HomeMy WebLinkAbout20143378.tiff * CDPHE COLORADO
CO 406 Department of Public
Health&Environment
Dedicated to protecting and improving the health and environment of the people of Colorado
Weld County - Clerk to the Board
1150 0 PO Box 758 RECEIVED
Greeley, CO 80632
NOV 0 3 2014
October 29, 2014
WELD COUNTY
COMMISSIONERS
Dear Sir or Madam:
On November 5, 2014, the Air Pollution Control Division will begin a 30-day public notice period for
for Bonanza Creek Energy Operating Company, LLC - State Antelope J-28 Production Facility. A copy
of this public notice and the public comment packet are enclosed.
Thank you for assisting the Division by posting a copy of this public comment packet in your office.
Public copies of these documents are required by Colorado Air Quality Control Commission
regulations. The packet must be available for public inspection for a period of thirty (30) days from
the date the public notice is published. Please send any comment regarding this public notice to the
address below.
Colorado Dept. of Public Health a Environment
APCD-SS-B1
4300 Cherry Creek Drive South
Denver, Colorado 80246-1530
Attention: Clara Gonzales
Regards,
a / c `,3
Clara Gonzales
Public Notice Coordinator
Stationary Sources Program
Air Pollution Control Division
Enclosure
4300 Cherry Creek Drive S., Denver,CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe I F/. 40.
John W. Hickenlooper,Governor I Larry Wolk,MD,MSPH,Executive Director and Chief Medical Officer ,a r,.r-,i*,
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eatbll.C/ I`�evlet.J 'rays'
11-5 -20N Cc:-p`�Wr L I) /3 2014-3378
CDPHE Public Notice Of A Proposed Project
Or Activity Warranting Public
CO
Comment
Website Title: Bonanza Creek Energy Operating Company, LLC - State Antelope J-28 Production Facility -
Weld County
Notice Period Begins: November 5, 2014
Notice is hereby given that an application for a proposed project or activity has been submitted to the
Colorado Air Pollution Control Division for the following source of air pollution:
Applicant: Bonanza Creek Energy Operating Company, LLC
Facility: State Antelope J-28 Production Facility
oil and gas exploration and production facility
SW/SW Sec 28, T5N, R62W
Weld County
The proposed project or activity is as follows: The applicant proposes to operate an oil and gas production
facility.
The Division has determined that this permitting action is subject to public comment per Colorado
Regulation No. 3, Part B, Section III.C due to the following reason(s):
• permitted emissions exceed public notice threshold values in Regulation No. 3, Part B, Section
III.C.1.a (25 tpy in a non-attainment area and/or 50 tpy in an attainment area)
• the source is requesting a federally enforceable limit on the potential to emit in order to avoid other
requirements
The Division has made a preliminary determination of approval of the application.
A copy of the application, the Division's analysis, and a draft of Construction Permit 13WE2810 have been
filed with the Weld County Clerk's office. A copy of the draft permit and the Division's analysis are
available on the Division's website at https://www.colorado.gov/pacific/cdphe/air-permit-public-notices
The Division hereby solicits submission of public comment from any interested person concerning the ability
of the proposed project or activity to comply with the applicable standards and regulations of the
Commission. The Division will receive and consider written public comments for thirty calendar days after
the date of this Notice. Any such comment must be submitted in writing to the following addressee:
Carissa Money
Colorado Department of Public Health and Environment
4300 Cherry Creek Drive South, APCD-SS-B1
Denver, Colorado 80246-1530
cdphe.commentsapcd@state.co.us
1 I OrCOLORADO
t- -u:..tt.
STATE OF COLORADO
DRAY P C HEALTH AND ENVIRONMENT
AIR POLLUTION CONTROL DIVISION
i
TELEPHONE: (303)692-3150 : •Cv9 ; `
•IB'!6•
CONSTRUCTION O. PERMIT
.I PERMIT NO: 13 V�A Y E20 I 0
Issuance 1
DATE ISSUED:
ISSUED TO: Bonanza Creek Energy Operating Company, LLC
THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS FOLLOWS:
Oil and gas exploration and production facility known as the State Antelope J-28
Production Facility, located in the SWSW Section 28, Township 5N, Range 62W, Weld
County, Colorado.
THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE FOLLOWING:
Facility AIRS
Equipment Point Description
ID
Condensate Twelve(12)500 bbl above ground atmospheric condensate
003 storage tanks controlled by ten enclosed flares. Each flare
Tanks has a minimum destruction efficiency of 95%.
Four(4)400 bbl above ground atmospheric produced water
PW Tanks 004 storage tanks controlled by ten enclosed flares and four(4)
60 bbl concrete vaults for produced water storage. Each flare
has a minimum destruction efficiency of 95%.
Truck 006 Truck Condensate Loadout
Loadout
FUG 007 Fugitive VOC equipment leaks
One emergency flare with a minimum combustion efficiency
Flare 008 of 95%. The flare is not enclosed.The emergency flare is
used during periods when the pipeline is not available.
Four low-pressure separators controlled by a VRU and ten
LP Sep 1-4 009 enclosed flares when the VRU is not operational. Each flare
has a minimum destruction efficiency of 95%.
One(1)pneumatic water transfer pump, rated at 600 scf/hr
Pump 1 010 (Sandpiper, Model G1F, Serial number 2091567).The
pneumatic pump is controlled by ten enclosed flares. Each
flare has a minimum destruction efficiency of 95%.
AIRS ID: 123/9BAA Page 1 of 21
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PoManion Control Division
Facility
Equipment Point Description
ID
One(1)pneumatic water transfer pump,rated at 600 sd/hr
Pump 2 011 (Sarn#pipr;Model G1F,Serial raa{Ilter 1587).The
pneiflicpmnp is controlled by te)ip need flares. Each
flarf es.a minimum destruction efikltency of 95%.
AIRS Points 010 and 011: Each pump may be replaced with another pump in
accordance with the provisiona dthe Alternate Operating Scenario(AOS)in this penult.
THIS PERMIT IS GRANTED SUBJECT ,,ALL RULES AND REGILATI(INS OF THE COLORADO
AIR QUALITY CONTROL C THE COLORADO AIR PO ZION PREVENTION AND
CONTROL ACT C.R.S. (2.644 ,.TO THOSE GE NERMLOWSMS AND CONDITIONS
INCLUDED IN THIS DOCUMENT LOWING SPECIFIC TERMS AND CONDITIONS:
• 1K„ ., :p
REQUIREMENTS TO SELF-CEOR FINAL AU TION '
1. YOU MUST notify the Air won Control D Division) no later than
fifteen days after issuance eft permit,Iry su "dice ics of Startup form to
the Division. The, , #I Startup form .:downloaded online at
www.akhe.state.co.us/ rms.html. Failure to notify the Division of startup
of the permitted source lli-t Aolation of Air Quality Combo( Commission (AQCC)
Regulation No. 3, Part B,Section 111.6.1 and can result in the revocation of the permit.
2. Within one hundred and eighty:guys (180)after issuance ofthis permit, compliance with
the conditions contained,In- b it shall be dernonstrajed to the Division. It is the
owner or operator's to Self-certify compliance with the conditions. Failure to
demonstrate compliance 180 days may result in revocation of the permit.
(Reference: Regulation No.3,Pert 8,III.6.2).
3. This permit shall expire if the armor or operator of the source for which this permit was
issued: (i) does not ccmmenq ponstructionknodifcation or operation of this source
within 18 months after either,,*Oita of Issuance of this construction permit or the date
on which such constriction or?adivlty was scheduled to commence as set forth in the
permit application associated this permit; (ii) discontinues construction for a period
of eighteen months or more does not complete won within a reasonable
time of the estimated date. The Division may grant extensions of the
deadline per Regulation No.,8„.Part B, III.F.4.b. (Reference: Regulation No. 3, Part B,.
III.F.4.)
4. AIRS Point 009:Within one hundred and eighty(180)days after issuance of this permit,
the operator shall install a flow meter to monitor and record volumetric flowrate of natural
gas vented from each iow pressure separator. The operaoshafl use the gas flow rate
listed in the application for acitid flow rate until the flow meter is installed, not to exceed
one hundred and eighty(180)days after Issuance of this penult.
5. The operator shall complete all initial compliance testing and sampling as required in this
permit and submit the results to the Division as part of the self-certification process.
(Reference: Regulation No. 3, Part 8,Section III.E.)
6. The operator shall retain the permit final authorization letter issued by the Division, after
completion of self-certification, with the most current construction permit This
construction permit alone does not provide final authority for the operation of this source.
AIRS ID: 123/9BAA Page 2 of 21
olor Depa en Ii ealth and Environment
it Pollution Control Division
EMISSION LIMITAJJ
7. Emissions of air pollutants shall not exceed the following limitations(as calculated in the
Division's preliminary analysis). (Reference: Regulation No. 3, Part B, Section II.A.4)
Annual Limits:
Facility MRS Tons per Year
Equipment ID Point NO, VOC CO Emission Type
Condensate 003 — 13.3 3.1 Point
Tanks
PW Tanks 004 2.1 Point
Truck Loadout 006 29.4 Point
FUG 007 24 Fugitive
Flare 008 — 3.2 2.1 Point
LP Sep 1-4 009 1.0 10.5 5.5 Point
Pump 1 010 — 1.9 1.2 Point
Pump 2 011 --- 1.9 1.2 Point
See "Notes to Permit Holder"for information on emission factors and methods used to calculate
limits.
Facility-wide emissions of each individual hazardous air pollutant shall be less than 8.0
tpy.
Facility-wide emissions of total hazardous air pollutants shall be less than 20.0 tpy.
Compliance with the annual limits shall be determined by recording the facility's annual
criteria pollutant emissions, (including all HAPs above the de-minimis reporting level)
from each emission unit, on a rolling twelve (12) month total. By the end of each month
a new twelve-month total shall be calculated based on the previous twelve months' data.
The permit holder shall calculate emissions each month and keep a compliance record
on site or at a local field office with site responsibility, for Division review. This rolling
twelve-month total shall apply to all permitted emission units, requiring an APEN, at this
facility.
8. AIRS Point 007: The operator shall calculate actual emissions from this emissions point
based on representative component counts for the facility with the most recent extended
gas analysis, as required in the Compliance Testing and Sampling section of this
permit. The operator shall maintain records of the results of component counts and
sampling events used to calculate actual emissions and the dates that these counts and
events were completed. These records shall be provided to the Division upon request.
9. The emission points in the table below shall be operated and maintained with the control
equipment as listed in order to reduce emissions to less than or equal to the limits
established in this permit(Reference: Regulation No.3, Part B, Section III.E.)
Facility AIRS Pollutants
Equipment Point Control Device Controlled
ID
AIRS ID: 123/9BAA Page 3 of 21
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ollution Control Division
Condensate D VOC
Tanks
PW Tanks 004 Enclosed Flare VOC
Flare 008 Open Rare VOC
LP Sep 1.4 009 Enclosed Rare VOC
Pump 1 010 Enclosed Flare VOC •
Pump 2 011— Enclosed Flare VOC
PROCESS LIMITATIONS AND RECORDS
10. This source shall be Gritted to the following maximum processing rates as listed below.
Monthly records of the actual processing rates shall be maintained by the owner or
operator and made available to the Division for inspection upon request (Reference:
Regulation 3, Part B, IIA.4)
•
Process/Consumption Limits
Facility AIRS
Equipment pans Process Parameter Annual Limit
ID
Condensate 003 Condensate Throughput 249,660 BBL
Tanks
PW Tanks 004 Produced Water Throughput 315,360 BBL
Truck 006 Oil Loaded 249,660 BBL
Loadout
FUG 007 NA NA •
Flare 008 Total Gas Vented from Separators to 8,7 MMSCF
Emergency Flare
LP Sep 1 4 009 Total Gas Vented from All Low-Pressure 24.2 MMSCF
Separators
Pump 1 010 Natural Gas Consumed 5.3 MMSCF
Pump 2 011 Natural Gas Consumed 5.3 MMSCF
Compliance with the annual throughput limits shall be determined ona rolling twelve(12)
month total. By the end of each month a new twelve-month total is calculated based on
the previous twelve months' data. Thepermit holder shall calculate throughput each
►ou9 Pot
month and keep a compliance record on site or at a local field office .with site
responsibility,for Division review.
11. MRS Point 009: Upon installation of the flow meter required under Condition 4, the
owner or operator shell continuously monitor and record the volumetric flowrate of
natural gas vented from all low pressure separators using a flow meter. The flow meter
shall continuously measure flowrate and record total volumetric flow vented from all low-
pressure separators. The owner or operator shall use the sum of monthly throughput
records from all low-pressure separators to.demonstrate compliance with the limits
specified in Condition 10 and to calculate emissions as described in this permit.
AIRS ID: 123/9BAA Page 4 of 21
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T E NTS epa en P li ealth and Environment
STATE AND FEDE
it Pollution Control Division
12. AIRS Points 003, 004, 006, 008—011: The permit number and AIRS ID point number
(e.g. 123/4567/890) shall be marked on the subject equipment for ease of identification.
(Reference: Regulation Number 3, Part B, III.E.)(State only enforceable)
13. Visible emissions shall not exceed twenty percent(20%)opacity during normal operation
of the source. During periods of startup, process modification, or adjustment of control
equipment visible emissions shall not exceed 30% opacity for more than six minutes in
any sixty consecutive minutes. Emission control devices subject to Regulation 7,
Sections XII.C.1.d or XVII.B.1.c shall have no visible emissions. (Reference: Regulation
No. 1,Section II.A.1. &4.)
14. This source is subject to the odor requirements of Regulation No. 2. (State only
enforceable)
15. This source is subject to Regulation No. 7, Section XII.C General Provisions (State only
enforceable). All condensate collection, storage, processing and handling operations,
regardless of size, shall be designed, operated and maintained so as to minimize
leakage of volatile organic compounds to the atmosphere to the maximum extent
practicable.The operator shall comply with all applicable requirements of Section XII.
16. No owner or operator of a smokeless flare or other flare for the combustion of waste
gases shall allow or cause emissions into the atmosphere of any air pollutant which is in
excess of 30% opacity for a period or periods aggregating more than six minutes in any
sixty consecutive minutes. (Reference: Regulation No. 1, Section II.A.5.)
17. AIRS Point 003: The flare covered by this permit is subject to Regulation No. 7, Section
XII.C General Provisions (State only enforceable). If a combustion device is used to
control emissions of volatile organic compounds to comply with Section XII.D, it shall be
enclosed, have no visible emissions, and be designed so that an observer can, by
means of visual observation from the outside of the enclosed combustion device, or by
other means approved by the Division, determine whether it is operating properly. The
operator shall comply with all applicable requirements of Section XII.
18. AIRS Point 003: This source is subject to the recordkeeping, monitoring, reporting and
emission control requirements of Regulation 7, Section XII. The operator shall comply
with all applicable requirements of Section XII.
19. AIRS Point 003: The condensate storage tanks covered by this permit are subject to
Regulation 7, Section XVII.C emission control requirements. These requirements
include, but are not limited to:
XVII.C.1.a. Beginning May 1, 2008, owners or operators of all atmospheric condensate
storage tanks with uncontrolled actual emissions of volatile organic compounds
equal to or greater than 20 tons per year based on a rolling twelve-month total
shall operate air pollution control equipment that has an average control
efficiency of at least 95%for VOCs on such tanks.
20. AIRS Points 003 and 004: The flare covered by this permit is subject to Regulation No.
7, Section XVII.B General Provisions (State only enforceable). These requirements
include, but are not limited to:
XVII.B.1.b If a flare or other combustion device is used to control emissions of volatile
organic compounds to comply with Section XVII, it shall be enclosed, have no
ii visible emissions during normal operations, and be designed so that an observer
AIRS ID: 123/9BAA Page 5 of 21
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WWI • • • Ilh and Environment
A Pollution Control Division
can, • I d the enclosed flare or
combustion device, or by other convenient means;approved by the Division,
determine whether ft Is operating properly. The operator shall comply with all
applicable requirements of Section XVII.
XVII.B.2.d.(ii) All corn devices installed before May 1, 2014, must be equipped
with an o auto-igniter by or before May 1, 2016, or after the next
combustion de'p$Ce planned shutdown,whichever comes first.
21. MRS Points 003 and 004: The storage tanks covered by this permit are subject to
Regulation 7, Section XVII.C emission control requirements. These requirements
include,but are not limited to:
Section XVII.C.1.Control and monitoring requirements for storage tanks
XVII.C.1.b. Owners or operators of storage tanks with uncontrolled actual emissions of
VOCs equal+to:ar greater than six (6) tons per year based on a rolling twelve-
month total must operate air pollution control legUipment that achieves an
average hydrocarbon control efficiency of 95%. If a combustion device is used, it
must have a design destruction efficiency of at least 98%for hydrocarbons.
XVII.C.1.b.(i)(b) Control requirements of Section XVIl.C.1.b. must be achieved
by May 1,2015.
XVII.C.1.d. Beginning May 1, 2014, or the applicable compliance date in Section
XVII.C.1.b.(i),.Whichever comes later, owners or operators of storage tanks
constructed befdte May 1, 2014 subject to Section XV11.C.1. must conduct audio,
visual,olfactory('AVO')and additional visual inspections of the storage tank and
any associated equipment (e.g. separator, airpollution control equipment, or
other pressure reducing equipment)at the samaequency as liquids are loaded
out from the storage tank. These inspections are not required more frequently
than every seven(7)days but must be conducted at least every thirty one (31)
days. Monitoring is not required for storage tanks or associated equipment that
are unsafe, difficult, or inaccessible to monitor,as defined in Section XVII.C.1.e.
The additional visual inspections must include,at a minimum:
XVII.C.1.d.(i)V$ual inspection of any thief hatch, pressure relief valve, or other
access point to ensure that they are dosed and properly sealed;
XVII.C.1.d.Qi) Visual inspection or monitoring of the air pollution control
equipment to ensure that it is operating, including that the pilot light is lit
on combustion devices used as air pollution control equipment;
XVII.C.1.d.(W)If a combustion device is used, visual inspection of the auto-igniter
and valves for piping of gas to the pilot light to ensure they are functioning
Properly
XVII.C.1.d.gv)Visual inspection of the air pollution control equipment to ensure
that the valves for the piping from the storage tank to the air pollution
controlequipment are open;and
XVII.C.1.d.(v) If a combustion device is used, inspection of the device for the `!
presence or absence of smoke. If srnpke is observed, either the
ffoor smoke and perform uipper*must be repairs yashn-in to investigate
ry�s,orEPA Method must be
AIRS ID: 123/9MA Page 6 of 21
Depa en ealth and Environment
T
llution Control Division
Dolor
isibns are present for a
period of at least one(1)minute in fifteen (15)minutes.
XVII.C.1.e. If storage tanks or associated equipment is unsafe, difficult, or inaccessible
to monitor, the owner or operator is not required to monitor such equipment until
it becomes feasible to do so.
XVII.C.2. Capture and monitoring requirements for storage tanks that are fitted
with air pollution control equipment as required by Sections XII.D. or
XVII.C.1.
XVII.C.2.a. Owners or operators of storage tanks must route all hydrocarbon emissions
to air pollution control equipment, and must operate without venting hydrocarbon
emissions from the thief hatch (or other access point to the tank) or pressure
relief device during normal operation, unless venting is reasonably required for
maintenance, gauging, or safety of personnel and equipment. Compliance must
be achieved in accordance with the schedule in Section XVII.C.2.b.(ii).
XVII.C.2.b. Owners or operators of storage tanks subject to the control requirements of
Sections XII.D.2., XVII.C.1.a, or XVII.C.1.b. must develop, certify, and implement
a documented Storage Tank Emission Management System ("STEM") plan to
identify, evaluate, and employ appropriate control technologies, monitoring
practices, operational practices, and/or other strategies designed to meet the
requirements set forth in Section XVII.C.2.a. Owners or operators must update
the STEM plan as necessary to achieve or maintain compliance. Owners or
operators are not required to develop and implement STEM for storage tanks
containing only stabilized liquids. The minimum elements of STEM are listed
below.
XVII.C.2.b.(i) STEM must include selected control technologies, monitoring
practices, operational practices, and/or other strategies; procedures for
evaluating ongoing storage tank emission capture performance; and
monitoring in accordance with approved instrument monitoring methods
following the applicable schedule in Section XVII.C.2.b.(ii) and Inspection
Frequency in Table 1.
XVII.C.2.b.(ii) Owners or operators must achieve the requirements of Sections
XVII.C.2.a. and XVII.C.2.b. and begin implementing the required
approved instrument monitoring method in accordance with the following
schedule:
XVII.C.2.b.(ii)(b) A storage tank constructed before May 1, 2014, must comply
with the requirements of Sections XVII.C.2.a. and XVII.C.2.b. by May 1,
2015. Approved instrument monitoring method inspections must begin
within ninety (90) days of the Phase-In Schedule in Table 1, or within
thirty(30) days for storage tanks with uncontrolled actual VOC emissions
greater than 50 tons per year.
XVII.C.2.b.(ii)(d) Following the first approved instrument monitoring method
inspection, owners or operators must continue conducting approved
instrument monitoring method inspections in accordance with the
Inspection Frequency in Table 1.
Table 1 —Storage Tank Inspections
AIRS ID: 123/9BAA Page 7 of 21
Teat and Environment
Pollution Control Division
Th I Phase-In
Uncontrolled Actual VOC Monitoring Method Inspection Schedule
Emissions(tpy) Frequency
>6 and E 12 Annually January 1, 2016
> 12 and<50 Quarterly July 1,2015
>50 Monthly January 1,2015
XVII.C.2.b.(01)Owners or operators are not required to monitor storage tacks and
associated equipment that are unsafe, difficult, or inaccessible to monitor,
as defined in Section XVII.C.1.e.
XVII.C2.b.(iv) STEM must include a certification by the owner or operator that
the selected STEM strategypes)are designed to minimize emissions from
storage tanks and associated equipment at the faclliy(ies), including thief
hatches and pressure relief devices.
XVII.C.3. Recordkeeping
XVII.C.3. The owner or operator of each storage tank subject to Sections XII.D. or
XVII.C. must maintain records of STEM, if applicable, including the plan, any
updates, and the certification, and make them available to the Division upon
request. In addition, for a period of two (2) years, the owner or operator must
maintain records of any,required monitoring and make them available to the
Division upon request,including:
XVII.C.3.a.The AIRS ID for the storage tank.
XVII.C.3.b. The date and duration of any period where the thief hatch, pressure relief
device, or other access point are found to be venting hydrocarbon emissions,
except for venting that is reasonably required for maintenance, gauging,or safety
of personnel and equipment.
XVII.C.3.c.The date and duration of any period where the air pollution control equipment
is not operating.
XVII.C.3.d. Where a combustion device is being used, the date and result of any EPA
Method 22 test or investigation pursuant to Section XVII.C.1.d.(v).
XVII.C.3.e. The timing of and efforts made to eliminate venting, restore operation of air
pollution control equipment,and mitigate visible emissions.
XVII.C.3.f. A list of equipment associated with the storage tank that is designated as
unsafe, difficult, or inaccessible to monitor, as descrbed in Section XVII.C.1.e.,
an explanation stating why the equipment is so designated, and the plan for
monitoring such equipment.
22. AIRS Point 006: This source is located In an ozone non-attainment or attainment-
maintenance area and is subject to the Reasonably Available Control Technology
(RACT)requirements of Regulation Number 3, Part B, III.D.2.a. Condensate loading to
truck tanks shall be conducted by submerged fill.(Reference: Regulation 3,Part B, III.E)
AIRS ID: 123/9BAA Page 8 of 21
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23. AIRS PointDolor
or w lo procedures that minimize
the leakage of VOCs to the atmosphere including, but not limited to (Reference:
Regulation 3, Part B, III.E):
a. Hoses, couplings, and valves shall be maintained to prevent dripping, leaking, or
other liquid or vapor loss during loading and unloading.
b. All compartment hatches (including thief hatches) shall be closed and latched at
all times when loading operations are not active, except for periods of
maintenance, gauging, or safety of personnel and equipment.
c. The owner or operator shall inspect loading equipment and operations on site at
the time of the inspection to ensure compliance with Condition 23 (a) and (b)
above. The inspections shall occur at least monthly. Each inspection shall be
documented in a log available to the Division on request.
24. AIRS Point 006: All hydrocarbon liquid loading operations, regardless of size, shall be
designed, operated and maintained so as to minimize leakage of volatile organic
compounds to the atmosphere to the maximum extent practicable.
25. AIRS Point 007: This source is subject to Regulation No. 7, Section XVII.F. leak
detection and repair requirements,which include but are not limited to:
XVII.F.1. As of the compliance date specified in XVII.F.4, the provisions of Section
XVII.F. shall apply in lieu of any directed inspection and maintenance program
requirements established pursuant to Regulation Number 3, Part B, Section
III.D.2.
XVII.F.4. Requirements for well production facilities
XVII.F.4.b. Owners or operators of well production facilities constructed before October
15, 2014, must identify leaks from components using an approved instrument
monitoring method within ninety (90) days of the Phase-In Schedule in Table 4;
within thirty (30) days for well production facilities subject to monthly approved
instrument monitoring method inspections; or by January 1, 2016, for well
production facilities subject to a one time approved instrument monitoring method
inspection. Thereafter, approved instrument monitoring method and AVO
inspections must be conducted in accordance with the Inspection Frequencies in
Table 4.
XVII.F.4.c. The estimated uncontrolled actual VOC emissions from the highest emitting
storage tank at the well production facility determines the frequency at which
inspections must be performed.
Table 4—Well Production Facility Component Inspections
Thresholds(per
XVII.F.4.c)—Well
Production Facilities Approved Instrument AVO
with Storage Tanks Monitoring method Inspection Phase-In
(tpy) Inspection Frequency Frequency Schedule
> 0 and < 6 One time Monthly January 1, 2016
AIRS ID: 123/9BAA Page 9 of 21
and Environment
Pollution Control Division
> ≤'1 January 1,2016
•
> 12 and≤50 Quarterly Monthly January 1, 2015
>50 Monthly January 1, 2015
XVII.F.5. If a component is unsafe, difficult, or inaccessible to monitor, the owner or
operator is not required to monitor the component until ft becomes feasible to do
so.
XVII.F.6 Leaks requiring repair. Leaks must be identified utilizing the methods listed in
Section XVII.F.6.Only leaks detected pursuant to Section XVII.F.6.require repair
under Section XVII.F.7.
XVII.F.6.a. For EPA Method 21 monitoring, or other Division approved quantitative
instrument based monitoring, at facilities constructed before May 1, 2014, a leak
is any concentration of hydrocarbon above 2,000 parts per million (ppm) not
associated with normal equipment operation,such as pneumatic device actuation
and crank case ventilation, except for well productionAfadlipes where a leak is
defined as any concentration of hydrocarbon above 50 ppm not associated with
normal equipment operation,such as pneumatic device actuation and crank case
ventilation.
XVII.F.6.c. For infrared camera and AVO monitoring, or other Division approved non-
quantitative instrument based monitoring, a leak is any,detectabie emissions not
associated with normal equipment operation,such as pneumatic device actuation
and crank case ventilation.
XVII.F.6.e. For leaks identified using an approved instrument monitoring method or AVO,
owners or operators have the option of either repairing the leak in accordance
with the repair schedule set forth in Section XVII.F.7..or conducting follow-up
monitoring using EPA Method 21 within five (5) working days of the leak
detection. If'the follow-up EPA Method 21 monitoring shows that the emission is
a leak as defined in Section XVII.F.6.,the leak must be repaired and remonitored
in accordance with Section XVII.F.7.
XVII.F.7.Repair and remonitoring
XVII.F.7.a. First attempt to repair a leak must be made no later than five (5) working
days after discovery, unless parts are unavailable, the equipment requires
shutdown to complete repair, or other good cause exists. If parts are unavailable,
they must be ordered promptly and the repair must be made within fifteen (15)
working days of receipt of the parts. If shutdown is required, the leak must be
repaired during the next scheduled shutdown. If delay is attributable to other
good cause, repairs must be completed within fifteen(15)working days after the
cause of delay ceases to exist
XVII.F.7.b. Within fifteen (15) working days of completion of a repair, the leak must be
remonitored to verify the repair was effective.
XVII.F.7.c. Leaks discovered pursuant to the leak detection methods of Section XVII.F.6.
shall not be subject to enforcement by the Division unless the owner or operator
fails to perform the required repairs in accordance with Section XVII.F.7.
AIRS ID: 123/9BAA Page 10 of 21
olor epa en P Ii ealth and Environment
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XVII.F.8. Rec in e or of e cility subject to the leak
detection and repair requirements in Section XVII.F. must maintain the following
records for a period of two (2) years and make them available to the Division
upon request.
XVII.F.8.a. Documentation of the initial approved instrument monitoring method
inspection for new well production facilities;
XVII.F.8.b. The date and site information for each inspection;
XVII.F.8.c. A list of the leaking components and the monitoring method(s) used to
determine the presence of the leak;
XVII.F.8.d. The date of first attempt to repair the leak and, if necessary, any additional
attempt to repair the leak;
XVII.F.8.e. The date the leak was repaired;
XVII.F.8.f. The delayed repair list, including the basis for placing leaks on the list;
XVII.F.8.g. The date the leak was remonitored to verify the effectiveness of the repair,
and the results of the remonitoring; and
XVII.F.8.h. A list of components that are designated as unsafe, difficult, or inaccessible
to monitor, as described in Section XVII.F.5., an explanation stating why the
component is so designated, and the plan for monitoring such component(s).
XVII.F.9. Reporting: The owner or operator of each facility subject to the leak detection
and repair requirements in Section XVII.F. must submit reports as specified in
Section XVII.F.9.
26. AIRS Point 007: Minor sources in designated nonattainment or attainment/maintenance
areas that are otherwise not exempt pursuant to Section II.D. of Regulation No. 3, Part
B, shall apply Reasonably Available Control Technology (RACT) for the pollutants for
which the area is nonattainment or attainment/maintenance (Reference: Regulation No.
3, Part B, III.D.2.a). Upon the compliance dated specified in Regulation No. 7, Section
XVII.F.4., the provisions of Section XVII.F. shall apply in lieu of RACT requirements
established pursuant to Regulation Number 3, Part B, Section III.D.2. This requirement
to apply RACT shall be satisfied by installing/implementing the following emission
controls:
a. Directed Inspection & Maintenance as described below shall satisfy the
requirement to apply RACT.
(i) Auditory/visual/olfactory inspection (AVO)will be performed on a semi-
annual basis. The first AVO inspection shall occur within one-hundred
and eighty(180)days after permit issuance.
(ii) For each leak found in the AVO inspection, a gas detector may be used
to determine the size of the leak. The gas detector shall be regularly
calibrated. Component leaks greater than 10,000 ppm shall be managed
in accordance with Item (vi)below, unless it is unfeasible to make the
repair without shutting down the affected operation of the facility.
Component leaks less than 10,000 ppm shall not require repair. For such
component leaks that require a shutdown to be repaired, repair shall
occur during the first shutdown of the affected operation after the leak is
discovered.
AIRS ID: 123/9BAA Page 11 of 21
ealth and Environment
Pollution Control Division
(iii) repaired will be dosed
if pla
e, minkni₹ing the volume released.
(iv) Fkepa%gd components shall be re-screened using AVO to determine if the
leak is repaired.
(v) The following records shall be maintained for a period of two years:
• The name of the site screened via AVO inspection and the
name of the inspector.
• Components evaluated with the gas detector.
• Repair methods applied.
• Dates of the AVO inspections, gas detector calibrations,
attempted repairs, successful repairs, repair delays, and post-
repair screenings.
(vi) Leaks shall be repaired as soon as practicable, but no later than 15
calendar days after detection, unless it is technically or operationally
infeasible to make the repair within 15 calendar days. Records
documenting the rationale shall be maintained if it is technically or
operationally infeasible to make the repair within 15 calendar days.
OPERATING&MAINTENANCE REQUIREMENTS
27. AIRS Points 003, 004, 008-011: Upon startup of these points, the owner or operator
shall follow the most recent operating and maintenance(O&M) plan and record keeping
format approved by the Division, in order to demonstrate compliance on an ongoing
basis with the requirements of this permit Revisions to your OW, plan are subject to
Division approval prior to implementation. (Reference: Regulation No. 3, Part B,Section
III.G.7,)
COMPLIANCE TESTRIG AND SAMPLING
Initial Testing Reauirements
28. AIRS Point 007:Within one hundred and eighty days(180)after Issuance of this permit,
the operator shall complete a hard count of components at the source and establish the
number of components that are operated in 'heavy liquid service", 'light liquid service',
"water/oil service" and "gas service". The operator shall submit the results to the
Division as part of the self-certification process to ensure compliance with emissions
limits.
29. AIRS Point 008:Within one hundred and eighty days(180)after issuance of this permit,
the owner or operator shall demonstrate compliance with opacity standards, using EPA
Method 9 to measure opacity from the flare when the flare is receiving gas from the
separator. (Reference: Regulation No. 1, Section II.A.1 &4)
Periodic retina ReauIrements
30. AIRS Point 007: On an annual basis,the owner or operator shall complete an extended
gas analysis of gas samples that are representative of volatile organic compounds
(VOC) and hazardous air pollutants (HAP)that may be released as fugitive emissions.
This extended gas analysis shall be used in the compliance demonstration as required in
the Emission Limits and Records section of this permit.
AIRS ID: 123/9BAA -. Page 12 of 21
epa en P li ealth and Environment
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ALTERNATE OPEDolor
31. AIRS Points 010 and 011: This pump may be replaced with a like-kind pump in
accordance with the requirements of Regulation 3, Part A, Section IV.A and without
I applying for a revision to this permit or obtaining a new construction permit. A like-kind
replacement pump shall be the same make, model and capacity as authorized in this
permit.
32. AIRS Points 010 and 011: The owner or operator shall maintain a log on-site or at a
local field office to contemporaneously record the start and stop dates of any pump
replacement, the manufacturer, model number, serial number and capacity of the
replacement pump.
33. AIRS Points 010 and 011: All pump replacements installed and operated per the
alternate operating scenarios authorized by this permit must comply with all terms and
conditions of this construction permit.
ADDITIONAL REQUIREMENTS
34. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation
No. 3, Part A, II.C)
a. Annually by April 30"' whenever a significant increase in emissions occurs as
follows:
For any criteria pollutant:
For sources emitting less than 100 tons per year, a change in actual emissions
of five(5)tons per year or more, above the level reported on the last APEN;or
For volatile organic compounds (VOC) and nitrogen oxides sources (NO,) in
ozone nonattainment areas emitting less than 100 tons of VOC or NO. per
year, a change in annual actual emissions of one(1)ton per year or more or five
percent,whichever is greater, above the level reported on the last APEN;or
For sources emitting 100 tons per year or more, a change in actual emissions
of five percent or 50 tons per year or more, whichever is less, above the level
reported on the last APEN submitted; or
For any non-criteria reportable pollutant:
If the emissions increase by 50% or five (5) tons per year, whichever is less,
above the level reported on the last APEN submitted to the Division.
b. Whenever there is a change in the owner or operator of any facility, process, or
activity; or
c. Whenever new control equipment is installed, or whenever a different type of
control equipment replaces an existing type of control equipment; or
d. Whenever a permit limitation must be modified;or
e. No later than 30 days before the existing APEN expires.
35. Federal regulatory program requirements (i.e. PSD, NANSR)shall apply to this source at
any such time that this source becomes major solely by virtue of a relaxation in any
permit condition. Any relaxation that increases the potential to emit above the applicable
Federal program threshold will require a full review of the source as though construction
AIRS ID: 123/9BAA Page 13 of 21
and Environment
f Pollution Control DMsion
had not yet not exceed the Federal
program threshold until a permit is granted. (Regulation No. Part D).
GENERAL TERMS AND CONDfitONS
36. This permit and any attachments must be retained and,made available for inspection
upon request. The permit may be reissued to a new owner by the APCD as provided In
AQCC Regulation No. 3, Part'B, Section 11.B upon a request for transfer of ownership
and the submittal of a revised APEN and the required fee.
37. If this permit specfdelly'states that final authorization has been granted, then the
remainder of this cordltlgh Is not applicable.Otherwise,the Ibeuance of this construction
permit does not provide liner$a for this activity oroperation of this source. Final
authorization of the permitrnu a secured from the APCO in writing in accordance with
the provisions of 257114.S(12Xa)C.R.S. and AQCC Regdation No. 3, Part B, Section
III.G. Final authorization cannot be granted until the operation or activity commences
and has been verified by the APCD as conforming in respects with the conditions of
the permit Once selfprWlca$on of all points has been reviewed and approved by the
DMsion, it will provide riMUstt doaanentation of such final authorization. Details for
obtaining final ai th.t n ;So operate are located in the Requirements to Self-
Certify for Final Authof4dg apctlon of this permit
•
38. This permit is issued in reliance upon the accuracy and completeness of information
supplied by the owner or and is conditioned upon conduct of the activity, or
construction, installation andoperation of the source, in acocrdence with this information
and with representations aowner or operator or puler or operator's agents.
It is valid only for the :aid operations or activity specifically identified on the
permit
39. Unless specifically stated othimmise,the general and specific conditions contained in this
permit have been determined byfhe APCD to be necessary to assure compliance with
the provisions of Section 2b-7414.9(7)(a),C.R.S.
40. Each and every condition of$1.permit is a material part hereof and is not severable.
My challenge to or appeal d*c onddition hereof shall constitute a rejection of the entire
permit and upon such ocptarerlce, this permit shall be deemed delved ate initio. This
permit may be revoked at any. ' , prior to self-certiflcatiogand final authorization by the
Air Pollution Control Division( CD) on grounds set forth in the Colorado Air Quality
Control Act and reguletions=otte Air Quality Control Commission (AQCC), including
failure to meet any=eigweetttenf) or condition of the permit If the Division denies a
permit, conditions imppopQ upgn a permit are contested by the owner or operator,or the
Division revokes a permit, thb twiner or operator of a source may request a hearing
before the AQCC for review of the Division's action.
41. Section 25-7-114.7(2Xa), C.R.S,requires that all sources required to file an Air Pollution
Emission Notice (APEN)must pay an annual fee to cover the costs of inspections and
administration. If a source cf dWity is to be discontinued, the owner must notify the
DMsion in writing requesting a cancellation of the permit. Upon notification, annual fee
billing will terminate.
42. Violation of the terms of a permit or of the provisions of the Colorado Air Pollution
Prevention and Control Act or the regulations of the AQCC may result in administrative,
civil or criminal enforcement actions under Sections 25-7-115 (enforcement), -121
(injunctions),-122(civil penalties),-122.1 (criminal penalties),C.R.S.
AIRS ID: 123/9BAA Page 14 of 21
olor epa en P Ii ealth and Environment
it Pollution Control Division
By:
Carissa Money
Permit Engineer
Permit History
Issuance Date Description
Issuance 1 This Issuance Issued to Bonanza Creek Energy Operating
Company, LLC
AIRS ID: 123/9BAA Page 15 of 21
D . r • • :� • = •< 7leafthlandEflvwonmeflt
ollution Control Division
Notes to Permit Holler :,
1) The permit holder is required to pay fees for the processing time for this permit.An invoice for these
fees will be issued after the permit is issued.The permit holder shall pay the invoice within 30 days of
receipt of the invoice. Failure to pay the invoice will result in revocation of this permit (Reference:
• Regulation No.3,Part A,Section VI.B.)
2) The production or raw material processing limits and emission limits contained in this permit are
based on the consumption rates requested in the permit application. These limits may be revised
upon request of the owner or operator providing there is no exceedance of any specific emission
control regulation or any ambient air quality standard. A revised air pollution emission notice(APEN)
and complete application form must be submitted with a request for a permit revision.
3) This source S subject to the Common Provisions Regulation Part II, Subpart E,Affirmative Defense
Provision for Excess Emissions During Malfunctions. The owner or operator shall notify the Division
. of any malfunction condition which causes a violation of any emission limit or limits stated in this
permit as soon as possible,but no later than noon of the next working day,followed by written notice
to the Division addressing all of the criteria set forth in Part II.E.1 of the Common Provisions
Regulation. See: 'jdtW/wow. .00v/cs/Satellife?c=Document C&childoaaename=CDPHE-
' Main%2FDocument C%2FCBONAdrllirmtView&cid=1251599389641&oaoename=BONWraooer
4) The foftov ing emissions of non-criteria reportable air pollutants are estimated based upon the
process limits as indicated in this permit. This information is listed to inform the operator of the
Division's analysis of the specific compounds emitted if the source(s)operate at the permitted
limitations.
Uncontrolled •
Emission Are the Controlled
MRS Rate emissions Emission Rats
Point Pollutant CAS 0 (IbhR) reportable? Pry►) '
Benzene 71432 3,348 Yes 167
n-Hexane 110543 19,752 Yes 988
Toluene 108883 2,254 Yes 113
003 Ethylbenzene 100414 185 No 9
Xylenes 1330207 672 Yes 34
2ylperdene 540841 938 Yes 47
UirtneUnylp
Benzene 71432 2,208 Yes 110
004
n-Hexane 110543 6,938 Yes 347
Benzene 71432 1,051 Yes 1,051
n-Hexane 110543 5,509 Yes 5,509
Toluene 108883 2,590 Yes 2,590
006 Ethylbenzene 100414 656 Yes 656
Xylenes 1330207 2,769 Yes 2,769
2'2'4 640841 775 --Yes 775
trimethylpentane
Benzene 71432 331 Yes 331
007
n-Hexane 110543 1,679 Yes 1,679
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Top 702
Ethylbenzene 100414 174 No 174
Xylenes 1330207 721 Yes 721
Benzene 71432 300 Yes 15
n-Hexane 110543 1,733 Yes 87
008 Toluene 108883 235 No 12
Ethylbenzene 100414 32 No 2
Xylenes 1330207 90 No 5
Benzene 71432 2,541 Yes 45
n-Hexane 110543 15,228 Yes 267
009 Toluene 108883 1,687 YeS 30
Ethylbenzene 100414 203 No 4
Xylenes 1330207 386 Yes 7
Benzene 71432 181 No 9
n-Hexane 110543 1,047 Yes 52
010 Toluene 108883 142 No 7
Ethylbenzene 100414 19 No 1
Xylenes 1330207 55 No 3
Benzene 71432 181 No 9
n-Hexane 110543 1,047 Yes 52
011 Toluene 108883 142 No 7
Ethylbenzene 100414 19 No 1
Xylenes 1330207 55 No 3
5) The emission levels contained in this permit are based on the following emission factors:
Point 003:
Emission Factors Emission Factors
Uncontrolled Controlled
Pollutant lb/BBL lb/BBL Source
Condensate Condensate
Throughput Throughput
VOC 2.1248 0.1062 _ E&P TANK
n-Hexane 0.0791 0.0040 E&P TANK
Benzene 0.0134 0.0007 E&P TANK
Toluene 0.0090 0.0005 E&P TANK
Ethylbenzene 0.0007 0.00004 E&P TANK
Xylenes 0.0027 0.0001 E&P TANK
2,2,4- 0.0038 0.0002 E&P TANK
trimethylpentane ,
AIRS ID: 123/9BAA Page 17 of 21
earth and Environment
Pollution Control Division
Note: The on control efficiency of 95%.A
HHV of 2,326 was used for combustion calculations.
Point 004: Emission-Factors Emission Factors
Uncontrolled Controlled
Pollutant IbWSBL Produced IbIBBL Produced Source
Water'Throughput Water Throughput
VOC 0.262 0.0131 CDPHE
n-Hexane 0.022 0.0011 CDPHE
Benzene 0.007 0.0004 CDPHE
Note: The controlled emissions for this point are based on the flare control efficiency of 95%.
Point 006:
on Factors-
led
Pollutant ed Source
VOC ""i{' Wad
edAP-42
Benzene .0042 AP-42
n4lexane 0.0221 AP-42
Toluene -0:0104 AP-42
EIftylbenzene 0.0026 AP-42
Xylenes 0.0111 AP-42
2,2,4- 0.0031 AP-42
trime0rylpentane
The uncontrolled VOC emission factor was calculated using AP-42, Chapter 5.2, Equation 1
(version 1/95)using theiobwing values:
L=12.46'S'P'M/T
S=0.6(Submerged loading:dedicated normal service)
P(true vapor pressure)=5.77 psia
M(vapor molecular weight)=68 lb/lb-mol
T(temperature of liquid loaded)=524 R
The uncontrolled noncriMria reportable air pollutant(NCRP)emission factors were calculated by
multiplying the mass fraction of each NCRP in the stable condensate by the VOC emission factor.
Point 007:
Component Gas Heavy Oil Light Oil Water/oll
Connectors 2663 0 1177 1003
Ranges 121 0 32 40
Open-ended Lines 79 0 12 4
Pump Seals 6 0 0 2 4
Valves - 386 0 150 111
Other 190 0 18 40
VOC Content(wt. 0.2476 1 0.9938 1
fraction)
Benzene Content{wL 0.000586 0 0.0t79 0.0012
Toluene Content(wt. 0.00046 0 0.0441 0.0003
AIRS ID: 123/9BAA Page 18 of 21
olor epa en P li ealth and Environment
it Pollution Control Division
fraction)
Ethylbenzene(wt. 0.000062 0 0.0112 0.0001
fraction)
Xylenes Content(wt" 0.000176 0 0.0471 0.0001
fraction)
-
n-hexane Content(wt. 0.003392 0 0.0938 0.0001
fraction)
`Other equipment type includes compressors, pressure relief valves, relief valves, diaphragms,
drains, dump arms,hatches,instrument meters, polish rods and vents
TOC Emission Factors(kg/hr-component):
Component Gas Service Heavy Oil Light Oil Weser/Oil
Service
Connectors 2.0E-04 7.5E-06 2.1E-04 1.1E-04
Flanges 3.9E-04 3.9E-07 1.1E-04 2.9E-06
Open-ended Lines 2.0E-03 1.4E-04 1.4E-03 2.5E-04
Pump Seals 2.4E-03 NA 1.3E-02 2.4E-05
Valves 4.5E-03 8.4E-06 2.5E-03 9.8E-05
Other 8.8E-03 3.2E-05 7.5E-03 1.4E-02
Source: EPA-453/R-95-017 Table 2-4
Compliance with emissions limits in this permit will be demonstrated by using the TOC emission
factors listed in the table above with representative component counts, multiplied by the VOC content
from the most recent extended gas analysis.
Point 008:
Weight Emission Emission
Pollutant Fraction of Factors Factors Source
Gas(%) Uncontrolled Controlled
lb/MMscf lb/MMscf
NOx -- 0.068 0.068 AP-42
(lb/MMBTU)
CO(Ib/MMBTU) — 0.37 0.37 AP-42
VOC 24.8 14,568 728.42 Gas Analysis
Benzene 0.06 34.422 1.7211 Gas Analysis
Toluene 0.05 26.989 1.3494 Gas Analysis
Ethylbenzene 0.01 3.6417 0.1821 Gas Analysis
Xylenes 0.02 10.365 0.5183 Gas Analysis
n-hexane 0.34 199.19 9.9596 Gas Analysis
Emission factors for CO and NOx found in AP-42 Table 13.5-1. A HHV of 1,283 BTU/scf was used
for calculations.
Point 009:
Weight Emission
Pollutant Fraction of Factors Source
Gas(%) Uncontrolled
lb/MMscf
AIRS ID: 123/9BAA Page 19 of 21
ea(th and Environment
Pollution Control Division
Pollutant Fraction of Factors Source
Gat(%) Uncontrolled
IblWlsof
NOx 0.068 AP-42
(Ib/MMBTU) —
CO 0.37 AP-42
(Ib/MMBTU)
VOC 56.7 49,639 Gas Analysis
Benzene 0.12 105.12 Gas Analysis
Toluene 0.08 69.781 Gas Analysis
Ethylbenzene 0.01 8.404 Gas Analysis
Xylenes 0.02 15.968 Gas Analysis
n-hexane 0.72 630.09 Gas Analysis
Note: The uncontrolled VOC and HAP emissions were calculated using a gas sample collided
9/11/2013 of the gas vented from the low pressure separator at State Antelope J-F-28HNB to
estimate the VOC and HAP content of the stream and a Promax model to estimate stream flow.
Actual controlled VOC and HAP emissions shall be calculated based on actual VRU operating time,a
control efficiency of 100%during VRU uptime,and a flare control efficiency of 95%during VRU
downtime.
Emission factors for CO and NOx are based do AP-42 Table 13.5-1. A HHV of 1,895 BTU/scf was
used for calculations.
Points 010 and 011:
Emission Emission
Factors- Factors-
Uncontrolled Controlled
Pollutant IblMMni vented IbMMscf vented Source
NOx 0.068 0.068 AP-42
(D/MMBTU)
CO 0.37 0.37 AP-42
Ib/MMBTU)
VOC 14,568 728.42 Gas Analysis
Benzene 34.422 1.7211 Gas Analysis
Toluene 26.989 1.3494 Gas Analysis
Ethylbenzene- 3.8417 0.1821 Gas Analysis
Xylenes 10.365 0.5183 Gas Analysis
n-hexane 199.19 9.9596 Gas Analysis
The displacement equation can found in'EPA Emission Inventory Improvement Program Publication:
Volume II,Chapter 10-Displacement Equation(10.4-3)."
Emission factors for CO and NOx found in AP-42 Table 13.5-1. A HHV of 1,283 BTU/sd was used
for combustion calculations.
6) In accordance with C.RS. 25-7-114.1, each Air Pollutant Emission Notice (APEN) associated with
this permit is valid for a term of five years from the date it was received,by the Division. A revised
APEN shal be submitted no later than 30 days before the five-year term expires. Please refer to the
most recent annual fee invoice to determine the APEN expiration date for each emissions point
associated with this permit. For any questions regarding a specific expiration date call the Division at
(303)-692-3150.
7) This facility is classified as follows:
•
AIRS ID: 123/9BAA Page 20 of 21
' olor. 1 eepa en P •li ealth and Environment
it Pollution Control Division
Applicable Status
Requirement
Operating Permit Synthetic Minor Source of:
VOC, HAPs
NANSR Synthetic Minor Source of
VOC
MACT HH Major Source Requirements: Not Applicable
Area Source Requirements: Not Applicable
8) Full text of the Title 40, Protection of Environment Electronic Code of Federal Regulations can be
found at the website listed below:
http://ecfr.gPoaccess.gov/
Part 60: Standards of Performance for New Stationary Sources
NSPS 60.1-End Subpart A—Subpart KKKK
NSPS Part 60,Appendixes Appendix A—Appendix I
Part 63: National Emission Standards for Hazardous Air Pollutants for Source Categories
MACT 63.1-63.599 SubpartA—SubpartZ
MACT 63.600-63.1199 Subpart AA—Subpart DDD
MACT 63.1200-63.1439 Subpart EEE—Subpart PPP
MACT 63.1440-63.6175 Subpart QQQ—Subpart YYYY
MACT 63.6580-63.8830 Subpart 7777—Subpart MMMMM
MACT 63.8980-End Subpart NNNNN—Subpart XXXXXX
9) A self certification form and guidance on how to self-certify compliance as required by this permit may
be obtained online at: htto://www.colorado.nov/pacific/cdphe/air-permit-self-certification
AIRS ID: 123/9BAA Page 21 of 21
Division Information
Engineer: Carissa Money
Control Engineer: NA
Review Date: 10/14/2014
Application Date: 10/07/2013
Facility Identifiers
Permit No. 13W E2810
AIRS County# 123 Weld
Facility 9BAA
Facility Type:exploration and production facility
17 Located In the 8-hour nn-attainment area? 0 True Minor
O Synthetic Minn for: F voc r Nox r co
Administrative Information
Company Name: Bonanza Creek Energy Operating Company,LLC
Source Name: Antelope J-28 Production Facility
Source Location: SWSW Section 28,Township 5N,Range 62W
SIC: 1311
Mailing Address 1: Bonanza Creek Energy Operating Company,LLC
Address Address 2: 410 17th Street,Suite 1500
/,State Zip: Denver,CO 80202
Name: Peg Young
Person To Phone: 720-440-6133
Contact Fax: 720-279-2331
Email: pvoung@bonanzacrk.com
'Requested Action
Self Certification Required? Yes
Issuance Number: 1
Source Description:
Oil and gas exploration and production facility known as the Antelope J-28 Production Facility,located in the SWSW
Section 28,Township 5N,Range 62W,Weld County,Colorado.
Point Name Type Control Action
Newly
003 Tanks Condensate Tanks Flare
reported
Newly
004 PW Tanks Water Tanks Flare
reported
006 Truck Newly
Loadout None
Loadout reported
Newly
007 FUG Fugitives None reported
008 Flare Separator Venting Flare Newly This is an emergency flare used
reported when pipeline not available
Newly Low pressure separators
009 LP Sep 1-4 Separator Venting Flare reported controlled by VRU and enclosed
Newly
010 Pump 1 Pump Flare reported
Newly
011 Pump 2 Pump Flare reported
r "raa.,T. ^TwahA er44 r'""F "^-
003 Twelve(12)500 bbl above ground atmospheric condensate storage tanks controlled by ten t
LResusted Throughput 249660 bbl
Control 'Flare
Efficiency I 95.0096)
Emissions Summary Table
Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source
VOC 2.1248 lb/bbi 265.2 tpy - 133 tray ESP TANK
Benzene 0.0134 lb/bbl 3348 lb/yr 167 Ib/yr ESP TANK
n-Hexane 0.0791 Ib/bbi 19752 lb/yr 988 lb/yr - , ESP TANK
Toluene 0.0090 lb/6bl 2254 lb/yr 113 Ib/yr E&P TANK
EB 0.0007 lb/bbl -185 Ib✓yr 9 Ib/yr E&P TANK
Kylene 0.0027 lb/bbl 672 lb/yr 34 lb/yr E&P TANK
2,2,4TMP 0.0038 lb/bbl 938 lb/yr 47 Ib/yr ER TANK
Nat 0.068 lb/Mmbtu 0.6 tpy 0.6 tpy AP-42 Table 1
CO - 0.37 lb/Mmbtu 3.1 tpy 3.1 tpy AP-42 Table 1
Regulatory Review
Section BA1-Except as provided In paragraphs 2 trough 6 below,no owner or operator of a source shall
allow or cause the emission into the abnosphere of any ale pollutant Mulch Is in excess @120%opacity.This
standard Is based on 24 consecutive opacity renew then at 15-second Intervals for six minutes.The
approved reference test method for visible emissions meeswenent Is EPA Method 9(40 CFR,Pan 60,
Appendix A(July,1992))in all subsections of Section II.A and B of this regulation.
Section 845-Smokeless Flare or Flares for the Combustion of Waste Gases No owner or operator of a
smokeless tare or other flare for the combustion of lute gases sisal allow or cause emissions kite the
atmosphere of any*pollutant which S In excess of 30%opacity for a period or periods aggregating more
than sot minutes In any sixty consecutive minutes.
Section IA-No person,wherever located,shall cause a allow the emission of odorous ale contaminants
from any single source such as to result In detectable odors which are measured lo excess of the followkq
limits: For areas used predominantly for residents or eomanerUel purposes It is a violation if odors are
detected after the odorous air has been d*rted wIth seven(7)or more volumes of odor free S.
NSPS Kb: for storage vessels greater than 19,000 gallon after 7123164.
The 500 bbl tanks are above the minimum capacity threshold of-471 bbl.However,the tanks are located at
the wellhead site,store condensate,and are prior to custody transfer,thus,the tanks are exempt from NSPS
Kb(60.110b(dX4)).
NSPS 0000:for storage vessels in the natural gas production,transmission,and processing
*mend.
This source is not subject because each tank emits less than 6 tray VOC.
k,. of i"P' ,'s.. "aIftrA}WW140044,3%
XII.VOLATILE ORGANIC COMPOUND EMISSIONS FROM OIL AND GAS OPERATIONS
Applicant la subtlest to fat emission control rpuYunatte for condensate tanks since it b located In
the namlfabpMntwee.
XVII.C STATEWIDE CONTROLS FOR OIL AND GAS OPERATIONS
Applicant it currently subject to this sloes actual uncontrolled emissions are greater than 20 tray of
VOC and actual unconf oarl omissions we greater than I Spy.
13WE2810.CP1 . 123/9BAA
004 Four(4)400 bbl above ground atmospheric produced water storage tanks controller
Emissions Calculations
Requsted Throughput 315360 bbl
Control Flare
Efficiency 95.00%
Emissions Summary Table
Pollutant Emission Factor Uncontrolled Emissions Controlled Emissions Source
VOC 0.262 lb/bbl 41.3 tpy 2.1 tpy CDPHE
Benzene 0.007 lb/bbl 2208 lb/yr 110.4 lb/yr CDPHE
n-Hexane 0.022 lb/bbl 6938 lb/yr 346.9 lb/yr CDPHE
Pollutant Controlled Emission Factor
VOC 0.0131 lb/bbl
Benzene 0.00035 lb/bbl
n-Hexane 0.0011 lb/bbl
Regulatory Review
Section II.A.1 -Except as provided in paragraphs 2 through 6 below, no owner or operator of a
source shall allow or cause the emission into the atmosphere of any air pollutant which is in excess
of 20%opacity.This standard is based on 24 consecutive opacity readings taken at 15-second
intervals for six minutes.The approved reference test method for visible emissions measurement is
EPA Method 9(40 CFR,Part 60,Appendix A(July, 1992))in all subsections of Section II.A and B of
this regulation.
Section ll.A.5-Smokeless Flare or Flares for the Combustion of Waste Gases No owner or operator
of a smokeless flare or other flare for the combustion of waste gases shall allow or cause emissions
into the atmosphere of any air pollutant which is in excess of 30%opacity for a period or periods
aggregating more than six minutes in any sixty consecutive minutes.
Regulation 2—Odor
Section IA-No person,wherever located,shall cause or allow the emission of odorous air
contaminants from any single source such as to result in detectable odors which are measured in
excess of the following limits: For areas used predominantly for residential or commercial purposes it
is a violation if odors are detected after the odorous air has been diluted with seven(7)or more
volumes of odor free air.
Reaulation 7—Volatile Organic Compounds
XVII.C.1.b
Applicant is subject since actual uncontrolled emissions are greater than 6 tpy.
13WE2810.CP1 123/9BAA
1008 ITruck Condensate Loadout
Calculations
L=12.46'S•P•M/T(AP-42:Chapter 5.2,Equation 1)
L=loading losses In lb per 1000 gallons loaded
Factor Meaning Value Units Source
S Saturation Factor 0.6 AP-42
P True Vapor Pressure - 5.77 psis Sales ON Analysis documenting RVP 7.9 and AP-
Molecular Weight of Va; 68 lb/lb-mole Sales oil analysis for RVP 7.9 and values from Al
T Liquid Temperature 523.67 deg.R EPA Tanks Met Data for Denver,CO
L 5.60 lb/10^3 gal
2.35E-01 lb/bbl
Annual requested Throughput 249660 BBL/yr
10485720 gal/yr
Annual requested VOC emissions 58735 lb/yr
29.37 tpy
Control: None
Efficiency: 0.00%
NCRN
Component Mass Fraction
Benzene 0.0179
n-hexane 0.0938
oluene 0.0441
EB 0.0112
Xylenes 0.0471
2,2,4-IMP 0.0132
Source: Pressurized oil analysis
Emissions Summary Table
Pollutant Emission Factor Uncontrolled EmissionsCorarolled Emissions Source
VOC 0.2353 lb/bbl 29.4 tpy _ 29.4 tpy AP-42
Benzene 0.0042 lb/bbl 1051 lb/yr 1051 lb/yr AP-42
n-Hexane 0.0221 lb/bbl 5509 lb/yr 5509 lb/yr AP-42,
Toluene 0.0104 lb/bbl 2590 lb/yr 2590 lb/yr AP-42
EB 0.0026 lb/bbl 656 lb/yr 656 lb/yr AP-42
Xylenes 0.0111 lb/bbl 2769 lb/yr 2769 lb/yr AP-42
2,2,4-IMP - 0.0031 lb/bbl 775 lb/yr 775 lb/yr AP-42
Regulatory Review
h• a sx�<, y s 'r1/ ;IP'- ' ,@,g.2sY�. vz ,.. @₹;' 'c
This facility is not considered a bulk plant(In Reg.7)because It does not distribute gasoline.
13WE2810.CP1 123/9BAA
•
007 FugeM VOC equipment leaks
Regale/Coo 7 Inbrms08n
Operating Hon 8760 hours/year
Emission Factor Source EPAdSVR-05-017 Table 2-4
Corte!Efficiency Source'. None
Calculations
Emission Factor(kglbr- Emissions
Sane Componsm Type Countsource) Control(%)Pollutant Maas Fraction (spy)
Table 24 Table 24 Rag.3
Connectors 2663 2.03E-0i 1.00E-05 00% VOC 02476 99260734
Flanges 121 3.90E-0i 5.70E-06 0.0% Benzene 0.000586 0023497
Coen-Ended Lines 79 2.00E-03 1.50E-05 0 0.000460% Toluene 00.0004600184447
Gas
Pump Seals 6 2.40E-03 3.50E-04 0.0% Elsylbemmne 0.000062 0.002486
Valves 386 4.50E-03 2.50E-055 00% %yienes 0000176 00070571
Other 190 800E-03 1.20E-04 0.0% n-Hexane 0.003392 0.1360098
Connectors 0 7.50E-00 7.50E-06 0.0% VOC 1
Flanges 0 3.90E-07 3.90E-07 0.0% Benzene
Heavy Oil Open-Ended Lines 0 140E-0i 7.20E-06 0.0% Toluene
Pump Seals 0 000E400 0.COE+3 0.0% Eth4benzene
Valves 0 0.40E-06 0.40E-06 0.0% Xylenee
Other 0 3.20E-05 3.20E-05 0.0% n-Heeana
Connectors 1177 2.10E-04 7.50E-06 00% VOC 0.9930 7.445443
Flanges 32 1.10E-04 2A0E-06 00% Benzene 0.0179 0.134104
Light GI Open-Ended Lines 12 1.40E-03 1.40E-05 0.0% Toluene0.0441 0.330392
Pump Seals 0 1.30E-02 5.10E-04 00% E8rylhenzene 0.0112 0083900
Valves 150 2.50E-03 1.90E-05 0.0% Xylenes 0.0471 0.352868
Other 18 7.50E-03 1.10E{H 0.0% mHezane 00938 07027396
Connectors 1068 1.10E-04 1.00E-05 0.0% VOC 1 66489556
Flanges 40 2.90E-06 2.90E-06 0.0% Benzene 0.0012 00079787
WatedOil Open-EMod Lines 4 2.50E-04 3.50E-06 0.0% Toluene 0.0003 00019947
Pump Seals 2 2.40E-05 2.40E-05 0.0% Elhylhenzene 0.0001 00008649
Valves 116 9.80E-05 9.70E-06 0.0% XyMres 0.0001 00008649
Other 40 1.40E-02 5.90E-05 0.0% nHenane 0.0001 00008649
Fmleslcns Summary Table
Pollutant Uncontrolled Emissions Controlled Emissions Source Ipy
VOC 24.02 tpv 24.021py EPA-453/R-95-017 Table 2-4
Benzene 331.181044 331.161Wyr EPAIS.YR-95-017 Table 2-4 017
Toluene 70168 lb* 701.86 lb/yr EPA4531R-95-017 Table 24 035
ENylbenzene 174.121644 174.12 lb/yr EPA4531R-95-017 Table 2-4 000
Xylenas 721.18 Ibis 721.16 lb/yr EPA453/R-95-017 Table 24 0.36
nllezene 167083 Iblyr 1678.83 lb/yr EPA.453/R-95017 Table 24 0.00
Regulatory Appllubllity
3 The dale of Interest for determining nether the source is nee or modified is therefore November 20,2007(the date of
the 0-tour one NA area designation).Since the site yips built eller the date above topemhon began 101261120131.
this source is considered nee or rnodhled2 Cpemhr has agreed on the Divisions standard conditions. 1
VOC and HAP cmcenlntbns for gas service are based on sales gas sample collected 8/26120 1 3 frail Stale PmelopeN
F-20HNB.Since sitespecirc and Whin 1 year of application dale,no Initial sampling required. I
•
13WE2810CP1 123/98M
•
One emergent/flan with a minimum combustion stridency of 95%. The Bars is not enclosed.Thy emergency here is
008 - used during periods Ann the pipette is not avallabis.
EatlpnrM Daeriptlon
This some vents natural gas bon: a wed heed separator sten the Ides gas pipelne Is not available or during emergencies
Emissions from this source are: routed batiste
(wad pas venting nominal heed sprat Wien the sees pas paeans Is not aralabe or dultp emend nds.EmisWm from this source m routed to •
CY6Wa6ats .
EPA Erasion ewenbry unnamed Program Ptlblcadon:Volume II,Chapter 10-Displacement Equation(10.4-3)
Ex•O•MW•Xx/C
Ex.;missions d potent x
Va - .
0 Q. anab flow rdNvdane d gas processed
MW Mohairweiga of gas SO of gas•MW dal
Xx•awe fradion nix In gas
C•molar volume of Ideal gas(379 sdt-ntal)at 60F and 1 urn
Ifhgglpna{0) � , star
2231b4nwl 10o079MR Mwc9d
male% MW eaand mew Radio. bar Wm toy
Hebn 0.01 4.0028 0.000 0.000 000 9.19 0.00
CO2 2.19 44.01 0.964 0.043 2.53 22124.61 11.08
N2 083 28.013 0233 0.010 081 533725 2.87
mean. 7396 16041 11813 0.532 3180 272310.03 13016
Barr 12.21 -30.063 3.872 0.185 962 5420302 42.15
propene / 7.10 44.092 8.124 0.140 870 71837.53 3592
Nebtlre. 0.83 58.118 0.389 0.017 007 547025 4.24
n-b is a 1.87 58.118 1809 0.040 2.85 25109.17 1250
leapsbte 0.32 72114 0227 0810 0.60 8210.44' 281
npesWts 040 72114 0.789 0.013 0.78 8838.45 322
agbpeSans 0.03 7013 0.022 0001 -006 507.10 0.23
n-exre 089 88.18 0.075 0.0394 020 173207 0.87
pydohsxrne 0.02 84.18 0.019 0.001 0.05 444.34 022
Other hexane 015 8818 0.175 0.006 0.33 208828 ' 1.44
tneatsra 0.07 10321 0.075 0.003 020 1720.65 0.85
ntwak'dolexre 0.02 9819 0018 0.001 0.06 407.97' 0.20
224-TAP 0.00 11423 0000 0500 moor 262 0.00
Brame 002 78,12 0.013„ 0.00050 0.0342 249.47 0.15
Tales 001 92.15 0010 000048 0.09 ' 23480 012
Earibwme 0.01 man 0.001 oalese 030 flee 002
%Pees 0.00 10817 0.004 0.00018 001 90.17 0.05
08+Heavies 0.05 118 0.063 0802 014 121157 861
VOC mass nee 0.2478 Tabs VOC(Uncontrolled) 8337
thalt
Mole
Mae%,MW,and mar fractions are based on saes gas analysis crawled 8126/2013 from State Antelope J-F-28HNB
Emissions are based an 8760 hours of operation per year. -
Assumed average MW of C8+is 116
•
•
13WE2a10.CP1 - 123/9954
Flaring Information
Equipment Description
Flare to combust produced gas until pipeline is available at this wellhead facility.
Mamdadurer Weatherford
Model Candlestick
Serial Number TBD
Gas Heating Value 1283_Btu/scf
Trrgtlput 11162.1 MMBtu/yr
VRU Information•NOT APPLICABLE
Equipment Description
Make
Modal
Requested Control 100.00%
Annual Bypass Ti 0.00%
Backup Flare
Overal Control 95.00%
Combustion emission factor source: APA2:Chapter 13.5
0.07 lib NOX/MMBtu 0.37 Ilb CO/MMBtu
Emissions Summary Table
Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions source
VOC 14568 lb/MMsd 728.42 lb/MMscf 63.4 toy 3.2 tpy Gas Analysis
Nom 0.07 Ib/MMBTU 0.07 Ib/MMBTU 0.38 tpy 0.38 spy AP-42
CO 0.37 lb/MMBTU 0.37 Ib/MMBTU 2.06 spy 2.06 tpy AP-42
Benzene 34.4223 lb/MMscf 1.7211 lb/rAMscf 299 lb/yr 15 lb/yr Gas Analysis
n-Hexane 199.1918 lb/MMscf 9.9596 lb/MMscf 1733 lb/yr 87 lb/yr Gas Analysis
Toluene 26.989 lb/MMscf 1.3494 lb/MMscf 235 lb/yr 12 lb/yr Gas Analysis
Xylenes 10.365 lb/MMscf 0.5182 lb/MMsd 90 lb/yr 5 lb/yr Gas Analysis
Ethylbenzene 3.6417 lb/MMscf 0.18211b/MMsd 32 lb/yr 2 lb/yr Gas Analysis
Regulatory Applicability
AOCC Regulation 1
This source is subject to the opacity requirements for flares in Section IIA.5:'No owner or operator of a smokeless flare or
other flare for the combustion of waste gases shal alcw or cause emissions into the atmosphere of any air polutant which is
in excess of 30%opacity.'
AOCC Regulation 9
Section I.A applies to all emission sources."No person,wherever located,shall cause or allow the emission of odorous air
contaminants from any single source such as to result In delectable odors which are measured In excess of the following
limits: For areas used predominantly for residential or commercial purposes It is a violation if odors are detected after the
odorous air has been diluted with seven(7)or more volumes of odor free air.'
13WE2810.CP1 123/9aAA
Fez kwpa.ue sepsis by•VRU end WA embed 0ers.Esdl lls.lies■niSmm
009 corntsdon eMds11Cy of 90%. ,
Equipment Daa.IpSan
1Ftesos.wile, .o O.from: as..Mad seminar
Brien Ian It mourn are raaarp..4
Nei.*on w•Yy Dm..•wM heed seoaala.EmOcra from tli...A.oang..M.
Calciallam
EWINSILIAGONSISOLI
EPA Embalm beets Improvement Program Pu..On:Volume 0,Ch.gr 10-OYOY.nwd EgiSon(10.44)
EzaQ•MW•XX/C _
Ex•.d.4m of pates•z
Q a ValnrMokw r.t&volns of g.grossed
MW•Mol.adrrnlpnt does SQafgm•MW 0.f*
Xa•new fradlon of it M gee
CC ammolar volume of SS 0. lb(379 ed mol)at OOF aid 1 elm
lF -,
mete% WW Itabealinefeallan tit RS _q Wv
Haan 0.00 4.0026 0.0 0.00 zit 0.00
CO2 231 44.01 1.1d 9000 SAM 732000 36.5
112 0.11 25.013 0.001 - or 0.22. . 156.5 093
mats 30.48 10.481 535 : -':'0.170 4248 37200721 190.00
sin 2434 30.048 7.311 _ ...0220 0322 400234.04 233.12
pasta 2231 44.002 10.039 0.303 7372 "04142748 320.71
teoa•sa 2.37 5.119 1.376 '0041 1001 97172.39 4836
*bare 77s 33119 4.215✓ .0.127 30.5 266047.42 13442
Less. 1.19 72.114 0.56 0.029 45 545730 27.30
nOrsa 1200 72114 1348 0.032 7.75 957= 3394
cockers - 0.11 70.13 0.075 .0002 0.5 4507.44 - 240 .
efts. 079 516 0730 .....00072 1.74 15276.05 731
catalyse 037 ale OAP 095 OA 3761.32 1.5
O5Show 049 6615 0.411 0.012 2.5 251335 13.11
Harass 071 10021 0210 0.05 100 134550 6.70 '
MalWee ots.s 0.06 519 0.05 .0301 0S 319976 1.5
324.1W 000 11423 0.000 X000000 0.04 75 '0.00
Bowan 0,05 7612 029 SOW 127
7a5r1a + 00} 92A5 0360 L :,''$005 0.197 16547 034
5aeraara MOO 1e.17 0.53 00001 0100 inn 010
Xelme 0.01 1517 0.05 0402 004- 355 0.19
CS.Haan. 011 1166 0.126_ SW 0.5 7972.. 3.91
5200 VOC mem.ac 0307 for VOC(UKaa..) 5005
$d5
.. , I %.Mw.aid pin tadna a. .d on LP.ep.a.weensyte atsdsd9/112013 has Ste Aaerpe J.F-2&IN9(Ws-speak sr no•5.s.
Emteabs re Sedan 5700 has of operation p.mfr.
Assumed weeps MW of CM le 1165
133/22310.211 223/9948
Flaring Information
Equipment Description
Flare to combust uced gas until pi ne is available at this wethead tacitly.
Manufacturer Lead
Model L30-0100
Serial Number 20734,20732,20679,20677,20733,20731.20680,20678,20937,20938
Gas Heating Value 1895 Bhr/sd
Throughput 29768.934 MMBIWyr
VRU Information
Equipment Description
Engine to recompress gas to sales tne.
Make Ga4J�
Model GJ230,48 hp
Requested Control 100.00%
Annual Bypass nm 35.00%
Backup Flare
Overal Control 98.25%
Combustion emission factor source: AP-42:Chapter 13.5
0.07 lb NOX/MMBtu 0.37 lib CO/MMBtu
Emissions Summary Table
Pollutant Uncontrolled Emission Factor Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source
VOC 49640 lb/MMsd 868.70 lb/MMscf 599.85 spy 10.50 tpy Gas Analysis
Nor 0.07 lb/MMBTU 0.07 Ib/MMBTU 1.01 WY 1.01 tpy AP-42
CO 0.37 lb/MMBTU 0.37 ls/MMBTU 5.51 tpy 5.51 tpy AP-42
Benzene 105.12 lb/MMsd 1.8396 lb/MMscf 2540.59 lb/yr 44.46 lb/yr Gas Analysis
n-Hexane 630.09 lb/MMscf 11.027 lb/MMscf 15228.06 lbhr 266.49 lb/yr Gas Analysis
Toluene 69.781 lb/MMscf 1.2212 lb/MMscf 1686.47 lb/yr 29.51 lb/yr Gas Analysis
Xylenes 15.968 lb/MMscf 0.279416/MMsd 385.90 lb/yr 6.75 lb/yr Gas Analysis
Ethylbenzene 8.4040 lb/MMscf 0,1471 lb/MMscf 203.11 lb/w 3.55 lb/yr Gas Analysis
Regulatory Applicability
AOCC Regulation 1
This source Is subject to the opacity requirements for flares in Section IIA.5:'No owner or operator of a smokeless flare or
other flare for the combuston of waste gases sisal alow or cause emissions into the atmosphere of any air pollutant which is
in excess of 30%opacity.'
AOCC Regulation 2
Section IA applies to all emission sources."No person,wherever located,shall cause or allow the emission of odorous air
contaminants from any single source such as to result in delectable odors which are measured in excess of the following
limits: Far areas used predominantly for residential or commercial purposes it is a violation if odors are detected after the
odorous air has been diluted with seven(7)or more volumes of odor free air."
13WE2810.CP1 123/980
One(1)pneumatic S transfer pump,rated at 600 soehr(Sandpiper. _
Model t31F,Serial number 2001507).Tha pnewnfc pump Is controlled by
010 an enclosed flare with a n*taan combustion aeicencyof 95%.
Pump Information
Manufactur Sandpiper
Model
Number.OW
Serial
Pump Number.2091567 Information
Pump
Pump
rapidly 9.1 pions per minute pumped
mural gas 600 . sd/lwwwed
consumpeb
Control Flare 95. Efiklency
Calculations
EPA Emission Inventory Improvement Program Publutlon:Volume II,Chapter 10-Displacement Equation(10.4-3)
Ex=Q=MW=Xx/C
Ex=emissions of pollutant x
Q=Volumetric flow rate/volume ofgas processed
MW=Molecular walght of gas=SG of gas a MW of air
Xx=mass fraction of x In gas
C a molar volume Sided gas(379 scf/lb-mol)at 60F and 1 aun
Q as scf/hr
MW 213 W/Ib-mof
Hondop. 8710 hanS. Requested Throughput 5256 MMscf/yr
Component mole% MW mass fraction Component Mr W/yr In
CO2 ' 2.19 44 0.0432 CO2 1525 13363276 6982 '
nitrogen 0.83 28 0.0104 nitrogen 0.368 3222.940 1.611
. methane 73.96 16.04 05319 methane 18.779 161502.562 , 82251
ethane 1221 30.07 0.1647 ethane 5.815 50936.458 25.468
propane 7.10 44.09 0.1403 propane 4954 43397205 21.699
laobutane 0.83 58.12 0.0165 Itobutane 0.584 5117.373 2559
n-butane 1.87 58.12 0.0489 n-butane 1.725 15109309 7555
isopentane 0.32 72.15 0.0102 Isopentane 0.360 3154.834 1.577
n-pentane 0.40 72.15 0.0130 n-pentane 0.458 4011.331 2.006
cydopentanti 0.03 70.15 0.0010 cyelopentane 0.035 306.446 0.153
n-hesene 0.09 86.18 0.0034 n-Mxane 0.120 1046952 0323
cyclahexane 0.02 84.18 0.0009 cyclohexane 0.031 268.505 0.134
Other hexanes 0.15 86.18 0.0056 Other hexane 0.199 1744.920 0972
heptanes 0.07 100.21 0.0034 heptanes 0319 1039310 0520
methykydohera 0.02 98.19 0.0008 matipordold 0.028 246469 0.123
224-1MP 0.00 114.22 0.0000224-TMP 0.000 1584 0.001
Benzene 0.02 78.11 0.0006 Benzene 0.021 180.900 0.090
Toluene 0.01 92.14 0.0006 Toluene 0.016 141.836 0.071
Eth tenzene 0.00 106.17 0.0001 Ethebenzene 0.002 19.141 0.010
Xylenes. 0.00 106.17 0.0002 Xylem 0.006 54.478 0.027
C8+Heavies 0.05 116 0.0024 C8+Heat 0.084 731.957 0.366
Mass Fraction VOC: 0.2476 Total VOC 38.287
Heating Value I 1111 BTU/scf I '
airmn am sour= WP-42 rlapra 133
13WE2a10.CP1 123/99.9.9
0.07 N NOXAIMBtu 0.37 b CO/MMBtu
Mole%.MW.and RIM fractions from:
sales gas analysis mlected 8126/2013 from State Antelope iF2eHNB
Assumed MW for CSr is 116
Emissions Summary Table
Pollutant Uncontrolled Emission Fa Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source
VOC 14568.79 lb/MMscf 728.44 lb/MMscf 38.3 tpy 1.9 tpy Gas Analysis
Nox 0.07 ib/MMBTU 0.07 lb/MMBTU 0.23 tpy 0.23 tpy AP-42
CO 0.37 Ib/MMBTU 0.37 Ib/MMBTU 1.25 tpy 1.25 tpy AP-42
Benzene 34.4179 lb/MMscf 1.7209 lb/MMscf 181 lb/yr 9 lb/yr Gas Analysis
n-Hexane 199.1918 lb/MMscf 9.9596 lb/MMscf 1047 lb/yr 52 lb/yr Gas Analysis
Toluene 26.9856 lb/MMscf 1.3493 lb/MMscf 142 lb/yr 7 lb/yr Gas Analysis
Xylenes 10.3649 lb/MMscf 0.5182 lb/MMscf 54 lb/yr 3 lb/yr Gas Analysis
Ethylbenzene 3.6417 lb/MMscf 0.1821 lb/MMscf 19 lb/yr 1 lb/yr Gas Analysis
13WE2810.CP1 123/9BAA
.
On.(1)pneumatic water test pump,rated at 600 sc&Ar(Sandpiper.
Modal OW.Serial number 2091587).11m pneumatic pump is cmtelled by
011 an enclosed flare with a mInktaen combustion a6lden y of 95%. _
Pranp Information
ManuhCan Sandpiper
Model
Number:OW
Serial
Pump 0_ties Number.2091587
411
Pump •
opacity 9.1 gallons per minute pumped
natural ps eao ad/hour used
co
Cannel Flare 95.00%Elnclency
Calculations
EPA Emission Inventory Improvement Program PubfcaWn:Volume It Chapter 10-Displacement Equation(10.4-3)
Ex-Q•MW•Xx/C
Ex=emissions of pollutant x
Q-Volumetric flow rate/volume of gas processed
MW=Molecular weight of gas a SG of ps•MW ofalr
sera mass fraction ofxin gas
C-molar volume of ideal gas(379 scf/lb-mal)at 60F and 1 atm
e sd/lr
MW 128 b/tirmol
ar0p. 8750 llareM Requested Throughput 5256 MMscf/yr
Cmymnent. mole% MW ma frecdce Comment !/hr 6Ar tpy
C02 2.19 44 0.0432 C02 1525 13363.276 6.682
nitrogen 0.83 28 0.0104 nitrogen 0.368 3222.940 1.611
methane 73.96 16.04 0.5319 methane 18.779 164507$62 82.251
ethane 12.21 30.07 0.1647 ethane 5.835 50936.468 - 25.468 ,
propane 7.10 44.09 0.1403 propane 4.954 43397905 21.699
Isobutane 0.63 58.12 0.0165 Isobutane 0.584 5117.373 2.559
n-butane 1.87 58.12 0.0489 n-butane 1.725 15109.509 7555
isopentane 0.32 72.15 0.0102 Isopentane 0.360 3154.834 1577
n-pentane 0.40 72.15 0.0130 n-pentane 0.458 4011.331 2.006
cydopentane 0.03 70.15 0.0010 cydopentane 0.035' 306.446 - 0.153
n•hexane 0.09 86.18 0.0034 n-henna 0.120 1046.952 0.523
cydohexane 0.02 84.18 0.0009 cyclohexane 0.031 268.505 0.134
Other hexanes 0.15 86.18 • 0.0056 Other hexane 0.199 1744920A 0.872
heptanes 0.07 100.21 0.0034 heptanes 0.119 1039510 0520
methylcydohaa 0.02 98.19 0.0008 nstlrykyclol - 0.028 246.469 0.123
224-TAP 0.00 114.22 - 0.0000 224-TMP 0.000 1584 0.001
lateens . 0.02 78.11 0.0006 Benzene 0.021 180900 0.090
Toluene 0.01 92.14 0.0005 Toluene 0.016 141.836 0.071
Ethymenrene 0.00 106.17 0.0001 EOrylbeeraene 0.002 19.1411 0.010
Xylenes 0.00 �106.17 0.0002 Xylenes 0.006 54.478 0.027 i
CB+Heavies 0.05 116 00024 CB+Heavies 0.084 731.957 0.366
Mass Fradbn VOC: 0.2476 Total VOC 38.287
Hating Value I 12m BfU/sd
erarun lector era np-a siwp rim •
13WE2810.CP1 123/91AA
L 0.07 lo NOX/MMBlu 037 lb COtAMBW
Nabs
Mob%,MW.and mass frapbns from:
sales gas analysis cdlected 8/26/2013 from State Antelope 1F20HNB
Assumed MW for Cot is 116
Emissions Summary Table
Pollutant Uncontrolled Emission Fa Controlled Emission Factor Uncontrolled Emissions Controlled Emissions Source
VOC 14568.79 lb/MMscf 728.44 lb/MMscf 38.29 tpy 1.91 tpy Gas Analysis
Nox__ _ 0.07 lb/MMBTU 0.07 lb/MMBTU 0.23 tpy 0.23 tpy AP-42
CO 0.37 lb/MMBTU 0.37 lb/MMBTU 1.25 tpy 1.25 tpy AP-42
Benzene 34.42 lb/MMscf 1.7209 lb/MMscf 180.90 lb/yr 9.05 lb/yr Gas Analysis
n-Hexane 199.19 lb/MMscf 9.9596 lb/MMscf 1046.95 lb/yr 52.35 lb/yr Gas Analysis
Toluene 26.99 lb/MMscf 1.3493 lb/MMscf 141.84 lb/yr 7.09 lb/yr Gas Analysis
Xylenes 10.36 lb/MMscf 0.5182 lb/MMscf 54.48 lb/yr 2.72 lb/yr Gas Analysis
Ethylbenzene 3.64 lb/MMscf 0.1821 lb/MMscf 19.14 lb/yr 0.96 lb/yr Gas Analysis
13WE2810.CP1 123/9BAA
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Air Pollutant Emission Notice(APEN)—and—Application for Construction Permit , ,
OIL AND GAS EXPLORATION AND PRODUCTION CRUDE OIL STORAGE TANK BATTERY -
Current Status(Check all that apply) A Reason for APEN Submittal(Check all that apply) 4T%J
AIRS ID#': 1'2_3 - 1 IDA- 003 0 APEN update only' ebld
® New or previously unreported battery - 0 Modification to existing sources
I 0 Previously grandfathered battery' C Q,'D 0 Registration for coverage under general permit no.GP0I_ __
❑ Synthetic minor facility 13" .<.v &cancellation request for individual permit:
O Located in the 8-hr Ozone Control Area' 0 Application for or Modification of an individual permit
❑ Registered under general permit no.GPO] 0 Administrative permit amendment'
❑ Permitted under individual permit: ❑ Other.
For individual permit applications,check if you wants: ®A copy of the preliminary analysis conducted by the Division
0 To review a draft of the permit prior to issuance
Company Name9: Bonanza Creek Energy Operating Company LLC OGCC Operator#: 8960
Mailing Address10: 410 17'"Street,Suite 1500
City: Denver State: CO Zip: 80202 E-mail: pyotmg@BonanzaCrk.com
Contact Name: Peg Young Phone: 720-440-6133 Fax: 720-279-2331
Tank Battery Name": State Antelope 3-28 Production Facility(COGCC#431937) Number of tanks: 12-500 bbl
Location12(QQ Sec.Twp.Range.): Sw/Sw Sec.28,T5N R62W County: Weld Total tank capacity[bbl]: 5,000
Calendar year for which"Actual"data applies": 2013 Year(s)tank(s)were placed in service": 2013
Lead L-30-010 ECD SNs:20734,20732,20679,20677,20733,20731, Control
Control Descriptions: 20680,20678,20937,20938 Efficiency16: 95%
Condensate Throughput'[[bbl/year] Requested'°: 249,660 Maximum for Pm calculation": 249,660
Actual" 208,050 While Controls Operational21 208,050
Other equipment at facility": Heater treater,produced water tanks,natural gas-fired engines,pneumatic pumps
Comments:
Estimated emissions at throughputs listed above. Use N/A for requested throughput/emission values unless requesting an individual permit
❑Check if the Division is to calculate emissions. 0 Check if site-specific emission factors provided to calculate emissions23.
Emission Factor Battery Requested Emissions's Actual Emissions20
Pollutant" [1b/bbl] PTEn Uncontrolled" Controlled" Uncontrolled" Controlled"
VOC[tons/year] 2.12 ,/ 265.24 265.24 ✓ 13.26 ✓ 221.04 ✓ 11.05
NOx[tons/year] 0.068./ N/A 0.57 N/A 0.47
CO[tons/year] 0.370 i N/A 3.10 N/A 2.58
Benzene[lbs/year] 0.013 / 3,348.0 3,348.0 ✓ 167.4 .. 2,790.0 / 139.5 /
n-Hexane[lbs/year] 0.079 / 19,752.0 19,752.0 „' 987.6 ✓ 16,460 ✓ 823.0 J
Wells serviced by this tank or tank batter?
API#: 05-123-36878 Name: State Antelope E14-A11-28HNB 0 Newly Reported Well
API#: 05-123-36877 Name: State Antelope I4-]1-28HNB 0 Newly Reported Well
API#: 05-123-36876 Name: State Antelope 114-F11-28HNB ®Newly Reported Well
API#: 05-123-36875 Name: State Antelope J-F-28HNB ®Newly Reported Well
API#: Name MI
.,Newly Reported Well
API#: Name: MI Newly Reported Well
API#: Name: tj^ Newly Reported Well
The signature below indicates that I have knowledge of the facts herein set forth and that the same are true,acctde and complete to the best of my
knowledge and belief. If this is a registration for coverage under general permit GP0I,I further certify that thishrce is and will be operated in
full corpp;iance with ch ndin i�q//f,� tieral permit GP0I. / 17i— a U l3
6,/ �f/4Si 4
Signature of Legally Autforized Person(not a vendor or consultant) Date =
David J.Lillo Vice Presidip*;Rocky Mt.Asset Mgmt
Type or Print Name of Person Signing Above Official Title.
Submit this form,along with$152.90 for each Colorado Department of Public Health and Environment For information call:
filing of up to 5 tank battery APENS. Include Air Pollution Control Division,APCD-SS-BI 299315 (303)692-3150
S250 General Permit fee for each new GP 4300 Cherry Creek Drive South
registration to: Denver,CO 80246-1530
FORM APCD-205
Page 1 of 2 BCEOC FormAPCD-205-E&PCondensateTankAPENl.docx
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