ll1egee C:onsulting 

Air Quality Permitting 4341 West 40th Street 

Environmental and Regulatory Consulting Casper, Wyoming 82604 

Phone 307-232-0303 Cell Phone 307-262-0270 Email 

September 30, 2011 

Minor NSR Permitting Coordinator 

U.S. EPA, Region 8 

1595 Wynkoop Avenue, 8P-AR 

Denver, Colorado 80202-1129 

RE: 	 Petro-Hunt, LLC 

Tribal NSR Air Quality Permit Applications 

Dear Sir or Madam: 

On behalf of our Client, Petro-Hunt, LLC (Petro-Hunt), enclosed are completed Form 

NEW and Form SYNMIN applications for six oil and gas production facilities located on the 

Fort Berthold reservation in North Dakota. These six facilities will begin construction prior 

to December 31, 2011. These applications are being submitted in accordance with the 

requirements of 40 CFR 49.151-49.161, the Federal Minor New Source Review in Indian 

Country program. In addition, this filing is in accordance with the recent Administrative 

Complaint and Consent Agreement between Petro-Hunt and EPA. 

The applications submitted herewith are for the following facilities: 


Ft Berthold #148-94-28A-33-1H, 2H Production Facility 


FtBerthold #152-93-18B-19-1H, 2H, 3H Production Facility 


Ft Berthold #148-94-33D-28-4H, 5H Production Facility 


Ft Berthold #147-94-3B-l 0-3H, 4H, 5H Production Facility 


Ft Berthold # 148-94-27D-22-2H Production Facility 


Ft Berthold #148-94-29B-32-1H, 2H Production Facility 


If we can provide any clarifications or additional information on these applications, 

please contact me at the letterhead address, telephone, or email. 

Michael A. Megee 

Permit/Regulatory Consultan 

Attachments 

Copy to: D. Clark 

D. Hanson 

J. Gillies Jr. 

T. Hall (without attachments) 
UNITED STATES ENVIRONMENTAL PROTECTION AGENCY 

Region 8 Air Program 

FEDERAL MINOR NEW SOURCE REVIEW PROGRAM IN INDIAN COUNTRY 

Checklist - Synthetic Minor Limit Request 

(Form SYNMIN) 

Use of tbis information request form is voluntary and not yet approved by tbe Office of Management and Budget. The 

following is a check list ofthe type ofinformation that Region 8 will use to process information on your proposed project. While 

submittal ofthis form is not required, it does offer details on the information we will use to complete your requested approval and 

providing the information requested may help expedite the process. Use of application forms for this program is currently under 

Office ofManagement and Budget review and these information request forms will be replaced/updated after that review is 

completed. 

Please submit information to following two entities: 

Federal Minor NSR Penn it Coordinator 

U.S. EPA, Region 8 

1595 Wynkoop Avenue, 8P-AR 

Denver, CO 80202-1129 

A. GENERAL INFORMATION 


B. ATTACHMENTS 


Joe Gillies Jr. 

Environmental Director - Environmental Division 

204 W. Main 

New Town, ND 58763-9404 

Company Name 

Petro-Hunt, LLC 

Facility Name 

Ft Berthold #148-94-33D-28-4H, 5H Production Facility 

Company Contact or Owner Name 

David Clark 

Title 

SafetylEnvironmental 

Director 

Mailing Address 

1601 Elm Street, Suite 3400, Dallas, TX 75201 

Email Address 

dclark@petrohunt.com 

Telephone Number 

214-880-8400 

i Facsimile Number 

214-880-710 1 

For each criteria air pollutant, hazardous air pollutant and for all emission units and air pollutantgenerating activities to be covered by a limitation, include the following: 

./ 	Item 1 - The proposed limitation and a description of its effect on current actual, allowable and the potential to 

emit. 

./ 	Item 2 - The proposed testing, monitoring, recordkeeping, and reporting requirements to be used to demonstrate 

and assure compliance with the proposed limitation. 

./ 	Item 3 - A description of estimated efficiency of air pollution control equipment under present or anticipated 

operating conditions, including documentation ofthe manufacturer specifications and guarantees. 

./ 	Item 4 - Estimates ofthe Post-Change Allowable Emissions that would result from compliance with the proposed 

limitation, including all calculations for the estimates. 

./ 	Item 5 - Estimates ofthe potential emissions of Greenhouse Gas (GHG) pollutants before and after proposed 

emission contrQls. 

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September 28, 2011 

Petro-Hunt, LLC 

Ft Berthold #148-94-33D-28-4H, 5H Production Facility 

ATTACHMENT ITEM 1: Requested Limitation 

Petro-Hunt, LLC (Applicant) is requesting a Synthetic Minor Permit for VOC emissions from 

storage tanks at this facility. Proposed operations at this facility include production of crude oil 

and natural gas from two wells. Storage and handling ofthe crude oil will result in vapor 

emissions from the storage tanks from flashing ofthe liquid from a pressurized state to 

atmospheric pressure. Additionally there are vapor emissions from the tanks from working, 

standing, and breathing conditions. Without controls, these VOC emissions could potentially 

amount to more than 200 tons per year. Applicant proposes to install a vapor vent system to 

collect the hydrocarbon vapors from the storage tanks and route these vapors to a pair of 

enclosed, vertical, smokeless incinerators which will provide at least 98% destruction ofthese 

vapors. 

The proposed emission control system will consist oftwo identical systems, each composed of 

tank vent piping, a liquids catch vessel, a back pressure/flame arrestor device, an enclosed 

vertical combustor with continuous pilot flame, a thermocouple and data recording system to 

monitor the presence of a pilot flame, and an automatic re-igniter system to re-light the pilot 

flame ifit goes out as a result ofwind or other conditions. Manufacturer data on the proposed 

combustors indicates a destruction efficiency greater than 99%, however Applicant has used a 

98% efficiency in emission calculations as a conservative estimate. 

Detailed calculations of controlled and uncontrolled emissions from storage tanks at this facility 

are provided within the Region 8 FORM NEW application which is concurrently filed with this 

application. A summary ofemissions is presented here: 

Uncontrolled Storage Tank VOC Emissions 150 tons per year 


Proposed Controlled Storage Tank VOC Emissions 3 tons per year 
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Total Facility Uncontrolled First Year VOC Emissions 209 t tons 


Total Facility Controlled First Year VOC Emissions 55 tons 


Potential emissions of carbon dioxide, methane, nitrous oxides and other "Greenhouse" gas 

constituents at this facility are very small (see attachments to Region 8 FORM NEW), and 

therefore are not included in this application for Synthetic Minor limits for VOCs. 

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Casper, Wyoming t 

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September 28, 2011 

Petro-Hunt, LLC 

Ft Berthold #148-94-33D-28-4H, 5H Production Facility 

ATTACHMENT ITEM 2: Proposed Testing, Monitoring, Recordkeeping, 

And Reporting 

Proposed Monitoring Requirements 

(a) 	 Total VOC emissions from each storage vessel (flashing and 

standinglworkinglbreathing) shall be determined using one or more of the 

following methods or combination ofmethods: 

i. 	Direct measurement of standing/workinglbreathing losses by sampling 

and lab analysis; 

ii. EPA Tanks 4.0.9d to calculate standinglworkinglbreathing losses; 

iii. Direct measurement of flashing emissions by sampling and lab analysis; 

iv. Process Simulator such as PRO MAX, HYSIM, HYSIS using sitespecific sampling and lab analysis to calculate flashing emissions in 

conjunction with EPA Tanks 4.0.9d to calculate standinglworkinglbreathing 

losses; 

v. API E&P Tanks Software V 2.0 using site-specific sampling and lab 

analysis to calculate standinglworkinglbreathing losses and flashing 

emISSIOns; or 

vi. Other methods approved by EPA. 

(b) 	 Total VOC emissions from each storage vessel shall be determined using the 

following input parameters: 

i. 	Current inlet hydrocarbon stream properties (extended laboratory 

analysis) for each stream entering a hydrocarbon storage vessel; 

it 	Current month's daily average hydrocarbon flow rate to the hydrocarbon 

storage vessel; 

iii. 	 Temperature and pressure ofthe hydrocarbon stream provided in the 

laboratory analysis; 

iv. Ambient pressure of 12.0 psi a and annual average ambient temperature 

of40-50°F; 

v. The emission reduction technology type and related data; and 

Proposed Recordkeeping Requirements 

(a) Total VOC emissions, in tons, from each hydrocarbon storage vessel shall be 

calculated and recorded at the end of each month, beginning with the first full calendar 
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month after operations commenced. Prior to twelve (12) full months of operation, the 

Applicant shall, at the end of each month, add the emissions for that month to the 

calculated emissions for all previous months since operations commenced, where 

applicable, and record the total. Thereafter, the Applicant shall, at the end of each month, J 

add the emissions for that month to the calculated emissions for the preceding eleven (11) 

months and record a new twelve (12) month total. I 

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(b) Records shall be kept of all input parameters and calculations, including the input 	 t 

! and output reports for the models, used to determine the monthly emissions. 

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Proposed Reporting Requirements 

1. 	 Any documents required to be submitted under this proposal shall be submitted 

to: 

U.S. Environmental Protection Agency 

Region 8 Office of Enforcement, Compliance & Environmental Justice 

Air Toxics and Technical Enforcement Program, 8ENF-AT r 

1595 Wynkoop Street f 

Denver, Colorado 80202 I 

2. 	 The Applicant shall submit an annual report ofrolling 12 month annual emissions I 

each year no later than April 1

st• The annual report shall cover the period for the 

previous calendar year. For the first calendar year the Applicant shall submit the i 

cumulative facility wide emissions. I 

3. 	 The Applicant shall promptly submit to EPA a written report of any deviations of 

emission or operational limits and a description of any corrective actions or 

preventative measures taken. A "prompt" deviation report is one that is post I t 

marked within thirty (30) days from the discovery of an exceedance. 

4. 	 The Applicant shall submit a report for any required performance test to the EPA 

Regional Office within 60 days after completing the test. 

The Applicant shall submit any record or report required by this permit upon EPA request 

Megee Consulting 


Casper, Wyoming 

September 28, 2011 

Petro-Hunt, LLC 

Ft Berthold #148-94-33D-28-4H, 5H Production Facility 

ATTACHMENT ITEM 3: Proposed Control Equipment Efficiency 

As proposed in this Synthetic Minor permit application, the VOC control devices for storage 

tank emissions are expected to operate at a minimum destruction efficiency of 98%. This is the 

accepted efficiency for enclosed flare devices ofthis type and service. Documentation from the 

manufacturer, Messco of Rock Springs, Wyoming, indicates typical destruction efficiencies of 

99.9% (a copy ofthis documentation is included in the attachments to Region 8 FORM NEW). 

The standard efficiency of 98% was used in the emission calculation for storage tanks provided 

with the application. 

Megee Consulting 


Casper, Wyoming 

September 28, 2011 

Petro-Hunt, LLC 

Ft Berthold #148-94-33D-28-4H, 5H Production Facility 

ATTACHMENT ITEM 4: Proposed Post Cbange Allowable Emissions 

Calculations of emissions from storage tanks are based upon mass balance methods using E&P 

Tanks V2.0 and EPA Tanks 4.0. A representative sample was calculated from extended 

hydrocarbon analyses taken from five area wells producing from the same formation and under 

the same operating conditions as the proposed facility. The Gas-Oil Ratio calculated by the E&P 

Tanks V2 software, along with a calculated average production rate, and the average VOC 

weight percent calculated from the same representative sample, is used to generate the proposed 

uncontrolled and post-change controlled emissions, expressed in tons per year. The detailed 

calculations are contained within the Attachments to the Region 8 FORM NEW Application, 

which is filed concurrently with this FORM SYNMIN Application. A summary ofthese 

emission rates is shown below: 

Uncontrolled Storage Tank VOC Emissions 156 tons per year 

Proposed Controlled Storage Tank VOC Emissions 3 tons per year 

Total Facility Uncontrolled First Year VOC Emissions 209 tons 

Total Facility Controlled First Year VOC Emissions 55 tons 

Megee Consulting 


Casper, Wyoming 

September 28, 2011 

Petro-Hunt, LLC 

Ft Berthold #148-94-33D-28-4H, 5H Production Facility 

ATTACHMENT ITEM 5: Greenhouse Gas Emissions 

Potential emissions of carbon dioxide, methane, nitrous oxides and other "Greenhouse" gas 

constituents at this individual oil and gas production facility are very small (see attachments to 

Region 8 FORM NEW). and therefore are not included in this application for Synthetic Minor 

limits for VOCs. 

Megee Consulting 


Casper, Wyoming 

UNITED STATES ENVIRONMENTAL PROTECTION AGENCY 

Region 8 Air Program 

FEDERAL MINOR NEW SOURCE REVIEW PROGRAM IN INDIAN COUNTRY 

Check List - Application for New Construction 

(Form NEW) 

Please check all that apply to show how you are using this form 

• Proposed Construction of a New Facility 

o Proposed Construction ofNew Equipment at an Existing Facility 

o Proposed Modification of an Existing Facility 

o Other - Please Explain 

Use of this information request form is voluntary and not yet approved by the Office ofManagement and Budget. 

The following is a check list of the type ofinformation that Region 8 wiD use to process information on your proposed 

project. While submittal ofthis form is not required, it does offer details on the information we will use to complete your 

requested approval and providing the information requested may help expedite the process. Use Of application forms for 

this program is currently under Office ofManagement and Budget review and these information request forms will be 

replaced/updated after that review is completed. 

Please submit information to following two entities: 

Minor NSR Permitting Coordinator 


'U.S. EPA, Region 8 


Jt595 Wynkoop Avenue, 8P-AR 


'Denver, CO 80202-1129 

A. GENERAL FACILITY INFORMATION 

1. 	(a) Comp~y~••e 


Petr~Runt, Itt 


(b) 	Operator Name 


PettO-Hunt, LLC 


ft Type of Operation 

Oil and Gas ProdUCtion 

6. NAICS Code 


211111 


8. 	Physical Address (home base for portable sources) 

See #12 below 

9. 	Reservation* 

Ft Berthold 

12a. Quarter Quarter Section * 

To Be Determined 

10. County* 

Dunn 

12b. Section* 

33 

Joe Gillies Jr. 


Environmental Director - Environmental Div. 


204 W. MaIn 


New Town. NO 58763-9404 


I 2. Facility Name 

Ft Berthold # I48-94-33D-28-4H, 5H Production 


Facility 


4. Portable Source? DYes X No 

5. 	 Temporary Source? DYes X No 

7. 	 SIC Code 

1311 

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11 a. Latitude* 11 b. Longitude* 

To Be Determined To Be Determined I 

12c. Township* 12d. Range* I 

148N 94W I

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*Provide all proposed locatIOns ofoperatIOn for portable sources t 

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B. PREVIOUS PERMIT ACTIONS (Provide infonnation in this fonnat for each pennit that has J 

b . een Issue d t 0 thO IS :fi aCllty. T P'd roVI e as an attac hm'f entl a dd' ItlOna '1' space IS necessary )

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Facility Name on the Permit 

Not Applicable New Facility 

Permit Number 

Date of the Permit Action 

Facility Name on the Permit 

Permit Number 

Date ofthe Permit Action 

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Facility Name on the Permit 

Permit Number 

Date of the Permit Action 

Facility Name on the Permit 

Permit Number 

Date of the Permit Action 

Facility Name on the Permit 

Permit Number 

Date ofthe Permit Action 
C. CONTACT INFORMATION 


Company Contact Title 

David Clark Safety (Environmental 

Director 

Mailing Address 

1601 Elm Street, Suite 3400, Dallas, TX 75201 

Email Address 

dc lark(@petroh.llnt.com ~ 

Telephone Number Facsimile Number 

214-880-8400 214-880-7101 

Operator Contact (if different from company contact) Title 

As Above 

Mailing Address 

Email Address 

Telephone Number Facsimile Number 

Facility Contact Title 

Doug Hanson District Safety Coordinator 

Mailing Address 

258 119 Ave. SW, Killdeer, ND 58640 

Email Address 

dhanson@Qetrohunt.com 

Telephone Number Facsimile Number 

701-863-6622 701-863-6620 

Compliance Contact Title 

Michael Megee Permit/Regulatory Consultant 

Mailing Address 

Megee Consulting 4341 W 40th St., Casper, WY 82604 

Email Address 

megeecgnsulting(l1lgwestoffice.net 

Telephone Number Facsimile Number 

307-232-0303 307-232-0303 

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D. ATTACHMENTS 


Include all of the following information (see the attached instructions) 

./ 	FORM SYNMIN - New Source Review Synthetic Minor Limit Request Form, ifsynthetic minor limits are 

being requested . 

./ 	Narrative description ofthe proposed production processes. This description should follow the flow of 

the process flow diagram to be submitted with this application . 

./ 	Process flow chart identifying all proposed processing, combustion, handling, storage, and emission control 

equipment. 

./ 	A list and descriptions of all proposed emission units and air pollution-generating activities . 

./ 	Type and quantity of fuels, including sulfur content of fuels, proposed to be used on a daily, annual and 

maximum hourly basis . 

./ 	Type and quantity of raw materials used or final product produced proposed to be used on a daily, annual and 

maximum hourly basis . 

./ 	Proposed operating schedule, including number of hours per day, number of days per week and number of 

weeks per year . 

./ 	A list and description of all proposed emission controls, control efficiencies, emission limits, and monitoring 

for each emission unit and air pollution generating activity . 

./ 	Criteria Pollutant Emissions - Estimates of Current Actual Emissions, Current Allowable Emissions, PostChange Uncontrolled Emissions, and Post-Change Allowable Emissions for the following air pollutants: 

particulate matter, PMlO, PM2.5, sulfur oxides (SOx), nitrogen oxides (NOx), carbon monoxide (CO), volatile 

organic compound (VOC), lead (Pb) and lead compounds, fluorides (gaseous and particulate), sulfuric acid 

mist (H2S04), hydrogen sulfide (H2S), total reduced sulfur (TRS) and reduced sulfur compounds, including all 

calculations for the estimates. 

./ 	These estimates are to be made for each emission unit, emission generating activity, and the project/facility in 

total. 

./ 	Modeling - Air Quality Impact Analysis (AQIA) 

./ 	ESA (Endangered Species Act) 

./ 	NHPA National Historic Preservation Act 

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E. TABLE OF ESTIMATED EMISSIONS 

The following tables provide the total emissions in tons/year for all pollutants from the calculations 

required in Section D ofthis form, as appropriate for the use specified at the top ofthe form. 

E(i) - Proposed New Facility 

Pollutant Potential Emissions 

(tpy) 

Proposed Allowable 

Emissions 

(tpy) 

PM NA NA PM - Particulate Matter 

PM10 - Particulate Matter less 

PM10 

PM 1.5 

NA 

NA 

NA ! than 10 microns in size 

NA PM2.5 - Particulate Matter less 

than 2.5 microns in size 

SOx 0 0 SOx - Sulfur Oxides 

NOx - Nitrogen Oxides 

NO. 1.67 1.97 CO - Carbon Monoxide 

CO 8.24 9.86 

voc -Volatile Organic 

Compound 

VOC 208.62 55.41 Pb - Lead and lead compounds 

Fluorides - Gaseous and 

Pb 0 0 particulates 

Fluorides NA NA H2S04 - Sulfuric Acid Mist 

HzS - Hydrogen Sulfide 

H2SO4 0 0 TRS - Total Reduced Sulfur 

HzS 0 0 RSC - Reduced Sulfur 

Compounds 

TRS 0 0 

RSC 0 0 

Emissions calculations must include fugitive emissions ifthe source is one the following listed 

sources, pursuant to CAA Section 3020): 

(a) Coal cleaning plants (with thermal dryers); 

(b) Kraft pulp mills; 

(c) Portland cement plants; 

(d) Primary zinc smelters; 

(e) Iron and steel mills; 

(f) Primary aluminum ore reduction plants; 

(g) Primary copper smelters; 

(h) Municipal incinerators capable of charging more than 

250 tons ofrefuse per day; 

(i) Hydrofluoric, sulfuric, or nitric acid plants; 

(j) Petroleum refineries; 

(k) Lime plants; 

(1) Phosphate rock processing plants; 

(m) Coke oven batteries; 

(n) Sulfur recovery plants; 

(0) Carbon black plants (furnace process); 

(p) Primary lead smelters; 

(q) Fuel conversion plants; 

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(r) Sintering plants; 

(s) Secondary metal production plants; 

(t) Chemical process plants 

(u) Fossil-fuel boilers (or combination thereof) totaling 

more than 250 million British thermal units per hour f 

heat input; 

(v) Petroleum storage and transfer units with a total i 

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storage capacity exceeding 300,000 barrels; 

(w) Taconite ore processing plants; 

(x) Glass fiber processing plants; 

(y) Charcoal production plants; 

(z) Fossil fuel-frred steam electric plants of more that 

250 million British thermal units per hour heat input, 

and 

(aa) Any other stationary source category which, as of 

August 7, 1980, is being regulated under section III or 

112 ofthe Act. 

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E(ii) - Proposed New Construction at an Existing Facility or Modification of an Existing Facility 

Not Applicable - New Facility 

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Pollutant Current 

Actual 

Emissions 

(tpy) 

Current 

Allowable 

Emissions 

(tpy) 

Post-Change 

Potential 

Emissions 

(tpy) 

Post-Change 

Allowable 

Emissions 

(tpy) 

PM 

PM10 

PM z.s 

SOx 

NO. 

CO 

VOC 

Pb 

NH3 

Fluorides 

HzS04 

HzS 

TRS 

RSC 

PM - Particulate Matter 

PMw - Particulate Matter less than lO microns in size 

PM2.5 - Particulate Matter less than 2.5 microns in size 

SOx - Sulfur Oxides 

NOx - Nitrogen Oxides 

CO - Carbon Monoxide 

VOC - Volatile Organic Compound 

Pb - Lead and lead compounds 

NH3 - Ammonia 

Fluorides - Gaseous and particulates 

H2S04 - Sulfuric Acid Mist 

H2S - Hydrogen Sulfide 

TRS - Total Reduced Sulfur 

RSC - Reduced Sulfur Compounds 
EMISSION SUMMARY 

Petro-H u nt, LLC ~~~-~~~-~~ 

Ft Berthold #148-94-33D-28-4H. 5H Production Facility ; -...--.-~- ~- ~~-~.---~ ~--- I ----~--~----" ­ -- -----i------ ­---~- .---------~~ 

~~-~-~.... -~. _>~_~> __L ... . ~.~~~~~~~--~~~. r ~-~~~~~~~~~~~~ ~~ ~~~~~-.~ ~ ~-~~--~ ~~-~~i~~>~·····~- ~--~~~ 

Attachment to Air Quality Permit Application --~.....------­ ---_....._------,-------- ----_..._---­ -:~------..... . 

EMISSIONS SUMMARY - TONSNEAR I-----~.~.~.~~....--~~~- ......--~-.. . 

----­ ~----

i HAPs NOx. CO ,502, H2S .~-~ .. _­ ~-:- ----~----;- -----~ -+­ -~ , Uncontrolled Emissions 

Source: 

TOTAL 

Controlled Emissions 

TOTAL 

There are no individual HAPs of more than 9 ....... ~~---'-----~ ... 

Megee Consulting .......-------­ -r Cas--er, Wyoming--"----······· 
PROCESS DESCRIPTION AND 


FACILITY SCHEMATIC 

September 28,2011 

Petro-Hunt, LLC 

Ft Berthold #148-94-33D-28-4H, 5H Production Facility 

Process and Facility Description 

Attachment to Air Quality Permit Application 

This facility is a two-well proposed Bakken Pool completion with equipment and operating 

parameters similar to other wells in the area. Production, equipment and operations for the two 

wells are identical. Fluids and gas produced from the wellbores will travel through flowlines to 

Hess Services Inc. 6x20 vertical heater-treater separators. These units have a 0.5 MMBtulhour 

heater which operates from produced gas with an estimated heat content of 1200 BtulFt3

• The 

separation equipment will operate at approximately 30 PSIG pressure and 1200 temperature. Gas 

from the separation equipment will initially flow to a ground or pit flare for incineration until a 

gas pipeline connection is constructed. This flare is mandatory for safety purposes since vented 

produced gas is an extreme safety hazard with substantial risk offire and explosion. The pit flare 

is equipped with an automatic ignition device. It is expected that the pit flare will be utilized for 

no more than a period of 90 days until the pipeline connection is in service. 

Fluids (oil and water) are separated within the heater-treater separation equipment and sent to 

tanks for storage and eventual loading into bulk trucks for sale or disposal. Loading conditions 

are submerged loading into a dedicated service tank trailer. For each well there are four-four 

hundred barrel welded steel oil tanks and two-four hundred barrel fiberglass water storage tanks. 

All tanks are of Hess Services manufacture. There are two 8 horsepower gasoline engine driven 

recycle pumps, one for each equipment train which may be used to re-circulate tank fluids 

through the heater-treater equipment as necessary. It is expected that these pumps will be 

operated no more than 70 hours per year each using commercial unleaded gasoline. 

The storage tanks in each equipment train are vented to an individual combustor system utilizing 

a Messco VOCinerator vertical smokeless incinerator which has destruction efficiency rating of 

more than 99%. The piping to each ofthese combustor devices includes a liquids catch pot and a 

backpressure/flame arrestor device. A thermocouple and data recording devices are installed to 

record the presence ofthe pilot flames. Automatic pilot re-ignition systems are also installed. 

Manufacturer data sheets and information on the equipment discussed above is included in the 

attachments to this application. 

Megee Consulting 


Casper, Wyoming 

---------------

2-Vertical6x20 HeaterTreater Separators, 30 

::r--l+_.....!P:.::S~IG:;!;,~1.::2~Oo______~. 

L.,..~~----fi. 

2-8 Hp 

Gaso 

Engine 

Recyct 

I 'co~~~tor Tank!Vent Line . I

-I - ­ -­

Truck 

Loadouts 

Truck 

Loadouts 

Petro-Hunt, LLC 

Ft Berthold #148-94-33D-28-4H, 5H 


Representational Production Facility Schen1atic 


Both a Pit Flare For Initial 

Separator Gas Emission Control 

and the Final Pipeline 

Connection are shown. The Pit 

Flare is estimated to be used for 

a maximum of 90 days. 

ToGas 

Sales 

Pit .. 

iQ Gas 

Meter 

Pumps 

Attachment to Air Quality Pennit Application 

4H Wellhead 

5H Wellhead 

NOTE: Not To Scale 

Oil Line 

.... --­ Gas Line ... ,.......... 


Water Line 

.l/egee C onsuiling 

Casper, Wvoming 

September 28, 20!! 
DESCRIPTIVE ATTACHMENTS 

-­

SepJem_~§!r?~J?J1 _' _____'''' 

Petro-Hunt, LLC '-'-'---'­ ,----+--­

~_~~_~~~~:~I::?_-~~~~J?tI--~~~(f~-~!~~-~~£!!ity-----

Atta.2.hmenU9 Air q~!lJity P_errpit AJ?PJicati2rl_l ____ 

-'-----+-­ -,--,--,--­

List and Description of Emission Sources/Units ~~~"""'----~~-""-------~---"'T----- ~----....---~-- --~--""--~--,------""--------~-""'----

. ._--------­ ---.-~---- -------­ - - --------­ ·c-----­ -~---.---

Process Bu_,!,er/Heate_r_Sources_ ,_~~__ , ______ ,._~,~_~, ,._,_~_~ L______, The two identical Hess Services vertical heater-treater separators each have a 0_500 MMBtu/hour heater, 

_ft.JE!'edV'li~produ~~~(E!~tirn~1290 Btu/~ef~n_~iimaIed to~operate-nO-:rl1ore,t~§Oo/Q~uty:cy£:~~ 

TruE~_L~<!QDe~.,! ___ _____ ,. ______=~-T____ . This facility is expected to process approximately 163,000 barrels of oil during the first year of operation, all 

of\'Vhich will be carrledawayfrom-itie Slteinbl.llktrucks:The process of loading oil intottiesebUlk tl'yCkswill g~irCl!~VOC emiSsions.t:f~~c:li~pla~rne~of lines·and truck tank9~ElPC!ctme.,t§J- -­-'C­ ' --,--­ ' -- ---­

,

, 

1§9i~~~~<:~____ ______ ______ -1­ _,_L_",,~ Normal operations generate fugitive leaks from connectors, valves, and other components of piping ---"-,-,---"--,--,---"'------,----"---' ---~-,-~-' - --~-'I-~-' -'--'-----"'-~"~---'- "'. ,.,,'---­

__ ~qUip'!l~Il!.Clt the site. 1__ __ ' , i --------~-

St~,r:a.B~!!I·lk,_~.!!Iis~r1f:l_,'_,_"~, _' _ __ , . ~i .__ 

St~rCl9~ tank!>.il1_hl'droca!~~1'1 liql:Ji~!>.ervi£:e!~~a.!>.~ vap~~!>.~hen~!I1_~liqujds <!~!rCl_I1~fer!~~~f~rna_hig~e!......."1_" 

_p~e_~sure velO~~1 such asa . ,!eate,.-!reate! ..to t~~atmQ.s£I'l~!lc. pr~!l>ur~§t~rag~t'!l1.ks:~I~<:I~ition there 

~ .are§lt~r!<:Ii.nglV\f()rking/Brei3thilJiLloss~~Jr()fll norfllal!al1k Op~f!it!on!3J!iUing ,_e,,_aporatio~. etctII'l~s_~___. ___ 

vapors are either released to the atmosphere (uncontrolled operation), or are piped to an incinerator or ! 

..... C()mb~!>.tC:,!1~i.c!es.triJ~tio~Icont~9Wed op~ra~ion)~ All tank vapors~at!l1i§Jlrod~~~onT~CllitLare contr~~~<[=---'"-i~'--

through the use of two Messco VOCinerators, vertical, smokeless, flare stacks which have a destruction 

-effi-c~.QcY of gr~Cl!~~thari~~:=-":_ .~==-=__==~~":_-_l··· ~-~-~----~-- --~~~'--' ,---~,---' I ,~----' 

Temporary Treate!.~..~_i___'" ~-'-1" '" ------­ ~" 

_[)LJ!i~9.an initiCtioperatin9_pe!~~~Yi'l'lile wCliting f~! cOfllpl~!ign~f aJlaspip~lin~~pl1_l1.e9.ic~n to!I'l~~~ell~~,. _~~-,-._ 

.. pr~uced ga_s_which is s~parate<:lfromJ.~J>,.~du~()l1.!tr~amiI1Jhe heatl~r-trea_t~r s~parati~n eqLIip"!~nt________ ~ 

.... .i!.PurnedJ~r safety reasons in .. g!ound ()rp!t!lare . .lhisls. nece!3sa!)'~incevel1ted natura! gas poselO_Cl.r1...__ 

extreme risk of fire and explosion. This flare equipment is fenced to prevent access by personnel or animals, 

and is equipped with an~automatic~jgnitersystem to mamtain flamepresence~afafl times-:--For calcl.llat~T~-~"· 

. purposes~sassumed thatthistreatergas flare wiiloperateforno more than90-d-ays-afterlnitia'­ ... -~---

production is-estabilShed.-Recognrzecfdestruction-efficiencYforthTs-typeoHfare isif6o~-" .---­ ---'~-'-I --"~-,----- --~---~,---­ ---.~--------;--- ._--------,' .-.-----­ ._._-------_. 

Gasoline En ine Rec cle Pum ,,------~-.....----.----.....-----.­ - ..... -~-- - - .. ~--------

_ It is!3~'!l~tirl!esl1~c~ssary tg!~"cy~e liqLJ.i<:ll:If!~mCl_s.!~rag~.!.al1~Jl'lro1l91'l!~~.Jl~ate!-t,.eater!3~PCl!atio.n __,___-+-_ 

_ ~uipfll~I1!.!()achie",~ maximLJrrlsepar~ti~nof oil_Clnd~ater.r=acl'l~oduc!ion train ha~as.!!lCll!J3_h.ors_epow~r 

gasolil1e engine (jriven pump to accomplish this. These engines are HondaGX-240 models and use unleaded __~" 

- gasoline as fuel: It is estimated thateach of theseengmes wili runnotmore than7(nloursperyear.---~· - - i ~---- ~""---"--I-,----~, "--,~'-~'-~~-~--"-----' --" ,---,-­

""._-------""-,,----"" ,,, -----+-----.,,~ "--~~~""~ ,---~--~- ,,,~, ,---.""~, j-----~""~ 

I MegeeConsulting--~~~~·· 

~i Casper; Wyoming 
----- ---

Petro-Hunt, LLC 

Ft Berthold #148-94-33D-28-4H. 5H Production Facility .._ ..__.c._..c._.cc_.._._.._._.____ ~]_c __________ .__._..._; __..__.

Attachment to Air Quality Permit Application ···--c ...--.. ·---··T-· 

Fuels _ .._ ......_c._.._c._.._ .. _ ... ___.... ... _ ...... _ ... ___..__J __. . __ . ....__._.. _. __.L ..... _. _.. _ 

Fuel used at this facility consist of produced natural gas, separated from the production stream at the 

heater-treater-separaiion equjpmenCarl<fasmaliamount ofunleade(fgasoline used for the recycle pump engines. 

--Gasofineforthe!)e-enginesTspurchasedfrom.abulkdistributor~-stOredai-Petr(;Hunt'sfield-officeTocaiions: .,------­

- an-dtranspo~d to the-w~ilsit~~!needed.-EStimatea annua.f unlea~e(L9:a.solfn~ lJseJsa!=>!=>f()xir!!.ateli'_35~~iIOnsfOr 

each engine Natural gas used as fuel for the heater-treater burners and the Tank Flare pilots is estimated to =~~PP!oXf~~!EiIi~~650MCFarld·350-MtF~~:r:esPJ39tivEliy~ - ---.... c· --.--•• -- • --.­

I 

L , -~~ --< t ---< 

Raw ___________ Mat ~~ er_______ ials/Finished .__________ ________ Products _ _ ________-'_ . ___.. _~ ________--.L____________

.. _ Es~mat~~ av~rag~_~lJ..a_'!~!Le! of 9rude ()j'-i1.nd_~~tll~~L g_~ to b~ "i.~dllce~, jJl"()cess~<L~fld~I~-~ ~'p~!)ed from..._ .__. 

thisf()(;ility are as follows: .----.-t _.... ,__ .___ .____. ____ Daily Average .~ Annual Average; Maximum Hourly;______ 

Crude Oil - Barrels 

411.8 

447.8 1§~,4±t 36.9 --~--- -------. ------------- ------­

Natural Gas - MCF j§O,28_9____ 32.6 

-------- ...-- ~---~-. -.---- ._--_., -'--~. ,_._-­

__ Ihe~.!I11_()unts_CJl:.e..!r:0mJhe ,=rod~tio,!_AsslJmp!!()ns,~ver~ge First'!l0nt~ ,=!()~uc!jg".'..;~!lC"L. ___ .~__ __ _ 

Ave.r:Ci.ge First Year Decline worksheets included in thi~_ap[>lication 

p!P~~S~~_OPf!l"~ti!!9 S~~_~dule ___Ihisprod!lctioflfacility will o[>~a~_?i.Il_()u~per day....ldCi}'!>' per ,.vee~, 52 weeks per yea!. The hea..te!:Jreater· -­

... ___~~_lI9~()n~9..uipf!1t}fl! burfl~r_~~tc:>!=>E3!~~1_?_h0.llrsPtl.r:.cta1'o.1dilY!> Ptl!.w.J3~k,_§.?we~~!>'jJ~r.'y"eCir:Ih~____ .__ 

temporary treater gas flare unit will o[>erate 24 hours per day, 7 days per week, not to exceed 90 days in the fir~t.1'ear.- ----- ------ . -- .----,-- --~ -- --- --- --- -- --- ----. ---­

i ~-.. I -­

~T---

--- i 
.1­____ 

Petro-Hunt, LLC 

t:!!!~r!!!~'-~~~:~1Q..~-4-!t~s._~~~,~~!!_~f~~i!y__ _ 

i 

i ----­ -------+ 

Emission Control Equipment i r~~-··~--~+ i 

Emission contr.<>.I~Lllpm~"1.t.£l:9~()_~edJort~i!;..l'roduction fa~liJY include!)l!tt~f()J!()wi~: I I 

j 

,!ank_r:!~res~~l__~___~_~_~_~__ L_..~.._~ ___ 

~mis~oD!!r~m th~_st()'!I9~t<!'!.~s ",,~!JI~out~_d!o ~o identic;:31 Ml;!ssco VOCin~!:CI!ors whichar~-"ertlcaJ, sll!().I<.eI~~s_ -------r.......-­

flare stacks with a manufacturer destruction efficiency estimate of more than 99%. For purposes of this application, an 

-:~ffi~~~~~atin~(980{()-was~~ed.~a~~~\JrerJl1!ormClt!()!i()11 thfs device!~-in~!lc:l.E!din}his-applicatio~n. ~missionljmjfsL___~~ 

for these incinerators are as shown in the Emission Summary-Controlled Emissions-Tank Flare and total 3.2 TPY VOC's, i 

___.~T:rPy.H.t\Ps:T'!.:.rpyF'!QX~ClDd 1.7TPYJ::O~tJ()~t~ringj~EI5~~~~d~i~~In~cI~~~~jin in~~t~lIe(fth.~rnl()~~I~~CI.,.~fdata ~ 

recorder to verify the presence of a pilot flame, and physical inspection by the lease. operator when conducting site visits ~.-~-".--- .. ~-- ·-···---···~~I··-··-~-···-~~···--~--- _.. _-­ ..~-- --~··---~··----··--~--1··-~· -_..._­ _ ..._-­ ---.. ~-

~-.---

!~mpor!..ryJ!!~~___~as£l.are_~_~.__~~_ .._~._~__ During an initial operating period while waiting for completion of a gas pipeline connection to the wellsite. -T-~ 

--=-jiod~£Ei~~s ~l~~ i~ s~p~~~ted"_~§m-t~~~pro~~~Ton.,-!~~~a'!~Jh~J~,~__~~~!~r~i~~!~~_~~~f~¥on~~9.~ip~~ilI_ I 

.._i~.~urne.~.!or ~a!~ty reCl~ons~'!.a g!"()lJn..d_()re~.!I.CIre. This is nece,sl).CIry~il1~e.\le.'!.~d_ na..turClI9C1.~.J)()ses an_~~.L_ 

.e.xtrE!!!l~.ris~_~ firE!_Cl.'!.d~x'plo_~~Thi~ fla~E!~eglJJp'!1ent..i~f~c;e.c:l.t() e!E!v~nt~a..c:c:e.ssJ>rpef!()fl!1e.~r_aniIl!Clls, i 

and is equipped with an automatic igniter system to maintain flame presence at all times. For calculation 

--purposes~it is ass-umedthatthisTreatergasiiarew~iOpeiatefoinomore thal190daysafter initiaj'-··--­

__pr.()~Ucti()fli!.~~~a.~ji~he~.J~~o!i~ized destruction ettic;fencifoithi~typeCl!~..ei~ 9(}oj~~~M()nit~d:flg~will--' 

~clu~e inspecti0..l1...Qr!h~ leas':l..2l'.~ajQrwhen ~c()~ductJn~g sitl:!..\Iisits. .CI_n..<L~_a.!.a reC()!"dingtQ~E!..rifyJ~ ___~ 

presence of a flame. Monthly hours of operation will be recorded to verify that operation does not exceed -the~initiaf90 dayperiCldproposed ["this ap-plicatiOn. --~~.-: -­ -.. -­....--~~ .~---..--_. i----···--T---~--~---·~--

...._-­ ----., -------­

I 

._._..­ .._-.-;­

.. ·-.:Megee~onsuftln.g_ .. _ 

Casper, Wyoming 
____ _ 

. __~_ 

·_­

S~l2.tem~~! _28,~2i>11 

Petro-Hunt, LLC 

.~.- -.. ---.-.--~..­ --_..__ .. _ .._--_... _-+--_. 

L 

Attachment to Air QUCl~~P~rmit Appn~~tion , 

__t ~--TI ~-'----1 

Modeling - Air Quality Impact Analysis (AQIA): _A~J3nlr1d.i~.<ilJal oil~d ~s pr()aUct;onsi!~=vVl!h -e-mi~,-sion~~~r,JtoTs· in~tal[~d_and ope!atfIl9.~ti!~re-§~oulCf~~~~ no significant impact to the Ambient Air Quality Standards at this site. Therefore, an AQIA was not --c()nduCted.--­ ----~-~---~ -~ -_ ..-_. -.--- ..-~-.--..~-

~ll"I"Ip~.\::t!.of t~1~r()jec!_()'"l..E.l]cf!i.il9~~.<i§>P~.\::~~_~~\I~_b_~e!! o!"~n p~acfd r~s~.E3.d in.!iI1__E!I'v'ironl"l"lental 

Analysis conducted for the area and summary information on this EA is being furnished to EPA under 

~=~epa~tecover~- ___~~~, __-~-:----

Nationa! H!storic_~~~e~ati0I!_A~~J_~tI!:'.~l ______ ~---, __________L 

Impactsofthis project ()n Cultural Resources have been or will be addressed in an Environmental 

. -J\6afys;)s co.ndu~~e(npr the area anaslJmmaryJnfo~matlorl()n this EA-is-li~9JlJrnishedto EPA under 

__s!3parc:l!~.£over~ .______~~ _ 
I 

i 

f 

I

i' PRODUCTION INFORMATION 

I 

J 

f 

I 

t 

f 

I 

J 

I 

~ 

I 

f 

,t 
28, 2011 

Petro - Hunt, LLC 

I-_::__ =-'=­___ ::_~~::="'::: 

ESTIMAT 

Ft. Berthold #148-94-33D-28-4H, 5H Production Facility -~,---- -'----. '-1--- - --- -- - --- ----- ---- --.----. ..---­

MCF 

MCFD 

Oil-BOPO Gas - MCFO ---- ----- ---- .. ---- ----+-- .. -. - .-.-~---- --------,--­ , 

560 515 

42.6% 

TOTAL FIRST YEAR PRODUCTION 163,441 Barrels 150,289 

447.8 BOPD 411.8 

1------------------------------------ -- ----- ---~-

1-------- ----- -------­
----

Petro - Hunt, LLC 

Ft. Berthold Well Production 

Calculation Of Average First Month Initial Production Rate 

1st Month Production Rate 

Oil - SOPO Gas - MCFO 

Ft Berthold # 152-94-13B-24-1 H 734 803 


Ft Berthold # 152-94-14C-11-1 H 850 1148 


Ft Berthold # 152-94-220-15-1H 512 536 


Ft Berthold # 148-94-170-08-1 H 669 631 


Ft Berthold # 152-93-17C-08-1 H 511 550 


Ft Berthold # 152-93-17C-08-2H 597 635 


Ft Berthold # 147-94-2A-11-1 H 323 71 


Ft Berthold # 147 -94-3A-1 0-1 H 671 570 


Ft Berthold # 148-94-22A-27-1H 469 294 


Ft Berthold # 148-94-25A-36-1H 504 353 


Ft Berthold # 148-94-350-26-1 H 459 294 


Ft Berthold # 148-94-90-04-1H 420 298 


Average 1st Month Production 560 515 


Average 1st Month Production 


Ex Non-Typical Wells 555 496 


Conclusion: Use All Wells In Average IP Rate 

Non-Typical 

Non-Typical 

<---­

I 

I 

I 

I 

I 

I 

I 

I 

I 

I 

I 

I 

I, 

f~

Megee Consulting 

Casper, Wyoming 
----

Ye~~/Month- r&J~~~~lr-l!a~:~~~~t.t·iJ~~~$~!ltlJfs~~b~D·t~·· ·r~T~~;~~-~~?~6~Di·-Jr·--J~~~;6~:~~~~~6~Dr ·t·6iT~~~:t~-~~:?~~FD 

Petro - Hunt~~LLC L j l~ Ft. Berthold Well Production I ~ - ~ -, 

Calculation Of AyelC!9,~_firstY~$l~~productio,rlJ)~clil'le .~.. ~ ~ : ' I I

-~"---"---- .-~---- L__ - --- \-- ~- ------ ------.--- - ------.-- ,L.____ ,-- -, ._-- , ,.. _-- i -+--_.- -""--,---,-- -- -, ... -.--- ..---- -

Feb 

Mar 


April 


~~Y. 

June July- .. ..._~. 

A~ Sap

Oct 

Nov 

Dec~ 

2011: 

Jan 

Feb 

Mar 

6p~H 

fIJIay 

June 

July ~.. .... 

~ . '--1 

550' T --l---~- ~--- 31~ - j .. __ '-1 

205 469' 157~" r 284 ~~---~.~--~-- -1· I ~.~ ... 

131 1~ 

109~ 146 

120~T24 

124 109 366--~ ~. 283-243­ 183~--' 

I

I 

Aug ----. ~--~l . -­ I 

1st 12 Months 

260 277 

249 

~ 669 

37.2% 

230 

197 

209 

230 

511 

45.1% 

5 WELL AVERAGE PRODUCTION FACTOR: 

._. 

201 ----­ -­ --------­

179 

199 

211 

550 

38.4% 38.8% 

42.6% 

I 

294 

223 

135 

106 

91 

91 

102 

88 

85 

84 

82 

272 ---­ ---_._­

228 

234 

224 

208 

192 

353 

212 

180 

139 

176 

174 

193 

137 

136 

139 

123 

120 

125 174 

294 

42.5% 

: 

~ 

L 

504 353 

51.0% 49.2% 

420 

259 ----~~-,-----

180 

142 

123 

206 

184 

298 

222 

117 

87 

85 1~ 130-~~-

I 

161 89 ---­ ------­

156 98 

148 98 

134 156 

1 18 

186 133 

420 298 

44.4% 44.6% 

__ ___t_ 

631 

34.9% 

1 ---~---~- .~~~ 4L--~J I~--~_-~. ____ t 

I 669 i 631 I r' 413~ -~r- --362~ I. . 270t ~. ~2f8 I r 511 

~~~262-' -j.. -158--i~-~~337 

163 i 143 235 

149" 123- 185 • • ___ • ______ • 

140 159 

127 144 

1 139 

108 136 

~-~r-- !

+ 

.( 

------- --- --,,- -f-- ------.--- , -----. "._-- ""------------------1 ---------.------, _, ______1. 

I 

---.--, ------ --- --­
OIL & GAS ANALYSES 

---" ---_. -----

lt8.e9~e. f.()n~u!ti,,-g 

PETRO-HUNT, LLC -­ ..._----­ ---­ "--­

Fort Berthold Area Wells -­ --- !­

Calculati~n _~tRe~resentative qjl_AI'l~Iy~is 

: Ft Berthold · Ft Berthold 1 Ft Berthold I Ft Berthold . r....I'~rn ... 

-.----.-~~··-;f47~94- --j---f4i:g4':--~--148:94~--r--15i~94~-: 

---­ .- ....- --2A-11-1H I .. 3A-10-1~ i 17o:08::1H1 22[:):~5-rt!-~ 

I 

j_:_ 0.000 0.000 0.000 1__0:0-"0_ _9:9Q.'L__ 0.000 0.000 0.000 0.000 0.000 

0.000 ·----6.006­ --0.006­ 0.000 0.000 --­ --­ ---­ .-­

0.000 0.000 0.000 0.000 0.000 -­ ----------------­

0.265 0.221 0.193 0.085 0.294 ----­ ---­ --_ ... --_. ------._-­

1.200 2.195 0.990 1.320 1.498 

~J}11. _ ,__ ~~11~ ____ ,__2.2~7_ __ ~.5!5§ __ .___3..1 

c 

_4 cc 3,._.._.. _ 

0.726 1.130 0.652 0.855 0.801 

3.481 5.072 3.110 3.422 3.345 

1.311 1.733 1.202 1.211 1.306 --- ­.._- .---­ .---­ --­ ---­ --­ --­ ----­ .--­ --­ ---­ .-­ .--­ .-­ - .-­

2.489 3.216 2.290! 2.276 2.445 ----­ --­ .. ~ 

4.278 5.315 4.096 3.316 3.963 .------ ._­ ._--­ ._----­ .. -­ -­----.--­ -­

4.515 5.381 4.013 3.325 3.847 

4.731 5.546 4.249 3.760 4.249 

3.513 4.212 3.290 3.633 3.290 .-­ ---­ ---­

0.237 0.293 0.189 0.159 0.238 

0.323 0.408 0.329 I 0.356 0.408 I~~I~~':;:;~~-""'--'--' -'--/11~r?- --.­ .-..- .. -.-....-.­ -.. --..·--..-·-·-..·T-..···-·­ .. ··--· ..·-­ . ---..-. -:--,.." - .... ­ 0.172 0.222. 0.137 • 0.109 0.118 

C10 + 

TOTAL 

0.674 -­ 0:-827­ __ c __ 0~768 --'-0.59~f -­ 0.787 --­ -----­ --­ ---­

1.700 2.086 1.585 1.506 1.756 

0.000 0.000 6~o06- 6.o0(j"---- -6-:-000 

67.474 

100.000 

245.000 

0.830 

57.032 

100.000 

245.000 

0.830 

100.000 

70.510 

245.000 

0.830 

245.000 

---­ ----- --­

0.830 
TECHNOLOGY LABORATORY, INC. 

Centre Professional Office Park 

1012 Centre Avenue 

Fort COllins, Colorado 80526 

1970)490-1414 

Extended Natural Gas Liquid Analysis (OHA) 

E & P Tank 2.0/HYSIS Information 

Petro Hunt, L.L.C. 

259119th Ave SW 

Sampled: 

Received: 

06/15/11 

06115111 

Killdeer, NO 58640 Analyzed: 06125111 

Customer Contact: Doug Hanson 

Sample 10: 

Well#: 

Liquid from Separator 

Fort Berthold 147-94-2A-11-1H 

Field: 

Cylinder: 

Dunn Co. NO 

yZ 58747 

LablD: 

Sampled By: 

Analyzed By: 

A4111-09 

Bill Emery 

Bill Emery 

Sample Temperature of: 

Sample Pressure (psig): 

Sampling Method: AST

28 

M-03700 

CQMPONENT ~ole% Weight % LV% 

Carbon Dioxide 

Nitrogen (Air) 

Methane 

Ethane 

Propane 

lsobutane 

n-Butane 

Isopentane 

n-Pentane 

Cyclopentane 

n-Hexane 

Cyclohexane 

Other Hexanes 

Other Heptanes 

Methycyc!ohexane 

2,2,4- Trimethylpentar 

Benzene 

Toluene 

Ethylbenzene 

Xylenes 

Other Octanes 

Nonanes 

Decanes Plus 

0.000 

0.000 

0265 

1.200 

2911 

0.726 

3.481 

1.311 

2.489 

0000 

1.700 

0.478 

2.715 

4.515 

1085 

0.000 

0237 

0.323 

0.172 

0.674 

4.731 

3.513 

67.474 

0.000 

0.000 

0028 

0.242 

0.859 

0283 

1354 

0.633 

1202 

0.000 

0.980 

0.269 

1.553 

3.004 

0.713 

0.000 

0124 

0199 

0.122 

0.479 

3.589 

2.983 

81.384 

0000 

0.000 

0.084 

0.545 

1.316 

0389 

1.793 

0.783 

1.471 

0000 

1.139 

0.265 

1.736 

3.249 

0.110 

0.000 

0.108 

0.176 

0.10B 

0.422 

3.757 

3.055 

78.894 

Total: 100.000 100.000 100.000 

API Gravity (from lank sample); NIA Vapor Pressure (from lank sample): NIA 


Analytical Methods: ASTM 01945. ASTM 06730 (DHA). & ASTM 05307 (Distillation) 

TECHNOLOGY LABORATORY, INC. 

Centre Professional Office Park 

1012 Centre Avenue 

Fort Collins, Colorado 80526 

(910)-490-1414 

Extended Natural Gas Liquid Analysis (OHA) 


E & P Tank 2.0/HYSISlnformation 


Petro Hunt, L.LC_ 

259119th Ave SW 

Killdeer, NO 58640 

Sampled: 

Received: 

Analyzed: 

06/15/11 

05115/11 

05125111 

Customer Contact: Doug Hanson 

Sample 10: 

Well#: 

Lab 10: 

Sampled By: 

Analyzed By: 

Liquid from Separator 

Fort Berthold 147-94-3A

A4111-10 

Bill Em@ry 

Bill Emery 

-l0-1H 

Field: Dunn Co. ND 

Cylinder: YZ 58748 

Sample Temperature OF: 

Sample Pressure Ipsig): 

Sampling Method: AST

40 

M-D3700 

~QMPONENT Mole % Weight % LV%. 

Carbon Dioxide 

Nitrogen (Air) 

Methane 

Ethane 

Propane 

lsobulane 

n-Butane 

Isopentane 

n-Pentane 

Cyclopentane 

n-Hexane 

Cyclohexane 

Other Hexanes 

Other Heptanes 

Methycyclohexane 

2,2.4- Trimethylpentar 

Benzene 

Toluen@ 

Ethylbenzene 

Xylenes 

Other Octanes 

Nonanes 

Decan@s Plus 

0.000 

0.000 

0221 

2,195 

5,111 

1130 

5,072 

1733 

3216 

0000 

2086 

0597 

3.382 

5.381 

1336 

0000 

0293 

0.408 

0222 

0827 

5.546 

4,212 

57.032 

0.000 

0,000 

0026 

0.478 

1.631 

0.475 

2.133 

0.905 

1,679 

0000 

1300 

0.363 

2092 

3,870 

0.949 

0.000 

0.166 

0.272 

0,171 

0.634 

4.547 

3.865 

74.444 

0000 

0000 

0.074 

1,055 

2.448 

0.641 

2,768 

1.097 

2,014 

0000 

1.482 

0.351 

2.288 

4,102 

0.926 

0,000 

0142 

0236 

0.148 

0.549 

4,654 

3.873 

71152 

Total: 100000 100000 100000 

API Gra\lit~ (from lank sample): NIA Vapor Pressure (from tank sample): NIA 


Ana'~ticar Methods: ASTM Dl945, ASTM D6730 (OHA). & ASTM 0 5307 (Distillation) 

TECHNOLOGY LABORATORY, INC. 

Centre Professional Office Park 

1012 Centre Avenue 

Fort COllins, Colorado 80526 

(970)-490-1414 

Extended Natural Gas Liquid Analysis (OHA) 

E & P Tank 2.0/HYSIS Information 

Petro Hunt, L.L.C. 

259119th Ave SW 

Killdeer, NO 58640 

Sampled: 

Received: 

Analyzed: 

06115111 

06115111 

06/25/11 

Customer Contact: Doug Hanson 

Sample 10: 

Well#: 

lab 10: 

Sampled By: 

Analyzed By: 

liquid from Separator 

Fort Berthold 148-94-17D-08-1H 

A4111-08 

Bill Emery 

Bill Emery 

Field: Dunn Co. ND 

Cylinder: YZ58750 

Sample Temperature of: 

Sample Pressure (psig): 

Sampling Method: AST

30 

M-D3700 

CQMPQN~NT Mole 0/. Weight % LV% 

Carbon Dioxide 

Nitrogen (Air) 

Methane 

Ethane 

Propane 

Isobutane 

n-Butane 

Isopentane 

n-Pentane 

Cyclopentane 

n-Hexane 

Cyclohexane 

Other Hexanes 

Other Heptanes 

Methycyclohexane 

2.2,4- Trimethylpentar 

Benzene 

Toluene 

Ethylbenzene 

Xylenes 

Other Octanes 

Nonanes 

Decanes Plus 

0,000 

0.000 

0,193 

0.990 

2.257 

0,652 

3,110 

1.202 

2.290 

0,000 

1585 

0477 

2.595 

4.013 

1.024 

0.000 

0.189 

0.329 

0,137 

0.768 

4.249 

3290 

70.650 

0,000 

0,000 

0.021 

0.198 

0,742 

0,252 

1.323 

0.578 

1.101 

0.000 

0,910 

0,268 

1,364 

2,668 

0.670 

0000 

0099 

0.202 

0.097 

0456 

3.D76 

2510 

83,445 

0000 

0,000 

0.062 

0.453 

1.151 

0352 

1.766 

0724 

1.365 

0.000 

1.071 

0.267 

1.569 

2.927 

0.676 

0.000 

0.087 

0.181 

0.087 

0.407 

3264 

2603 

80.988 

Total: 100.000 100.000 100.000 

API Gravity (from tank sample): NfA Vapor Pressure (from tank sample): NfA 


Analytical Methods: ASTM 01945, ASTM 06730 (DHA), & ASTM 0 5307 (Distillation) 

TECHNOLOGY LABORATORY, INC. 

Centre Professional Office Park 

1012 Centre Avenue 

Fort Collins, Colorado 80526 

(970)-490.1414 

Extended Natural Gas Liquid Analysis (OHA) 


E & P Tank 2.0/HYSIS Information 


Petro Hunt, l.L.C. 

259119th Ave SW 

Killdeer, NO 58640 

Sampled: 

Received: 

Analyzed: 

06/14111 

06114/11 

06/25/11 

Customer Contact: Doug Hanson 

Sample 10: 

Well II: 

Lab ID: 

Sampled By: 

Analyzed By: 

Liquid from Separator 

Fort Berthold 152-94-22D-15-1H 

A4111-05 

Bill Emery 

Bill Emery 

Field: McKenzie Co. 

Cylinder: YZ 52477 

Sample Temperature OF: 

Sample Pressure (psig): 

Sampling Method: AST

NO 

35 

M-D3700 

CQMPONENT Mole % Weight 06> LV% 

Carbon DiOXide 

Nitrogen (Air) 

Methane 

Ethane 

Propane 

Isobulane 

n·Butane 

Isopentane 

n-Pentane 

Cyclopentane 

n-Hexane 

Cyclohexane 

Other Hexanes 

Other Heptanes 

Methycyclohexane 

2 2 4- Trimethylpenlar 

Benzene 

Toluene 

Ethylbenzene 

Xylenes 

Other Octanes 

Nonanes 

Decanes Plus 

0.000 

0.000 

0.085 

1.320 

3.558 

0.855 

3422 

1 211 

2.276 

0000 

1506 

0.377 

2067 

3.325 

0.872 

0000 

0159 

0356 

0.109 

0.599 

3.760 

3.633 

70 510 

0.000 

0.000 

0.009 

0269 

1.062 

0.148 

1.346 

0591 

1 111 

0.000 

0878 

0215 

1.197 

2.241 

0579 

0000 

0084 

0.222 

0078 

0430 

2884 

3.105 

83.551 

0.000 

0.000 

0.027 

0611 

1.642 

0.208 

1.799 

0738 

1.373 

0.000 

1.031 

0.213 

1360 

2.465 

0.583 

0000 

0074 

0.198 

0.070 

0.383 

3.047 

3.159 

81019 

Total: 100 000 100 000 100.000 

API Gravtty (from lank sample): N/A Vapor Pressuro (from lank sample): N/A 


Analytical Methods: ASTM 01945 ASTM 06730 (DHA). & ASTM D 5307 (Distillation) 

TECHNOLOGY LABORATORY, INC. 

Centre Professional Office Park 

1012 Centre Avenue 

Fort Collins. Colorado 80526 

(970)-490·1414 

Extended Natural Gas Liquid Analysis (OHA) 


E & P Tank 2.0/HYSIS Information 


Petro Hunt, L.L.C. 

259119th Ave SW 

Killdeer, NO 58640 

Customer Contact: Doug Hanson 

Sample 10: 

Well#: 


Lab 10: 


Sampled By: 


Analyzed By: 


Liquid from Separator 

George Tank 151-96-1OC-3-3H 

A4111-07 

Bill Emery 

Bill Emery 

COMPQtt(;!!T 

Carbon Dioxide 

Nitrogen (Air) 

Methane 

Ethane 

Propane 

Isobutane 

n-Butane 

lsopentane 

n·Pentane 

Cyclopentane 

n-Hexane 

Cyclohexane 

Other Hexanes 

Other Heplanes 

Methycyclohexane 

22.4- Trimethylpentar 

Benzene 

Toluene 

Ethylbenzene 

Xylenes 

Other Octanes 

Nonanes 

Decanes Plus 

Total: 

Mole % Weighl"/! 

0.000 0000 

0000 0000 

0294 0032 

1498 0307 

:I 143 0944 

0801 0.317 

3345 1323 

1306 0642 

2445 1201 

0.000 U.OOO 

1756 1030 

0501 0287 

2351 1369 

3847 2608 

1111 0.743 

0.000 0000 

0238 0127 

0.408 0256 

0.118 0085 

0.787 0569 

4249 3278 

3290 2841 

68512 82041 

100.000 100.000 

Sampled: 06/15/11 

Received: 06/15111 

Analyzed: 06/25/11 

Field: McKenzie Co ND 

Cylinder: yZ 52475 

Sample Temperature of: 

Sample Pressure (pslg): 36 

Sampling Method: ASTM-D3700 

LV 0/" 

0.000 

0000 

0095 

0697 

1456 

0439 

1766 

0800 

1482 

0000 

1.207 

0285 

1555 

2871 

0.746 

0000 

o111 

0228 

0076 

0.506 

3453 

2934 

;9293 

100 000 

API Gravity (from tank sample)·, NIA Vapor Pressure (from tank sample) NIA 


Analytical Methods: ASTM D1945 ASTM 06730 (DHAI & ASTM D 5307 (0IsIii1alton) 

PETRO-HUNT, LLC 

Fort Berthold Area Wells 

-

...........,.......... _.~_.__.. ~~_._C.alcu lation of ReJ)r~sen~!!.~~Qll~_~f1~ly~i~ 

. Ft Berthold Ft Berthold ~" """""" ~"-"~~~~"-147-iJ4~·················~-----14j~-94:----

"­ -----------------­ ............................ _----­ ------­

2A-11-1H 3A-10-1H 

.---------~-----~---- .... 

TOTAL 100.000 

Btu/Cubic Foot HHV 1200.0 1200.0 -,·----·--·r-----~·········-----····+--------

~JE:~timated) 

1200.0 1200.0 

.­ - ...-.--­ -----~----~-----~_l 

! 

I 

! 

I 

I 

J 

t 

I 
• 

I 

( 

TECHNOLOGY LABORATORY, INC. 

Centre Professional Office Park 

1012 Centre Avenue 

Fort Collins, Colorado 80526 

(970)·490·1414 

Extended Natural Gas Liquid Analysis (OHA) 

Petro Hunt, L.L.C. 

259119th Ave SW 

Killdeer, NO 68640 

Customer Contact: Doug Hanson 

Sample 10: Gas from Separator 

Well #: Fort Berthold 147 ·94·2A·11·1 H 

Lab 10: A4111-09 

Sampled By: Bill Emery 

Analyzed By: Bill Emery 

COMPONENT 

Helium 

Hydrogen 

Carbon Dioxide 

Nitrogen 

Methane 

Ethane 

Propane 

Isobutane 

n·Butane 

Isopenlane 

n-Pentane 

Cyclopentane 

n·Hexane 

Cyclohexane 

Other Hexanes 

Heptanes 

Methycydohexane 

2.2.4- Trimethylpentane 

Benzene 

Toluene 

Elhylbenzene 

Xylene,; 

C8+ heaVieS 

Subtotal 

Oxygen/Argon 

Total: 

Analytical Methods: 

Sampled: 06115/11 

Received 06115/11 

Analyzed 06125/11 

Field: Dunn Co. NO 

Cylinder: 150 SS 

Sample Temperature of: 

Sample Pressure (psig): 28 

Sampling Method: ASTM·D3700 

Mole % Weight"!. 

0000 0.000 

0.000 0.000 

0.493 0.787 

2.585 2.628 

49.647 28.907 

25.547 27.881 

14.533 23.259 

1.351 2.850 

3.965 8.364 

0.544 1425 

0.729 1.909 

0.000 0000 

0132 0.413 

0.021 0.064 

0.292 0.911 

0.112 0.406 

0.000 0.000 

0.000 0000 

0.014 0.040 

0005 0.017 

0.000 0.000 

0000 0.000 

0030 0.139 

100.000 100.000 

0.000 0.0000 

100.000 100.000 

ASTM 01945 & 06730 (DHA) 
i 

I 

TECHNOLOGY LABORATORY, INC. 

Centre Professional Office Park 

1012 Centre Avenue 

Fort COllins, Colorado 80526 

(970)-490·1414 

Extended Natural Gas Liquid Analysis (OHA) 

Petro Hunt. L.L.C. 

259 119th Ave SW 

Killdeer, NO 58640 

Customer Contact: Doug Hanson 

Sample 10: Gas from Separator 

Well #: Fort Berthold 147-94-3A-1Q..1H 

Lab 10: A4111-10 

Sampled By: Bill Emery 

Analyzed By: Bill Emery 

COMPONENT 

Helium 

Hydrogen 

Carbon Dioxide 

Nitrogen 

Methane 

Ethane 

Propane 

Isobulane 

n·Butane 

Isopentane 

n-Pentane 

Cyclopentane 

n-Hexane 

Cyclohex8ne 

Other Hexanes 

Heptanes 

Methycydohexane 

2,2.4- Trimelhylpentane 

Benzene 

Toluene 

Ethylbenzene 

Xylenes 

C8+ heavies 

Subtotal 

Oxygen/Argon 

Total: 

Analytical Methods. 

Sampled: 06115111 

Received 06115111 

Analyzed 06125/11 

Field: Dunn Co. NO 

Cylinder: 150 S5 

Sample Temperature of: 

Sample Pressure (psig): 40 

Sampling Method: ASTM·03700 

Mole"!. Weight "Iu 

I 

f 

t 

I 

t 

t 

I 

l 

I 

I 

i

•

I 

I 

! 

I 

I 

I 

! 

t 

I 

!. 

0.000 

0000 

0.507 

2.878 

57.409 

23.103 

11185 

0.955 

V26 

0356 

0.475 

0000 

0.087 

0.014 

0.188 

0073 

0000 

0000 

0.009 

0.003 

0000 

0000 

0.030 

100.000 

0000 

100000 

0.000 

0000 

0.884 

3.195 

36507 

27.537 

19.550 

2.200 

6.285 

1018 

1.358 

0.000 

0297 

0047 

0.641 

0.289 

0.000 

0.000 

0.028 

0011 

0000 

0.000 

0152 

100.000 

00000 

100.000 

ASTM 01945 & 06730 (OHA) 

t 

I 
TECHNOLOGY LABORATORY, INC. 

Centre Professional Office Park 

1012 Centre Avenue 

Fort Collins, Colorado 80526 

(970)-490·1414 

Extended Natural Gas Liquid Analysis (OHA) 

Petro Hunt, L.L.C. 

259 119th Ave 5W 

Killdeer, NO 58640 

Customer Contact: Doug Hanson 

Sample 10: Gas from Separator 

Well#: Fort Berthold 148-94-170-08-1 H 

Lab 10: A4111-08 

Sampled By: Bill Emery 

Analyzed By: BlII Emery 

COMPONENT 

Helium 

Hydrogen 

Carbon DIoxIde 

Nitrogen 

Methane 

Ethane 

Propane 

Isobulane 

n-Butane 

tsopenlane 

n-Pentane 

Cyclopentane 

n-Hexane 

CyCiohexane 

Other Hexanes 

Heptanes 

Melhycydohexane 

2.2.4- Tlimethylpentane 

Benzene 

Toluene 

Ethyloenzene 

Xylenes 

C8+heavles 

Subtotal 

Oxygen/Argon 

Total: 

Analytical Methods: 

~ 

0000 

0000 

0673 

2714 

55528 

21.814 

12.248 

1249 

3768 

0564 

0768 

0.000 

0.148 

0025 

0317 

0124 

0000 

0000 

0014 

0006 

0000 

0000 

0.040 

100.000 

0000 

100000 

Sampled: 06/15/11 

Received 06/15/11 

Analyzed 06/25/11 

Field: Dunn Co NO 

Cylinder: 150 5S 

Sample Temperature OF: 

Sample Pressure (psigl: 30 

Sampling Method: ASTM-D3700 

Weight % 

0000 

0.000 


1 121 


2876 


33725 


24832 


20447 


2.746 

8.291 

1541 

2098 


0000 


0.483 


0060 


1032 


0469 


0.000 

0.000 

0.041 


0021 


0000 


0000 


0194 


100000 


0.0000 


100000 


ASTM 01945 8. 06730 (DHA) 

f 

I 

! 

I 

I 
TECHNOLOGY LABORATORY, INC. 

Centre Professional Office Park 

1012 Centre Avenue 

Fort Collins, Colorado 80526 

(970)-490·1414 

Extended Natural Gas Liquid Analysis (OHA) 

Petro Hunt, LL.C. 

259119th Ave SW 

Killdeer, NO 58640 

Customer Contact: Doug Hanson 

Sample 10: 

Well#: 


Lab 10: 


Sampled 8y: 


Analyzed 8y; 


Gas from Separator 

Fort Berthold 152-94-22D-15-1 H 

A4111-05 

Bill Emery 

Bill Emery 

COMPONENT 

Helium 

Hydrogen 

Carbon Dioxide 

Nitrogen 

Methane 

Ethane 

Propane 

Isobutane 

n-Butane 

Isopenlane 

n-Pentane 

Cyclopentane 

n-Hexane 

Cyclohexane 

Other Hexanes 

Heptanes 

Methycyclohexane 

2.2.4- Trimethylpentane 

Benzene 

Toluene 

Ethylbenzene 

Xylenes 

C8+ heavies 

Subtotal 

Oxygen/Argon 

Total: 

Analytical Methods: 

Sampled: 06/14/11 

Received 06/14/11 

Analyzed 06125/11 

Field: McKenzie Co. ND 

Cylinder: 150 S5 

Sample Temperature OF: 

Sample Pressure (psigl: 35 

Sampling Method: ASTM-037DD 

Mole"!. Wejaht% 

0.000 0.000 

0.000 0.000 

0.631 1.119 

2006 2.264 

58.849 38.042 

23.122 28015 

11.042 19.620 

0.943 2209 

2.435 5703 

0.300 0872 

0.393 1143 

0000 0.000 

0.068 0236 

0.010 0.034 

0.133 0.461 

0.049 0197 

0.000 0000 

0.000 0.000 

0.006 0.019 

0000 0.000 

0000 0000 

0000 0000 

0.013 0.067 

100.000 100000 

0.000 0.0000 

100.000 100.000 

ASTM D1945 & 06730 (DHA) 
TECHNOLOGY LABORATORY, INC. 

Centre Professional Office Park 

1012 Centre Avenue 

Fort Collins, Colorado 80526 

(970)-490-1414 

Extended Natural Gas liquid Analysis (DHA) 

Petro Hunt, L.L.C. 

259119th Ave SW 

Killdeer, NO 58&40 

Customer Contact: Doug Hanson 

Sample ID: Gas from Separator 

Well #: George Tank lS1-96-10C-3-3H 

Lab 10: A4111-07 

Sampled By: Bill Emery 

Analyzed By: Bill Emery 

COMPONENT 

HelllJm 

Hydrogen 

Carbon Dioxide 

Nitrogen 

Methane 

Ethane 

Propane 

Isobutane 

n-Butane 

Isopentane 

n·Pentane 

CyCiopentane 

n-Hexane 

Cyclohexane 

Other Hexanes 

Heptanes 

Melhycyclohexane 

2.2.4- Trimelhylpentane 

Benzene 

Toluene 

Ethylbenzene 

Xylenes 

C8+ heavies 

Subtotal 

Oxygen/Argon 

Total: 

Analytical Methods: 

Sampled: 06/15/11 

Received 06115111 

Analyzed 06/25/11 

Field: McKenzie Co. NO 

Cylinder: 150 SS 

Sample Temperature OF: 

Sample Pressure (psig): 36 

Sampling Method: ASTM-D3700 

Mole % Weight % 

0000 

0000 

0.673 

1.849 

61.134 

20.992 

10.083 

1.022 

2.764 

0.416 

0.565 

0.000 

0117 

0020 

0.217 

0.086 

0.000 

0.000 

0012 

0.006 

0.000 

0000 

0.044 

100000 

0.000 

100.000 

0.000 

0.000 

1197 

2 093 

39.627 

25.504 

f7.965 

2.400 

6.491 

1.213 

1.647 

0.000 

0.407 

O.OM 

0754 

0.347 

0000 

0.000 

0038 

0.022 

0.000 

0.000 

0.228 

100000 

0.0000 

100000 

ASTM 01945 & 06730 (DHA) 
PROCESS BURNER EMISSIONS 

__ ___ 

Petro-Hunt, LLC 

Ft Berthold #148-94-33D-28-4H. 5H Production Facility ~~"--.-.-..-~.-~--.--.---..~--.--.---... 

Attachment to Air Quality£,e~rni~.A.ppJi~_a_tion 

-_. --­ -_.--- ._-q..._-­ ..._­

Calculation of Process Burner Emissions 

Burner Size MMBtu/hr 

RunTime-% Shi/Fi3-:"-CHV-" --~ 

Emission Factor Ib/mmcf .. _---_.-----

NOx 

'~cb~-

voe 

- .._---.._-

HAPs 

e£ll£ul£l!i9~E°fll'l~~~Jt\jQ~_~X!mp~eL_ ~____. 

emisSions -TPY 

NOx 

00 

VQC 

HAPs 

.'---­ .._­"- ,--­ ,--. ,---­

Note:-V()CWeight%-FraCiIonand fuel gas LHV from representative analYSisand-calCulation spreadshee~ -EmissiOnFaClOrsfTomAP42:-with-iiaturalgasaf1020~Bfi.i7Ftr-r~ ..-~--

Heater-Treater #2 

-.~--.---.----~--.----~~.-- _._- ---~.-:--~-.~----- ._-- -- -----~~-.-~-

i ._--- -t--- -_.._- -_ .._­

t~ 

: Heater-Treater #1 -I- ­

I 

0.50 

50.00% 

1,084.8 

100.0 100.0 

84.0 84.0 

5.5 5.5 --. ---. 

1.89 ----.­ "---­ ---­ ---­ 1.89 -----. ; -----------t-. --.. --_. --._--­ -----­ _ ... 

. _~_~_~ _____ ________~_ . ___ ._~_~~ 

NOx Emissi0r:!~=_(Q~5~M~!!JII!r)-,*~1 09 Ib/MM~!)*{!g85 Btu/1 0~~LBttlj*(1_!)(;f/1 020 BtLlr~()RHrslYr)~(t(mI200QJ~) _=_I'=-"'­

_--1 

TOTAL BURNERS 

0.1142 0.1142 0.2283 

0.0959 0.0959 0.1918 

0.0063 0.0063 0.0126 

0.0022 0.0022 0.0043 

I "'--­ .,'--- -~."---

i-­

I 

- _0..__ 

-..----~ -_._--_.__ .. -._- -.~-

Me!1.ee COllsultin9~~_ .. __. 

Casper, Wyomin 
TEMPORARY TREATER GAS FLARE 

EMISSIONS 
___ 

___ 

S~p~mber 28,1011 

Petro-Hunt, LLC 

Ft Berthold #148-94-33D-28-4H, 5H Production Facility ----- ___________________ ~ ____ ~ __ .~ ____ ~M___________ --------,---------- ------------------------- -------- :--------- --------, .-----------i---------------'-------- ---T-----------------­

Attachment to Air Quality Permit Application --_________________________, ___,._ •• _, __ <___• __ M ____M __ -----1---­ _M___ M ____ M __._+-___M_

-~.-.-.-... -. - ... - .. _-'---... ---... - .. -- --~ ,-- .-.. -~. --- ~ -~ -- ---. --.. ,---. 

Calculation of Te~p~r.aryJ·reater Gas Flare Emissions 

-- -------------------------- ------ -----,- -----... ----------- -------- ------ ---------,-------------- -- . -------­

Assu'!l~s..P!t.f1.<i.r.t)J(:~,..!reatt),..9.<isi~gp~r.<i!ed}or CI~Q_day pel"i()~ until ~.9~!>Jl~therin9.P.i(Jelirle 

connection is constructed. The pit flare will be equipped with an automatic re-igniter and 

maintained suCt,iEcilt an a_~a.ge-of aTIeasf900k destruCtIVe effidency-isattaine(f~-·~~ 

Flare volume: -~--- --~-- ,------- ----~--.-----~- ---~---------- -------, ---------------._­

____ . -17'~ 995«~8 

431.9~:MCFD-- ---.­ __ f1f"!>L~d~y!>~!>timated avera~e"pr~lJct-,io_n. __ M -, TSCF/h-r

Lower Heating Value--- ~-- 1~084.8---'BtuiF{3~~ 

~~J\i~tag~~Moi~culai~~ighC-----25.j3 ifbTlb-mole 

__VO'<:;_V'V~i.9.~1f..J".~~i()n_____ _ _ __ ____ _ __ 

_ H!-Ps_Weight F!actig!!..._ 0.42% __ _________ ;____ 

_ _Ng~E_mi.!>S~n F.<ictor..Q.0E!~_ _ .1!>Jf\I1M!3!u i 

CO Emission Factor 0.370 Ib/MMBtu -- ~----------------~-----. ---------- -------- -- ~ 

Destruction Efficiency i 90.00% -----.------------------------.~---"-,-.---,~.-,+ ... ~,---,---,--.. -,~.,.-,.-

__ H()_urs ()f OperatiC>.I!J~O day& .. _._ . __ ._.. ___ .____-.1. 1§Q.__Hour:.~ 

Note that there are no H2S or S02 emissions since the burned gas does not contain these compounds. 


EMISSIONS: -_._-_.__._-,,-..__. - ..~.--

voe: --(17995.8-SCFihr)*(1/379-scfllb-mole)*(25.73IbJib-,:mOle);;(34.34°/~)*(100%-90%) =:~·41.9539-ntislhr 

_=-14f~5~91!>~hr)*(~}§Jrh-'"~:T1T()ni26061~~L ._~~~~~~-~_~---=~~-~______-~ ______-~ 46.3103 TPY 

__ '::I~j:I=- ________~__ ___~_______ .L._~~~~~____~'-~ _____ __~, __ ~~ __ 

(17995.8 SCF/hr)*(1/379 scfllb-mole)*(25.73 Ib/lb-mole)*(0.42%)*(100%-90%) = O.51311bsiEr 

--(o.5131TbSlhr)*(2160Ers)*(1icln/2000Ibs) , -- ~ -~~ ----~-- 0.6542 TPY NO£--------- -------~--- --- ~------r--- ------ i 

------(17995-.8StF'ihr)*(1084.8BtI.lIFt3)*-(fMMBtu/{o66;60oB1u)*(0. 06S-lb/MMBtu) -;-~ -1:3275 Ibsihr 

-_==j1.3~75[bsihr)*(216(fhrs);;(1tolli2oQo.!~_~)-=~I"":__-~_~=~~____ ____ -~ 1.4337 TPY 

CO:~___,__._. __... __ . __ .__._._._.. _. ___.... __:. _______.... _ ..._____ ._.~... _._.. _._ 

(17995.8 SCF/hr)*(1084.8 Btu/Ft3)*(1 MMBtu/1,000,000 Btu)*(0.370 Ib/MMBtu) = ~j~2231- !Tbs/hr 

-=rf2231TbS7hr)*(43-80h~:!J t~1!/2600IbS) .-r~=~__ _= ____ _ ~ 7.8009 TPY 

._+ 
 ------ - ---- --! 

<___ <_. <__ ,, ___ <______ ~< ______M __ ~_< __ ~~M ___ <_____ ~M' ___ "M ______ "M __<_______ <__ 

i ________,,__ ~ _____________ ~ ~ ~ ~ ______ ___ . __ __ , ___ __ .__________..__ __________ ___L __. 

Note: Calculation methodology from ND Oil & Gas production facilities permitting guidance 

=VQ~'a.I1(jB~~_weigE.tfraCtiOn from ~Iculati~n spreadsheet-----­

__ ~nnuaJjJr()'!uction averag~ fr().r'l calculation sJlreadsheet 

--<----~<--'-- -<,---- -<--­

~ii~{j~c;()fl$'!/fi!!g ~ !Casper, Wyoming 
TANK EMISSIONS 

Petro-Hunt, LLC 

Ft Berthold #148-94-33D-28-4H. 5H Production Facility -~-~" .---.~----~~~----~--------------.. ----.--------------.-~~--- ----------,-- --- -----.---~!--~---- .. ~-- --.­

__ . __.L,_ 

Attachment to Air Qual~ty Permit~p~ication 

Calculation of Tank Flashing Emissions (Controlled) --'--' ---1--- ----- ---­

j 

Tank emissions include flashing, working, standing and breathing volumes, E&P Tanks V2 

-.is-used asThe basis fOr this ftashIng-emission-calculation. EPA TSI1ks4.Oisused to 

Calcuiatewol1<ing, standing-al1(rbreathing-emissions. Twoenclosed:-smoketes-s flares 

... (~l!!b~sJt:l~-=wWi be II1Staljedal1dwillhave atieasfa-98o/;destruct,ve ~ffi:a~~~y~_---

Flare volume: --.. _,---._- --... .-----._-,---- ---- ----­

_~s!irllat~d al1.l1ual.<~vera.~produ.~()rl_... 447.8 

E&P Tanks GOR r-26~28--~

_-.~Qaily::yol~'!1e!oCo_l1ibus·~to-r- ..._..-_--.- ____ ._.. __ ,7~~2 ---:SCF 

__HourlyVollJlllE:! to COI!!l:lustor __________ .-- ~0.3 - SCF/hr 

E&P Tanks Flash Gas Data: 

__ L()~erJ;...e_ati~£L\t'alue __ ?~Q44& .. Average Molecular Weight 39.35 Ib/lb-mole 

- "-~<2.~ei!jEtFra.ciiol1=~~_________ _______ 67.33% 

_J;~P!)~~i[~t f!.a.ction .. L --O~7~r;~::::~-'::::~-~::::~-:::::::: 

'-NOXEmissiOn-Fiictor--....-... ....- ......',..-. .-O.06lf---·lblMMBtu 


'co Emission"'Factor- ---- -- ,----- ,--- 0.370 i"U,/M-MBtu­ --.,--"--..~,--..--,-.,-----..-,--..-.- --.. _-,- --.,,-­

Destruction Efficiency 98.00% 

-'8~~~_~[Q~]~~~B~'---- .. --82~6~~_ ,_~_8~~!~ 

Note that there are no H2S or S02 emissions since the burned gas does not contain these compounds. 

_. 

EMISSIONS: 

VOC: -- --~- .. --------_._-_.- ------ ----- ---_.- -----. '--- - ----,. ---_.-­

(490.3 SCF/hr)*(1/379 scf/lb-mole)*(39.35 Ib/lb-mole)*(67.33%)*(100%-98%) 0.6856 iIbs/hr 

_ .. (0 6856lbslhf)*(8760hrs)*n-tor1l2000'lbs)'- r---- -- 3.0027 TPY -HAP: .. -.- ..---_.-.- --.- r 

I - ..~- ---.._--- -..~-- .._---­ -···-(49<f3sCF/hr)*(1/379·sCffi&:moie)*(39.35Ib/lb-mOle)*(O.790

A;Y(1oo%:9S%Y; 0.0080 ,Ibs/hr

--(0.00801bslhr)"(im30hrS)*[itorl12-60Cfibs)- .j- -..-....--- ---..... NOx:----- 0.0352 TPY . -. ;-- . 

-- - (490~SCF/hr)·(2044.8 Btu/Ft3)*(TMMBtLl/l,OOO.OOO-Btu)*(b.OO8IbIMMBtu) = 0.06821bslhr 

---[O.OO82Ibslhr)*(8766 hrs)*(fton!2000Ibs)--'- .--..--- ---­ 0.2988 TPV 

_c;Q:--=__-~=--=~~_-:'::::____ .... 1___________ _ (490.3 SCF/hr)*(2044.8 Btu/Ft3)*(1 MMBtu/1,000,000 Btu)*(0,370 Ib/MMBtu) = 0.371 Cf"""lbsil1r 

.... _(Q.3IiOTt)i7l1r)*1?7t3<ihr_st(1ton72Q90Tb~)--- - -- --- ---­ 1.8249 TPY 

Note:-Cal(;ulatiol1-melh.~I09Y frorTi:BD~OiT&=GaS-p!od~O~=~ilili.es_perf"l1ltlin~iuidanCe vae and HAPs weight fraction from calculation spreadsheet 

Annualpr()(jucti~~v~ge-fT.im~culatioo~p!..eadsheet 
______ 

_ 

• 

Petro-Hunt, LLC 


Attachment to Air Quality_PermitJ\Pp~i~CiJ~on 

Calculation of Tank Flashi_l1i1 Emission~JUncontrolledL 

____________~ _____________________________________L _______________ 

Tank emissions include flashing, working, standing and breathing volumes, E&P Tanks V2 

- isusedas-thebaSiifor this-flasllingemisslon calculation.EPA Tanks 4.0lSused 

-calCUlate woiki6:g, ~t~dil1!Lan{~ec::ltl1lng::e~i~s~ns'-_--- -r-­

Flare volume: -~.. ­ -_..­ .---~~-.- -­ --~~- .. ~---

_-'::sti'!1<lted__~_nnlJ~lav~.r:135;1~E~Cl(j_lJt:ti.2l1_ 

E&P Tanks GOR 

E&P Tanks Flash Gas Data: 

Lowe'"--t-I~a~l1gyaJu.e__ 

__ ~\le.r:<l9~ ~.QI~(;IJ!<lrW~9hL_ 

YO_G_W.ei9l!t fr~t:tiQrl_.___~_. __ ~_,_ 

HAPs Weight Fraction 

-~--~-------------~- "~-------.---

NOx Emission Factor ._._- ---..----..-~-..­

CO Emission Factor 

-_··-t-­ _+ ___ 6,7.33% 

0.79% 

----- ---6.-ooa -----------IIblMM-Stu 

--0.370 ---·lblMMBtu 

--" _._-­ ~-~ ------~~--

, 

---- -------­ .-_.._--- -_._---­ ------­ ----­ ~-

__~~~ut:tion §.ftide.l19' 0.00% 

Hours ofQperation __~,7_t3Q. : Hours 

Note that there are no H2S or S02 emissions since the burned gas does not contain these compounds. 

EMISSIONS: 

VOC: 

.-------..-~----,,----- ------ ------- ----- - --------- - ------ ------- ------ --_._- ----1-­ (490.3 SCF/hr)*(1/379 scf/lb-mole)*(39.35Ibllb-mole)*(67.33%) = 34.2778 llbs/hr 

. --=- (3i, 2!'Z~JbJS/~I}1~76('- hrs)*{1 ton/2000Tbs-)--~-- - ,.-- ----, 150.1366 TPY 

HAP: --" .. ~~ --..~~ 

(490TSCFlhrj*{fi379sdilt>=more)*(39~35Ibjlb-mole)*(0.79%) = 0.4022 iIbs/hr 

_Jb-:-46221i:is/h!)~T876()'tirsi0ton/2000IbS) .....~..-.- -­ 1.7616 TPY 

___.. ~.~ __ ~. _____ .. ___.. ____ .. __ . ___ ~_ ""_____ .~_~_ .__ .___ 1 _.~. 

N0tEl:",cal<:!J~on..m~thod()IogY frorn..NPIVV'fSlil Gas producti<>rtfacilities.eerrni!tiI'~l.lluida.n.ce 

VaG and HAPs weight fraction from calculation spreadsheet 

-AnnualproductIon average fromcalculation-spreadSheet-I - ..~--- -.. ~-- "•.- - ..~---"-..~-- ""--.~-- --"'-1-­

i 
E&P TANK V2.0 Calculation Report--- Developed by DB Robinson & Associates Ltd. 2011.09.28 

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

* Project setup Information * ****************************************************************************************** 

Project File 

Flowsheet Selection 

Calculation Method 

Control Efficiency 

Known Separator Stream 

Entering Air Composition 

Filed Name 

Well Name 

Well ID 

Permit Number 

Date 

C:\Megee Consulting\Petro-Hunt North Dakota\Table A-2 Wells\FTB # 148-94-33D 

Oil Tank with Separator 

RVP Distillation 

98.0% 

Low Pressure Oil 

No 

Fort Berthold Reservation - North Dakota 

14B-94-33D-28-4H, 58 

Separator To Atmospheric 

EPA NSR Application 

2011.09.28 

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

Data Input * * ****************************************************************************************** 

Separator Pressure 

Separator Temperature 

Ambient Pressure 

Ambient Temperature 

C10+ SG 

C10+ MW 

Low Pressure Oil 

No. Component 

1 H2S 

2 02 

3 C02 

4 N2 

5 C1 

6 C2 

7 C3 

8 i-C4 

9 n-C4 

10 i-C5 

11 n-C5 

12 C6 

13 C7 

14 C8 

15 C9 

16 C10+ 

17 Benzene 

18 Toluene 

19 E-Benzene 

20 Xylenes 

21 n-C6 

22 224Trimethylp 

30.00 [psig] 

120.00 [F) 

14 . 70 [psia] 

70.00[F] 

0.8300 

245.00 

mol % 

0.0000 

0.0000 

0.0000 

0.0000 

0.2120 

1.4410 

3.3960 

0.8330 

3.6860 

1.3530 

2.5430 

4.1940 

4.2160 

4.5070 

3.5880 

66.8360 

0.2230 

0.3650 

0.1520 

0.7310 

1. 7270 

0.0000 

Sales Oil ----------------------------------------------------------------------------­ Production Rate 447.B[bbl/day] 

Days of Annual Operation 365 [days/year] 

API Gravity 39.0 

Reid Vapor Pressure 5.282[psia] 

**************************************************************************•••****••••••*.* 

Calculation Results * • *••*****.*••****•••••************•••**********••••  ••** *******************•••********** 

-- Emission Su:mmary 

Item uncontrolled uncontrolled Controlled Controlled 

page 1 
E&P TANK V2.0 Calculation Report--- Developed by DB Robinson & Associates Ltd. 2011.09.28 

[ton/yr} [lb/hr} [ton/yr} [lb/hr} 

Total HAPs 1.800 0.411 0.036 0.008 

Total HC 241.091 55.044 4.822 1.101 

VOCs, C2+ 237.013 54.113 4.740 1.082 

VOCs, C3+ 185.610 42.377 3.712 0.848 

Uncontrolled Recovery Info. 

Vapor 11.7700 [MSCFD] 

HC Vapor 11.7700 [MSCFD] 

GOR 26.28 [SCF/bbl} 

Emission Composition -----------------------------------------------------------------­ No Component Uncontrolled Uncontrolled Controlled Controlled 

[ton/yr] [lb/hr] [ton/yr] [lb/hr} 

1 H2S 0.000 0.000 0.000 0.000 

2 02 0.000 0.000 0.000 0.000 

3 CO2 0.000 0.000 0.000 0.000 

4 N2 0.000 0.000 0.000 0.000 

5 C1 4.078 0.931 0.082 0.019 

6 C2 51.403 11. 736 1.028 0.235 

7 C3 112.313 25.642 2.246 0.513 

8 i-C4 12.368 2.824 0.247 0.056 

9 n-C4 37.320 8.521 0.746 0.170 

10 i-C5 6.149 1.404 0.123 0.028 

11 n-C5 8.564 1.955 0.171 0.039 

12 C6 4.495 1.026 0.090 0.021 

13 C7 1.727 0.394 0.035 0.008 

14 C8 0.663 0.151 0.013 0.003 

15 C9 0.210 0.048 0.004 0.001 

16 C10+ 0.001 0.000 0.000 0.000 

17 Benzene 0.162 0.037 0.003 0.001 

18 Toluene 0.087 0.020 0.002 0.000 

19 E-Benzene 0.014 0.003 0.000 0.000 

20 .Ky1enes 0.057 0.013 0.001 0.000 

21 n-C6 1.480 0.338 0.030 0.007 

22 224Trimethy1p 0.000 0.000 0.000 0.000 

Total 241.091 55.044 4.822 1.101 

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

mol % mol % mol % mol % mol % mol % 

1 H2s 34.80 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 

2 02 32.00 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 

3 CO2 44.01 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 

4 N2 28.01 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 

5 Cl 16.04 0.2120 0.0615 0.0000 12.0025 1. 7509 4.4835 

6 C2 30.07 1.4410 0.9961 0.0160 36.2963 27.9205 30.1531 

7 C3 44.10 3.3960 3.0232 1.3348 32.5946 49.4075 44.9260 

8 i-C4 58.12 0.8330 0.8011 0.6880 3.3334 3.9059 3.7533 

9 n-C4 58.12 3.6860 3.5985 3.3067 10.5288 11.6153 11.3257 

10 i-C5 72.15 1.3530 1.3515 1.3455 1.4661 1.5168 1.5033 

11 n-C5 72.15 2.5430 2.5492 2.5652 2.0500 2.1095 2.0936 

12 C6 86.16 4.1940 4.2356 4.3552 0.9278 0.9497 0.9439 

13 C7 100.20 4.2160 4.2658 4.4095 0.3080 0.3162 0.3140 

14 C8 114.23 4.5070 4.5631 4.7253 0.1030 0.1063 0.1054 

15 C9 128.28 3.5880 3.6333 3.7645 0.0281 0.0309 0.0301 

16 CI0+ 245.00 66.8360 67.6871 70.1509 0.0001 0.0001 0.0001 

17 Benzene 78.11 0.2230 0.2254 0.2322 0.0360 0.0368 0.0366 

18 Toluene 92.13 0.3650 0.3694 0.3823 0.0164 0.0168 0.0167 

19 E-Benzene 106.17 0.1520 0.1539 0.1594 0.0022 0.0023 0.0023 

20 Xylenes 106.17 0.7310 0.7402 0.7668 0.0093 0.0096 0.0095 

21 n-C6 86.18 1. 7270 1.7452 1.7976 0.2976 0.3049 0.3029 

22 224Trimethylp 114.24 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 

MW 191.11 193.05 198.48 39.35 43.68 42.53 


Stream Mo1e Ratio 1.0000 0.9874 0.9527 0.0126 0.0347 0.0473 


Heating Va1ue [BTU/SCF] 2261. 95 2494.50 2432.52 


Gas Gravity [Gas/Air] 1.36 1.51 1.47 


page 2 
E&P TANK V2.0 Calculation Report--- Developed by DB Robinson & Associates Ltd. 2011.09.28 

Bubble Pt. @ 100F [psia] 29.11 20.20 7.36 

RVP @ 100F [psia] 13.06 10.79 5.66 

Spec. Gravity @ 100F 0.726 0.727 0.729 

page 3 
Vertical Fixed Roof Tank 


Williston, North Dakota 


Identification 

User Identification: 


City: 


State: 


Company: 


Type of Tank: 


Description: 


Tank Dimensions 

Shell Height (ft): 


Diameter (ft): 


Liquid Height (ft): 


Avg. Liquid Height (ft): 


Volume (gallons): 


Turnovers: 


Net Throughput (gallyr): 


Is Tank Heated (yin): 


Paint Characteristics 

Shell ColorlShade: 


Shell Condition: 


Roof Color/Shade: 


Roof Condition: 


Roof Characteristics 

Type: 


Height (ft): 


Slope (ftlft) (Cone Roof): 


Breather Vent Settings 

Vacuum Settings (psig): 

Pressure Settings (psig): 

TANKS 4.0 


Emissions Report - Summary Format 


Tank Identification and Physical Characteristics 


FT Berthold #148-94-33D-28-4H, 5H 

Williston 

North Dakota 

Petro-Hunt, llC 

Vertical Fixed Roof Tank 

8-400 BBl Oil Tanks III.!-­

20.00 

12.00 

18.00 

12.00 


15,228.53 


60.05 

858,065.00 ,<).f! If' ~k N 

Gray/Medium 

Good 

Gray/Medium 

Good 

Cone 

0.50 

0.08 

-0.03 

0.75 

Meteorological Data used in Emissions Calculations: Williston, North Dakota (Avg Atmospheric Pressure 13.82 psia) 

9/28/20112:41:32 PM Page 1 
Vertical Fixed Roof Tank 

Williston, North Dakota 

TANKS 4.0 

Emissions Report - Summary Format 

Liquid Contents of Storage Tank 

MiJdure/Component Month 

Daily Liquid Surf. 

Temperatures (deg F) 

AV9· Max. 

Liquid 

Bulk 

Temp 

(dell. F) 

Vapor Pressures (psia) 

AVII Min. Max. 

Vapor 

Mol. 

WeiGht 

Liquid 

Mass 

Freet. 

Vapor 

Mass 

Fraet. 

Mol. 

Weil/ht 

Basis for Vapor Pressure 

Calculations 

Crude oil (RVP 5) All 49.69 39.44 59.95 44.51 2.3409 1.8900 2.8749 50.0000 207.00 Option 4: RVP=5 

9/28/20112:41:32 PM Page 2 
Vertical Fixed Roof Tank 


Williston, North Dakota 


TANKS 4.0 


Emissions Report - Summary Format 


Individual Tank Emission Totals 


Annual Emissions Report 

.... Los.ses(lt:>sl..._~~. .~_......._~ 

19~u~~o~rf~tp· .Yllorkin.9. LO.SS i .. E!~El~thin9Lo.ss .........:. TotaIEmiSS>L~ns...l:tllt 0 -r:;::...bS
 5)··· .1,194.90 I 352.78 L 1,547.68 I r " fA--,... ::. /~ 1'3 (/1."" t <75

;. ~, fer lDN5/~""1' 

GtV .,..~" c... E'rrft:I£;VcY = qg> ~ 

~A.JrlP(}£'t..E~ ~(F$/b.vs': t!>, 10l /.AI.5/~1t4' 

9128/2011 2:41 :33 PM Page 3 
TRUCK LOADING EMISSIONS 

September 2011 

Petro-Hunt, LLC 

~!_~~~~~I~.!!1~~~~~33D-28-4H, 5H Prod uc!i()~_f~~~~~~tx 

AttachrT'l~rlJi~l~,i Q uali!YP~rrl'lit~RPJJg~ti Q!!___ _ 

Calculation of Truck Loading Emissions --~--,--------------------- -~-

Average BOPO Production __ ~_. __ . 447.8 

Annual Volume (Avg BOPO*365 days) ! 163,441 

Saturation Factor (Submerged loading, Normal SerVicer------------~~O.60~~ 

TrueVapo~pressure of Liquid @ 500 -- --­ - 2.3 .---,---------~~---------~-------------. 

Molecular ~.!tlgh[oer~nky~p~rs~([b!I~i1i~r-~-------T---------c----50 

~~l.'.n_d~~QQQJlallo~~IC)~~~~:_______ ____ ___________ 

_ _____L!__::J'12.4~):(~t*(Pl* (Mfl}____ 

I-c-c---=-~~---------~-- -----­

Note: Calculations in accordance with NOIWY Guidance and AP-42 factors 

----~-~--- -----~-----~--------

- -­ -----------­ --­ -------------------------~-----~---
RECYCLE PUMP ENGINE EMISSIONS 

Petro-Hunt, LLC ~~~~.......~~~~~~ ~~~~~~~~--~ 

F~J~~r:!~~!c:I~~148=~~=~~~~~~~I:I~, ~~me~~()~~~n Facil~!xL~_~~_~~~~~~_~~ I ~~--~-~~- ~ -~- ~--~-.~-~ ........................-~--~-~-~---~--~.~- -. - .... -- ~·-----~-·~-·~---t--~---- .............................~~-~-~-~.--~~~~-~~~-

Attachment to Air Quality Permit Application ! ~""""'-'-"-~~~-----~---~"""", .--~~~--- .--.­ - ~--~ ---~~~-~-~~-----~---····r-~~----~-~~-~-

.+ ~--~-~--~~-~--~ ............... ~--I 

_ __________________ ..........l .....___ _____ _____________ 

~!Jculll~i~~()f_~~l!Ii~s_ion~s~~~!!l_~~cy_~_~~~I.JI'l1P Eng!!'1_~~_~~._ , 

--~----~-~-~-... -.... --~~-~---~~----"'---..-..... . 

2 Identical Honda GX-240 8 Horsepc>\I'I~I Gasoline estimated to run 70 hour~per year e~ach_ 

Emission Factors from AP-42 Table 3.3-1 

Pollutant: Emission Factor Unit #1 Unit #2 TOTAL 

____ ~_~___ Ibs/Hp-Hr ~~-~ ........... ;:-:----::-~~-~ 

Ibs/hr T9ntlYUr TgnelYUr Tons/Year 

NOx 0.011 0.0880 0.0031 0.0031 0.0062 ~----------~.............. ~~~ ~--~~----

0.439 0.1229 0.1229 0.2458 

SOx 5.91E-04 0.0047 0.0002 0.0002 0.0004 ~--~---------- ---­

PM-10 7.21E-04 0.1727 0.0002 0.0002 0.0004 

!_QQJ"1"otal of Exhaust, __ _______~~~ 0.006 0.006 0.012 

Evaporative, Crankcase, 

andRefueITi1gf~§tors)-~-T 

~~_~ ___ ....................... _~~_~_ ~'!.~!:I!~~C~nsuitifl!:l~~~ Casper, Wyoming 
FUGITIVE EMISSIONS 

I 

! 

( 

I

! 

t 

i 

I 

I 

I 

~ 

I 

I 
---

Connector _.... ---_.. 

Flange 

=_~Qp~ri Uri~==-_~ Other 

__~u_rr1P 

Valve 

Connector . -----_... _­

_... fl~I'1!!~~ __ Qeen hine~_ 

Other 

PU_rT1J.)___~_ 

Valve 

Connector .._--.. -...._------­

. __ Flang~_ 

------c~~nC~()~0~~6 

10 

u=JH~ 

, 

__ _____,_------0.4000 

0.69Q()--=~_=- 2.7609. 

0.1300 6.5000 

THC 

Lbs/Day! 

0.3300--0.292--~----0.00155 --------~-~-----

O.O~?~~_J ... 

_.. 9p~l1j..il1~ .. __________________.___ ' _______ -,-----_______ _ Other 

0.0000 

4.0000--t 

f'.uf11P.. __ __ _ Valve 

0.0000 I --.. c--------c----- '--­ - ----t----------­

2.6009.___1

_ 

! 

Petro-Hunt, LLC : ...._____ . __ l 

f~~_~~_~~_!' 148-94-33D-28-4H, 5H Production Facility --~ ------- -------... ----------- ---~- ------------)--- -----.- ---T --------~.-----------.--~ 

Attachment to Air Quality Permit Application -_ .. --- -_... --- - ...---- - .- -- '" -----. ·------T--- ------ . 

Calculation of Fugitive Emissions .. -,.~---- ...---~------- ..~--- ---i"'~-- . i 

T~rC~EmissiOn-Factor: IbSlcomponentlday:---- . • -.---..- --------.. - -T ----... ---­

i ! i Waterl _ 

-Eq---~-iO~~~:o~.Ye~--~--J-~~~~cf- <_-T~~;1t~~if~+ L~~;~5~iI~J=-- ---1 Speciilted El11i!tSio~~~ton;~Aps Total 

__~E!~I!~____ ___________ _ ____ c_______ 0_.021 0 -1---0. oosir- r 0.0002 __ ._____________ _____lhig~!.g!.ll.de ___~~-0.29I~==o:QO15~= _<:>pe_rl Line 0.1100 0.0740 0.0130 iGas Production 0.035 0.00074 

Other 0.4700 0.400(f---- -- (fi400 -.._---_... ­

~u...!11P__ 0.1300 : 0.6900 i 0.0013 


Valve ---i---~---Oc.24()()-------o._f3()O~- 1--O-:-0052---~-IGas Service: ! Component: THC HAPs 

VOCTPY HAPsTPY _L~;~~y F;b~~rci.~~~r4~ 0.0021 0.00004 

0.02Tol 0.2100-tfo3S- ·--O~00074-- 0.0013 0.00003 

0.1foA==T q·99.QQ--[ _~rQ~~~--==AQq074-- 0.0000 0.00000 

0.4700 I 1.8800 I 0.035 . 0.00074 0.0120 0.00025 0.130cf--i--- 0.000-0---+-···· o.6~f5-----+····· 0.-00'074­ 0.0000 0.00000 

T-------~~--

0.2400-r~-4.8606- -t-~-6.035 0.00074 0.0307 0.00065 

THC VOC HAPs 

I Lbs/Day l_£a.!=to.. .L~-F~r VOCTPY HAPsTPY 

0.0110 i 0.6600 i_9.:.~~~_.1 ___.Q~Q01_55 0.0352 0.00019 

a.q()ss--=: q~~9_~8-=_J O:?_~~_~ 0:QQ1§§_ .. 0.0111 0.00006 

0·QZ~_0__4 O:og.9.9~_J 0.2_~2____t 0:90~1§_§__ 0.0000 0.00000 

I 4.00Q.Q__ J__ 0.29?_ . _~__ 0.00_1___5__5~__ ___ _ 0.2132 0.00113 

__~__ 0.292 0.001??_____ 0.1471 0.00078 

0.292 0.00155 0.3464 0.00184 

VOC HAPs 

Factor! Factor VOCTPY HAPsTPY 

0.0176 0.00009 -,------_.. -----­ ----~ 

O·~~~ __L~ O.O_Q~§§ ____ 0.0049 0.00003 

0.292 0.00155 0.0000 0.00000 ()~:f92------·(f()6155- 0.2132 0.00113 .. ------_.._---- ----_..._-------­

0.292 0.00155 0.0000 0.00000 

0.292 0.001 __5__ .5_~___ 0.1386 0.00074

TOTAL FUGITIVE EMISSIONS TPY 1.1733 0.0070 

I - ______~___ I 

NOTE: iCl_ctors and calculationlTlE!!I1..().<:J()~().9Y in accordance with the NDIWY 

Pro..<:JlJ.<::!ion Facilities Permittin99uid~I'1~E:!:C0rTlponenL~ounts~r~~C! rep'r~sentative estimate MegeeCon~E.'!!.,!JI 

based u on an onsite review and ical Petro-Hunt wellsite e ui ment Casper, Wyoming 

I 

I 

f 

l 

I 
MISCELLANEOUS INFORMATION 

I

i 

._---_...[

I ---...---­

44.097 521.138 \----.--.-.- ··-i--..-· .. -----­ +-----64.168---" 58.123 ------~ ----. 

58.123 182.041 --.,...-_.__ . 

72.150 31.457 _ .._ ..... ·-4--····_· 

72.150 42.280 ._-_...._----- ...-...-~-..- .., 86.177 42.485 ----_.. 

-.-----.---.---'----.---..------.....-.-~-----. ---.---;--- ...-.---..-. ,.--.----.....---1 

883.570 

-------- ..-.-------~.-----_-...-- -.---.-- .. 

1,689.1-'!.I 

. L_. ___ . , I IC3+ Fractioni34.34% ...--------.-..-.--,------- ...-..-~--....----- .. - .1----..... _..__--,____ . __..______. __ .._._..L _______ ....--..-..--..... -.----.. -1 

Petro-Hunt, LLC 

Ft Berthold #148-94-33D-28-4H, 5H Production Facility!

-_...- -~==-=~~~==--=::y- .-~~~ ---===-==-~~]-==-. 

Attachment to Air Ql,jalityPermit Appli~~tion 

Calculation of HAPs &C3 + VOC Weight Percent of Treater Gas 

Comegmmt 

Propa_ne _____ . 

Iso Butane --------- -------+--- ----.--

Normal Butane 

Iso Pentane ._._.....---_._-------_....--_.. 

Normal Pentane -_...__ . 

Hexanes + 

I---c=--...--.-----.--..---- - ... ----. 

Total C3+ Fraction 

Carbon Dioxide 

Nit~~9.~I1 __.. ___ ._._ 

Methane 

., ~---~~-~--

Ethane --------..··------r---·-·---------"----·-·-c... -.. -----+..-.--.--

Total Other Fraction 

-totaTAI-1CO\!1pon~llts .---- ··---T--99.999---[ 

___..__._.___.......___._ .....____ 

J---.....- ..---.---..-.-.---......-

HAPs FRACTION 0.42% 

M~I o/~Jiom ci3lclj!ated a~ea~~res~I1!~tiye 9~!>.i!_r1al}'si;. ____ 

Component Molecular Weight from GPA Standard 2145-83; - ..- ------....-,-------......--.- ----~~-~····-----··------····-T------ --------... ~--
.......---­

Petro-Hunt, LLC 

Ft Berthold #148-94-33D-28-4H. 5H Production Facility! ---·~"···--·~·--·----~----T----·--------"~---·- ----..T~·-~-----·-····-!---··---·-~ --~--------------"---"---"-,­

Attachment to Air Quality Permit Application ~ ~~~---~ I--···~~~ ~--..... ~~~~~~~~~

Calculation of HAPs &C .3 + VOC Weight Percent of Flash Gas 

Weighted 

Component FractiOn~~~

~r()£C3~rl~_~~_ 

Iso Butane 

Normal Butane 

Iso Pentane 

Normal Pentane 

Hexanes + 

Total C3+ Fraction 

Carbon --_..__Dioxide ._-_...__._-_.._-_._----­

~i!rogerl~_~~~~_~~ 

Methane 

~-.... -~~ ~~~~~ ... ~~~~

Ethane 

32.595 i 44.097 . . ~3.333-'~ 58.123 

10:5?~_~_1 ·~~~58.12-3 

1.46~_~ 72. 50 

2.050' 72.150 

1,437.324 

.....----"'---.---~ - ...------ -_...-----

L_1.729 86.177 

193.747 --...~---- ... 

148.957 

611.965 

105.779 

147.908 

Total Other Fraction 

Total All C0'!lpof1~f1ts 

HAPs ~-..---------..--­-

Benzene 0.036 78.1 --'._--_._--­ ._.----------­

~!~~~3.98~~r~ ~ 

I 3,929.666 -;-_.._-------­ -_ ...-----­ , 

Toluene 0.0164 92.1 1.510 .~~-....~~~~~ ... ~~~~-~~ .. -~~~.~~ ~~~ .. ~-~~~ 

Et~)llbenzene -f- O:QO?_~~~ 1 06.2 ~ Q,-?~~ 

~!~:~:~e ~~-~~~~~ ~~~~~ ~~~~~~..~~~~~~ 18~~J-~~+-~2Q5~583 -~--~-T~ 

~"2.4--T-ii~ethylpenta_n~~e·~.~~~-~+··~~~~ ~~o.OOO~--- NA 

TOTAL HAPs~I~~Oj615 --~~ ....~~~~~ ~ ------...------~ 31.19646 ~~~~~~-.. ~ 

HAPs FRACTION 0.79% ~~~.. -i:-~~~~~~ .. ~~~~-.. ~ ~~~-...~~~ 

Mol % from E&P Tanks V2.0 Flash Gas stream data Com2oneni M91~cular~Wei~6t]~~n, GPA~Stan~dard2145-83; 

--.. -~~~~ ~~ ..~~-~~~. 
EQUIPMENT INFORMATION 


MANUFACTURER DATA SHEETS 

Our VOCinerator eliminates nearly 

99.9% of BTEX and voc emissions. 

INNOVATIVE SOLUTION 

With worldwide attention focused on global warming, the greenhouse 

effect and overall air Quality, the oil and gas industry is facing mounting 

pressure to reduce- and eventually eliminate- harmful emissions from 

being released into the atmosphere. 

MESSCO has responded by creating an emissions eliminator with superior 

emissions control: The VOctnerator'''. Our patented product eliminates 

BTEX and VOC emissions at 99.9% efficiency, exceeding EPA standards. 

Not only does the gas burner syste{Tl destroy VOC and BTEX emissions. 

but the patented vortex design, allows cooling to occur, thus lowering 

any pollutants created by high temperatures, such as NOx. 

The VOCinerator'" is smokeless, with fully automated controls. The 

automation, in combination with the engineered, patented design, allow 

the VOCinerator'" to keep functioning efficiently and effectively even 

when liquids are lntroduced. Because the VOCinerator"", along with the 

automatioi\ ~,s 1esigned and proven to be user-friendly. if challenges or 

problems do arise with the system, the situation is Quickly and easily 

resolved, minimizing down-time. The VOCinerator's"" efficiency, reliability 

and durability means a lower overall lifetime cost than other available 

emissions elimination products. 

Our products and solutions, including the VOCineratorlM are field-tested 

in a live environment. so clients can be sure of real-world functionalitynot just results based on engineered calculations. Actual field tests have 

conSistently produced results of 99.9% emissions destruction, shattering 

other emission control device results. 

~ 

MESSeD 
Recently completed location 

showcasing MEsseo Dehy Units and 

VOCinerators. 

Our products minimize environmental 

impact while maximizing client 

production. 

~ 

MESSeO 

2220 Upland Street 

Rock Springs. Wy(>rnlng 82901 

3073872926 

www.messcO.com 

HOW IT WORKS 

Our water and hydrocarbon condenser system utilizes dehydrated gas 

as the cooling agent and expels condensed liquids to the on-location 

production tank. 

Regenerator emissions leave the condenser and move from the upper 

vaporization chamber. into the lower chamber. then into the waste gas 

bumer system where emissions are ignited and create enough heat to 

maintain vaporization within the enclosed chamber. 

The VOCineratorT>' creates a vortex in the burn chamber that forces 

pollutants to circulate until they are completely consumed. This vortex 

maintains the ideal temperature for proper emissions destruction while 

protecting the integrity of the eQuipment. MESSCO has gone to great 

measures assuring the safety of the unit and its functions, virtually 

eliminating the risk of the unit burning down. 

EXPERT SERVICES 

MESSCO provides a wide array of services designed to assist our clients 

with all aspects of installation, maintenance. or refurbishment of their 

equipment. Our service programs are designed to assure efficient 

operation and extended life of our clients' equipment. 

INSTALLATION 

't. . 

MESSeO'S' fteel ~f state-of-the-art vehicles includes all modern 

equipment necessary to install our products efficiently, safely. and 

correctly at any location our client requests. As part of the installation 

process, our experienced technicians are on-site for the start-up of the 

equipment to assure the best possible project completion. 

MAINTENANCE 

Although all MESSCO products are built to the highest standards, we 

know that to ensure optimum performance, achieve maximum product 

life. and incur lowest long-term product cost, it is critical to have the 

equipment properly inspected and regularly maintained. That is why 

MESSeO offers a manufacturer's maintenance program. 
~ MP051211·02 Quote REV 1 

MESSeD As Per Your Request 

Customer: Petro Hunt LLC Job Name; VOGlneratcr Quote Page: 

Account No.: N/A Location; NO!1h Dakota Data: 612112011 

Ph_No.: 701-863-6622 F.O.B.: Rock Springs Salesperson: MP 

Requested by: Doug Han&On Acct. Rep'.. Mike Pavicic Data Requlntd' ASAP 

Item Description Cost Per 

NEW 42" VOClnerator Enclosed Flare (Combustor) 

1 

42" Combustor· Skid Mounted raIed for 100 MPH Winds requiring 00 guy wires with Bird Cone h;luded: capacity 42 MSCFO MaK 

Instantaneous lIare gas 1'l'IIe@ 2200 BTU I SCF. Includes InIemaI Pre CcndiDonIng steam Chamber. Uquld Knock Out. Refr.rtCby InsWled 

Stack and Palented +98% VOC OestrucIIon .,temal deslgn./oJStJ Includes lnsulQ5d WlI$Ie Gas Inlet V:We and Flame Ivrestsr and Fuel Gas 

SysIIlIII. 

.' , { 

.::. ' 

PRELIMINARY OPTIONS 

2B ACL 5100 Combustion Safety Controller wilh Low Walt SoIt!nc:JId$. Rsgulalcn. liquid level SIOiIch & 24" Premium Plot System Installed, 

Offers AuIomated lighting, RemoIe Shut Down and Start Up. ESO and dry contacts for system status. ?, . .. J ' 

3 J<irnraoI4· Kin'Ir.iIy Fill Close ( pressure to open) SDV. 150 Flanged for Pneumati:: Automated Wasle Gas line Opening to be used IOitl'l Opljon 

2 above. .., 

4 KimIJY 3" Fail Open (Pressure-to-Close) ESV. 150 # RF flange valve for Aa.rtoolatsd Waste Gas Open and Close 

5 4· Enatdo Series 7 Model7080410-C4R12 Flame ArreslOrwith Oc'ain PQ1s. OIfers Flame Protedion witll mlnlmum Back Pressure and liquid 

drain for P<*Ir'tUai build up and freeze oW in ......et gas applicalion$. .; ~ 

7 Naowta CoalescIng Filter for Fuel Gas system drying and liquid removal to prevent freeze up of Fuel Gas system. 

8 

Sdar~pack.ageincludingtwo 15 WatlSdar Panels and Brackelllwith two 100Ah gel cell batIer1es. ooe24Yo1tSlU1 saversolar~. 

one large baII.ery box with mounting hardware. one 2" l( 10' cmduft additional conduit and wi", with portable solar stand. (4 days Autonany to 

item 2 above If local ptM'$f II not available) 

Estimated Shipping Charges 2 FLares per b'ud<lol'ld 

An prices are FOB Petro Hunt Ship Poit\t ­ Shipping Pre Pay and Add without Mark-up - Tax to be added to IIMlice 

Dellw.ry wi! be 4 • 5 per week starting 6 - 8 weeks ARO 

Entire System Offered I>bt:Ne is Pre Assembled. Tested and shipped in :2 , 

Due to instabiily In the steel mBll'lret Messco wil confirm pricing atlme d order 

Prices quoted are based on a quantity d 50 or more. Sizes can be mixIild to reach tdal quantily d 50. 

.­ Quote I&a t!9! ITlCIudf1: InsJallatlon 

. . ThIS Quote WIll Be Good For 30 Days 
HESS 6'x:ZO' COLD WEATHER VERTICAL HEATER TREATER 

DESIGN SPECIFICATIONS 

DC!5i1GN CODe: A!:iMC SeCT/CJN VIH 01'11"[$;;10 ..... r 

uU H SrAMI-1t:r> & NAt/O!""uu BOAi.I[) Rf,t.;f~rt.:I.I,-n "­

r 

I OpeRATING PRCSEU.OII:: 75 PStG 

F'Wf'ffDX RArtN(;; !:iDD.DDO ttHS'HR 

NO.... 'N""t 0,,,. CAPACIT..: sao IJUL 0 r.: 

NO ....INIAL WATeR CAPACITY: GOO OBL..'O 

STANDARD ACCESSORIES 


UCN UU vrc.;'VALH': rANI( CONNl'crj[J!I>J!) 


,", ;':' "J:;" ,!;Af.(,'. Nf.,t.IL." VAL""'" 


t '_' ," 'f"l&.HIC£ JNL",MO:JrAr iN,T" 

,ut.HMUWLt.L .......,...._~_ 1-..1" 1'",,',-1'#"111 

('.1 'Jul ,.ut:L vAS PI4t. 5!iUUt, lj.l.UcJr.. ...,...---C........... ~O .... , .... 

; I! 't1.J:;I fHL~MO""LfLI./ 

t:.n J' M;.IMJ.1A"t' A;IM-,l(l,'WA t-1H.. ""A'L.~ VALVL!' 

f;':' J );,IMUAY ~J,",JlA'r' rrll Ct)M"'A,NIUN 

'-LA~{):L. tJC f ", r;.-" ".."""()WA'IC 

;:- KI,..UA'r' I('M-ZUb UM't-t'''' ljA:; (JAC""'­

IINI.:9!.iUH" VAL"L. A()JHfI: r.... n~ 6 If! '·Wt.ltMA"lil; IU(t U-A!.t "'l{;U.t~\ro'" 

f'.CtC;Jt,:; ...q;!:I \'\«-,lIt (J i Nt V£Utl.tIL( • '''u:-rlJUI~ 

po,," '1"'I"'l.' j I) ~uu" lin,; IJUUNC,W "lAM1. AH~Lt>rou 

~ GAS';:.: t 

I'i ".l..AU..""" arACK WUu"", aUA.'JNli 

if; ,;:' x .:..le,· "'''!j !fCf.lut."Jf..~ rANI( 

{~'.I ~ 1I [i",uc,... t:oc'CU 

If,. ~ u' x 24' (,AUUt: GLAUS 

(PI !'io U :.\ .'u' (JAUUl" tiLA.UU 

IZ; '0" fir.'ANW,",YS 

It) c~o.,..s NeST 

If} LAOOLR 

II, !i'PHC""I ',LJflC ASflClotlfLY WiTH 

ADJUSTADLC rIQCRU,LAIi!i WI:,Q NIPPLt 

111 ;, GA4.V... NiU ..... , O,--Ut: "'CAD A ~OO[ 

WlTH "'. VICTAtJI..IC COUPLING 

OPTIONAl.. ACCESSORIES 

I' J rllJCROLASS PIPr HCU!llNO 

DSHA APPtH::J .... t:O 1. .... 00£:'1 Wtf'H CAD'; 

tlJ (J'Xf1)(lJ' CO.... Cr:U:TC PAO 

III sal RARr. fU.OC:~ ANODE W/TM '.0 i,C040 

'NTC-flNAl. COATING 

VERTICAL EMULSION TREATER OPERATION 

THE EMUL.Slr/ED WELL STREAM ENTERS THE TOP SECTION or THE TREATER. STREAM 

VEL.OC/TY IS THEN REDUCED THROUGH THE USE or AN INLET DIVERTER. THE ENTRAINED 

GAS SEPARATES rROM THE EMULSION rLOW IN THE GAS SEPARATION SECTION, THEN 

GOES THROUGH A MIST EXTRACTOR AND IS EXTRACTED F'ROM THE TOP "GAS SECTION." 

THE REMAINING EMULS/rlED LIQUID PASSES THROUGH TI-1E DOWNCOMER TOWARD THE 

BASE OF' THE TREATER. OIL AND WATER IS THEN DISPCRSED BY A SPREADER AND 

ALLOWED TO RISC THROUGH TI-1E HCATCD WATER WASH SeCTION. TI-1E NOW I-1CATCD OIL 

AND EMULSION ENTERS THE COALESCENCE SECTION AND IS RETAINED UNTIL WATER 

DROPLETS COALESCE AND SETTLE TO TI-1E BOTTOM. CLEAN TREATER OIL F'LOWS OUT or 

THE OIL OUTLET AT THE TOP or THE COALESCENCE SECTION TO A I-1£AD OPERATED DUMP 

VALVE. WATER EXITS TI-1E TREATER TI-1ROUGH AN EXTERNALLY ADJUSTABLE WE:IR NIPPLE 

AND HE:AD OPERATeD DUMP VALVE. 

WWW.HESS-SERVICES.CClM 

HESS Two PHASE GAS SEPARATOR 

DESIGN SPECIFICATIONS ::----.... A5 CUT

DESIGN CODE: 

ASME SeCTION VI/I DIVISION J 

"u" STAMPED & NATIONAL BOARD REGISTERED 

SIZE: 30"x 1 0' ----'---MIST eXTRACTOR 

,.. J 25 PSIG MAWP (HIGHER MAWP AVAILABLE) 'a 

STANDARD ACCESSORIES 

(1) WIRE MESH MIST EXTRACTOR 

/ J J 2" RELIEF VALVE 

----INLET OlvelffTER 

/ J J FLOAT &. FLOAT ARM 0- ---INLET 

(J) TRUNION WITH HAMMER UNION 

(1) 2" MECHANICAL OIL DUMP VALVE FLOAT OPERATED 

(') GUAGE GLASS ASSEMBLY 

(') PRESSURE GUAGE WITH VALVE 

OPTIONAL ACCESSORIES 

(I J STEEL LADDER 

(1) 4'X4'X7" CONCRETE PAD 

(I) 2" BACK PRESSURE VALVE 

INTERNAL COATING 

GAS SEPARATOR OPERATION 

THE WELL STREAM ENTERS THE MID SECTION OF THE SEPARATOR. STREAM VELOCITY IS 

THEN REDUCED THROUGH THE USE OF AN INLET DIVERTER. THE GAS THEN FLOWS 

VERTICALLY TOWARDS THE GAS OUTLET AT A LOW VELOCITY ALLOWING THE HEAVIER 

LIQUIDS TO FALL DOWNWARD AND COLLECT IN THE OIL SECTION. THE GAS THEN FLOWS 

THROUGH A MIST EXTRACTOR WHERE SMALL DROPLETS ARE CAPTURED ALLOWING CLEAN 

GAS TO FLOW FROM THE GAS OUTLET. LIQUID /S COLLECTED IN THE BOTTOM SECT/ON OF 

THE SEPARATOR WITH A FLOAT OPERATED DUMP VALVE, THEN DISCHARGED TO NEXT 

PROCESS. 

WWW.HESS-SERVICES.CCJM 
 . . 
HESS STEEL & FIBERGLASS PRODUCTION TANKS 

F"lOERGLASS TANKS STEEL TANKS 

OUA I"IOC"'01.... 90 T"'NI(5 "'''C 

"'CLOLU ON Spe:CI...LLY tJUILT p------------.. TMC "TCCL T"'NI< PAOOUCTlO'" 

"''''NOA£LII n·....T "'LLOW US TO 

PROOUel: ... T ... NI( THAT ...... 11 NO 

5C ...... £1 .N T ... e BOTTOM 0" 

&MC\..L. THtO 'NCACA1;;;Ca, "He 

'''''1''&:.o",y.., 0"- THiL TANJ( 

T ..I:... "NDOUII........NO "'005 

£1lO.TCNOCO ..In:. "'''''''L...n .. £ "" 

"''''N''' 5,....... 0 .....0 !'IIZCfl. 

SUILT Pe:u API S"'..Clr,e""'ON5 

9Ize:lII: 100BBL TO !tOOBBL. 

OTHeR S,zes'" COLORS 

A"""L"'U..e: U ... ON Re:OULST 

SpI:CI..... RCfilNS A"""L"'OL£ TO 

ACCO..OO...TC F"OA He"'T '" 

C ........ 'C..... ReSIST... NCe:. 

DELIVERY & SETUP SERVICES 

...._----_... 

WE HAVE TRUCKS. TRAIL.ERS, & CRANES AVAILABLE 

TO SET ALL SIZES OF" TANKS QUICKLY, SAF"ELY, ANO 

ECONONMICALLY. OUR EQUIPMENT INCLUOES 

CRANES RANGING F"ROM 1 7 TONS TO 275 TONS. 

ALSO AVAILABLE ARE SPECIAL TANK HAULING 

TRAILERS AND STRETCH DROP DECKS. 

WE ALSO CAN PROVIDE, STAIRs, WALKWAYS, PIPING, 

VALVES, AND F"ITTINGS. 

.T....U. WIT ... T ... ' ....I:ETII 

aCINa CNC Pl........... CUT TO 

LENeT... A.NO WIDTH. ALao, 

TH&: CO.......R PL... CC. ...f,;NTIl "NO 

ALL OT ... eR ...TT... C .....!:.N,.!) "'At;; 

CUT OUT "'NO .,L"'''",,,, ......""l.0 

"0" "'CCUA"'I:T, T ... £ T"NI(II 

A.llfE T"'CN "£:ILLIt 0 "NO WCLO£O 

aT i!llClLLCO p£"'IIO"'CL. WC 

THCN. INOPCCT. S ... NDOL"'OT, 

&. "'AINT TO THI. CUBTO"'EIl. 

SPe:C.,.ICATfCNS. AVAtLA8LE IN 

...... N ... 8""'NO"'110 .,ze8. 

9,zes: I ooSeL TO 7S0SBL 

On-tCA SIZCS &. COLOAS 

AVAILAo.. e UPON RCQueoT 

WWW.HESS-SERVICES.CDM 
1-1ESS STANDARD F""/B£RGLASS '0' DIA GUNfJARR£LS BUILT peR API- 1 2-P SPECS: 

INCLUDED: B" FLUME & STACK. SPREADER. 3")(6" INSIDE SIPHON. ROUND 

MANWAY. 9-3" CONNECTIONS. rUNLESS OTHERWISE SPECIFIED' 

PRE SSURE VACUUM THIEF' HATCH. OUTSIDE STEE:L LADDE:R. 

LIFTING LUGS. & STANDARD BLACK GEL COAT. 

ALL OTHER COLORS CAN BE QUOTED UPON REQUEST. 

HESS STANDARD FIBERGLASS 12' DIA GUNBARRELS BUILT PER API- I 2-P SPECS: 

INCLUDED: '0" FLUME & STACK. SPREADER. 4"X6" INSIDE SIPHON, 

(20' HIGH & ABOVE" 2" DIA FLUME 6")( 10" INSIDE SIPHON. 

ROUND MANWAY. 9'3" CONNECTIONS. rUNLESS OTHERWISE SPECIFIED' 

PRESSURE VACUUM THIEF HATCH, OUTSIDE STEEL LADDER. 

LIFTING LUGS. & STANDARD BLACK GEL COAT. 

ALL OTHER COLORS CAN BE QUOTED UPON REQUEST. 

H£SS STANDARD FlfJERGLASS PRODUCTION TANKS BUILT peR API- r 2·P SPECS: 

INCLUDED: ROUND MANWAY, 7-3" CONNECTIONS, (UNLESS OTHERWISE SPECIFIED} 

PRESSURE VACUUM THIEF HATCH, WALKWAY LUGS, 

LIFTING LUGS & STANDARD BLACK GEL COAT. 

ALL OTHER COLORS CAN BE QUOTED UPON REQUEST 

HESS STANDARD FIBERGLASS SALTWATER TANKS WITH CLOSED TOP DESIGN 

INCLUDED: 2-3" CONNECTIONS, , ,2" CONNECTION. (UNLESS OTHERWISE: SPECIF'IEOJ 

OUTSIDE STEEL LADDER. LIFTING LUGS & STANDARD BLACK GEL COAT. 

ALL OTHER COLORS CAN BE QUOTED UPON REQUEST. 

J 

* 


WWW.HESS-SERV/CES.COM 

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5 
Order#: 

, [ 

Requested Date: 

Carrier: 

Sold To: 

HESS SERVICES, INC. 

P.O. BOX 843 

HAYS, KANSAS 67601 

Ship To: 

HESS SERVICES, INC. 

2670 E. 9th 

HAYS, KANSAS 67601 

po: 

PO Date: Contact: AP/JD Job#: 

MODEL: 5818-18 Qty; 12 Bl'U/hr: 500,000 Duty 

BODY: Aluminum O-Type 1 Piece 

Inlet Connections: Size Orientation Distance 

Pilot 1/';''' o STD 

r4ain 3/4" o STD 

Flange Pattern: 8 ( 5/8" ) Ho2.es on 19-3/'<;;" B.C. 

NOTES: TRIM TO B.C. AT 180 DEGREES 

FLANGE 00 IS 22" 

ELEMENT: Size: 18" 00 X 4" width Qty: 1 Materi~l: Aluminum 

Core: 6 5/8 

Notes: 

ASSEMBLY: 

Pilot: no 

Notes: 

Burner: Qty: 1 ECLIPSE 2" MixerHead 

NS Orifice: 5/32" 

Notes: 

Nozzle: Rosebud 2" 

Notes: 

SERIAL NUMBERS: Inspected: Wt. # 

GENERAL NOTES: MARK BOX tlNO PILOT" 


TRIM FLANGE 1" AT BOTTOl'<1. 

FLAME ARRESTOR/BURNER 


DATA SHEET 


I 

i 

I 

I 

f 

Customer: HESS PO#. N/A 


Job#: N/A Order Date: January 2. 2011 


Model No.: 5818-18 Serial No.: N/A 	 Flameco Ref.: N/A I 

i 

Fuel: NATURAL GAS Gas Value: 1000 BTU Fuel Gravity: O.Gs.G. ! 

Btu/Hr. Rating: 5001000 Burner Size: 2" ECLIPSE Burner Orifice: ~ Pilot Orifice: #70 	 Burner Pressure: 10-14LBS. Pilot Pressure: 3 - 5 # i 

Site Elevatioll: UNKNOWN Draft Available: AMPLE I 

1 

I 

t 

OPERATING INSTRUCTIONS 	 f 

! 

Operation ofthe burner should be by qualified personnel only! 

I 

r Consult API Specification RP 12N before proceeding with the following burner ignition steps. 

1. 	 Make sure the atmosphere is suitable for open flame. The use of a portable combustible gas ignitor is 

recommended. 

2. Close all gas supply valves for the main burner and pilot. 

3 Drain fuel gas scrubbers if so equipped. 

4. 	 Check for an adequate fluid level above the firetube, Ensure that the firebox and stack are clear and free of I

foreign debns. 

5. 	 Open the lighting port of the firebox. Do not stand directly in front of the firetube or the lighting port, Stand to 

the side, and up-wind, if possible, of Ihe lighting port and end plate of the firelube. 

6. 	 Determine if combustible gas is present. If a combustible gas indicator is available, check for combustibles 

in the pilot area and also down the firetube. If combustibles are indicated, recheck positive closing on the I 

valves. wait for the firetube to ventilate, and re-test for combustible gases. If a portable combustible gas 


indicator is not available. then adequate purge time, with all gas supply valves closed. must be allowed 


before trying to light the burner system, When a satisfactory gas check has been secured, proceed to light 


the pilot. 


7. 	 The torch should be pre-measured to reach precisely to the pilot. Light the torch using diesel fuel or 

kerosene. The torch should be of such material that debris will not be left in the firebox after lighting. 

Caution: Do not use gasoline or any other volatile fuel. Pass the torch in front of the opening to check 

for possible flashback. (If flashback occurs, start over at step #1.) Insert the torCh, placing it next to the pilot. 

Leave the torch in position and slowly open the pilot valve until the pilot ignition is heard. Caution: If the 

pilot does not light in a reasonable amount oftime, close the pilot valve and begin step #6. Remove 

the torch and extinguish. Caution: Do not place the torch on the ground as hydrocarbons may be 

present. 

8. 	 The flame should be centered in the firetube. The burner should be regulated for continuous firing when 

possible. The air/gas mixer should be set to provide proper burning quality and to prevent hazardous firetube 

carbon deposit. This may require that the system be shut down, adjusted, and re-lit several times if the 

adjustments cannot be made without opening the arrestor housing. 

Periodical maintenance and testing are mandatory for safe operation. 
MAINTENANCE INSTRUCTIONS FOR FLAME AND STACK 


ARRESTORS 


FLAME ARRESTORS 

Semklllllually. Ihl: name cell should be removed nnu inspected 1(lr dear air passages. )1' 

envil'lllllllental conditions (such as cxcc:ssive dust) warrant. this inspection should bc donc more 

frequcntly. Tn clean. use a hose to force clean water through cell ill the direction opposite III 

norm,11 .,ir flow nnd Ihcn blowout trapped water with compresscd air. Compressed 'Iir will be 

suflicient if the cell i!' not heavily clogged. At this time. the namc arrestor hody should he 

inspected and cleaned or debris. The 111~lling flange gasket shoulu be rcpl:.u.:(:u cach time thl.' Ilame 

<l1Tl:stor is unbollcu I'rol11 the vessel. All gaskets should be inspected for cracks. breaks and 

e:';cl.'ssi,e wem eadl time thc unit is opencd and rcplaeed to maintain arrestor integrity. Replacing 

the center thll1ge gaskct is in addition til n.:placilll:; the mating Ilange gasket eaeh time the unit is 

unbolted rrom the \'essel. 

STACK AI~IU~STORS 

Semi-annually. the spark cell should bl.! n:mo\'cd and inspected ti)l' clear air passage::;, II' 

cll\'ironllll.!lltal conditillllS (slIch as cxccssi,'c ash) warrallt. this inspection :should be don.: mon.: 

!i·clIul.!nlly. Ttl elcan. lISC n hose to force d:an water through cell in the din:ction opposite to 

1I0rl11al air no\\' anu thcll blow Ollt trapped W:lter with comprcssl:u air. Compresscd air ",ill bc 

sufliciclII if the cell is not hemily ciugged.;\1 this time. the slack mrestor body should he 

inspected and cleaned of uebris. The mt:lting !lange gasket should he rcp141ccd each time the 

stack arrestor is unbolted from the stack. All gaskets should be inspected for cracks. bn:'l!-'s and 

excessivc wcar each timc the unit is unbolted Ulld repiacl!d to Illuinwin arrestor integrity. 
MIXER HEADS 


DIMENSIONS 


[­

'S" N.PJ. Gas Inle: / 

Low Pressure 

''P:' N.P.l 

Mixture 

Oullet 

C 

j 

"S" N.P.l Gas Inlel/ 

High Pressure 

Assembly Number 

Catalog With Gas Less Gas 

Number Cock Cock 

NS·3 300101 300116 

NS-4 300103 300118 

NS·5 300105 300120 

.. NS·6 300107 300122 

NS·B 300109 300124 

NS·l0 300111 300126 

NS·12Q 300112 300127 

NS-l60 300113 300128 

NS·2OO 300114 300129 

Catalog With Valve Less Valve 

NUmber & Gaugc &G:JUge 

H0-3-" 300311 300301 

H0-4 300312 300302 

HO-S 300313 300303 

H0-6 300314 300304 

HO·S 300315 300305 

HO-lO 300316 300306 

HO-I2Q 300317 300307 

HO-l60 300318 300308 

HO-200 300319 300309 

NOTE: All dimensions are in inches. 

Packing Gland 

Low Pressure 

Low Pressure 

DimenSions 

A B C 0 E F 

314 31B 3·112 1·3IB 4 

1 314 4-15/16 1·13116 5-13116 - 1·114 3/4 5·118 2 5-5/8 

1-112 3/4 5-1/8 2 6 

2 1 6-1/4 2·5/B 6-318 

2.1/2 I 6-3116 2·9/16 5-114 - 3 1-1/4 6-118 2·112 7·7/16 - 4 1·114 7 3·3/8 8-3116 -

5 j.l/4 7·7/8 4·1/4 9·1/8 - High Pressure 

A B C D E F 

3/4 3/8 4·3/4 1-718 3-318 5-3/8 

1 3/4 4-7/8 1·7/B 5-114 8-314 

1-1/4 3/4 5 2 5-114 8-718 

1.1/2 3/4 5 2 4-7/8 7·3/4 

2 , 5 2 5·3/4 9·1/4 

2·1/2 1-114 5·5/8 2·5/B 6 9·1/2 

3 1-1/4 5-5/8 2·5/8 6-1/4 8·314 

4 1-1/4 5-3/4 2..3J4 7·318 10·718 

5 '·114 6-112 3-112 7 10-114 

Gas Inlel 

High Pressure 

Primary Air Shulter 

Orifice Spuc 

Mixture 

Oullel 

• ECLIPSE COMBUSTION 

2" ROSEBUD NOZZLE 

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SIZE H WT. 

2" 2-5/8" 1.5 

FLAMECO INDUSTRIES 

2" ROSEBUD NOZZLE 

DHD 

DATE: 9-9-11 SHEET 1 OF 1 
EKARDO Products: Gauge Hatches: Spring Loaded Thief Hatch-Models 660 and 660-L Page I of.2 

ENARDO hIHMTc.....~ly 

~-

Products 

Flame and 

OetOO.tt1OIl AmlstOfS 

PreSSI/rl'V.1cuum 

Reief Valves 

Emergency PresSUII 

Relief Vents 

~Venls 

SiZing ProQram 

New Products 

CUllom Enoinllerlld 

SolutiDns 

Testing Capabilities 

Service 

Technical Support 

tDntaci ENARDO 

Users Lisl 

,­

ENARDO Model 660 and 660-L 

Spring-Loaded Thief Hatch 

Model 660 Applications 

The Model 660 is a premium hatch designed with a round base 

and cover and is intended for use in applications where tight 

sealing is critical such as sour crude/gas or where strict 

environmental emissions standards are enforced 

Features 

• SIze Bolt pattern 10-3/8~ circle API 

• Pressure setting 2.3,4,6,8, 12. 16, 24 and 32 oz. 

• Vacuum setting 04. 0.9 and 3.5 oz 

• Materials: Aluminum castings (non-sparkling) 

Model 660-L Applications 

The Model 660-L is apremium hatch designed with a 

long base and cover and is intended for use in 

applications where tight sealing is critiCdI such as sour 

crude/gas or where strict environmental emissions 

standards are enforced. The long basin serves as a thief 

shelf. The Model 660-L also includes an inclining base to 

keep the basin leveL 

Features 

• Size: Bolt pattern 10-3/8' circle API 

• Pressure selling: 2, 3, 4, 6, 8, 12, 16, 24 and 32 oz. 

• Vacuum setting: 04, 0,9 and 3.5 oz. 

• Materials: Aluminum castings (non-sparkling) 

• 	Review;.:·:;'-: (PDF) 


Get the free Acrobat PDF Reader from the 


• 

• Review'>' , 

MARKET APPLICATIONS 

http: '\\'\\'\\' .cnardo.com products prod gh _660 _6601. htm 	 <):8;:2011 
Model BBO and BBO-L 

Thiel Hatches 

The Model 660 spring loaded thief hatch is Model 880 

designed with a round base and cover. It is intended 

for use on steel and fiberglass tanks which require a 

tighter seal for reduced vapor loss. 

The Model 660-L is a spring loaded thief hatch Model 880-L 

designed with a long basin and cover. The long basin 

serves as a thief shelf. The design also includes an 

inclining base to keep the basin level. 

Valve Setting Range 

Model Bolt Pattern 

Model 660 10-318" Circle API 

Model 660-L 10-318" Cirde API 

Pressure Vacuum 

2.3.4.6, B. 12.16.24 and 32 oz. OA, 0.9 and 3.5 oz. 

2,3,4,6,6,12,16.24 and 32 oz. OA, 0.9 and 3.5 oz. 

Materials of Construction 

Model Construction Optional Equipment Shipping Weight 

Model 660 Aluminum caslings 

(non-sparking) 

Plastic Trim (PT), Base Gasket, 

Bolt Set, 

Non-Corrosive Coating 

25 Ibs. (approx,) 

Model 660-l Aluminum castings 

(non-sparking) 

Ductile IrOil 

Plastic Trim (pn, Base Gasket, 

Boll Set, 

Non-Corrosive Goating 

45 /bs. (approx.) 

ENARDO • 4470 S. 70th East A\le .• Tulsa. OK 74145-4607 • 1-800-336-2736 U.S. and Canada. www.enardo.com 'At,,. 11 
:;:'1.1 £-IV, ~A'DM 

TAtlk; ?'c r ,He 

+­

7/ffttnA- Ie> p£.*~t 

Series 7 Inli.le Flame Arrestor 

Enardo Series 7 Inline Flame Arrestors are designed 

to stop the propagation of confined low pressure 

deflagrations. The Series 7 is typically used for end-ofline and near end of line applications when the system 

operating pressure is near atmospheric levels and 

when there is minimal probability of a flame stabilizing 

on the Flame Arrestor element for an extended period. 

The Series 7 prevents flame propagation by absorbing 

and dissipating heat using spiral wound crimped 

ribbon flame cells. These cells allow maximum flow 

with maximum protection. 

Designed with flanged connections. this arrestor 

allows removal of the flame cell element for easy 

cleaning and replacement without removing the 

arrestor body from the pipe connection. Standard 

housing construction is aluminum, carbon steel. and 

stainless steel. The element is available in aluminum or 

stainless steel. SpeCial material and protective 

coatings are available on request. 

Features and Benefits 

I' 

, 

EN 12874 Approved 2 in. (50 mm) - 12 in. (300 mm) IIA 


and 1183 


Factory Mutual Approved 2 in. (50 mm) 12 in. 


(300 mm). IIA (D) 


Enardo's large crimp opening provide: 

• Maximum flow 

• Less pressure Drop 

• Easy Cleaning 

• Less Clogging 

• Less Maintenance 

flame Arrestor Specifications 

Materials 01 Construction 

• Single Element Design. 

• Fluoropolymer coated hardware provides outstanding 

corrosion and chemical resistance. I • Easily accessible and removable flame cell for easy 

inspection and service. 

• Bi-directional design. 

• Standard temperature probe on EN models. 

• Available in ANSI, DIN and JIS flanges. I

~ 

Model Sizes Available 

Series 7 Inlinc Flame Arrestor 1" (25 mm) through 4(1" (1220 mm) 

EN Series ?-EN 12874 Approved 2" (50 mm) through 12" (300 mm) 

Factory Mutual Approved 2" (50 mm) through 12" (300 mm) 

Housing Cell Gas Group 

Aluminum Aluminum IIA (OJ 

carbon Steel 

304 SS 

304 SS 

316 SS 

liB 3 (e)

lie (B) 

316 SS Hastelloy 

Hastelloy 

. 
 ENARDO • 4470 S. 70th East Ave .• Tulsa, OK 74145-4607· 1-800-336-2736 U.S. and Canada· www.enamo.com 37 
-- ::';":=i=== === 

I 

30 Mile Range · 

, 

eaturing the latest state-of-the-art 

solar panel with superior charging 

the Magnum 12 Solar-Pak 

inates battery recharging. 

thereby saving you time and money. 

The sun's energy charges the fencer 

by day and a sealed 12 volt 

rechargeable battery powers the 

fencer at night. Battery included. The 

Magnum 12 Solar-Pak was deSigned'i 

developed and is manufactured 

exclusively by Parmak. 100% 

http://www.pannakusa.com/Fenccrs/solar2.htm 

Parker McCrory M(g Co 

American made. 

Uses the same advanced and 

exclusive circuitry as the 

Magnum 12, including 

Parmak's exclusive built-in 

performance meter. 

Our totally new and improved 

solar panel uses free energy 

from the sun to provide 

maximum shock ... longer life. 

No operating costs! Power line 

convenience with a battery 

fencer. 

Full 2 year warranty - From date of 

retail purchase - Covers damage 

caused by lightning. Twelve-volt 

battery warranted one year. 

For outdoor installation, 

UL listed. 

Iijl' XY \,~"-&"::I_II; ':~,;' LISTED 

Effective applications: 

~~~~ ,.....~~ 

PERFORMANCE SPECIFICATIONS 

IFENCE LOAD I OUTPUT . .____.-J~TAGE 

; Open Circuit I 9.500 

500 ohms I 6,100 

___ ~ 100 ohms J 

Model MAG.12-SP 


Low Impedance 


12 Volt Battery Operated 


A·.cilldbie at y',)~lr It;aUlrlCl 

farn1 supply s:ore. 

-
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6'"'Jt-S ;:-1--1f~EIGAlI170Al 5y.sTtE~ 

918/2011 

Page 3 of3