2.61E+00 g/HP-HR 1925 HP x 1 lb / 453.6 grams = 1.11E+01 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 4.86E+01 CO TPY 

SO2: 4.52E-06 g/HP-HR 1925 HP x 1 lb / 453.6 grams = 1.92E-05 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 8.40E-05 SO2 TPY 

PM: 4.85E-06 g/HP-HR 1925 HP x 1 lb / 453.6 grams = 2.06E-05 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 9.02E-05 PM TPY 

VOC: 1.42E-01 g/HP-HR 1925 HP x 1 lb / 453.6 grams = 6.02E-01 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 2.64E+00 VOC TPY 

HAP: 1.02E-06 g/HP-HR 1925 HP x 1 lb / 453.6 grams = 4.33E-06 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 1.90E-05 HCHO TPY 

CO2: 2.54E-03 g/HP-HR 1925 HP x 1 lb / 453.6 grams = 1.08E-02 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 4.71E-02 CO2

CH4: 2.10E-02 g/HP-HR 1925 HP x 1 lb / 453.6 grams = 8.91E-02 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 3.90E-01 CH4

N2O: 4.20E-03 g/HP-HR 1925 HP x 1 lb / 453.6 grams = 1.78E-02 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 7.81E-02 N2O

Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Reciprocating Engine Emissions 

x

x

x

x

x

x

x

x

x
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Reciprocating Engine Emissions 

56 MAX HP 0% CO DRE 0% VOC DRE 0% SO2 DRE 0% HAP DRE 0% PM DRE

##### #### ##### #### ### 100.00%

NOx: 4.99E+00 g/HP-HR 56 HP x 1 lb / 453.6 grams x 0.62 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 2.70E+00 NOx TPY 

CO: 3.16E+00 g/HP-HR 56 HP x 1 lb / 453.6 grams x 0.39 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 1.71E+00 CO TPY 

SO2: 2.68E-01 g/HP-HR 56 HP x 1 lb / 453.6 grams = 3.31E-02 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 1.45E-01 SO2 TPY 

PM: 3.27E-01 g/HP-HR 56 HP x 1 lb / 453.6 grams = 4.04E-02 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 1.77E-01 PM TPY 

VOC: 9.80E+00 g/HP-HR 56 HP x 1 lb / 453.6 grams x 1.21 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 5.30E+00 VOC TPY

HAP: 2.20E-01 g/HP-HR 56 HP x 1 lb / 453.6 grams = 0.03 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 1.19E-01 HAP TPY 

CO2: 4.90E+02 g/HP-HR 56 HP x 1 lb / 453.6 grams = 6.05E+01 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 2.65E+02 CO2 TPY 

CH4: 2.10E-02 g/HP-HR 56 HP x 1 lb / 453.6 grams = 2.59E-03 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 1.14E-02 CH4 TPY

N2O: 4.20E-03 g/HP-HR 56 HP x 1 lb / 453.6 grams = 5.19E-04 lb/hr x 8760 hr/yr x 1 ton / 2000lb = 2.27E-03 N2O TPY

ENGINE #2

x

x

x

x

NOx DRE

x

x

x

x

x
Dakota-3 E&P Company, LLC

Frank R Fox 21-16H Pad

Associated Wells:

Frank R Fox 21-16HA, 21-16HB, 21-16HC 21-16HD, 21-16HW, 21-16HX, 21-16HZ

Reciprocating Engine Emissions 

3.04E+01

5.03E+01

1.45E-01

1.77E-01

7.93E+00

1.19E-01

2.65E+02

4.02E-01

8.03E-02

SO2 TPY 

CO2 TPY 

CH4 TPY

N2O TPY

TOTALS

NOx TPY 

CO TPY 

VOC TPY 

PM TPY 

HAP TPY 
Dakota-3 E&P Company, LLC. 

NSR Synthetic Minor Application 

WEP211324 

ATTACHMENT C: FLASHING EMISSIONS CALCULATIONS 

• E&P Tanks Emission Summary

• E&P Tanks Linear Relationship (Emission Factor)
Mandaree Field 1000 BOPD wt%

******************************************************************************************

* Project Setup Information *

******************************************************************************************

Project File : Y:\Projects\Williams Exploration & Production WEP\WEP211324 Ft. Berthold

IR Well Work\E&P Tanks\Mandaree Field 1000 BOPD.ept

Flowsheet Selection : Oil Tank with Separator

Calculation Method : RVP Distillation

Control Efficiency : 100.0%

Known Separator Stream : Low Pressure Oil

Entering Air Composition : No

Filed Name : Mandaree

Well Name : Cross 2-13H and Patricia Charging 4-15H Averages

Permit Number : Dakota-3 E&P Company, LLC

Date : 9/24/2010

******************************************************************************************

* Data Input *

******************************************************************************************

Separator Pressure : 51.00[psig]

Separator Temperature : 82.50[F]

Ambient Pressure : 14.70[psia]

Ambient Temperature : 70.00[F]

C10+ SG : 0.8000

C10+ MW : 235.14

-- Low Pressure Oil ----------------------------------------------------------------------

 No. Component wt %

 1 H2S 0.0014

 2 O2 0.0000

 3 CO2 0.0042

 4 N2 0.0015

 5 C1 0.0320

 6 C2 0.3654

 7 C3 1.2089

 8 i-C4 0.3443

 9 n-C4 1.5191

 10 i-C5 0.6508

 11 n-C5 1.2185

 12 C6 1.3933

 13 C7 6.7524

 14 C8 15.9338

 15 C9 14.3170

 16 C10+ 53.7971

 17 Benzene 0.0479

 18 Toluene 0.0997

 19 E-Benzene 0.0600

 20 Xylenes 0.3998

 21 n-C6 1.4864

 22 224Trimethylp 0.3663

-- Sales Oil -----------------------------------------------------------------------------

Production Rate : 1000[bbl/day]

Days of Annual Operation : 365 [days/year]

API Gravity : 41.85

Reid Vapor Pressure : 5.90[psia]

******************************************************************************************

* Calculation Results *

******************************************************************************************

-- Emission Summary ----------------------------------------------------------------------

Item Uncontrolled Uncontrolled 

 [ton/yr] [lb/hr] 

Page 1---------------------------------------------------------------- E&P TANK 

Total HAPs 8.550 1.952 

Total HC 812.744 185.558 

VOCs, C2+ 796.480 181.845 

VOCs, C3+ 612.595 139.862 

Page 1
Mandaree Field 1000 BOPD wt%

 

Uncontrolled Recovery Info. 

 Vapor 40.2300 [MSCFD] 

 HC Vapor 40.0300 [MSCFD] 

 GOR 40.23 [SCF/bbl] 

-- Emission Composition ------------------------------------------------------------------

No Component Uncontrolled Uncontrolled 

 [ton/yr] [lb/hr] 

1 H2S 0.689 0.157 

2 O2 0.000 0.000 

3 CO2 2.160 0.493 

4 N2 0.786 0.179 

5 C1 16.264 3.713 

6 C2 183.886 41.983 

7 C3 375.375 85.702 

8 i-C4 37.149 8.482 

9 n-C4 112.787 25.750 

10 i-C5 17.863 4.078 

11 n-C5 24.862 5.676 

12 C6 8.648 1.974 

13 C7 13.803 3.151 

14 C8 10.281 2.347 

15 C9 3.270 0.747 

16 C10+ 0.004 0.001 

17 Benzene 0.234 0.053 

18 Toluene 0.136 0.031 

19 E-Benzene 0.027 0.006 

20 Xylenes 0.156 0.036 

21 n-C6 7.394 1.688 

22 224Trimethylp 0.604 0.138 

 Total 816.378 186.388 

-- Stream Data ---------------------------------------------------------------------------

No. Component MW LP Oil Flash Oil Sale Oil Flash Gas W&S Gas Total Emissions

 wt % wt % wt % wt % wt % wt % 

1 H2S 34.80 0.0014 0.0010 0.0000 0.0873 0.0856 0.0861 

2 O2 32.00 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 

3 CO2 44.01 0.0042 0.0020 0.0000 0.4818 0.1765 0.2642 

4 N2 28.01 0.0015 0.0001 0.0000 0.3044 0.0123 0.0962 

5 C1 16.04 0.0320 0.0079 0.0000 5.2226 0.6866 1.9891 

6 C2 30.07 0.3654 0.2356 0.0039 28.3624 20.1288 22.4930 

7 C3 44.10 1.2089 1.0468 0.4786 36.1613 49.8497 45.9192 

8 i-C4 58.12 0.3443 0.3257 0.2757 4.3503 4.6218 4.5438 

9 n-C4 58.12 1.5191 1.4623 1.3185 13.7647 13.8076 13.7953 

10 i-C5 72.15 0.6508 0.6432 0.6257 2.2771 2.1480 2.1850 

11 n-C5 72.15 1.2185 1.2094 1.1888 3.1795 2.9854 3.0410 

12 C6 86.16 1.3933 1.3945 1.3984 1.1369 1.0640 1.0850 

13 C7 100.20 6.7524 6.7753 6.8342 1.8207 1.7133 1.7442 

14 C8 114.23 15.9338 16.0015 16.1730 1.3430 1.2744 1.2941 

15 C9 128.28 14.3170 14.3815 14.5440 0.4133 0.4189 0.4174 

16 C10+ 235.14 53.7971 54.0465 54.6758 0.0006 0.0005 0.0006 

17 Benzene 78.11 0.0479 0.0480 0.0483 0.0298 0.0281 0.0285 

18 Toluene 92.13 0.0997 0.1001 0.1011 0.0174 0.0165 0.0166 

19 E-Benzene 106.17 0.0600 0.0603 0.0610 0.0035 0.0032 0.0033 

20 Xylenes 106.17 0.3998 0.4016 0.4059 0.0196 0.0187 0.0191 

21 n-C6 86.18 1.4864 1.4889 1.4959 0.9466 0.8874 0.9045 

22 224Trimethylp 114.24 0.3663 0.3677 0.3711 0.0772 0.0726 0.0739 

 

 MW 143.08 144.90 148.98 39.02 43.55 42.14 

 Stream Mole Ratio 1.0000 0.9829 0.9448 0.0171 0.0381 0.0552 

 Heating Value [BTU/SCF] 2225.52 2481.29 2401.97 

 Gas Gravity [Gas/Air] 1.35 1.50 1.45 

 Bubble Pt. @ 100F [psia] 32.28 20.39 7.37 

Page 2---------------------------------------------------------------- E&P TANK 

 RVP @ 100F [psia] 15.35 12.04 6.01 

 Spec. Gravity @ 100F 0.677 0.678 0.680 

Page 2
Emission estimates are based on using the E&P TANK V2.0 Model, RVP Distillation Column

As shown below, the E&P Tanks summary output has a linear relationship with the production rate

of the oil with the given inputs listed below.

Inputs:

Low pressure oil from average of 2 representative Mandaree Field Dakota-3 Wells

Separator: 51 psig, 83 degF

Flash Valve: 13.7 psia, 50 degF

Sales Oil: API Gravity 41.9, Reid Vapor Pressure 5.90 psia, 365 days/year

Outputs:

Oil Production Rates (bbl/day) (P) 0 50 100 300 1000

Emission (tons/yr)

Total HC 0 40.6372 81.2744 243.8232 812.744

VOCs, C3+ 0 30.62975 61.2595 183.7785 612.595

Total HAPs 0 0.4275 0.855 2.565 8.55

VOC (C3+) Emission Factor: 0.6126 tpy/BOPD

HAP Emission Factor: 0.00855 tpy/BOPD

Oil Storage Tank Flashing Emissions Calculation Methodology

E&P Tanks Linear Relation between Production (bbls/day) and Emissions (tons/yr)

y = 0.00855x

R2 = 1.00000

y = 0.6126x

R2 = 1

0

100

200

300

400

500

600

700

0 500 1000 1500

tons/year

bbl/day

Tank Emissions by Production Rate

Total HAPs

VOCs, C3+

Linear (Total HAPs)

Linear (VOCs, C3+)
Dakota-3 E&P Company, LLC. 

NSR Synthetic Minor Application 

WEP211324 

ATTACHMENT D: REPRESENTATIVE LOW PRESSURE OIL 

ANALYTICAL DATA 
Company .................... ZENERGY

Lab Number ................ CRͲ10330 Study Number.......... CRͲ2

Date Sampled .............. 7Ͳ15Ͳ2010 Date Tested............. 7Ͳ23Ͳ2010

S l Id tifi ti CROSS 2 13 H CRUDE OIL

 EXTENDED HYDROCARBON (GLYCALC) LIQUID STUDY

Sample Identification .................... CROSS 2-13 H CRUDE OIL

Sample Location .......... MONTANA.

Sample Pressure ......... 22 PSIG Sample Temperature.... 95 F

Type Sample ............... SPOT County...................... DUNN

Test method ................ GPAͲ2286 Sampling Method........ YZ PISTON

 Components Mole % Weight % Liq. Vol. %

Hydrogen Sulfide .......... 0.003 0.001 0.001

Oxygen ...................... 0.000 0.000 0.000

Carbon Dioxide ............ 0.013 0.004 0.004

Nitrogen ..................... 0.007 0.001 0.001

Methane ..................... 0 180 . 0 021 . 0 050 .

Ethane ....................... 1.602 0.342 0.709

Propane ..................... 4.036 1.264 1.839

isoͲButane .................. 0.855 0.353 0.463

nͲButane .................... 3.974 1.640 2.072

isoͲPentane ................ 1.378 0.706 0.833

nͲPentane ................... 2.569 1.316 1.540

Hexanes ..................... 2 510. 1 536. 1 707.

Heptanes .................... 10.694 7.610 8.159

Octanes ..................... 19.351 15.699 16.394

Nonanes ..................... 17.072 15.551 15.886

Decanes+ ................... 31.435 51.099 47.376

Benzene...................... 0.093 0.052 0.043

Toluene....................... 0.166 0.109 0.092

Ethylbenzene............... 0.104 0.078 0.066

Xylenes....................... 0.618 0.466 0.397

nͲHexane .................... 2.798 1.712 1.903

2,2,4ͲTrimethylpentane... 0.542 0.440 0.466

TOTALS ..................... 100.000 100.000 100.000
ADDITIONAL BETX DATA

 Components Mole % Weight % Liq. Vol. %

2-Methylpentane 1.486 0.910 1.011

3-Methylpentane 3-Methylpentane 1 024 . 0 627 . 0 696 .

n-Hexane 2.798 1.712 1.903

2,2,4-Trimethylpentane 0.542 0.440 0.466

Benzene 0.093 0.052 0.043

Toluene 0.166 0.109 0.092

Ethylbenzene 0.104 0.078 0.066

m-Xylene 0.066 0.050 0.042

p-Xylene 0.436 0.329 0.280

o-Xylene 0.116 0.087 0.074

API GRAVITY AT 60/60 F, calculated........................................................................ 60.3

SPECIFIC GRAVITY AT 60/60 F, calculated.............................................................. 0.7378

RELATIVE SPECIFIC GRAVITY OF DECANES+ (C10+) FRACTION ............................... 0.7958

AVERAGE MOLECULAR WEIGHT .......................................................................... 140.803

AVERAGE MOLECULAR WEIGHT OF DECANES+ (C10+) FRACTION .......................... 228.881

TRUE VAPOR PRESSURE AT 100 F PSIA calculated TRUE VAPOR PRESSURE AT 100 F, PSIA, calculated................................................ 33 400 .

AVERAGE BOILING POINT, F, ................................................................................ 299.063

CUBIC FEET OF GAS / GALLON OF LIQUID, as Ideal Gas .......................................... 19.106

BTU / GALLON OF LIQUID AT 14.73 PSIA, calculated ................................................. 122456.887

LBS / GALLON OF LIQUID, calculated ...................................................................... 6.152

NOTATION: ALL CALCULATIONS PERFORMED USING PHYSICAL CONSTANTS FROM GPA 2145-09, THE TABLES

 OF PHYSICAL CONSTANTS FOR HYDROCARBONS AND OTHER COMPOUNDS OF INTEREST

 TO THE NATURAL GAS INDUSTRY.
 EXTENDED HYDROCARBON LIQUID STUDIES

 CERTIFICATE OF ANALYSIS

Company................ PRECISION ANALYSIS

L bN ba umer............. CR-10330 CR 10330 Study Number............ St d N b CR-2B 

Date Sampled............. 7-15-2010 Date Tested.............. 7-22-2010

Sample Identification................ ZENERGY - CROSS 2-13 H CRUDE OIL

Sample Location......... MONTANA.

Sample Pressure.......... N/A Sample Temperature.... N/A

Flowrate................... N/A County..................... DUNN

Test Method.............. VARIOUS Sample Container........

1-QUART 

BOTTLE

TEST PERFORMED RESULTS

API GRAVITY AT 60/60 F (ASTM D-287), observed...................... / ( ), 42.5

SPECIFIC GRAVITY AT 60/60 F (ASTM D-1657), calculated.......... 0.8132

REID VAPOR PRESSURE (ASTM D-323), PSIG AT 100 F.............. 5.2 PSIG

TOTAL SULFUR CONTENT (ASTM D-5453), PPMW.................. PPMW 658.98

TRUE VAPOR PRESSURE (ASTM D-2889), PSIA AT 100 F ........... N/A

BASIC SEDIMENT AND WATER CONTENT, % BY VOLUME.... N/A

COPPER STRIP CORROSION (ASTM D-130), 1 HOUR AT 100 F........... N/A

FREE WATER, observed......................................................... N/A

NOTATION : ALL TESTING PROVIDED ABOVE WAS PERFORMED IN ACCORDANCE TO METHODOLOGY

 OUTLINED BY THE AMERICAN SOCIETY FOR TESTING AND MATERIALS (ASTM).
5HSRUW5HSRUW(GLWRU

Chromatogram Cross 2-13H C:\GCsolution\DRO\DRO Data\08-2010\08-01-2010\Cross 2-13H.gcd - Channel 1

min

Intensity 0.0

2.5

5.0

7.5

10.0

12.5

15.0

17.5

20.0

22.5

25.0

27.5

30.0

0 50000 100000 150000 200000 250000

 1.055 / 1.137 / 1.306 / 1.405 / 1.552 / 1.668 / 

 1.729 / 1.901 / 1.979 / 2.039 / 2.109 / 2.280 / 2.417 / 2.565 / 2.667 / 2.854 / 2.949 / 3.034 / 3.092 / 3.213 / 3.342 / 3.420 / 3.539 / 3.632 / 3.773 / 3.862 / 3.965 / 4.069 / 4.148 / 4.335 / 4.448 / 4.508 / 4.583 / 4.692 / 4.751 / 4.901 / 5.021 / 5.164 / 5.365 / 5.508 / 5.608 / Decane (C10) 5.816 / 5.947 / 6.069 / 6.188 / 6.286 / 6.393 / 6.509 / 6.569 / 6.657 / 6.714 / 6.777 / 6.896 / 7.083 / 7.220 / 7.323 / 7.381 / 7.455 / 7.559 / 7.632 / 7.703 / 7.769 / 7.836 / 7.907 / 7.967 / 8.056 / 8.184 / 8.268 / 8.329 / 8.452 / 8.540 / 8.633 / 8.744 / 8.808 / 8.998 / 9.128 / 9.270 / 9.380 / 9.467 / 9.526 / 9.596 / 9.724 / 9.862 / 9.939 / 10.055 / 10.150 / 10.257 / 10.332 / 10.427 / 10.487 / 10.568 / 10.638 / 10.766 / 10.828 / 10.911 / 11.051 / 11.216 / 11.469 / 11.613 / 11.706 / 11.785 / 12.031 / 12.128 / 12.182 / 12.302 / 12.409 / 12.463 / 12.536 / 12.607 / 12.700 / 12.822 / 13.004 / 13.088 / 13.203 / 13.305 / 13.372 / 13.447 / 13.582 / 13.674 / 13.803 / 13.929 / 14.089 / 14.146 / 14.316 / 14.427 / 14.515 / 14.592 / 14.691 / 14.773 / 14.896 / 15.041 / 15.129 / 15.249 / 15.300 / 15.369 / 15.430 / 15.566 / 15.620 / 15.691 / 15.787 / 15.947 / o-terphenyl 16.113 / 16.187 / 16.339 / 16.456 / 16.570 / 16.661 / 16.813 / 16.894 / 16.979 / 17.143 / 17.306 / 17.449 / 17.519 / 17.642 / 17.787 / 17.954 / 18.052 / 18.153 / 18.222 / 18.292 / 18.434 / 18.549 / 18.723 / 18.887 / 18.991 / 19.197 / 19.331 / 19.474 / 19.663 / 19.724 / 19.785 / 19.850 / 19.927 / 19.995 / 20.077 / 20.222 / 20.182 / 20.345 / 20.443 / 20.634 / 20.789 / 20.871 / 20.945 / 21.059 / 21.134 / 21.205 / 21.310 / 21.542 / 21.695 / 21.795 / 21.855 / 21.905 / 21.966 / 22.073 / 22.181 / 22.367 / 22.425 / 22.599 / Octacosane (C28) 22.737 / 22.808 / 22.879 / 23.003 / 23.058 / 23.117 / 23.217 / 23.351 / 23.418 / 

 23.678 / 23.816 / 23.905 / 24.027 / 24.086 / 24.202 / 24.264 / 24.400 / 24.521 / 24.587 / 24.651 / 24.765 / 24.809 / 24.874 / 24.981 / 25.069 / 25.142 / 25.201 / 25.273 / 25.334 / 25.401 / 25.462 / 25.568 / 25.705 / 25.765 / 25.966 / 26.056 / 26.229 / 26.397 / 26.487 / 26.575 / 26.665 / 26.758 / 26.958 / 27.073 / 27.191 / 27.327 / 27.441 / 27.561 / 27.668 / 27.798 / 27.952 / 28.073 / 28.297 / 28.467 / 28.689 / 28.833 / 28.995 / 29.193 / 29.393 / 29.601 / 
Company .................... ZENERGY

Lab Number ................ CRͲ10330 Study Number.......... CRͲ3

Date Sampled .............. 7Ͳ15Ͳ2010 Date Tested............. 7Ͳ23Ͳ2010

S l Id tifi ti PATRICIA CHARGING 4 15 H CRUDE OIL

 EXTENDED HYDROCARBON (GLYCALC) LIQUID STUDY

Sample Identification .................... PATRICIA CHARGING 4-15 H CRUDE OIL

Sample Location .......... MONTANA.

Sample Pressure ......... 80 PSIG Sample Temperature.... 70 F

Type Sample ............... SPOT County...................... DUNN

Test method ................ GPAͲ2286 Sampling Method........ YZ PISTON

 Components Mole % Weight % Liq. Vol. %

Hydrogen Sulfide .......... 0.008 0.002 0.002

Oxygen ...................... 0.000 0.000 0.000

Carbon Dioxide ............ 0.014 0.004 0.004

Nitrogen ..................... 0.008 0.001 0.001

Methane ..................... 0 398 . 0 043 . 0 107 .

Ethane ....................... 1.921 0.387 0.811

Propane ..................... 3.914 1.155 1.702

isoͲButane .................. 0.862 0.335 0.445

nͲButane .................... 3.606 1.403 1.795

isoͲPentane ................ 1.238 0.598 0.715

nͲPentane ................... 2.329 1.125 1.333

Hexanes ..................... 2 180. 1 257. 1 415.

Heptanes .................... 8.849 5.934 6.445

Octanes ..................... 21.103 16.133 17.068

Nonanes ..................... 15.296 13.130 13.589

Decanes+ ................... 34.917 56.412 52.378

Benzene...................... 0.085 0.044 0.038

Toluene....................... 0.148 0.091 0.078

Ethylbenzene............... 0.060 0.043 0.037

Xylenes....................... 0.473 0.336 0.290

nͲHexane .................... 2.204 1.271 1.431

2,2,4ͲTrimethylpentane... 0.387 0.296 0.317

TOTALS ..................... 100.000 100.000 100.000
ADDITIONAL BETX DATA

 Components Mole % Weight % Liq. Vol. %

2-Methylpentane 1.272 0.734 0.826

3-Methylpentane 3-Methylpentane 0 908 . 0 524 . 0 590 .

n-Hexane 2.204 1.271 1.431

2,2,4-Trimethylpentane 0.387 0.296 0.317

Benzene 0.085 0.044 0.038

Toluene 0.148 0.091 0.078

Ethylbenzene 0.060 0.043 0.037

m-Xylene 0.058 0.041 0.036

p-Xylene 0.298 0.212 0.183

o-Xylene 0.117 0.083 0.072

API GRAVITY AT 60/60 F, calculated........................................................................ 57.8

SPECIFIC GRAVITY AT 60/60 F, calculated.............................................................. 0.7475

RELATIVE SPECIFIC GRAVITY OF DECANES+ (C10+) FRACTION ............................... 0.8050

AVERAGE MOLECULAR WEIGHT .......................................................................... 149.417

AVERAGE MOLECULAR WEIGHT OF DECANES+ (C10+) FRACTION .......................... 241.399

TRUE VAPOR PRESSURE AT 100 F PSIA calculated TRUE VAPOR PRESSURE AT 100 F, PSIA, calculated................................................ 46 319 .

AVERAGE BOILING POINT, F, ................................................................................ 314.836

CUBIC FEET OF GAS / GALLON OF LIQUID, as Ideal Gas .......................................... 18.857

BTU / GALLON OF LIQUID AT 14.73 PSIA, calculated ................................................. 122700.693

LBS / GALLON OF LIQUID, calculated ...................................................................... 6.232

NOTATION: ALL CALCULATIONS PERFORMED USING PHYSICAL CONSTANTS FROM GPA 2145-09, THE TABLES

 OF PHYSICAL CONSTANTS FOR HYDROCARBONS AND OTHER COMPOUNDS OF INTEREST

 TO THE NATURAL GAS INDUSTRY.
 EXTENDED HYDROCARBON LIQUID STUDIES

 CERTIFICATE OF ANALYSIS

Company................ ZENERGY

L bN ba umer............. CR-10330 CR 10330 Study Number............ St d N b CR-3B 

Date Sampled............. 7-15-2010 Date Tested.............. 7-22-2010

Sample Identification................ PATRICIA CHARGING 4-15 H CRUDE OIL

Sample Location......... MONTANA.

Sample Pressure.......... N/A Sample Temperature.... N/A

Flowrate................... N/A County..................... DUNN

Test Method.............. VARIOUS Sample Container........

1-QUART 

BOTTLE

TEST PERFORMED RESULTS

API GRAVITY AT 60/60 F (ASTM D-287), observed...................... / ( ), 41.2

SPECIFIC GRAVITY AT 60/60 F (ASTM D-1657), calculated.......... 0.8193

REID VAPOR PRESSURE (ASTM D-323), PSIG AT 100 F.............. 6.6 PSIG

TOTAL SULFUR CONTENT (ASTM D-5453), PPMW.................. PPMW 940.25

TRUE VAPOR PRESSURE (ASTM D-2889), PSIA AT 100 F ........... N/A

BASIC SEDIMENT AND WATER CONTENT, % BY VOLUME.... N/A

COPPER STRIP CORROSION (ASTM D-130), 1 HOUR AT 100 F........... N/A

FREE WATER, observed......................................................... N/A

NOTATION : ALL TESTING PROVIDED ABOVE WAS PERFORMED IN ACCORDANCE TO METHODOLOGY

 OUTLINED BY THE AMERICAN SOCIETY FOR TESTING AND MATERIALS (ASTM).
5HSRUW5HSRUW(GLWRU

Chromatogram PC 4-15 1-100 C:\GCsolution\DRO\DRO Data\08-2010\08-01-2010\PC 4-15 1-100.gcd - Channel 1

min

Intensity 0.0

2.5

5.0

7.5

10.0

12.5

15.0

17.5

20.0

22.5

25.0

27.5

30.0

0 50000 100000 150000 200000 250000

 1.054 / 1.137 / 1.407 / 1.593 / 1.670 / 

 1.730 / 1.902 / 2.040 / 2.109 / 2.280 / 2.363 / 2.418 / 2.566 / 2.667 / 2.855 / 2.950 / 3.035 / 3.136 / 3.214 / 3.343 / 3.421 / 3.540 / 3.635 / 3.773 / 3.863 / 3.967 / 4.070 / 4.149 / 4.335 / 4.509 / 4.584 / 4.694 / 4.750 / 4.901 / 5.022 / 5.166 / 5.366 / 5.510 / 5.610 / Decane (C10) 5.818 / 5.949 / 6.070 / 6.190 / 6.288 / 6.397 / 6.512 / 6.564 / 6.660 / 6.714 / 6.780 / 6.901 / 7.016 / 7.084 / 7.156 / 7.221 / 7.326 / 7.384 / 7.457 / 7.561 / 7.634 / 7.747 / 7.836 / 7.908 / 7.969 / 8.059 / 8.184 / 8.270 / 8.331 / 8.453 / 8.542 / 8.634 / 8.745 / 8.812 / 9.000 / 9.129 / 9.271 / 9.381 / 9.469 / 9.529 / 9.597 / 9.725 / 9.863 / 9.942 / 10.057 / 10.149 / 10.260 / 10.334 / 10.429 / 10.488 / 10.570 / 10.640 / 10.768 / 10.830 / 10.913 / 11.059 / 11.220 / 11.472 / 11.615 / 11.787 / 12.031 / 12.130 / 12.184 / 12.318 / 12.414 / 12.470 / 12.541 / 12.606 / 12.706 / 12.826 / 13.005 / 13.088 / 13.306 / 13.376 / 13.450 / 13.583 / 13.673 / 13.728 / 13.934 / 14.091 / 14.148 / 14.319 / 14.445 / 14.516 / 14.595 / 14.692 / 14.779 / 14.896 / 15.042 / 15.130 / 15.246 / 15.373 / 15.431 / 15.568 / 15.658 / 15.621 / 15.775 / 15.883 / 15.950 / o-terphenyl 16.056 / 16.118 / 16.191 / 16.341 / 16.460 / 16.573 / 16.667 / 16.814 / 16.894 / 16.987 / 17.144 / 17.313 / 17.452 / 17.528 / 17.644 / 17.796 / 17.963 / 18.087 / 18.144 / 18.226 / 18.292 / 18.436 / 18.558 / 18.723 / 18.924 / 18.986 / 19.083 / 19.198 / 19.272 / 19.329 / 19.473 / 19.627 / 19.786 / 19.849 / 19.928 / 20.077 / 20.180 / 20.244 / 20.372 / 20.431 / 20.488 / 20.634 / 20.798 / 20.870 / 20.952 / 21.027 / 21.131 / 21.218 / 21.313 / 21.422 / 21.538 / 21.594 / 21.705 / 21.795 / 21.845 / 21.966 / 22.068 / 22.188 / 22.368 / 22.426 / 22.604 / Octacosane (C28) 22.717 / 22.799 / 22.997 / 23.054 / 23.217 / 23.347 / 23.408 / 23.605 / 23.663 / 23.817 / 24.040 / 24.163 / 24.292 / 24.402 / 24.498 / 24.572 / 24.634 / 24.695 / 24.758 / 24.836 / 24.977 / 25.088 / 25.178 / 

 25.438 / 25.504 / 25.571 / 25.721 / 25.797 / 26.044 / 26.117 / 26.208 / 26.366 / 26.438 / 26.526 / 26.626 / 26.733 / 26.830 / 26.947 / 27.166 / 

 27.448 / 27.552 / 27.669 / 27.776 / 27.974 / 

 28.293 / 28.432 / 28.616 / 28.720 / 28.944 / 29.074 / 

 29.336 / 

 29.688 / 29 920 /
Dakota-3 E&P Company, LLC. 

NSR Synthetic Minor Application 

WEP211324 

ATTACHMENT E: REPRESENTATIVE GAS ANALYSIS 
	

	





	






























































 




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	Dakota-3 E&P Company, LLC. 

NSR Synthetic Minor Application 

WEP211324 

ATTACHMENT F: ENGINE MANUFACTURER’S SPECS 
This section of the document has been redacted because it 

contains copyrighted information. The redacted information 

can be viewed from the hard copy of the docket, which is 

available at the EPA Region 8 Office upon request. 






Dakota-3 E&P Company, LLC. 

NSR Synthetic Minor Application 

WEP211324 

ATTACHMENT G: EMISSION CONTROL DEVICE 

MANUFACTURER’S SPECS 


	



	











 


TYPICAL MANDAREE AREA 

SEVEN WELL PAD FACILITY PLOT PLAN 

Dakota-3 E&P Company, LLC 

FBIR, North Dakota 

NOT TO SCALE 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl 

Prod. H2O 

Recycle 

Pump 

Vent lines 

Chemicals 

(7)Wellheads 

Tank Vent line 

Utility 

Flare

 

LACT 

Gas to sales

Gas Meter

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl 

Prod. H2O 12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl 

Prod. H2O 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl 

Prod. H2O 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl 

Prod. H2O 12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl 

Prod. H2O 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

Enclosed 

Combustor

Recycle 

Pump 

Recycle 

Pump 

Recycle 

Pump 

Recycle 

Pump 

Recycle 

Pump 

Recycle 

Pump 

LACT 

Unit 

LACT 

Unit 

LACT 

Unit 

LACT 

Unit 

LACT 

Unit 

LACT 

Unit 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

12’d x 20’h 

400 bbl oil 

Valve

Valve

Valve

Valve

Valve

Valve

Valve

Recycle Line 

6’d x 20’h 

vertical treater 

Separator 30” d 

by 10’ h 

6’d x 20’h 

vertical treater 

Separator 30” d 

by 10’ h 

6’d x 20’h 

vertical treater 

Separator 30” d 

by 10’ h 

6’d x 20’h 

vertical treater 

Separator 30” d 

by 10’ h 

6’d x 20’h 

vertical treater 

Separator 30” d 

by 10’ h 

6’d x 20’h 

vertical treater 

Separator 30” d 

by 10’ h 

6’d x 20’h 

vertical treater 

Separator 30” d 

by 10’ h 

Gas Meter 

(7) Gensets 

Genset

Oil Pipeline 

Water 

Pipeline 

24 bbl 

Diesel 

Gas Meter 

Legend 

Berms 

Water Line 

Crude Line 

Flowline 

Buried Recycle Lines 

Gas Sales Line 

Tank Vapor Line 

Flared Gas Line 
	



	










 


Dakota-3 E&P Company, LLC. 

NSR Synthetic Minor Application 

WEP211324 

ATTACHMENT J: DIESEL TANK EPA TANKS 4.09D 

EMISSIONS SUMMARY 
TANKS 4.0.9d

Emissions Report - Detail Format 

Tank Indentification and Physical Characteristics

Identification

 User Identification: 1000 gallon diesel tank

 City: Williston

 State: North Dakota

 Company: Williams E&P, LLC

 Type of Tank: Horizontal Tank

 Description: 1,000 gallon diesel tank to fuel onsite diesel generators. Tank throughput is based on engine fuel consumption.

Tank Dimensions

 Shell Length (ft): 10.00

 Diameter (ft): 4.16

 Volume (gallons): 1,000.00

 Turnovers: 2,244.31

 Net Throughput(gal/yr): 2,244,312.00

 Is Tank Heated (y/n): N

 Is Tank Underground (y/n): N

Paint Characteristics

 Shell Color/Shade: Gray/Medium

 Shell Condition Good

Breather Vent Settings

 Vacuum Settings (psig): -0.03

 Pressure Settings (psig) 0.03

Meterological Data used in Emissions Calculations: Bismarck, North Dakota (Avg Atmospheric Pressure = 13.86 psia)

TANKS 4.0 Report Page 1 of 6

file://C:\Program Files\Tanks409d\summarydisplay.htm 9/29/2011
1000 gallon diesel tank - Horizontal Tank

Williston, North Dakota 

TANKS 4.0.9d

Emissions Report - Detail Format 

Liquid Contents of Storage Tank

Daily Liquid Surf. 

Temperature (deg F)

Liquid

Bulk

Temp Vapor Pressure (psia)

Vapor

Mol. 

Liquid

Mass 

Vapor

Mass Mol. Basis for Vapor Pressure

Mixture/Component Month Avg. Min. Max. (deg F) Avg. Min. Max. Weight. Fract. Fract. Weight Calculations

Distillate fuel oil no. 2 All 50.18 39.72 60.64 44.68 0.0045 0.0031 0.0067 130.0000 188.00 Option 1: VP50 = .0045 VP60 = .0065

TANKS 4.0 Report Page 2 of 6

file://C:\Program Files\Tanks409d\summarydisplay.htm 9/29/2011
1000 gallon diesel tank - Horizontal Tank

Williston, North Dakota 

TANKS 4.0.9d

Emissions Report - Detail Format 

Detail Calculations (AP-42)

Annual Emission Calcaulations

Standing Losses (lb): 0.2654

 Vapor Space Volume (cu ft): 86.5719

 Vapor Density (lb/cu ft): 0.0001

 Vapor Space Expansion Factor: 0.0780

 Vented Vapor Saturation Factor: 0.9995

Tank Vapor Space Volume:

 Vapor Space Volume (cu ft): 86.5719

 Tank Diameter (ft): 4.1600

 Effective Diameter (ft): 7.2797

 Vapor Space Outage (ft): 2.0800

 Tank Shell Length (ft): 10.0000

Vapor Density

 Vapor Density (lb/cu ft): 0.0001

 Vapor Molecular Weight (lb/lb-mole): 130.0000

 Vapor Pressure at Daily Average Liquid

 Surface Temperature (psia): 0.0045

 Daily Avg. Liquid Surface Temp. (deg. R): 509.8466

 Daily Average Ambient Temp. (deg. F): 41.5958

 Ideal Gas Constant R

 (psia cuft / (lb-mol-deg R)): 10.731

 Liquid Bulk Temperature (deg. R): 504.3458

 Tank Paint Solar Absorptance (Shell): 0.6800

 Daily Total Solar Insulation

 Factor (Btu/sqft day): 1,276.2450

Vapor Space Expansion Factor

 Vapor Space Expansion Factor: 0.0780

 Daily Vapor Temperature Range (deg. R): 41.8377

 Daily Vapor Pressure Range (psia): 0.0036

 Breather Vent Press. Setting Range(psia): 0.0600

 Vapor Pressure at Daily Average Liquid

 Surface Temperature (psia): 0.0045

 Vapor Pressure at Daily Minimum Liquid

 Surface Temperature (psia): 0.0031

 Vapor Pressure at Daily Maximum Liquid

 Surface Temperature (psia): 0.0067

 Daily Avg. Liquid Surface Temp. (deg R): 509.8466

 Daily Min. Liquid Surface Temp. (deg R): 499.3872

 Daily Max. Liquid Surface Temp. (deg R): 520.3060

 Daily Ambient Temp. Range (deg. R): 24.3583

Vented Vapor Saturation Factor

 Vented Vapor Saturation Factor: 0.9995

 Vapor Pressure at Daily Average Liquid:

 Surface Temperature (psia): 0.0045

 Vapor Space Outage (ft): 2.0800

Working Losses (lb): 5.6720

 Vapor Molecular Weight (lb/lb-mole): 130.0000

 Vapor Pressure at Daily Average Liquid

 Surface Temperature (psia): 0.0045

 Annual Net Throughput (gal/yr.): 2,244,312.0000

TANKS 4.0 Report Page 3 of 6

file://C:\Program Files\Tanks409d\summarydisplay.htm 9/29/2011
 Annual Turnovers: 2,244.3120

 Turnover Factor: 0.1800

 Tank Diameter (ft): 4.1600

 Working Loss Product Factor: 1.0000

Total Losses (lb): 5.9375

TANKS 4.0 Report Page 4 of 6

file://C:\Program Files\Tanks409d\summarydisplay.htm 9/29/2011
Emissions Report for: Annual 

1000 gallon diesel tank - Horizontal Tank

Williston, North Dakota 

TANKS 4.0.9d

Emissions Report - Detail Format 

Individual Tank Emission Totals

Losses(lbs)

Components Working Loss Breathing Loss Total Emissions

Distillate fuel oil no. 2 5.67 0.27 5.94

TANKS 4.0 Report Page 5 of 6

file://C:\Program Files\Tanks409d\summarydisplay.htm 9/29/2011
TANKS 4.0 Report Page 6 of 6

file://C:\Program Files\Tanks409d\summarydisplay.htm 9/29/2011