~"i

, -. BISON

ENGINEERING, INC.

October 4,2011

Ms. Kathleen Paser

EPA Region 8 Tribal Air Coordinator

U.S. EPA, Region 8

1595 Wynkoop Avenue, 8P-AR

Denver, CO 80202-1129

Dear Ms. Paser:

140011'" AVENUE' HElENA. MT 59601 • 406-442-5768

FAX: 406·449-6653 • E·MAll: bison@bison-eng.com • www,bison-eng.com

Duplicate submittal provided via

e-mail to: paser.kathleen@epa.gov

RE: Synthetic Minor Permit Application for the FBIR Headless Turtle 44X-22 Pad

Bison Engineering, Inc. (Bison), as contracted by XTO Energy, Inc. (XTO), is submitting

a Synthetic Minor Permit Application for the Headless Turtle 44X-22 Pad. This

application is being submitted in accordance with the requirements of the August 29,

2011, Consent Agreement, regarding compliance with the Federal Minor New Source

Review Rule.

If the Agency has any questions or concerns, please contact me (406.442.5768 or

bret@bison-eng.com). I will be pleased to assist you.

Sincerely,

BISON ENGINEERING, INC.

Bret Gallo

Project Engineer

Attachment

cc: John McMichael, XTO Energy, Inc.

Joe Gillies, Jr., Environmental Director, Environmental Division, 204 W. Main,

New Town, NO 58763-9404

Tex Hall, Chairman, Three Affiliated Tribes, 404Frontage Road, New Town, NO

58763-9404

(Letter Only)

Bison File XT0211339

An Employee Owned Company
	

		

	

	

	
	

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NSR Synthetic Minor Permit Application 

XTO211339 

ATTACHMENT B: EMISSION INVENTORY 

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 QUESTAR APPLIED TECHNOLOGY

1210 D. Street, Rock Springs, Wyoming 82901

(307) 352-7292

LIMS ID: N/A Description: Jane 11x-20

Analysis Date/Time: 8/30/2011 1:00 PM Field: Lostbridge

Analyst Initials: AST ML#: XTO

Instrument ID: Instrument 1 GC Method: Quesbtex

Data File: QPC73.D

Date Sampled: 8/24/2011

Component Mol% Wt% LV%

Methane 65.8105 43.1118 54.9906

Ethane 14.7115 18.0637 19.4481

Propane 8.4823 15.2736 11.5292

Isobutane 1.1052 2.6230 1.7833

n-Butane 3.4281 8.1362 5.3312

Neopentane 0.0052 0.0152 0.0097

Isopentane 0.6395 1.8841 1.1547

n-Pentane 0.9259 2.7278 1.6541

2,2-Dimethylbutane 0.0048 0.0169 0.0099

2,3-Dimethylbutane 0.0447 0.1571 0.0902

2-Methylpentane 0.1557 0.5477 0.3186

3-Methylpentane 0.0847 0.2979 0.1704

n-Hexane 0.2101 0.7394 0.4261

Heptanes 0.3050 1.1676 0.6006

Octanes 0.0396 0.1837 0.0965

Nonanes 0.0125 0.0618 0.0313

Decanes plus 0.0012 0.0071 0.0037

Nitrogen 3.4649 3.9635 1.8738

Carbon Dioxide 0.5686 1.0219 0.4780

Oxygen 0.0000 0.0000 0.0000

Hydrogen Sulfide 0.0000 0.0000 0.0000

Total 100.0000 100.0000 100.0000

Global Properties Units

Gross BTU/Real CF 1401.5 BTU/SCF at 60°F and14.73 psia

Sat.Gross BTU/Real CF 1378.5 BTU/SCF at 60°F and14.73 psia

Gas Compressibility (Z) 0.9952

Specific Gravity 0.8476 air=1

Avg Molecular Weight 24.490 gm/mole

Propane GPM 2.324682 gal/MCF

Butane GPM 1.438725 gal/MCF

Gasoline GPM 0.892199 gal/MCF

26# Gasoline GPM 1.971372 gal/MCF

Total GPM 4.656794 gal/MCF

Base Mol% 99.883 %v/v

Sample Temperature: 74 °F

Sample Pressure: 34 psig

H2SLength of Stain Tube N/A ppm
Component Mol% Wt% LV%

Benzene 0.0239 0.0763 0.0330

Toluene 0.0090 0.0337 0.0148

Ethylbenzene 0.0007 0.0031 0.0014

M&P Xylene 0.0024 0.0102 0.0045

O-Xylene 0.0006 0.0024 0.0010

2,2,4-Trimethylpentane 0.0195 0.0908 0.0483

Cyclopentane 0.0000 0.0000 0.0000

Cyclohexane 0.0382 0.1314 0.0642

Methylcyclohexane 0.0378 0.1515 0.0749

Description: Jane 11x-20

GRI GlyCalc Information

Component Mol% Wt% LV%

Carbon Dioxide 0.5686 1.0219 0.4780

Hydrogen Sulfide 0.0000 0.0000 0.0000

Nitrogen 3.4649 3.9635 1.8738

Methane 65.8105 43.1118 54.9906

Ethane 14.7115 18.0637 19.4481

Propane 8.4823 15.2736 11.5292

Isobutane 1.1052 2.6230 1.7833

n-Butane 3.4281 8.1362 5.3312

Isopentane 0.6447 1.8993 1.1644

n-Pentane 0.9259 2.7278 1.6541

Cyclopentane 0.0000 0.0000 0.0000

n-Hexane 0.2101 0.7394 0.4261

Cyclohexane 0.0382 0.1314 0.0642

Other Hexanes 0.2899 1.0196 0.5891

Heptanes 0.1766 0.6839 0.3654

Methylcyclohexane 0.0378 0.1515 0.0749

2,2,4 Trimethylpentane 0.0195 0.0908 0.0483

Benzene 0.0239 0.0763 0.0330

Toluene 0.0090 0.0337 0.0148

Ethylbenzene 0.0007 0.0031 0.0014

Xylenes 0.0030 0.0126 0.0055

C8+ Heavies 0.0496 0.2369 0.1246

Subtotal 100.0000 100.0000 100.0000

Oxygen 0.0000 0.0000 0.0000

Total 100.0000 100.0000 100.0000
XTO Energy, Inc. 

NSR Synthetic Minor Permit Application 

XTO211339 

ATTACHMENT D: 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. 
XTO Energy, Inc. 

NSR Synthetic Minor Permit Application 

XTO211339 

ATTACHMENT E: NSCR CONTROL MANUFACTURER’S 

SPECS 
XTO Energy, Inc. 

NSR Synthetic Minor Permit Application 

XTO211339 

ATTACHMENT F: ENCLOSED COMBUSTOR 

MANUFACTURER’S SPECS 
CIMARRON ENERGY INC.

Home Office: 1-(580) 338-5496 FAX 1-(580) 338-0885 P.O. Box 1406, Guymon, Oklahoma 73942 

Administrative Office: 1-(405) 928-7373 FAX 1-(405) 928-7380 P.O. Box 722110, Norman, Oklahoma 73070 

EMISSION CONTROL DEVICES (ECD) 

Cimarron Energy Tank VOC Emission Control Devices are enclosed combustors 

that are low maintenance with safe reliable operation, user friendly, easy to 

install, and highly efficient. These units are engineered to capture and combust 

VOC emissions from the Oil/Condensate Production Tanks with clean efficient 

destruction. Cimarron ECDs have been independently tested and certified to 

exceed the strict EPA requirements with a 99% destruction rate. 

Specifications on the next page. 

Auto Ignition systems also available. 
Specifications 

24”D x 8’.5”L ECD 30”D x 8’.5”L ECD 

Capacity: 8 mcf/d @ 10 oz. Capacity: 11mcf/d @ 10oz. 

MAWP: Atmospheric MAWP: Atmospheric 

MMBTU/hr: .7 MMBTU/hr. MMBTU/hr: 1 MMBTU/hr. 

Number of Jets: 64 Number of Jets: 88 

Flame Cell: 24” Flame Cell: 30” 

Burner: 16” Burner: 25” 

Backdraft: 2” or 3” Inline Wenco Backdraft: 2” or 3” Inline Wenco 

Inlet Connection: 3” NPT Inlet Connection: 3” NPT 

48”D x 12’L ECD 60”D x 13’L ECD 

Capacity: 26 mcf/d @ 10 oz. Capacity: 60 mcf/d @ 10 oz. 

MAWP: Atmospheric MAWP: Atmospheric 

MMBTU/hr: 2 MMBTU/hr. MMBTU/hr: 5 MMBTU/hr. 

Number of Jets: 210 Number of Jets: 440 

Flame Cell: 48” Flame Cell: 60” 

Burner: 34” Burner: 42” 

Backdraft: 2” or 3” Inline Wenco Backdraft: 3” Inline Wenco 

Inlet Connection: 3” NPT Inlet Connection: 3” NPT 

48”D x 25’L HV ECD 

Capacity: 130 mcf/d @ 10 oz. 

MAWP: Atmospheric 

Number of orfices: 88 

Flame Cell: 4) 36” 

Inlet Connection: 3” NPT 

Backdraft: 2” or 3” Inline Wenco 
XTO Energy, Inc. 

NSR Synthetic Minor Permit Application 

XTO211339 

ATTACHMENT G: PROCESS FLOW DIAGRAM OF 

FACILITY 
Gas & Liquids

2-Phase Production Separator(s) 

(Up to 6 Separators Site Wide, 

one Separator for each Well)

Liquids (Oil & Produced Water)

0.5 MMBTU/HR Heater Treater(s) 

(Up to 6 Heater Treaters Site 

Wide, One for each well)

Oil

Produced Water

*Gas Gas

Well Head(s) & Pumping Unit(s)

 (Up to 6 Well Heads & 6 

Pumping Units Site Wide, One 

for each well)

400 bbl Oil Tank(s)

 (Up to 24 Tanks Site Wide, 

Four Tanks for each well)

400 bbl Produced Water Tank(s) 

(Up to 12 Tanks Site Wide, Two 

Tanks for each well)

L.A.C.T. Unit(s)

(Pipeline Sales)

Sales Oil

Water Pump(s) 

(Up to 12 Water Pumps Site Wide, one 

for each Tank) / Pipeline to Disposal

Tank Vapors

Produced Water

Enclosed Combustor(s)

(99% DRE of VOC)

(Up to 3 Combustors, site 

wide total)

Utility Flare

(98% DRE of VOC) Sales Gas

Gas Meter

(Pipeline Sales)

*Gas from Separator(s) will either be sent to pipeline

 sales, or will be flared if we cannot tie into a sales 

pipeline or shut in by third party

3 – GENSETS

500KW (680 hp)

Diesel Engines (Supplies 

Electric Power Pumping Unit, 

Water Transfer Pumps, 

Recycle Pumps, and L.A.C.T 

Units

XTO Energy, Inc. 

Fort Berthold Indian Reservation

Process Flow Diagram – Six (6) Well Pad Design

3 – 1000 Gallon 

Diesel Storage 

Tanks

Fuel
Gas & Liquids

2-Phase Production Separator(s) 

(Up to 6 Separators Site Wide, 

one Separator for each Well)

Liquids (Oil & Produced Water)

0.5 MMBTU/HR Heater Treater(s) 

(Up to 6 Heater Treaters Site 

Wide, One for each well)

Oil

Produced Water

*Gas Gas

Well Head(s) & Pumping Unit(s)

 (Up to 6 Well Heads & 6 

Pumping Units Site Wide, One 

for each well)

400 bbl Oil Tank(s)

 (Up to 24 Tanks Site Wide, 

Four Tanks for each well)

400 bbl Produced Water Tank(s) 

(Up to 12 Tanks Site Wide, Two 

Tanks for each well)

L.A.C.T. Unit(s)

(Pipeline Sales)

Sales Oil

Water Transfer Pump(s) 

(Up to 12 Water Transfer Pumps Site 

Wide, One for each Tank) / Pipeline to 

Disposal

Tank Vapors

Produced Water

Enclosed Combustor(s)

(99% DRE of VOC)

(Up to 3 Combustors, Site 

wide total)

Utility Flare

(98% DRE of VOC)

Sales Gas Gas Meter

(Pipeline Sales)

*Gas from the Separator(s) will either be sent to pipeline

 sales, or will be flared if we cannot tie into a sales 

pipeline or shut in by third party

**When VRU is down or being by passed, Tank Vapors 

are controlled by the Enclosed Combustor(s)

VRT

(Vapor Recovery Tower)

Up to 6 VRTs Site Wide, 

One for each well.

Stable Oil

VRU

(Vapor Recovery Unit)

Gas

Gas Meter

(Pipeline Sales) Gas

3 – GENSETS

500KW (680hp) Diesel Engines

(Supplies Electric Power for the 

VRU, Pumping Units, Water 

Transfer Pumps, Recycle 

Pumps, and L.A.C.T. Units

3 -1000 gal 

Diesel Fuel 

Tanks

Fuel

XTO Energy, Inc.

Fort Berthold Indian Reservation

Process Flow Diagram – Six (6) Well Pad
XTO Energy, Inc. 

NSR Synthetic Minor Permit Application 

XTO211339 

ATTACHMENT H: PRODUCTION DECLINE CURVE 

CALCULATIONS (CONFIDENTIAL) 
XTO Energy, Inc. 

NSR Synthetic Minor Permit Application 

XTO211339 

ATTACHMENT I: 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: XTO Energy

 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: 314.48

 Net Throughput(gal/yr): 314,484.00

 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): 1.1569

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

 Vapor Pressure at Daily Average Liquid

 Surface Temperature (psia): 0.0045

 Annual Net Throughput (gal/yr.): 314,484.0000

TANKS 4.0 Report Page 3 of 6

file://C:\Program Files\Tanks409d\summarydisplay.htm 9/29/2011
 Annual Turnovers: 314.4840

 Turnover Factor: 0.2621

 Tank Diameter (ft): 4.1600

 Working Loss Product Factor: 1.0000

Total Losses (lb): 1.4223

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 1.16 0.27 1.42

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