**~"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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# 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 ppmComponent 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 100.0000XTO 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 **S PECS** XTO Energy, Inc. NSR Synthetic Minor Permit Application XTO211339 

# ATTACHMENT F: ENCLOSED COMBUSTOR **M ANUFACTURER’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 WencoXTO Energy, Inc. NSR Synthetic Minor Permit Application XTO211339 

# ATTACHMENT G: PROCESS FLOW DIAGRAM OF **F ACILITY** 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 FuelGas & 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 PadXTO Energy, Inc. NSR Synthetic Minor Permit Application XTO211339 

# ATTACHMENT H: PRODUCTION DECLINE CURVE **C ALCULATIONS (CONFIDENTIAL)** XTO Energy, Inc. NSR Synthetic Minor Permit Application XTO211339 

# ATTACHMENT I: 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: 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) 

### Page 1 of 6 TANKS 4.0 Report

9/29/2011 file://C:\Program Files\Tanks409d\summarydisplay.htm1000 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.htm1000 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): 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 

### Page 3 of 6 TANKS 4.0 Report

9/29/2011 file://C:\Program Files\Tanks409d\summarydisplay.htmAnnual Turnovers: 314.4840 Turnover Factor: 0.2621 Tank Diameter (ft): 4.1600 Working Loss Product Factor: 1.0000

Total Losses (lb): 1.4223 

### 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 1.16 0.27 1.42 

### Page 5 of 6 TANKS 4.0 Report

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### Page 6 of 6 TANKS 4.0 Report

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