# ll1egee C:onsulting
Air Quality Permitting 4341 West 40 th 

### 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 of information 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 Pennit 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 of the potential emissions of Greenhouse Gas (GHG) pollutants before and after proposed emission contrQls. 

# I 

# ! t 

# I I ! l 

## f 

# t I I 

# I 

# I r


# t

## 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 ofcrude 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 of wind 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 

# I
t Total Facility Uncontrolled First Year VOC Emissions 209 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. 

# f f Megee Consulting 

## I Casper, Wyoming 

# t 

# 1

## 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 of methods: 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 PROMAX, 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 of the hydrocarbon stream provided in the

laboratory analysis; iv. Ambient pressure of 12.0 psia 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

# I t
! ! 

## 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 ofeach 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 I (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. 

# I i , 

# t 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 t

# I

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 of these 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 of information 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 of Management 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 

# f



# t 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 # 

### I 48-94-33D-28-4H, 5H Production Facility

4. Portable Source? DYes X No 5. Temporary Source? DYes X No 7. SIC Code 

### 1311 

# I
11 a. Latitude* 11 b. Longitude* To Be Determined To Be Determined 

# I

12c. Township* 12d. Range* 

# I I 148N 94W 

# t *Provide all proposed locatIOns ofoperatIOn for portable sources 

# t 

# I i

# f I I 

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

# J b . d t thO 

## :fi 

## T P'd hm'f dd' 

## '1' )

een Issue 0 

### IS aCllty. roVI e as an attac entl a ItlOna space IS necessary 

# I I 

# I 

# I [ 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 

# I t



### 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 40 th 

### St., Casper, WY 82604 Email Address megeecgnsulting(l1lgwestoffice.net Telephone Number Facsimile Number 307-232-0303 307-232-0303 

# I I

< 

## t t !, 

# t t i 

# { I 

# l ! f i

# I t

# ! I ! t 

# t 

# I I ! r**~.** 

# I t

f

## D. ATTACHMENTS Include all of the following information (see the attached instructions) ./ FORM SYNMIN

- New Source Review Synthetic Minor Limit Request Form, if synthetic 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, PM lO , 

### 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 (H 2

### S04), 

### hydrogen sulfide (H 2

### S), 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 

# r 

# i

I 

# t
f 

# I 

# I I
r 

# I !

## 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 of the form. E(i)

- Proposed New Facility Pollutant Potential Emissions (tpy) Proposed Allowable Emissions (tpy) PM 

## NA NA PM

- Particulate Matter PM 10

- 

### Particulate Matter less 

### PM 10 

### 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 H2

### S04 - 

### Sulfuric Acid Mist HzS

- Hydrogen Sulfide 

### H 2

### SO 4 

## 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; 

# I 1 

### (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 I I 

### 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.



## f 

# I 

# i t

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



# I 

# I t 

# I t Pollutant Current Actual Emissions (tpy) Current Allowable Emissions (tpy) Post-Change Potential Emissions (tpy) Post-Change Allowable Emissions (tpy) PM PM 10 

### PM 

### z .s SOx NO. CO VOC

Pb NH3 

### Fluorides

Hz S04 

### HzS 

### TRS RSC PM

- Particulate Matter PM w - 

### Particulate Matter less than lO microns in size PM 2.5
- 

### 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 H 2

### S04 - 

### Sulfuric Acid Mist H2

### S - Hydrogen Sulfide TRS

- Total Reduced Sulfur RSC

- Reduced Sulfur Compounds

# EMISSION SUMMARY

# Petro-H unt, 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 BtulFt 3 • 

## 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 of fire 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 of the 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 Consuiling 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 as a . ,!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**  

### norfll a l!al1 k**Op~f!it!on!3J!iUing ,_e,,_aporatio~.**  

### etc**tII'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**



### gasoli l1 e 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 runnot more**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~ lJseJs

### a!=>!=>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 Mater 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**~--T** I**~-'----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"le ntal 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 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**l~** j 

# 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 

### 1 st 

### 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**---~---~- .~~~**  

# 4**L--~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: AST40 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 

### o 111 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

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 I l

# 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

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/Fi 3 

# -:"-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 analYSis and-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 Be rthold #148-94-33D-28-4H, 5H Production Facility

----- ___________________ ____ __ ____**~M** ___________ --------,---------- ------------------------- -------- :--------- --------, .-----------i---------------'-------- ---T-----------------­**~ ~** **.~** 

## Attach men t to Ai r Quality Permit Application

--

_________________________ , ___ ,._ •• _, __ <

___ •
__ M

____ M

__ _M

___ M

____ M

__ ._+-

___ M_ -----1---­**-~ -~.-.-.-**  ... -.
- ... - .. _-'--- ... --- ... - .. --**--~** ,-- .- ..**-~.** ---**~** -- ---. -- .. ,---. 

# 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** 

## i fbTlb-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 H 2

### S or S02 emissions since the burned gas does not contain these compounds. 

### EM ISSIONS : -_._-_.



# __ ._-,,- ..

### __ . - ..**~.--**



## 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 Bert hold #148-94-33D-28-4H. 5H Production Facility**-~-~" .---.~----~~~----~--------------**  ..**----.--------------.-~~---** ----------,-- ---**-----.---~! --~----**  ..**~--** --.­

__ . __ .L,_ 

## Attachment to Air**Qual~ty Permit~p~ication**  

## Calculat io n 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;~::::~-'::::~-~::::~-::::::::



## '-NOX EmissiOn-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 H2 S 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 

### i Ibs/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- -..-....--- --- ..... 0.0352 TPY

NOx:-----

. -. ;--
.

-- -**(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 H 2 S 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 i Ibs/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 -Annual productIon average fromcalculation- spreadSheet-I

- ..**~---** - ..**~--** " •. - - ..**~---"-** ..**~-- ""--.~--**  --"'-1-­ iE&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 1E&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 2E&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 3Vertical 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 1Vertical 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 2Vertical Fixed Roof Tank Williston, North Dakota 

## TANKS 4.0 Emissions Report
- Summary Format Individual Tank Emission Totals Annual Emissions Report

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

...**_~~. .~_......._~** 



## .Yll orkin. 9

. LO.SS 

### i

......... :.
... 

## l:tllt 0 

### -r:;::...bS

..**E!~El~thin9Lo.ss TotaIEmiSS>L~ns** 

# 19~u~~o~rf~tp· 5)··· 

# ::.**/~** 

# 1'3 (/1."" 

# t <75 .1,194.90 I 352.78 

### L 1,547.68 

### I r " fA--,... 

# ;.**~,** 

# 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 @ 

# 50 0
-- --­ - 

### 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** 

# F**acil~!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 T9ntlYU 

### r TgnelYU 

### r 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 ! 

# ( 

# 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:QO**15~=** _<:>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---~-I**  

## Gas Service: ! 

### Com ponent : 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**0.2400-r~-4.8606- -t-~-6.035**  

### 0.00074 0.0307 0.00065**T-------~~--** 

### 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

__ 0.1386 0.00074

__5**.5_~** 

### ___ 

## 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 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 

# & 

# C 3 

# + 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-1**CO\!1pon~llts** 

### .---- 

# ··---T-- 99.999---[



# ___..__ ._.___.......___._ .....____ J---

.....- .. ---.--- .. -.-.--- ...... -



## HAPs FRACTION 

## 0.42%**M~I o/~Jiom**  

### ci3 lclj!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~·-~-----·-····-!---··---·-~ --~--------------"---"---"-,**  ­ 

# A

ttachment to Air Quality Permit Application**~ ~~~---~** **I--···~~~ ~~~~~~~~~** **~--** 

# ..... Calculation 

# of HAPs 

# & C .3 

# + VOC Weight Percent 

# of Flash Gas
Weighted**FractiOn~~~** 

### Component

### ~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?_~~~** 

### 106.2**~ 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 SHEETSOur 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 VOCinerator lM 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.

# ~ 

# MESSeDRecently 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

::----
.... A5 CUT DESIGN SPECIFICATIONS 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 "£:ILL It 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.CDM1-1ESS 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 

# I 

# I *

WWW.HESS-SERV/CES.COM

### /-­ 

## ,//' 

## /

.........**""«",,,,~.** 

## ct0.**~t'"** I.'**'t~.tt** .. · '\. 

## f ".'

. L, L .,.



# J

...-.;;,**~-** 

# . " -",



### .....

# _­**X'~ ~**  •**W~l,** v:**$(.~.[** $.**~f~** $(l .. l ;) 'lit 

## ,!,.,

..**~**



# I I I n:lr 

## ." ,

# .. " 

# I " {' )1**~.** 

## ,','
l.......o

# """l~ I 

### " 

# Lc 7-Q:, L t I i**1;"Ik:"~~' l"'~'-**  

# r'

! ,....J.((. 

### '\



## c:it '.1 !

..

# _'1~ I**r_~'** 

# _.­

I , 

## S-I !'.l;**h(1I~":** r::


### Jr.

, 

# r-·
¢**S:~l(** 0 ICC**~·····~-----------za------------~**

000

# ~1HI o o o o o iii o o o o o o o o o o o o 

### I o o 

## : I 

# I

o 0 00 0 o· 0 0 0 0 00 0 0

### ~

## ~1·~--------2.----------~

o o o o 4:; 

# r I**~"IS** O
.... JlNG

't.ISI In
... • ",nlllef,. PIOPill[lARt**~IGHT$** "1£ CtA.M(O I. Hf£ M.HrJlIAl**Dl~ClOS£D** 011 5S I 4 I 3 I 2 I I**61L~** Of N;.fr'IUS I fl:.**o£Snlp'fJO~** IOH V!lI00R PIN I wUElIA", l'OU ,ill i 'UI "'JIIIEI ! (A-1:60P**~[.** I**S,~(** CUANOOI Iii,",**G~'tl** , 1**~"sn.o** 100_['[' ,.,10.11'

.. · .. ''''ll631**r'~N.r[D** (**~oP (HAl~tT**  "AJI£ uASlI(i 1 , I u."')s l./jtU I to' DIJROME'l£!f**!Vil~i&~III'\~1I1** PT- IJI5-.U r 'llIIClf,D : 

# K 28 

# 21. 

# - " " 

## " " " 

## " " " 

## " " 

## " " o!o 

# I

:

## ~~AC~**~~.X** " " 

# I**~O~,51¥E** 

### " " LOCT. IE J 

## • • 

# " AD3BCIJ 

## " :' 

# - •**~LH** I 

### • 

## " i TIP , 

### " 

# I • • 

# · " 0 

# · · " " 

# · • 

## " " 

# · I 

### • 

## " " • • 40 

### • 0 

## " 

# I 

# · · " 

## " 

# · • 

# I • 0 

## " 

# · " 

## "

# ~~ " " 

# " I) 

# ) " I) 

## " 

## "

- 

# " "**.~** 

# " 0 

### " 

## " 0 

## " 

## " 

# " " 

## " 

## " " 

## " " 

# f1 " -t- 118

IIUT un j**O~~S"f~~{lJ '~Ij(iAli'f**  1I,GfI!S All CVIIi£!) ..**IU~'** II-I 

### HESS SilI_'tn. 

### cr.", 1111 THi lUHRIAL**DISCl,.O~[O** ijIII HilS OUWlili**'(jI~l** 

# -­ " t UI .t**'I~** 

# I I I , ;£1(11 I '(I lOt

... .1'11 fl·) !,It) ItliLII_ 

# ... II'**~ ~.**  .. .. tU.f au.»"It' 

### ".,

.. 1)1., AS-IIII)' ASS[O ."IIUSt.,"

(L[AMlUT rRl.04[ GASKEI ASS[IIBLV
I'£v Ofsti I PI 10. OHE it.1 r «'\0 '-;Sd}fU6 

# r O.M 

### I 5Hl 1 or Ire 

# r f)

Ir 

### ,

lB

A**sCJ.~r** J.J6 '



### 'E' 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: 500 1

### 000 

### 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 of the 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. 

# I

4. 

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



# <\. 

# S\H

- [7 -1? t::::i:,'\j 

# i 

# (/« r::S I**~ -.-.-.--.~.-.** **.-.-.~.-.-.** 

### '-'-'-'-' 

## '-'-'­

. I I 

# C?**I~**



# <!:? :**/~** 

# 0li]J·-D;'\)
I

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 1**0-3/8~** 

### 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 a premium 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 OUTPUT 

# I

. .____**.-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. 

# - / EHfJo;eM 

## y / tfE,f'lTA?, 

# 6'"' Jt-S

## ;:-1--1f~EIGAlI170Al

# 5y.sTtE~

918/2011
Page 3 of3