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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 pro duction. Mscfd 4019 Average daily production of gas in Mscf per day, ba sed on the predicted first 30 days of production. Decline Factor 0.505 Expected decline factor for the first year of opera tion. Based on data from previously producing wells in t he 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 expe cted to produce using the above entered decline fac tor.

Oil/Condensate Tank Data Description Flash Gas Method: Process Simulator Use the drop down menu to choose the appropriate fl ash gas method. Process Simulator Estimated scf/bbl 39.1 The scf/bbl from direct measurement or representati ve sample. Based on representative E&P Tank Emission Summary O utput. 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 O utput. Molecular Weight 40.93 Molecular weight of the tank vapors in pounds per p ound-mole (lb/lb-mole). Based on representative E&P Tank Emission Summary O utput. VOC% 73.87712 VOC weight fraction of the tank vapor gas (C3+). Based on representative E&P Tank Emission Summary O utput. VOC TPY/BOPD Emission Factor 0.6514 Based on representative E&P Tank Emission Summary O utput. (Summary Output creates a linear relationshi p between TPY and BOPD) HAP% 0.7286263 HAP weight fraction of the tank vapor gas. Based on representative E&P Tank Emission Summary O utput. HAP TPY/BOPD Emission Factor 0.0056 Based on representative E&P Tank Emission Summary O utput. (Summary Output creates a linear relationshi p 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 O utput.
H 2 S weight % 0.09% H 2 S weight percent of the tank vapor gas. Based on representative E&P Tank Emission Summary O utput.
H 2 S mole % 0.11% H 2 S mole percent of the tank vapor gas. Based on representative E&P Tank Emission Summary O utput.
Enclosed Smokeless Combustor Use the drop down menu to choose the appropriate em ission control type. Control Destruction Efficiency 98% Control efficiency of any applicable controls. Thi s 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 inputFacility 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 l b/lb-mole. (From representative field gas analysis) Specific Gravity 1.0236429 If necessary to convert specific gravity to molecul ar weight, enter the specific gravity of the wellst ream 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: We ight%, 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)
H 2 S weight % 0.000% H 2 S weight percent of the wellstream gas. (From representative field gas analysis)
H 2 S mole % 0.000% H 2 S mole percent of the wellstream gas. (From representative field gas analysis)
Connected to sales line Use the drop down menu to choose the appropriate em ission control type. Control/Capture Efficiency 100% If routed to pipeline, assumed 100% capture of gas. If flared, control efficiency of any applicable co ntrols (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 th e 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 oi l sales method. If oil is sold through a LACT, no i nput values are required in Lines 30-35. Submerged loading: dedicated normal service 0.6 Use the drop down list to choose the appropriate mo de of operation. The saturation factor will automat ically 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 sq uare inch absolute (psia) If no site specific data is available, please refer to Table 2 on Truck Loa ding tab. Temperature 50.00 Temperature of bulk liquid loaded in Fahrenheit. If no site specific data is available, use an estimat ed 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) DescriptionFacility:

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 H 2 S SO 2 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 Ne gligible RICE Engine 7.93 1.19E-01 30.44 0.18 0.18 0.18 50.26 N/A 1.4 5E-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 Neg ligible Glycol Dehydrator N/A N/A N/A N/A N/A N/A N/A N/A N/A Negligi ble

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 H 2 S SO 2 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 Ne gligible RICE Engine 7.93 1.19E-01 30.44 0.18 0.18 0.18 50.26 N/A 1.4 5E-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 Neg ligible Glycol Dehydrator N/A N/A N/A N/A N/A N/A N/A N/A N/A Negligi ble

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, su lfuric 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 Pollutants a 

# Dakota-3 E&P Company, LLC

Allowable Potential to Emit 

## Emission Summary

Uncontrolled Potential to EmitFacility:

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

CO 2 CH 4 N 2 O CO 2 CH 4 N 2 O
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 c reated from O&G production operations. Actual Greenhouse Gases b Potential To Emit Greenhouse Gases bBOPD

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, 21-1 6HW, 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, 21-1 6HW, 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 EMISSIONS a

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, 21-1 6HW, 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, 21-1 6HW, 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 Ta ble 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, 21-1 6HW, 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 = 2502.40 TPY 1 ton/2000 lb x 1/379 scf/lb-mole

1 ton/2000 lb 1.47

6.43

571.32 

## REGULATED GREENHOUSE GAS EMISSIONS b

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, 21-1 6HW, 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, 21-1 6HW, 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

x 0.00 1/379 scf/lb-mole

1 ton/2000 lbscf/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, 21-1 6HW, 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, 21-1 6HW, 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 9 8% = 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 9 8% = 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 EMISSIONS a

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, 21-1 6HW, 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, 21-1 6HW, 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 % H 2 S: 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 % H 2 S: 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, 21-1 6HW, 21-16HX, 21-16HZ 

## Casing Head Gas

SO2 Created by Combustion (PTE):
wt% Control % SO 2 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 % SO 2 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, 21-1 6HW, 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, 21-1 6HW, 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 EMISSIONS b

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, 21-1 6HW, 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 9 8% = 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 9 8% = 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, 21-1 6HW, 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 al l of the proposed heater treater burners at the fac ility.

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, 21-1 6HW, 21-16HX, 21-16HZ



## Heater Treater Burner a

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, 21-1 6HW, 21-16HX, 21-16HZ



## Heater Treater Burner a

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, 21-1 6HW, 21-16HX, 21-16HZ



## Heater Treater Burner a

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, 21-1 6HW, 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 tpyCombined 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 FENGINE #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, 21-1 6HW, 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, 21-1 6HW, 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, 21-1 6HW, 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 TPYDakota-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 1Mandaree 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 2Emission 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 R 2 = 1.00000 y = 0.6126x R 2 = 1

0 100 200 300 400 500 600 700

0 500 1000 1500tons/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

................ CR

Ͳ 10330 Study Number.......... CR

Ͳ 2
Date Sampled

.............. 7

Ͳ 15

Ͳ 2010 Date Tested............. 7

Ͳ 23

Ͳ 2010

S l Id tifi ti CROSS 2 13 H CRUDE OIL 

### EXTENDED HYDROCARBON (GLYCALC) LIQUID STUDY

Samp l e I d enti f ication

.................... C R OSS 2-13 H C RUDE O IL



### Sample Location .......... MONTANA. Sample Pressure ......... 22 PSIG Sample Temperature.... 95 F Type Sample ............... SPOT County...................... DUNN Test method ................ 

### GPA

Ͳ 2286 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


### iso

Ͳ Butane

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



### n

Ͳ Butane

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


### iso

Ͳ Pentane

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



### n

Ͳ Pentane

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


### H 2 510 1 536 1 707 

### exanes

..................... . . . 

### 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



### n

Ͳ Hexane

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

### 2,2,4

Ͳ Trimethylpentane... 0.542 0.440 0.466


### TOTALS

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



### Components Mole % Weight % Liq. Vol. % 2-Methylpentane 1.486 0.910 1.011 3-Methylpentane 1 024 0 627 0 696 3

- Methylpentane

. . . 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 33 400 TRUE VAPOR PRESSURE AT 100 F

, PSIA

, calculated

................................................ . 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 b CR 10330 St d N b a umer............. CR-10330 Study Number............ 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

A PI 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.................. 658.98 PPMW

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 1min 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 / 20.182 / 20.222 / 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

................ CR

Ͳ 10330 Study Number.......... CR

Ͳ 3
Date Sampled

.............. 7

Ͳ 15

Ͳ 2010 Date Tested............. 7

Ͳ 23

Ͳ 2010

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

### EXTENDED HYDROCARBON (GLYCALC) LIQUID STUDY

Samp l e I d enti f ication

.................... PATRI C IA C HAR G IN G 4-15 H C RUDE O IL



### Sample Location .......... MONTANA. Sample Pressure ......... 80 PSIG Sample Temperature.... 70 F Type Sample ............... SPOT County...................... DUNN Test method ................ 

### GPA

Ͳ 2286 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


### iso

Ͳ Butane

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



### n

Ͳ Butane

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


### iso

Ͳ Pentane

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



### n

Ͳ Pentane

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


### H 2 180 1 257 1 415 

### exanes

..................... . . . 

### 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



### n

Ͳ Hexane

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

### 2,2,4

Ͳ Trimethylpentane... 0.387 0.296 0.317


### TOTALS

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



### Components Mole % Weight % Liq. Vol. % 2-Methylpentane 1.272 0.734 0.826 3-Methylpentane 0 908 0 524 0 590 3

- Methylpentane

. . . 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 46 319 TRUE VAPOR PRESSURE AT 100 F

, PSIA

, calculated

................................................ . 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 b CR 10330 St d N b a umer............. CR-10330 Study Number............ 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

A PI 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.................. 940.25 PPMW

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 1min 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 / 15.621 / 15.658 / 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 F lare **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 **E MISSIONS 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) 

### Page 1 of 6 TANKS 4.0 Report

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

### 1000 gallon diesel tank - Horizontal Tank Williston, North Dakota 

### T ANKS 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 

### Page 2 of 6 TANKS 4.0 Report

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

### 1000 gallon diesel tank - Horizontal Tank Williston, North Dakota 

### T ANKS 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 

### Page 3 of 6 TANKS 4.0 Report

9/29/2011 file://C:\Program Files\Tanks409d\summarydisplay.htmAnnual Turnovers: 2,244.3120 Turnover Factor: 0.1800 Tank Diameter (ft): 4.1600 Working Loss Product Factor: 1.0000

Total Losses (lb): 5.9375 

### Page 4 of 6 TANKS 4.0 Report

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

### Emissions Report for: Annual

1000 gallon diesel tank - Horizontal Tank Williston, North Dakota 

### T ANKS 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 

### Page 5 of 6 TANKS 4.0 Report

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

### Page 6 of 6 TANKS 4.0 Report

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