HomeMy WebLinkAbout20173234.tiffCOLORADO
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
1150O St
PO Box 758
Greeley, CO 80632
September 12, 2017
Dear Sir or Madam:
RECEIVED
SEP 1 5 2017
WELD COUNTY
COMMISSIONERS
On September 14, 2017, the Air Pollution Control Division will begin a 30 -day public notice period for
Verdad Resources LLC — Johnson 8-30N. 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
beginning of the public notice period. Please send any comment regarding this public notice to the
address below.
Colorado Dept. of Public Health & Environment
APCD-SS-B1
4300 Cherry Creek Drive South
Denver, Colorado 80246-1530
Attention: Clara Gonzales
Regards,
Clara Gonzales
Public Notice Coordinator
Stationary Sources Program
Air Pollution Control Division
Enclosure
Pub t
RA,v; tL
c;/aO/17
4300 Cherry Creek Drive S., Denver, CO 80246-1530 P 303-692-2000 www.colorado.gov/cdphe
John W. Hickenlooper, Governor Larry Wolk, MD, MSPH, Executive Director and Chief Medical Officer
CCI PLCM(n/ TP.)S HLC7T),
Pt,JcER/cH, JmrcK)
i'7
2017-3234
Air Pollution Control Division
Notice of a Proposed Project or Activity Warranting Public
Comment
Website Title: Verdad Resources LLC — Johnson 8-30N — Weld County
Notice Period Begins: September 14, 2017
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: Verdad Resources LLC
Facility: Johnson 8-30N
exploration and production facility
NENW, S31, T2N, R65W
Weld County
The proposed project or activity is as follows: operator requests to permit a E&P site consisting of storage
tanks, separators, combustion device, and loadout
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 17WE0136 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:
Kirk Bear
Colorado Department of Public Health and Environment
4300 Cherry Creek Drive South, APCD-SS-B1
Denver, Colorado 80246-1530
cdphe.commentsapcd@state.co.us
CQtb4a,R�.
1 IAV
STATE OF COLORADO
COLORADO DEPARTMENT OF PUBLIC HEALTH AND ENVIRONMENT
AIR POLLUTION CONTROL DIVISION
TELEPHONE: (303) 692-3150
CONSTRUCTION PERMIT
PERMIT NO: 17WE0136
DATE ISSUED:
ISSUED TO: Verdad Resources LLC
!8
Issuance 1
THE SOURCE TO WHICH THIS PERMIT APPLIES IS DESCRIBED AND LOCATED AS
FOLLOWS:
Oil and gas facility, known as the Johnson 8-30N, located in NENW, S31, T2N, R65W, in
Weld County, Colorado.
THE SPECIFIC EQUIPMENT OR ACTIVITY SUBJECT TO THIS PERMIT INCLUDES THE
FOLLOWING:
Equipment ID
AIRS
Point
Description
Condensate
Storage Tanks
001
Three 400 barrel fixed roof condensate storage tanks
Produced
Water Tank
002
One 400 barrel fixed roof produced water storage tank
Loadout
003
Truck loadout of condensate
Separator
Venting
004
One separator
THIS PERMIT IS GRANTED SUBJECT TO ALL RULES AND REGULATIONS OF THE COLORADO AIR
QUALITY CONTROL COMMISSION AND THE COLORADO AIR POLLUTION PREVENTION AND
CONTROL ACT C.R.S. (25-7-101 et seq), TO THOSE GENERAL TERMS AND CONDITIONS
INCLUDED IN THIS DOCUMENT AND THE FOLLOWING SPECIFIC TERMS AND CONDITIONS:
REQUIREMENTS TO SELF -CERTIFY FOR FINAL AUTHORIZATION
1. YOU MUST notify the Air Pollution Control Division (the Division) no later than
fifteen days of the latter of commencement of operation or issuance of this permit,
by submitting a Notice of Startup form to the Division. The Notice of Startup form
may be downloaded online at https://www.colorado.gov/pacific/cdphe/other-air-
permittinq-notices. Failure to notify the Division of startup of the permitted source is a
violation of Air Quality Control Commission (AQCC) Regulation No. 3, Part B, Section
III.G.1 and can result in the revocation of the permit.
2. Within one hundred and eighty days (180) of the latter of commencement of operation or
issuance of this permit, compliance with the conditions contained in this permit shall be
demonstrated to the Division. It is the owner or operator's responsibility to self -certify
123 9FOF
Page 1 of 11
Colorado Department of Public Health and Environment
Air Pollution Control Division
compliance with the conditions. Failure to demonstrate compliance within 180 days may
result in revocation of the permit. (Reference: Regulation No. 3, Part B, III.G.2).
3. This permit shall expire if the owner or operator of the source for which this permit was
issued: (i) does not commence construction/modification or operation of this source within
18 months after either, the date of issuance of this construction permit or the date on which
such construction or activity was scheduled to commence as set forth in the permit
application associated with this permit; (ii) discontinues construction for a period of
eighteen months or more; (iii) does not complete construction within a reasonable time of
the estimated completion date. The Division may grant extensions of the deadline per
Regulation No. 3, Part B, III.F.4.b. (Reference: Regulation No. 3, Part B, III.F.4.)
4. Point 004: Within one hundred and eighty days (180) after issuance of this permit, the
operator shall install a flow meter to monitor and record volumetric flow rate of natural
gas vented from each separator covered by this permit. Until the flow meter is installed,
the operator shall monitor and record condensate/crude produced through the separator
and estimate the gas flow rate based on standard cubic feet (scf) per barrel (bbl) of
scf/bbl estimated in the permit application.
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 B, 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.
EMISSION LIMITATIONS AND RECORDS
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:
Equipment ID
AIRS
Point
Tons per Year
Emission Type
NO.
VOC
CO
Condensate
Storage Tanks
001
1.9
35.6
8.6
Point
Produced
Water Tank
002
--
0.3
--
Point
Loadout
003
--
19.7
--
Point
Separator
Venting
004
4.1
24.2
18.5
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-minimus reporting level)
from each emission unit, on a rolling twelve (12) month total. By the end of each month
123 9FOF
Page 2 of 11
Colorado Department of Public Health and Environment
Air Pollution Control Division
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. The owner or operator shall track emissions from all insignificant activities at the facility
on an annual basis to demonstrate compliance with the facility potential emission
limitations as seen below. An inventory of each insignificant activity and associated
emission calculations shall be made available to the Division for inspection upon
request. For the purposes of this condition, insignificant activities shall be defined as any
activity or equipment, which emits any amount but does not require an Air Pollution
Emission Notice (APEN) or is permit exempt.
Total potential emissions from the facility, including all permitted emissions and potential
to emit from all insignificant activities, shall be less than 100 tons per year of VOC.
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 perm t (Reference: Regulation No.3, Part B, Section III.E.)
Equipment
ID
AIRS
Point
Control Device
Pollutants
Controlled
Condensate
Storage
Tanks
001
Enclosed combustor
VOC, HAP
Produced
Water Tank
002
Enclosed combustor
VOC, HAP
Separator
Venting
004
Enclosed combustor
VOC, HAP
PROCESS LIMITATIONS AND RECORDS
10. This source shall be limited to the following maximum processing rates as listed below.
Monthly records of the actual processing rate shall be maintained by the owner or operator
and made available to the Division for inspection upon request. (Reference: Regulation
3, Part B, II.A.4)
Process/Consumption Limits
Equipment
ID
AIRS
Point
Process Parameter
Annual Limit
Condensate
Storage
Tanks
001
Condensate
166,800 barrels
Produced
Water Tank
002
Produced water
41,975 barrels
Loadout
003
Condensate
166,800 barrels
Separator
Venting
004
Separator Gas
100.0 MMscf
11. Point 003: Condensate loading to truck tanks shall be conducted by submerged fill.
(Reference: Regulation 3, Part B, III.E)
123 9F0F
Page 3 of 11
Colorado Department of Public Health and Environment
Air Pollution Control Division
12. Point 004: Upon installation of the flow meter, the owner or operator shall continuously
monitor and record the volumetric flow rate of natural gas vented from the separator(s)
using the flow meter. The owner or operator shall use monthly throughput records to
demonstrate compliance with the process limits contained in this permit and to calculate
emissions as described in this permit.
STATE AND FEDERAL REGULATORY REQUIREMENTS
13. Point 001, 002, 004: 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)
14. Point 002, 003: 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. (Reference: Regulation No. 1, Section
II.A.1. & 4.)
15. Point 001, 002, 003, 004: This source is subject to the odor requirements of Regulation
No. 2. (State only enforceable)
16. Point 001, 004: This source is subject to Regulation Number 7, Section XII. The
operator shall comply with all applicable requirements of Section XII and, specifically,
shall:
• Comply with the recordkeeping, monitoring, reporting and emission control
requirements for condensate storage tanks; and
• Ensure that the combustion device controlling emissions from this storage tank
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. (Regulation Number 7, Section XII.C.) (State only
enforceable)
17. Point 001, 004: The combustion device covered by this permit is subject to Regulation
Number 7, Section XVII.B.2. General Provisions (State only enforceable). 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 visible emissions during normal
operations, as defined under Regulation Number 7, XVII.A.16; and be designed so that
an observer can, by means of visual observation from the outside of the enclosed flare
or combustion device, or by other convenient means approved by the Division,
determine whether it is operating properly. This flare must be equipped with an
operational auto -igniter according to the following schedule:
• All combustion devices installed on or after May 1, 2014, must be equipped with
an operational auto -igniter upon installation of the combustion device;
• All combustion devices installed before May 1, 2014, must be equipped with an
operational auto -igniter by or before May 1, 2016, or after the next combustion
device planned shutdown, whichever comes first.
123 9F0F Page 4 of 11
Colorado Department of Public Health and Environment
Air Pollution Control Division
18. Point 001: The storage tank covered by this permit is subject to the emission control
requirements in Regulation Number 7, Section XVII.C.1. The owner or operator shall
install and operate air pollution control equipment 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 except where the combustion
device has been authorized by permit prior to May 1, 2014. The source shall follow the
inspection requirements of Regulation Number 7, Section XVII.C.1.d. and maintain
records of the inspections for a period of two years, made available to the Division upon
request. This control requirement must be met within 90 days of the date that the
storage tank commences operation.
19. Point 001: The storage tanks covered by this permit are subject to the venting and
Storage Tank Emission Management System ("STEM") requirements of Regulation
Number 7, Section XVII.C.2.
20. Point 003: 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)
21. Point 003: The owner or operator shall follow loading procedures that minimize the
leakage of VOCs to the atmosphere including, but not limited to (Reference: Regulation
3, Part B, III.D.2):
Hoses, couplings, and valves shall be maintained to prevent dripping, leaking, or
other liquid or vapor loss during loading and unloading.
All compartment hatches at the facility (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.
The owner or operator shall inspect onsite loading equipment during loading
operations to monitor compliance with above conditions. The inspections shall
occur at least monthly. Each inspection shall be documented in a log available
to the Division on request.
22. Point 003: 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.
23. Point 004: The separator covered by this permit is subject to Regulation 7, Section
XVII.G. (State Only). On or after August 1, 2014, gas coming off a separator, produced
during normal operation from any newly constructed, hydraulically fractured, or
recompleted oil and gas well, must either be routed to a gas gathering line or controlled
from the date of first production by air pollution control equipment 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.
OPERATING & MAINTENANCE REQUIREMENTS
24. Point 001, 002, 004: 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
123 9F0F Page 5 of 11
Colorado Department of Public Health and Environment
Air Pollution Control Division
the requirements of this permit. Revisions to your O&M plan are subject to Division
approval prior to implementation. (Reference: Regulation No. 3, Part B, Section III.G.7.)
25. Point 003: This source is not required to follow a Division -approved operating and
maintenance plan.
COMPLIANCE TESTING AND SAMPLING
Initial Testing Requirements
26. Point 001: The owner or operator shall complete site specific sampling including a
compositional analysis of the pre -flash pressurized condensate routed to these storage
tanks and a sales oil analysis to determine RVP and API gravity. Testing shall be in
accordance with the guidance contained in PS Memo 05-01. Results of testing shall be
used to determine a site -specific emissions factor using Division approved methods.
Results of site -specific sampling and analysis shall be submitted to the Division as part
of the self -certification and used to demonstrate compliance with the emissions factors
chosen for this emissions point.
27. Point 001, 004: The owner or operator shall demonstrate compliance with opacity
standards, using EPA Reference Method 22, 40 C.F.R. Part 60, Appendix A, to
determine the presence or absence of visible emissions. "Visible Emissions" means
observations of smoke for any period or periods of duration greater than or equal to one
minute in any fifteen minute period during normal operation. (Regulation Number 7,
Sections XII.C, XVII.B.2. and XVII.A.16)
ADDITIONAL REQUIREMENTS
28. A revised Air Pollutant Emission Notice (APEN) shall be filed: (Reference: Regulation No.
3, Part A, II.C)
a. Annually by April 30th 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 (NOX) 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
123 9FOF Page 6 of 11
Colorado Department of Public Health and Environment
Air Pollution Control Division
d. Whenever a permit limitation must be modified; or
e. No later than 30 days before the existing APEN expires.
f. Within 14 calendar days of commencing operation of a permanent replacement
engine under the alternative operating scenario outlined in this permit as
Attachment A. The APEN shall include the specific manufacturer, model and serial
number and horsepower of the permanent replacement engine, the appropriate
APEN filing fee and a cover letter explaining that the owner or operator is
exercising an alternative -operating scenario and is installing a permanent
replacement engine.
29. Federal regulatory program requirements (i.e. PSD or 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
had not yet commenced on the source. The source shall not exceed the Federal program
threshold until a permit is granted. (Regulation No. 3 Part D).
GENERAL TERMS AND CONDITIONS
30. 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 II.B upon a request for transfer of ownership and the
submittal of a revised APEN and the required fee.
31. If this permit specifically states that final authorization has been granted, then the
remainder of this condition is not applicable. Otherwise, the issuance of this construction
permit does not provide "final" authority for this activity or operation of this source. Final
authorization of the permit must be secured from the APCD in writing in accordance with
the provisions of 25-7-114.5(12)(a) C.R.S. and AQCC Regulation 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 all respects with the conditions of the
permit. Once self -certification of all points has been reviewed and approved by the
Division, it will provide written documentation of such final authorization. Details for
obtaining final authorization to operate are located in the Requirements to Self -
Certify for Final Authorization section of this permit.
32. This permit is issued in reliance upon the accuracy and completeness of information
supplied by the owner or operator and is conditioned upon conduct of the activity, or
construction, installation and operation of the source, in accordance with this information
and with representations made by the owner or operator or owner or operator's agents. It
is valid only for the equipment and operations or activity specifically identified on the
permit.
33. Unless specifically stated otherwise, the general and specific conditions contained in this
permit have been determined by the APCD to be necessary to assure compliance with the
provisions of Section 25-7-114.5(7)(a), C.R.S.
34. Each and every condition of this permit is a material part hereof and is not severable. Any
challenge to or appeal of a condition hereof shall constitute a rejection of the entire permit
and upon such occurrence, this permit shall be deemed denied ab initio. This permit may
be revoked at any time prior to self -certification and final authorization by the Air Pollution
Control Division (APCD) on grounds set forth in the Colorado Air Quality Control Act and
1239F0F Page 7of11
Colorado Department of Public Health and Environment
Air Pollution Control Division
regulations of the Air Quality Control Commission (AQCC), including failure to meet any
express term or condition of the permit. If the Division denies a permit, conditions imposed
upon a permit are contested by the owner or operator, or the Division revokes a permit,
the owner or operator of a source may request a hearing before the AQCC for review of
the Division's action.
35. Section 25-7-114.7(2)(a), 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 or activity is to be discontinued, the owner must notify the
Division in writing requesting a cancellation of the permit. Upon notification, annual fee
billing will terminate.
36. 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.
By:
Kirk Bear
Permit Engineer
Permit History
Issuance
Date
Description
Issuance 1
This Issuance
Issued to Verdad Resources LLC
123 9F0F Page 8 of 11
Colorado Department of Public Health and Environment
Air Pollution Control Division
Notes to Permit Holder at the time of this permit issuance:
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 is 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:
https://www. colorado. qov/pacific/cdphe/agcc-reps
4) The following 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.
AIRS
Point
Pollutant
CAS #
Uncontrolled
Emissions
(Ib/yr)
Reportable
Controlled
Emissions
(lb/yr)
001
Benzene
71432
4003
Yes
200
Toluene
108883
2335
Yes
117
Ethylbenzene
100414
167
No
8
Xylenes
1330207
667
Yes
33
n -Hexane
110543
21184
Yes
1059
224 TMP
540841
1835
Yes
92
002
Benzene
71432
294
Yes
15
n -Hexane
110543
923
Yes
46
003
Benzene
71432
68
No
NA
n -Hexane
110543
600
Yes
NA
004
Benzene
71432
1567
Yes
78
Toluene
108883
5130
Yes
257
Ethylbenzene
100414
532
Yes
27
Xylenes
1330207
672
Yes
34
n -Hexane
110543.
13098
Yes
655
224 TMP
540841
30
No
2
5) The emission levels contained in this permit are based on the following emission factors:
Emission Factor Sources:
123 9FOF
Page 9 of 11
Colorado Department of Public Health and Environment
Air Pollution Control Division
Point 001:
CAS #
Pollutant
Uncontrolled
Emission Factors
lb/bbl
Source
NOx
0.068
CDPHE
CO
0.310
CDPHE
VOC
8.52
TANKS
71432
Benzene
0.024
TANKS
108883
Toluene
0.014
TANKS
100414
Ethylbenzene
0.001
TANKS
1330207
Xylene
0.004
TANKS
110543
n -Hexane
0.127
TANKS
540841
224 TMP
0.011
TANKS
Note: The controlled emissions factors for this point are based on the flare control efficiency of 95%.
Point 002:
CAS #
Pollutant
Uncontrolled
Emission Factors
lb/bbl
Source
VOC
0.262
CDPHE
71432
Benzene
0.007
CDPHE
110543
n -Hexane
0.022
CDPHE
Note: The controlled emissions factors for this point are based on the flare control efficiency of 95%.
Point 003:
CAS #
Pollutant
Uncontrolled
Emission Factors
lb/bbl
Source
VOC
0.1400
AP -42
71432
Benzene
0.0017
AP -42
110543
n -Hexane
0.0153
AP -42
Point 004:
CAS #
Pollutant
Uncontrolled
Emission Factors
lb/MMscf
Source
NOx lb/MMBtu
0.068
AP -42
CO lb/MMBtu
0.310
AP -42
VOC
9717
mass balance
71432
Benzene
15.67
mass balance
108883
Toluene
51.30
mass balance
100414
Ethylbenzene
5.320
mass balance
1330207
Xylene
6.720
mass balance
110543
n -Hexane
131.0
mass balance
540841
224 TMP
0.300
mass Balance
Note: The controlled emissions factors for this point are based on the flare control efficiency of 95%.
5) In accordance with C.R.S. 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 shall 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
123 9F0F
Page 10 of 11
Colorado Department of Public Health and Environment
Air Pollution Control Division
associated with this permit. For any questions regarding a specific expiration date call the Division at
(303)-692-3150.
6) This facility is classified as follows:
Applicable
Requirement
Status
Operating Permit
Synthetic Minor Source of: VOC, HAP
NANSR
Synthetic Minor Source of: VOC, HAP
7) 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
Subpart A — Subpart Z
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 ZZZZ — Subpart MMMMM
MACT
63.8980 -End
Subpart NNNNN — Subpart XXXXXX
8) A self -certification form and guidance on how to self -certify compliance as required by this permit may
be obtained online at: http://www.colorado.gov/pacific/cdphe/air-permit-self-certification
123 9F0F Page 11 of 11
Colorado Air Permitting Project
Project Details
Review Engineer:
Package #:
Received Date:
Review Start Date:
Section 01 - Facility Information
Company Name:
County AIRS ID:
Plant AIRS ID:
Facility Name:
Physical Address/Location:
Type of Facility:
What industry segment?
Is this facility located in a NAAQS non -attainment area?
If yes, for what pollutant? aarbon Monoxide (CO)
Kirk Bear
358210
2/10/2017
5/15/2017
Verdad:Resources LLC
123
9FOF
Johnson 8-30N
NENW, Section 31, T2N, R65W
Exploration & Production Well Pad
& Natural Gas Production & Processing
Weld
Section 02 - Emissions Units In Permit Application
Y
(J articulate Matter (PM)
Quadrant
Section
Township
Range
NENW,
lzone (NOx & VOC)
AIRs Point #
Emissions Source Type
Equipment Name
Emissions
Control?
Permit #
Issuance #
Self Cert
Required?
Action
Engineering
Remarks
001
Condensate Tank
Condensate Storage Tanks
Yes
17WE0136
1
Yes.
Permit Initial- i.
Issuance
002
Produced WafierTank
Produced Water Tank
Yes
17WE0136
1
Yes
Permit initial :'
Issuance
003
Hydrocarbon ilk( acting
Condensate Loading
Pto
17WE0136
1
Yes
Permit Initial =_
issuanc€,
004
SeparatorVenting
Separator Venting
Yes
17WE0136
1
Yes
Permit Initial
Issuance
Section 03 - Description of Project
Permit request for this oil and gas exploration and production site
Section 04 - Public Comment Requirements
Is Public Comment Required? Yes
If yes, why? Requesting Synthetic Minor Permit
Section 05 - Ambient Air Impact Analysis Requirements
Was a quantitative modeling analysis required? Na
If yes, for what pollutants?
If yes, attach a copy of Technical Services Unit modeling results summary.
Section 06 - Facility -Wide Stationary Source Classification
Is this stationary source a true minor?
Is this stationary source a synthetic minor?
If yes, indicate programs and which pollutants:
Prevention of Significant Deterioration (PSD)
Title V Operating Permits (OP)
No
Yes
SO2 NOx CO VOC PM2.5 PM10 TSP HAPs
❑ ❑ ❑ ❑ ❑
❑ ❑ ❑ CI 0
O
❑ (]
Colorado Air Permitting Project
Non -Attainment New Source Review (NANSR)
Is this stationary source a major source?
If yes, explain what programs and which pollutants here:
Prevention of Significant Deterioration (PSD)
Title V Operating Permits (OP)
Non -Attainment New Source Review (NANSR)
SO2 NOx
❑ ❑
❑ ❑
❑
CO VOC PM2.5 PM10 TSP HAPs
❑ ❑ ❑
❑ ❑ ❑
❑ ❑
Condensate Storage Tank(s) Emissions Inventory
Section 01 - Administrative Information
'Facility AlRs ID:
123
County
9FOP....
Plant
Point
Section 02 - Equipment Description Details
Detailed Emissions Unit Three 400barrel condensate storage tanks
Description:
Emission Control Device Enclosed coin
Description:
Requested Overall VOC & HAP Control
Efficiency %:
Section 03 - Processing Rate Information for Emissions Estimates
Primary Emissions - Storage Tank(s)
Actual Condensate Throughput =
Requested Permit Limit Throughput =
Potential to Emit (PTE) Condensate
Throughput =
166800. Barrels (bbl) per year
166,800? Barrels (bbl) per year
166,800£ Barrels (bbl) per year
Secondary Emissions - Combustion Device(s)
Heat content of waste gas = 2330: Btu/scf
Volume of waste gas emitted per BBL of liquids
produced = 143 scf/bbl
Actual heat content of waste gas routed to combustion device =
Request heat content of waste gas routed to combustion device =
Actual Condensate Throughput While Emissions Controls Operating = 166,800 Barrels (bbl) per year
55,576 MMBTU per year
55,576 MMBTU per year
Potential to Emit (PTE) heat content of waste gas routed to combustion device = 55,576 MMBTU per year
Section 04 - Emissions Factors & Methodologies
Will this storage tank emit flash emissions?
Emission Factors Condensate Tank
Uncontrolled Controlled
(lb/bbl) (16/bbl)
Pollutant
VOC
Benzene
Toluene
Ethylbenxene
Xylene
n -Hexane
224 TMP
(Condensate (Condensate
Throughput) Throughput)
Emission Factor Source
Control Device
Pollutant
Uncontrolled Uncontrolled
(Ib/MMBtu) (lb/bbl)
(waste heat
combusted)
(Condensate
Throughput)
Emission Factor Source
PM10
PM2.5
NOx ..0.0680 0.0680
CO 0.3100.. 0.3100
0.0000
0.000
Section 05 - Emissions Inventory
Criteria Pollutants
Potential to Emit
Uncontrolled
(tons/year)
Actual Emissions
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(tons/year) (tons/year)
VOC
PM10
PM2.5
NOx
CO
710.6
710.6
35.5
710.6
35.5
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
1.9
0.5
0.5
0.5
0.5
8.6
2.2
2.2
2.2
2.2
Hazardous Air Pollutants
Potential to Emit
Uncontrolled
(tons/year)
Actual Emissions
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(Ibs/year( (lbs/year)
Benzene
Toluene
Ethylbenxene
Xylene
n -Hexane
224 TMP
2.0016
2.0016
0.1001
2.0016
0.1001
4003
200
1.1676
1.1676
0.0584
1.1676
0.0584
2335
117
0.0834
0.0834
0.0042
0.0834
0.0042
157
8
0.3336
0.3336
0.0167
0.3336
0.0167
667
33
10.5918
10.5918
0.5296
10.5918
0.5296
21184
1059
0.9174
0.9174
0.0459
0.9174
0.0459
1835
92
Section 06 - Regulatory Summary Analysis _
Regulation 3, Parts A, B
Regulation 7, Section XII.C, D, E, F
Regulation 7, Section XII.G, C
Regulation 7, Section XVILB, C.1, C.3
Regulation 7, Section XVII.C2
Regulation 6, Part A, NSPS Subpart Kb
Regulation 6, Part A, NSPS Subpart 0000
Regulation 8, Part E, MACT Subpart HH
(See regulatory applicability worksheet for detailed analysis)
Facility attainment -area status has not been established yet
Storage tank is subject to Regulation 7, Section XII.C-F
Storage Tank is not subject to Regulation 7, Section 011.0
Storage tank is subject to Regulation 7, Section XVII, B, C.1 & C.3
Storage tank is subject to Regulation 7. Section XVII.C.2
Storage Tank is not subject to NSPS Kb
Storage Tank is not subject to NSPS 0000
Storage Tank is not subject to MACT HH
3 of 14
K:\PA\2017\17 W E 0136. CPT.xlsm
Condensate Storage Tank(s) Emissions Inventory
Section 07 - Initial and Periodic Sampling and7aatina Requirements
Er)
Does the company use the state default emissions factors to estimate emissions? %ice
If yes, are the uncontrolled actual or requested emissions estimated to he greater than or equal to 80 tons VOC per year? ,.
If yes, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01.
Does the company use a site specific emissions factor to estimate emissions?
If yes and if there are flash emissions, are the emissions factors based on a pressurized liquid sample drawn at the
facility being permitted? This sample should he considered representative which generally means site..specific and
collected within one year of the application received date. However, if the facility has not been modified (e.g., no
new wells brought on-line), then it may be appropriate to use an older site -specific sample. Yes
If no, the permit will contain an 'Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01.
Does the company request a control device efficiency greater than 95% for a flare or combustion device?
If yes, the permit will contain and initial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling
Section 08 - Technical Analysis Notes
Section 09 - Inventory SCC Coding and Emissions Factors
AIRS Point 8
Process 8 SCC Code
Uncontrolled
Emissions
Pollutant Factor Control % Units
PM10 0.00 0 lb/1,000 gallons condensate throughput
PM2.5 0.00 0 lb/1,000 gallons condensate throughput
NOx 0.14 0 lb/1,000 gallons condensate throughput
VOC 202.9 95 lb/1,000 gallons condensate throughput
CO 0.63 0 lb/1,000 gallons condensate throughput
Benzene 0.57 95 lb/1,000 gallons condensate throughput
Toluene 0.33 95 lb/1,000 gallons condensate throughput
Ethylbenzene 0.02 95 lb/1,000 gallons condensate throughput
Xylene 0.10 95 lb/1,000 gallons condensate throughput
n -Hexane 3.02 95 lb/1,000 gallons condensate throughput
224 TMP 0.26 95 lb/1,000 gallons condensate throughput
4 of 14 K:\PA\2017\17WE0136.CP1.xlsm
ate Tank Regulatory
ubJect to NSPS 0000 per
G
0.
Produced Water Storage Tank(s) Emissions Inventory
Section 01- Administrative Information
'Facility AIRs ID:
123 9€OF:'. ' .002
-ountv Plant Point
Section 02 - Equipment Description Details
Detailed Emissions Unit
Description:
400 barrel produced water storage tank
Emission Control Device
encfosed combti
Description:
Requested Overall VOC & HAP Control
Efficiency %:
ss
Section 03- Processing Rate Information for Emissions Estimates
Primary Emissions - Storage Tank(s)
Actual Produced Water Throughput =
Requested Permit Limit Throughput =
Potential to Emit (PTE) Produced Water
Throughput =
Secondary Emissions - Combustion Device(s)
Heat content of waste gas=
Volume of waste gas emitted per BBL of liquids
produced = s. 344: scf/bbl
Actual heat content of waste gas routed to combustion device =
Request heat content of waste gas routed to combustion device =
Barrels )bbl) per year
41,975 Barrels (bbl) per year
41,975. Barrels (hbl) per year
2330 Btu/scf
Actual Produced Water Throughput While Emissions Controls Operating = 41,975
23,864 MMBTU per year
23,864 MM BTU per year
Potential to Emit (PTE) heat content of waste gas routed to combustion device = 23,864 MMBTU per year
Section 04 - Emissions Factors & Methodologies
Will this storage tank emit flash emissions?
Emission Factors
Produced Water Tank
Pollutant
Uncontrolled Controlled
(lb/bbl) (lb/bbl)
(Produced Water
Throughput)
(Produced
Water
Throughput)
VOC
Benzene
Toluene
Ethylbenzene
Xylene
0.262
0.007
0.01
0.000
0.000
0.000
0.000
0.001
0.000
Control Device
n -Hexane
224 TMP
0,022
Pollutant
Uncontrolled Uncontrolled
(lb/MMBtu) (lb/bbl)
(waste heat
combusted)
(Produced
Water
Throughput)
PM10
PM2.5
NOx
CO
0.0000
0.0000
0.0000
0.0000
Section 05 - Emissions Inventory
Emission Factor Source
Emission Factor Source
Criteria Pollutants
Potential to Emit
Uncontrolled
(tons/year)
Actual Emissions
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(tons/year) (tons/year)
VOC
PM10
PM2.5
NOx
CO
5.5
S.5
0.3
5.5
0.3
0.0
0.0
0.0
0.0
&O
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Hazardous Air Pollutants
Potential to Emit
Uncontrolled
(tons/year)
Actual Emissions
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(lbs/year) (Ibs/year)
Benzene
Toluene
Ethylbenzene
Xylene
n -Hexane
224 TMP
0.15
0.15
0.01
0.15
0.01
294
55
0.00
0.00
0.00
0.00
0.00
0
0
0.00
0.00
0.00
0,00
0.00
0
0
0.00
0.00
0.00
0.00
0.00
0
0
0.46
0.46
0.02
0.46
0.02
923
46
0.00
0.00
0.00
0.00
0.00
0
0
Section 06 - Regulatory Summa y Analysis
Regulation 3, Parts A, B
Source requires a permit
Regulation 7, Section XVII.B, C.1, C.3
Storage Tank is not subject to Regulation 7, Section XVII
Regulation 7, Section XVI I.C.2
Storage Tank is not subject to Regulation 7, Section XVII.C.2
Regulation 6, Part A, N5PS Subpart 0000
Storage Tank is not subject to MPS 0000
(See regulatory applicability worksheet for detailed analysis)
70114
K:\PA\2017\17W E0136.CP1.xlsm
Produced Water Storage Tank(s) Emissions Inventory
Section 07 - Initial and Periodic Sampling and Testing Requirements
Does the company use a site specific emissions factor to estimate emissions?
If yes and if there are flash emissions, are the emissions factors based on a pressurized liquid water sample drawn a
the facility being permitted and analyzed using flash liberation analysis? This sample should be considered
representative which generally means site -specific and collected within one year of the application received date.
However, if the facility has not been modified (e.g., no new wells brought on-line), then it may be appropriate to use
an older site -specific sample.
If no, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor. See PS Memo 14-03, Questions 5.9 and 5.12 for additional guidance on testing.
Does the company request a control device efficiency greater than 95% for a flare or combustion device?
If yes, the permit will contain and initial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling
Section 08 - Technical Analysis Notes
Section 09 - Inventory SCC Coding and Emissions Factors
AIRS Point #
002
Process # SCC Code
01 4-04-003-15 Fixed Roof Tank, Produced Water, working+breathing+flashing losses
Uncontrolled
Emissions
Pollutant Factor Control% Units
PM10 0.00 0 lb/1,000 gallons liquid throughput
PM2.5 0.00 0 lb/1,000 gallons liquid throughput
NOx 0.00 0 lb/1,000 gallons liquid throughput
VOC 6.2 95 lb/1,000 gallons liquid throughput
CO 0.00 0 lb/1,000 gallons liquid throughput
Benzene 0.17 95 lb/1,000 gallons liquid throughput
Toluene 0.00 95 lb/1,000 gallons liquid throughput
Ethylbenzene 0.00 95 lb/1,000 gallons liquid throughput
Xylene 0.00 95 16/1,000 gallons liquid throughput
n -Hexane 0.52 95 lb/1,000 gallons liquid throughput
224 TMP 0.00 95 lb/1,000 gallons liquid throughput
8 of 14 K:\PA\2017\ 17WE0136.CP1.xlsm
a
z
d
L
O
d
O
d
m
O
d
-O
%
C
E
d
00
N
E
d
3
ra
U
di C
Y
C
O m
3 r s
U W
d
N
.' 3 J
a a
c O w
a 2
>' �a E
O g-
m a
00 = z
di U.
= E a
- Q
d
a • CO
F t m
00 A
d
b0 a a
2
O • r
N N a
a m
N
d Z o
R N •'
3
• d y
0z
V C O
O 0.1 o
O
a v°
0.
0
}
C
Y
ATTAINMENT
6
w m
ti
C
o
a
v m
• O
o • a
JV ° o
d
v L v
a '. a
c
0
41
-
Y
NON -ATTAINMENT
ulation 7. Section XVII
Colorado Re
4- 0
O
0
0
a
E
O
0
C
O
0
3
0
O
0
J
0
0.
a
0
0
x
7
5
u° a
CL
c0
X
U
Section XVII.C.1 - Emissio
a
m
0
.5
c
ea
C
3
O
c0
•0
>
00
N w
a o
O
a w s
O 9 3
4
u 0 .'
X 'a
c
v Y
N o0
d with Air Pollution Control Equipment
v
4,1
re and Mon
Section XVII.C.2 - Cap
art OOOO. Standards of Performance for Crude Oil and Natural Gas Production, Transmission and Distribution
40 CFR. Part 60. Sub
0
age vessel located at a facility in the onshore oil and natural gas production segment, natural gas processing segment or natural gas transmission and storage segment of the industry?
torage vessel constructed, reconstructed, or modified (see definitions 40 CFR, 60.2) between August 23, 2011 and September 18, 2015?
is' from the individual storage vessel greater than or equal to 6 tons per year?
41
m
0
O
O
E
O
O
O
0
O
a
ct to 51515 OOOO
O
O
O
O
0.
z
6 w H m u U N d 3
N m rn o - n
t m m a+ .y .i r. v 4,
m a m a s
a N N N 1!1 Vf « C W V
.041000000 o<
N �a+ vn •m w ? d U
U
•0 0
f§
{04:
[\
) k}
\n
E.0�
§ a 2 , = :
\0
7272{/)%
}3§(\!
ar:))§
-kf2}\
ti:
\ -k\
))72\{72}
\ 7276&{}
/=\8k�
222\/2
\\\/\\
§ di 272:a
/2222\
/,:k2
\/k)L:3\
."2, 2E
.\\j\\
){.}\)
/\\\\\
) \\\j)
▪ )]§w%
\/51.
Division Information
Engineer:
Control Engineer:
Review Date:
Application Date:
Facility Identifiers
Permit No.
AIRs County #
Facility #
Point #
Kirk Bear
Stephanie Spector
5/17/2017
2/10/2017
17WE0136
123 Weld
9F0F
003
Section 01: Administrative Information
Company N Verdad Resources LLC
Source Name: Johnson 8-30N
Source Location: NENW, S31, T2N, R65W
SIC:
Elevation (feet)
1311
5006
Section 02 - Emissions Inventory Analysis
AP -42: Chapter 5.2
Equation 1
L = 12.46*S*P*M/T
L = loading losses in lb per 1000 gallons loaded
S = Saturation Factor
P = true vapor pressure of liquid loaded [psia]
M = molecular weight of vapors [lb/lb-mole]
T= temperature of bulk liquid loaded [deg. R]
1 degree Fahrenheit = 460.67 degree Rankine
Criteria Pollutants
Variables
S
P
M
T
L
0.6 Submerged loading: dedicated normal service
5.9821 psia
39.86 lb/lb-mole bbl/year
520 deg. R 166800
0.236 lb/bbl
19.7 tpy
Non -Criteria Reportable Air Pollutants/Hazardous Air Pollutants
Componen State Defai State Defau Mass Ratio Emissions ( Are Emissions Reportable?
Benzene 0.00041 0.0004 1.025 68 Yes/No
n -hexane 0.0036 0.236 0.015254 600 Yes/No
Section 03 - Regulatory Considerations
Is this site considered an exploration and production location (e.g. well pad)? Yes/No
If yes, review the following two exemptions for applicability:
Does the operator unload less than 10,000 gallons (238 BBLs) of crude oil per day on an annual average Yes/No
If yes, this emissions point is categorically exempt from permit requirements per Regulation 3, Part B, Section II.D.1.1
Does this operator unload less than 6,750 bbls per year of condensate via splash fill or
16,308 bbls per year of condensate via submerged fill procedure? Yes/No
If yes, this emissions point is categorically exempt from permit requirements per Regulation 3, Part B, Section II.D.1.1
Is this site located in an ozone non -attainment area? Yes/No
If yes, this source is subject to Reasonably Available Control Technology (RACT) requirements under Regulation 3, Part B
Section III.D.2.a. This requirement may be met using "submerged fill" and/or vapor balance with emissions routed to an
emissions control device.
Is this facility classified as a major source of HAPs? Yes/No
If yes, evaluate if 40 CFR, Part 63, Subpart EEEE "Organic Liquids Distribution" MACT provisions apply
Does this facility involve the loading of refined crude/condensate in the form of "gasoline"? Yes/No
If yes, proceed to evaluate the following:
Is this facility classified as a "Terminal" as defined per Regulation 7, Section VI.C.2.a? Yes/No
If yes, the provisions of Regulation 7, Section VI.C.2 may apply
Is this facility classified as a "Bulk Plant" as defined per Regulation 7, Section VI.C.3.a? Yes/No
If yes, the provisions of Regulation 7, Section VI.C.3 may apply
Section 04 - SCC Coding
Pollutant Emissions Factor (lb/1,000 gallons)
VOC 3.81 Ib/1,000 gallons
Benzene 0.0065 Ib/1,000 gallons
n -hexane 0.058 Ib/1,000 gallons
40600132: Crude Oil: Submerged Loading (Normal Service) Use if S = 0.6
40600137: Crude Oil: Splash loading (normal Service) Use if S = 1.45
40600142: Crude Oil: Submerged Loading (balanced Service) Use if S = 1.00
40600145: Crude Oil: Splash loading (Balanced Service) Use if S = 1.00 and splash loading
40600148: Crude Oil: Submerged Loading (Clean tanks) Use if S = 0.5
Equipment Description
This source vents natural gas from:
a well head separator
Emissions from this source are:
routed2to anenclosed flare
Natural gas venting from a well head separator. Emissions from this source are routed to an enclosed flare.
Emission Calculation Method
EPA Emission Inventory Improvement Program Publication: Volume II, 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 = SG of gas • MW of air
Xx = mass fraction of x in gas
C = molar volume of ideal gas (379 scf/lb-mol) at 60F and 1 atm
I
RequestedThroughput (Q) 100.0000 MMscf/yr
11415.5 scf/hr I 0.002 MMscf/d I 8.49 MMscf/mo
Vented #DIV/0!
MW 20.290 Ib/Ib-mol
Component
mole %
MW
Ibx/tbmol
mass fraction
E
lb/hr
lb/yr
tpy
Helium
0
4.0026
0.000
0.000
Helium
0.0
0
0.00
CO2
1.1262
44.01
0.496
0.024
CO2
14.9
130776
65.39
N2
1.127
28.013
0.316
0.016
N2
9.5
83300
41.65
methane
82.3101
16.041
13.203
0.651
methane
397.7
3483737
1741.87
ethane
8.6231
30.063
2.592
0.128
ethane
78.1
684001
342.00
propane
3.6681
44.092
1.6173
0.080
propane
48.7
426738
213.37
isobutane
0.5016
58.118
0.2915
0.014
isobutane
8.8
76918
38.46
n -butane
1.5274
58.118
0.8877
0.044
n -butane
26.7
234220
117.11
isopentane
0.3637
72.114
0.2623
0.013
isopentane
7.9
69203
34.60
n -pentane
0.394
72.114
0.2841
0.014
n -pentane
8.6
74968
37.48
cyclopentane
0.0169
70.13
0.0119
0.001
cyclopentane
0.4
3127
1.56
n -Hexane
0.0576
86.18
0.0496
0.002
n -Hexane
1.5
13098
6.55
cyclohexane
0.0092
84.16
0.0077
0.000
cyclohexane
0.2
2043
• 1.02
Other hexanes
0.0813
86.18
0.0701
0.003
Other hexanes
2.1
18487
9.24
heptanes
0.1091
100.21
0.1093
0.005
heptanes
3.3
28847
14.42
methylcyclohexane
0.0251
98.19
0.0246
0.001
methylcyclohexane
0.7
6503
3.25
224-TMP
0.0001
114.23
0.0001
0.000
224-TMP
0.0
30
0.02
Benzene
0.0076
78.12
0.0059
0.000
Benzene
0.2
1567
0.78
Toluene
0.0211
92.15
0.0194
0.001
Toluene
0.6
5130
2.57
Ethylbenzene
0.0019
106.17
0.0020
0.000
Ethylbenzene
0.1
532
0.27
Xylenes
0.0024
106.17
0.0025
0.000
Xylenes
0.1
672
0.34
C8+ Heavies
0.0265
138.237
0.0366
0.002
C8+ Heavies
1.1
9666
4.83
Notes
100 VOC mass fraction: 0.1815 Total VOC Emissions (Uncontrolled)
annual limit assuming 95% control
485.9
24.3
Flaring Information
Equipment Description
Flare to combust low-pressure separator gas during VRU downtime.
Manufacturer
Model
Serial Number
Gas Heating Value
Throughput
1190
119000
Combustion emission factor source:
Btu/scf
MMBtu/yr
AP -42: Chapter 13.5
0.068
lb NOX/MMBtu
tpy NOX
0.31
lb CO/MMBtu
tpy CO
4.05'
18.45
Emissions Summary
Uncontrolled/PTE
Controlled
485.9
24.3
tpy VOC
tpy VOC
Uncontrolled
Total (Ib/yr)
Scenario A
Reportable?
Controlled Total
(lb/yr)
Benzene
1567
Yes
78
Toluene
5130
Yes
257
Ethylbenzene
532
Yes
27
Xylenes
672
Yes
34
n -hexane
13098
Yes
655
224-TMP
30
No
2
Emission Factors for Permit
meter installed:
Modeled liquid thorughput to separator
SCF vented gas/BBL liquid throughput:
Uncontrolled
600 bbl/yr
0.0 scf/bbl
NOX
21.07
Ib/MMscf natur
CO
114.63
lb/MMscf nature
VOC
9717.49
Ib/MMscf nature
Benzene
15.67
Ib/MMscf nature
Toluene
51.30
lb/MMscf nature
Ethylbenzene
5.32
lb/MMscf natur
Xylenes
6.72
Ib/MMscf nature
n -Hexane
130.98
lb/MMscf nature
224-TMP
0.30
lb/MMscf nature
Controlled
NOX
21.07
Ib/MMscf nature
CO
114.63
Ib/MMscf nature
VOC
485.87
Ib/MMscf nature
Benzene
0.78
lb/MMscf nature
Toluene
2.57
lb/MMscf nature
Ethylbenzene
0.27
lb/MMscf nature
Xylenes
0,34
Ib/MMscf nature
n -Hexane
6.55
Ib/MMscf nature
224-TMP
0.02
lb/MMscf nature
Regulatory Applicability
AQCC Regulation 1
This source is subject to the opacity requirements for flares in Section II.A.5:'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.'
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
A
CC Re
lation 2
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 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."
AQCC Regulation 3
Part A.
An APEN is required for this source because uncontrolled VOC emissions exceed two
tons per year in an attainment area.
Part B:
#REF!
#REF!
Is public comment
required?
yes
AQCC Regulation 7
Was the well newly constructed, hydraulically fractured, or recompleted on or after August 1, 2014?
yes
This separator is subject to Reg 7, Section XVII.G. and control requirements of Reg 7, XVII.B.2
Dropdown List
Yes
No
Colorado Air Permitting Project
Project Details
Review Engineer:
Package #:
Received Date:
Review Start Date:
Section 01 - Facility Information
Company Name:
County AIRS ID:
Plant AIRS ID:
Facility Name:
Physical Address/Location:
Type of Facility:
What industry segment?
Is this facility located in a NAAQS
If yes, for what pollutant?
Kirk Bear
358210
2/10/2017
5/15/2017
non -attainment area?
Verdad Resources LLC
123
9FOF
Johnson 8-30N
NENW, Section 31, T2N, R65W
Exploration:& Production Well Pad
#?il & Natural Gas Production & Processing
Yes
❑Carbon Monoxide (CO) [particulate Matter (PM)
Weld
Section 02 - Emissions Units In Permit Application
Quadrant
Section
Township
Range
31
2N
azone (NOx & VOC)
AIRS Point #
Emissions Source Type
Equipment Name
Emissions
Control?
Permit #
Issuance #
Self Cert
Required?
Action
Engineering
Remarks
001
Condensate Tank
Condensate Storage Tanks
Yes
17WE0136
1
Yes
Permit initial
issuance
002
Produced Water Tank _
Produced Water Tank
Yes=-
17WE0136
1
Yes-`
Permit Initial
issuance
003
Hydrocarbon liquid Loading
Condensate Loading
No
17WE0136
1
Yes
Permit Initial
issuance
004
Separatorilenting
Separator Venting
Yes
17WE0136
1
Yes
Permit Initial
issuance
Section 03 - Description of Project
Permit request for this oil and gas exploration and production site
Section 04 - Public Comment Requirements
Is Public Comment Required? Yes
If yes, why? Requesting Synthetic Minor Permit
Section 05 - Ambient Air Impact Analysis Requirements
Was a quantitative modeling analysis required?
If yes, for what pollutants?
If yes, attach a copy of Technical Services Unit modeling results summary.
Section 06 - Facility -Wide Stationary Source Classification
Is this stationary source a true minor?
Is this stationary source a synthetic minor?
If yes, indicate programs and which pollutants:
Prevention of Significant Deterioration (PSD) •
Title V Operating Permits (OP)
No
SO2
NOx
No
Yes
CO
VOC PM2.5 PM10 TSP
❑ ❑
HAPs
U
❑ ❑ El
Colorado Air Permitting Project
Non -Attainment New Source Review (NANSR)
Is this stationary source a major source?
If yes, explain what programs and which pollutants here:
Prevention of Significant Deterioration (PSD)
Title V Operating Permits (OP)
Non -Attainment New Source Review (NANSR)
SO2 NOx
❑ ❑
❑ ❑
0
CO VOC PM2.5 PM10 TSP HAPs
❑ ❑ ❑
❑ ❑ ❑
CI
❑ ❑
Condensate Storage Tank(s) Emissions Inventory
Section 01- Administrative Information
Facility AIRS ID:
123 SEGE 001.....
County Plant Point
Section 02 - Equipment Description Details
Detailed Emissions Unit Three 400 barrel condensate storage tan
Description:
Emission Control Device Englosedcombbstor
Description:
Requested Overall VOC & HAP Control
Efficiency %:
Section 03 - Processing Rate Information for Emissions Estimates
Primary Emissions - Storage Tank(s)
Actual Condensate Throughput=
Requested Permit Limit Throughput =
Potential to Emit (PTE) Condensate
Throughput =
166,800 Barrels (bbl) per year
166,800. Barrels (bbl) per year
800. Barrels (bbl) per year
Secondary Emissions- Combustion Device(s)
Heat content of waste gas= 2330.: Btu/scf
Volume of waste gas emitted per BBL of liquids
produced = 143 scf/bbl
Actual heat content of waste gas routed to combustion device =
Request heat content of waste gas routed to combustion device =
Actual Condensate Throughput While Emissions Controls Operating = 166,800 Barrels (bbl) per year
55,576 MMBTU per year
55,576 MMBTU per year
Potential to Emit (PIE) heat content of waste gas routed to combustion device = 55,576 MMBTU per year
Section 04 - Emissions Factors & Methodologies
Will this storage tank emit flash emissions?
Emission Factors
Condensate Tank
Pollutant
Uncontrolled Controlled
(Ib/bbl) (Ib/bbl)
(Condensate
Throughput)
(Condensate
Throughput)
VOC
8.52
0.024
0.014
0.001
0.004
0,127
0.011 -..
0.43
0.001
0.001
0.000
0.000
0.006
0.001
Benzene
Toluene
Ethylbenzene
Xylene
n -Hexane
224 TMP
Pollutant
Control Device
Uncontrolled Uncontrolled
(lb/MMBtu) (lb/bbl)
(waste heat (Condensate
combusted) Throughput)
PM10
PM2.5
0.0000
0.0000
0.0680
0.3100
NOx
CO
0.0680
0.3100
Section 05 - Emissions Inventory
Emission Factor Source
Emission Factor Source
Criteria Pollutants
Potential to Emit
Uncontrolled
(tons/year)
Actual Emissions
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(tons/year) (tons/year)
VOC
PM10
PM2.5
NOx
CO
710.6
710.6
35.5
710.6
35.5
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
1.9
0.5
0.5
0.5
0.5
8.6
2.2
2.2
2.2
2.2
Hazardous Air Pollutants
Potential to Emit
Uncontrolled
(tons/year)
Actual Emissions
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(lbs/year) piss/year)
Benzene
Toluene
Ethylbenzene
Xylene
n -Hexane
224 TMP
2.0016
2.0016
0.1001
2.0016
0.1001
4003
200
1.1676
1.1676
0.0584
1.1676
0.0584
2335
117
0.0834
0.0834
0.0042
0.0834
0.0042
167
8
0.3336
0.3336
0.0167
0.3336
0.0167
667
33
10.5918
10.5918
0.5296
10.5918
0.5296
21184
1059
0.9174
0.9174
0.0459
0.9174
0.0459
1835
92
Section 06 - Regulatory Summary Analysis _
Regulation 3, Parts A, B
Regulation 7, Section XII.C, D, E, F
Regulation 7, Section XII.G, C
Regulation 7, Section XVII.8, C.1, C.3
Regulation 7, Section XVII.C.2
Regulation 6, Part A, NSPS Subpart Kb
Regulation 6, Part A, NSPS Subpart 0000
Regulation B, Part E, MACT Subpart HH
(See regulatory applicability worksheet for detailed analysis)
Facility attainment -area status has not been established yet
Storage tank is subject to Regulation 7, Section XII.C-F
Storage Tank is not subject to Regulation 7, Section XII.G
Storage tank is subject to Regulation 7, Section XVII, B, C.1 & C.3
Storage tank is subject to Regulation 7, Section XVII.C.2
Storage Tank is not subject to NSPS Kb
Storage Tank is not subject to NSPS 0000
Storage Tank is not subject to MACT NR
3 of 14
K:\PA\2017\17 W E0136. CP1.xlsm
Condensate Storage Tank(s) Emissions Inventory
Section 07 - Initial and Periodic Sampling and Testing Requirements
Does the company use the state default emissions factors to estimate emissions?
If yes, are the uncontrolled actual or requested emissions estimated to be greater than or equal to 80 tons VOC per year? wt,a,rm
If yes, the permit will contain an 'Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01.
Does the company use a site specific emissions factor to estimate emissions?
If yes and if there are flash emissions, are the emissions factors based on a pressurized liquid sample drawn at the
facility being permitted? This sample should be considered representative which generally means site -specific and
collected within one year of the application received date. However, if the facility has not been modified (e.g., no
new wells brought online(, then it maybe appropriate to use an older site specific sample. Yes
If no, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01.
Does the company request a control deuce efficiency greater than 95% for a flare or combustion device? 'j`�.
If yes, the permit will contain and initial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling
Section 08 - Technical Analysis Notes
Section 09 - Inventory SCC Coding and Emissions Factors
AIRS Point #
2
Process # SCC Code
01 4.1?'443401,14147
Sri e
Uncontrolled
Emissions
Pollutant Factor Control % Units
PM10 0.00 0 lb/1,000 gallons condensate throughput
PM2.5 0.00 0 lb/1,000 gallons condensate throughput
NOx 0.14 0 lb/1,000 gallons condensate throughput
VOC 202.9 95 lb/1,000 gallons condensate throughput
CO 0.63 0 lb/1,000 gallons condensate throughput
Benzene 0.57 95 lb/1,000 gallons condensate throughput
Toluene 0.33 95 lb/1,000 gallons condensate throughput
Ethylbenzene 0.02 95 lb/1,000 gallons condensate throughput
Xylene 0.10 95 lb/1,000 gallons condensate throughput
n -Hexane 3.02 95 lb/1,000 gallons condensate throughput
224 TMP 0.26 95 lb/1,000 gallons condensate throughput
4 of 14 K:\PA\2017\17WE0136.CP1.xlsm
MACTHH - There are no MAR
a
should remain subject to WS OOOO per 50.5365 (e)(2) even
e
iew PACT requir
Produced Water Storage Tank(s) Emissions Inventory
Section 01- Administrative Information
Facility AIRs ID:
123
County
9FOF r._ 002'.
Plant Point
Section 02 - Equipment Description Details
Detailed Emissions Unit
Description:
Emission Control Device
enclosed combustor
Description:
Requested Overall VOC & HAP Control
Efficiency %:
400 barrel produced water storage tank
Section 03- Processing Rate Information for Emissions Estimates
Primary Emissions - Storage Tank(s)
Actual Produced Water Throughput =
Requested Permit Limit Throughput =
Potential to Emit (PTE) Produced Water
Throughput =
Secondary Emissions - Combustion Device(s)
Heat content of waste gas
Volume of waste gas emitted per BBL of liquid
produced =
Actual heat content of waste gas routed to combustion device =
Request heat content of waste gas routed to combustion device =
Barrels (bbl) per year
Barrels (bbl) per year
41,975, Barrels (bbl) per year
Btu/scf
scf/bbl
Actual Produced Water Throughput While Emissions Controls Operating =
23,364 MMBTU per year
23,864 MMBTU per year
Potential to Emit (PTE) heat content of waste gas routed to combustion device = 23,864 MMBTU per year
Section 04- Emissions Factors & Methodologies
Will this storage tank emit flash emissions?
Emission Factors
Produced Water Tank
Pollutant
Uncontrolled Controlled
(Ib/bbl) (lb/bbl)
(Produced Water
Throughput)
(Produced
Water
Throughput)
VOC
0.262
0.007
0.01
0.0W
0.000
0.000
0.000
0.001
0.000
Control Device
Benzene
Toluene
Ethylbenzene
Xylene
n -Hexane
224 TMP
0.022.
Pollutant
Emission Factor Source
Uncontrolled Uncontrolled
(lb/MMBtu) (Ib/bbl)
(waste heat
combusted)
(Produced
Water
Throughput)
PM10
PM2.5
0.0000
0.0000
0.0000
0.0000
NOx
CO
Section 05 - Emissions Inventory
Emission Factor Source
Criteria Pollutants
Potential to Emit
Uncontrolled
(tons/year)
Actual Emissions
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(tons/year) (tons/year)
VOC
PM10
PM2.5
NOx
CO
5.5
5.5
0.3
5.5
0.3
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0,0
0.0
Hazardous Air Pollutants
Potential to Emit
Uncontrolled
(tons/year)
Actual Emissions
Uncontrolled Controlled
(tans/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(Ibs/year) (Ibs/year)
Benzene
Toluene
Ethylbenzene
Xylene
n -Hexane
224 TMP
0.15
0.15
0.01
0.15
0.01
294
IS
0.00
0.00
0.00
0.00
0.00
0
0
0.00
0.00
0.00
0.00
0.00
0
0
0.00
0.00
0.00
0.00
0.00
0
0
0.46
0.46
0.02
0.46
0.02
923
46
0.00
0.00
0.00
0,00
0.00
0
0
Section 06 - Regulatory Summary Analnsis
Regulation 3, Parts A, B
Regulation 7, Section XVII.B, C.1, C.3
Regulation 7, Section XVII.C.2
Regulation 6, Part A, NSPS Subpart 0000
(See regulatory applicability worksheet for detailed analysis)
Source requires a permit
Storage Tank is not subject to Regulation 7, Section XVII
Storage Tank is not subject to Regulation 7, Section XVII.C.2
Storage Tank is not subject to NSPS 0000
7 of 14
K.\PA\2017\ 17 W E0136.C P1.x l sm
Produced Water Storage Tank(s) Emissions Inventory
Section 07 - Initial and Periodic Sampling and Testing Requirements
Does the company use a site specific emissions factor to estimate emissions? �z
If yes and if there are flash emissions, are the emissions factors based on a pressurized liquid water sample drawn
the facility being permitted and analyzed using flash liberation analysis? This sample should be considered
representative which generally means site -specific and collected within one year of the application received date.
However, if the facility has not been modified (e.g., no new wells brought on-line), then it maybe appropriate to use
an older site -specific sample.
If no, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor. See PS Memo 14-03, Questions 5.9 and 5.12 for additional guidance on testing.
Does the company request a control device efficiency greater than 95% for a flare or combustion device?
If yes, the permit will contain and initial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling
Section 98 - Technical Analysis Notes
Section 09 - Inventory SCC Coding and Emissions Factors
AIRS Point
002
Process !I SCC Code
01 4-04-003-15 Fixed Roof Tank, Produced Water, working+breathing+flashing losses
Uncontrolled
Emissions
Pollutant Factor Control% Units
PM10 0.00 0 lb/1,000 gallons liquid throughput
PM2.5 0.00 0 lb/1,000 gallons liquid throughput
NOx 0.00 0 lb/1,000 gallons liquid throughput
VOC 6.2 95 lb/1,000 gallons liquid throughput
CO 0.00 0 lb/1,000 gallons liquid throughput
Benzene 0.17 95 lb/1,000 gallons liquid throughput
Toluene 0.00 95 lb/1,000 gallons liquid throughput
Ethylbenzene 0.00 95 lb/1,000 gallons liquid throughput
Xylene 0.00 95 lb/1,000 gallons liquid throughput
n -Hexane 0.52 95 lb/1,000 gallons liquid throughput
224 TMP 0.00 95 lb/1,000 gallons liquid throughput
8 of 14 K:\PA\2017\17WE0136.CP1.xlsm
a
2
3
d
c
a
a
d
v
G1
O
O
Co
3
C,
d
r
t
m
O
v
C
c
w
E
m
E
v
3
v
v c
L r
C
a r
3
To
o W
c
Q u
>' O.
O 0'
3
7
C) D
m
Y C)
c
F- ..
v m
00
.0
O Y
H a
wt
d 2
as m
3
2
U 0
:11!
O
a a
E
d B - APEN and Permit Reg
a
a
0
c
=
d that source is in the Non
c
> 2
Q
is in the Non -Attainment Area
v v
O
w
ri ry ri
Section XVII
Colorado Re
2
O .O O °
U U U'
0
or natural gas processing pla
H N rtl
an 6 tons per year VOC?
m >
O O
2
F-
T
0
O
a
0
3
0
v
0
}
Y
O
O
d with Air Pollution Control Equipm
-
2
a
Section XVII.C.2 - Cap
sion and Distribution
Standards of Performance for Crude Oil and Natural Gas Production. Tra
ci
b
C
a
LL
a
0
Does thi
a
O
O
2
n
U
o
>
4 o
� N
O -O A
.mgt O
L
O S O - O .°
N 0 0 .>
a ° 5 o v, c
^avv0a°
v v w
> 0 a 0 a . E
E
a
2
o.
O
O
O
O
a
2
a
c
E
O
9
0
E
m
a
u
O
ci
a,
T
a
0
b
0
m
0
E
0
V
O
O
O
O
a
2
O
w
.,
N~
d W
v o .!°4.
" v c
a C C °
o 2 y E
v °
a « a v
c > • ¢ T a
2
Q
a
c
a
C
z
v
o " y m u
O > O .3 c u P
O m w v m> g
c 9 « z ° o A 3 N
O w r U u ` 3
u m 9
,n o w a 3
m a m ti a •a 'c >
m ui vi v� ,n v� 'E ' 5
0 00 0
o °o °a °o °o ? d
Disclaimer
N N
L
Division Information
Engineer:
Control Engineer:
Review Date:
Application Date:
Facility Identifiers
Permit No.
AIRs County #
Facility #
Point #
Section 01: Administra
Company fs
Source Name:
Source Location:
SIC:
Elevation (feet)
Kirk Bear
Stephanie Spector
5/17/2017
2/10/2017
17W E0136
123 Weld
9FOF
003
tive Information
Verdad Resources LLC
Johnson 8-30N
NENW, S31, T2N, R65W
1311
5006
Section 02 - Emissions Inventory Analysis
AP -42: Chapter 5.2
Equation 1
L = 12.46*S*P*M/t
L = loading losses in lb per 1000 gallons loaded
S = Saturation Factor
P = true vapor pressure of liquid loaded [psia]
M = molecular weight of vapors [lb/lb-mole]
T = temperature of bulk liquid loaded [deg. R]
1 degree Fahrenheit = 460.67 degree Rankine
Criteria Pollutants
Variables
S
P
M
T
0.6 Submerged loading: dedicated normal service
5.9821 psia
39.86 lb/lb-mole bbl/year
520 deg. R 166800
0.236 Ib/bbl
19.7 tpy
Non -Criteria Reportable Air Pollutants/Hazardous Air Pollutants
Componen State Defai State Defau Mass Ratio Emissions ( Are Emissions Reportable?
Benzene 0.00041 0.0004 1.025 68 Yes/No
n -hexane 0.0036 0.236 0.015254 600 Yes/No
Section 03 - Regulatory Considerations
Is this site considered an exploration and production location (e.g. well pad)? Yes/No
If yes, review the following two exemptions for applicability:
Does the operator unload less than 10,000 gallons (238 BBLs) of crude oil per day on an annual average Yes/No
If yes, this emissions point is categorically exempt from permit requirements per Regulation 3, Part B, Section II.D.1.1
Does this operator unload less than 6,750 bbls per year of condensate via splash fill or
16,308 bbls per year of condensate via submerged fill procedure? Yes/No
If yes, this emissions point is categorically exempt from permit requirements per Regulation 3, Part B, Section II.D.1.1
Is this site located in an ozone non -attainment area? Yes/No
If yes, this source is subject to Reasonably Available Control Technology (RACT) requirements under Regulation 3, Part B
Section III.D.2.a. This requirement may be met using "submerged fill" and/or vapor balance with emissions routed to an
emissions control device.
Is this facility classified as a major source of HAPs? Yes/No
If yes, evaluate if 40 CFR, Part 63, Subpart EEEE "Organic Liquids Distribution" MACT provisions apply
Does this facility involve the loading of refined crude/condensate in the form of "gasoline"? Yes/No
If yes, proceed to evaluate the following:
Is this facility classified as a "Terminal" as defined per Regulation 7, Section VI.C.2.a? Yes/No
If yes, the provisions of Regulation 7, Section VI.C.2 may apply
Is this facility classified as a "Bulk Plant" as defined per Regulation 7, Section VI.C.3.a? Yes/No
If yes, the provisions of Regulation 7, Section VI.C.3 may apply
Section 04 - SCC Coding
Pollutant Emissions Factor (Ib/1,000 gallons)
VOC 3.81 lb/1,000 gallons
Benzene 0.0065 lb/1,000 gallons
n -hexane 0.058 lb/1,000 gallons
40600132: Crude Oil: Submerged Loading (Normal Service) Use if S = 0.6
40600137: Crude Oil: Splash loading (normal Service) Use if S = 1.45
40600142: Crude Oil: Submerged Loading (balanced Service) Use if S = 1.00
40600145: Crude Oil: Splash loading (Balanced Service) Use if S = 1.00 and splash loading
40600148: Crude Oil: Submerged Loading (Clean tanks) Use if S = 0.5
Equipment Description
This source vents natural gas from:
a well head separator
Emissions from this source are:
routed to an enclosed flare
Natural gas venting from a well head separator. Emissions from this source are routed to an enclosed flare.
Emission Calculation Method
EPA Emission Inventory Improvement Program Publication: Volume II, Chapter 10 - Displacement Equation (10.4-3)
Ex = 0 MW'Xx/C
Ex = emissions of pollutant x
Q = Volumetric flow rate/volume of gas processed
MW = Molecular weight of gas = SG of gas * MW of air
Xx = mass fraction of x in gas
C = molar volume of ideal gas (379 scf/lb-mol) at 60F and 1 atm
I
RequestedThroughput (O) 100.0000 MMscf/yr
11415.5 scf/hr I 0.002 MMscf/d I 8.49 MMscf/mo
% Vented #DIV/0l
MW 20.290 Ib/Ib-mol
Component
mole %
MW
lbx/Ibmol
mass fraction
E
Ib/hr
lb/yr
tpy
Helium
0
4.0026
0.000
0.000
Helium
0.0
0
0.00
CO2
1.1262
44.01
0.496
0.024
CO2
14.9
130776
65.39
N2
1.127
28.013
0.316
0.016
N2
9.5
83300
41.65
methane
82.3101
16.041
13.203
0.651
methane
397.7
3483737
1741.87
ethane
8.6231
30.063
2.592
0.128
ethane
78.1
684001
342.00
propane
3.6681
44.092
1.6173
0.080
propane
48.7
426738
213.37
isobutane
0.5016
58.118
0.2915
0.014
isobutane
8.8
76918
38.46
n -butane
1.5274
58.118
0.8877
0.044
n -butane
26.7
234220
117.11
isopentane
0.3637
72.114
0.2623
0.013
isopentane
7.9
69203
34.60
n -pentane
0.394
72.114
0.2841
0.014
n -pentane
8.6
74968
37.48
cyclopentane
0.0169
70.13
0.0119
0.001
cyclopentane
0.4
3127
1.56
n -Hexane
0.0576
86.18
0.0496
0.002
n -Hexane
1.5
13098
6.55
cyclohexane
0.0092
84.16
0.0077
0.000
cyclohexane
0.2
2043
1.02
Other hexanes
0.0813
86.18
0.0701
0.003
Other hexanes
2.1
18487
9.24
heptanes
0.1091
100.21
0.1093
0.005
heptanes
3.3
28847
14.42
methylcyclohexane
0.0251
98.19
0.0246
0.001
methylcyclohexane
0.7
6503
3.25
224-TMP
0.0001
114.23
0.0001
0.000
224-TMP
0.0
30
0.02
Benzene
0.0076
78.12
0.0059
0.000
Benzene
0.2
1567
0.78
Toluene
0.0211
92.15
0.0194
0.001
Toluene
0.6
5130
2.57
Ethylbenzene
0.0019
106.17
0.0020
0.000
Ethylbenzene
0.1
532
0.27
Xylenes
0.0024
106.17
0.0025
0.000
Xylenes
0.1
672
0.34
C8+ Heavies
0.0265
138.237
0.0366
0.002
C8+ Heavies
1.1
9666
4.83
Notes
100 VOC mass fraction: 0.1815 Total VOC Emissions (Uncontrolled)
annual limit assuming 95% control
485.9
24.3
Flaring Information
Equipment Description
Flare to combust low-pressure separator gas during VRU downtime.
Manufacturer
Model
Senal Number
Gas Heating Value
Throughput
1190
119000
Combustion emission factor source:
Btu/scf
MMBtu/yr
AP -42: Chapter 13.5
0.068
lb NOX/MMBtu
tpy NOX
0.31
lb CO/MMBtu
tpy CO
4.05'
Emissions Summary
Uncontrolled/PTE
485.9
tpy VOC
Controlled
24.3
tpy VOC
Uncontrolled
Total (lb/yr)
Scenario A
Reportable?
Controlled Total
(Ib/yr)
Benzene
1567
Yes
78
Toluene
5130
Yes
257
Ethylbenzene
532
Yes
27
Xylenes
672
Yes
34
n -hexane
13098
Yes
655
224-TMP
30
No
2
Emission Factors for Permit
meter installed:
Modeled liquid thooughput to separator:
SCF vented gas/BBL liquid throughput:
Uncontrolled
600 bbl/yr
0.0 scf/bbl
NOX
21.07
lb/MMscf nature
CO
114.63
lb/MMscf nature
VOC
9717.49
lb/MMscf nature
Benzene
15.67
lb/MMscf nature
Toluene
51.30
lb/MMscf nature
Ethylbenzene
5.32
lb/MMscf nature
Xylenes
6.72
lb/MMscf nature
n -Hexane
130.98
lb/MMscf nature
224-TMP
0.30
lb/MMscf nature
Controlled
NOX
21.07
lb/MMscf nature
CO
114.63
lb/MMscf nature
VOC
485.87
lb/MMscf natur
Benzene
0.78
lb/MMscf nature
Toluene
2.57
lb/MMscf nature
Ethylbenzene
0.27
lb/MMscf nature
Xylenes
0.34
lb/MMscf nature
n -Hexane
6.55
lb/MMscf nature
224-TMP
0.02
lb/MMscf nature
Regulatory Applicability
AQCC Regulation 1
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
This source is subject to the opacity requirements for flares in Section II.A.5:'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.'
AQCC Regulation 2
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 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."
AQCC Regulation 3
Part A:
An APEN is required for this source because uncontrolled VOC emissions exceed two
tons per year in an attainment area.
Part B:
#REF!
#REF!
Is public comment
required?
yes
AQCC Regulation 7
Was the well newly constructed, hydraulically fractured, or recompleted on or after August 1, 2014?
yes
This separator is subject to Reg 7, Section XVII.G. and control requirements of Reg 7, XVII.B.2
Dropdovm Lst
Yes
No
Colorado Air Permitting Project
Project Details
Review Engineer:
Package #:
Received Date:
Review Start Date:
Section 01- Facility Information
Company Name: Verdad Resources LLC
County AIRS ID: 123
Plant AIRS ID: 9fOF
Facility Name: Johnson 8-30N
Physical Address/Location: NENW, Section 31, T2N, R65W
Type of Facility: Exploration;& Production Well Pad
What industry segment? Oil & Natural Gas Production & Processing
Is this facility located in a NAAQS non -attainment area? Yes
If yes, for what pollutant? ❑Carbon Monoxide (CO) Dartrulate Matter (PM)
Kirk Bear'
358210
2/10/2017
5/15/2017
Weld
1
Section 02 - Emissions Units In Permit Application
Quadrant
Section
Township
Range
31
21,1_
zone (NOx & VOC)
AIRS Point #
Emissions Source Type
Equipment Name
Emissions
Control?
Permit #
Issuance #
Self Cert
Required?
Action
Engineering
Remarks
001
Condensate Tank
Condensate Storage Tanks
Yes
17WE0136
1
Yes
Permit initial
Issuance
002
Produced Water Tank
Produced Water Tank
Yes
17WE0136
1
Yes
Permit initial
Issuance
003
HydrocarbonLiquidLoading;
Condensate Loading
No
17WE0136
1
Yes
ier 't initial,
Issuance
004
tor Venting
Separator Venting
Yes
17WE0136
1
Yes
Permit initial
Issuance
Section 03 - Description of Project
Permit request for this oil and gas exploration and production site
Section 04 - Public Comment Requirements
Is Public Comment Required? Yes
If yes, why? Requesting Synthetic Minor Permit
Section OS - Ambient Air Impact Analysis Requirements
Was a quantitative modeling analysis required? fto
If yes, for what pollutants?
If yes, attach a copy of Technical Services Unit modeling results summary.
Section 06 - Facility -Wide Stationary Source Classification
Is this stationary source a true minor?
Is this stationary source a synthetic minor?
If yes, indicate programs and which pollutants:
Prevention of Significant Deterioration (PSD)
Title V Operating Permits (OP)
S02
NOx
El
No
Yes
CO
VOC PM2.5 PM10 TSP
❑ ❑
El ❑
HAPs
El
❑'
El El
Colorado Air Permitting Project
Non -Attainment New Source Review (NANSR)
Is this stationary source a major source?
If yes, explain what programs and which pollutants here:
Prevention of Significant Deterioration (PSD)
Title V Operating Permits (OP)
Non -Attainment New Source Review (NANSR)
LI
SO2 NOx
❑ ❑
El ❑
❑
O
CO VOC PM2.5 PM10 TSP HAPs
❑ ❑ ❑
❑ ❑ El El
❑ ❑
Condensate Storage Tank(s) Emissions Inventory
Section 01 - Administrative Information
Facility AIRS ID:
123
County
9FOF 001.
Plant Point
Section 02 - Equipment Description Details
Detailed Emissions Unit Three400 barrel condensate;:
Description:
Emission Control Device
Description:
Requested Overall VOC & HAP Control
Enclosed combustor.
95
Section 03 - Processing Rate Information for Emissions Estimates
Primary Emissions - Storage Tank(s)
Actual Condensate Throughput =
Requested Permit Limit Throughput =
Potential to Emit (PTE) Condensate
Throughput=
166,800 Barrels (bbl) per year Actual Condensate Throughput While Emissions Controls Operating =
166800 Barrels (bbl) per year
166,.800.. Barrels (bbl) per year
Secondary Emissions - Combustion Device(s)
Heat content of waste gas= 2330: Btu/scf
Volume of waste gas emitted per BBL of liquids
produced = 143> scf/bbl
Actual heat content of waste gas routed to combustion device =
Request heat content of waste gas routed to combustion device =
55,576 MMBTU per year
55,576 MMBTU per year
Potential to Emit (PTE) heat content of waste gas routed to combustion device = 55,576 MMBTU per year
Section 04 - Emissions Factors & Methodologies
Will this storage tank emit flash emissions?
Emission Factors
Condensate Tank
Pollutant
Uncontrolled Controlled
(16/661) (16/661)
(Condensate
Throughput)
(Condensate
Throughput)
Emission Factor Source
VOC
Benzene
Toluene
8.52....
0.024
0.014
0.001
0.004-.:
0.127
0.011
0.43
0.001
0.001
0.000
0.000
0.006
0.001
Control Device
Ethylbenzene
Xylene
n -Hexane
224 TMP
Pollutant
Emission Factor Source
Uncontrolled Uncontrolled
(Ib/MMBtu) (lb/bbl)
(waste heat
combusted)
(Condensate
Throughput)
PM10
PM2.5
NOx
CO
0.0000
0.0000
0.0680
0.3100
Section 05 - Emissions Inventory
0.0680
0.3100
Criteria Pollutants
Potential to Emit
Uncontrolled
(tons/year)
Actual Emissions
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(tons/year) (tons/year)
VOC
PM10
PM2.5
NOx
CO
710.6
710.6
35.5
710.6
35.5
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
1.9
0.0
0.5
0.5
0.5
8.6
2.2
2.2
2.2
2.2
Hazardous Air Pollutants
Potential to Emit
Uncontrolled
(tons/year)
Actual Emissions
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(Its/year) (Ibs/year)
Benzene
Toluene
Ethylbenzene
Xylene
n -Hexane
224 TMP
2.0016
2.0016
0.1001
2.0016
0.1001
4003
200
1.1676
1.1676
0.0584
1.1676
0.0584
2335
117
0.0834
0.0834
0.0042
0.0834
0.0042
167
8
0.3336
0.3336
0.0167
0.3336
0.0167
667
33
10.5918
10.5918
0.5296
10.5918
0.5296
21184
1059
0.9174
0.9174
0.0459
0.9174
0.0459
1835
92
Section 06 - Re • ulatory Summary Anah<sts
Regulation 3, Parts A, B
Regulation 7, Section XII.C, D, E, F
Regulation 7, Section XII.G, C
Regulation 7, Section XVII.8, C.1, C.3
Regulation 7, Section XVII.C.2
Regulation 6, Part A, SOPS Subpart Kb
Regulation 6, Part A, NSPS Subpart 0000
Regulation 8, Part E, MACT Subpart HH
(See regulatory applicability worksheet for detailed analysis)
Facility attainment -area status has not been established yet
Storage tank is subject to Regulation 7, Section XII.C-F
Storage Tank is not subject to Regulation 7, Section )(ILO
Storage tank is subject to Regulation 7, Section XVII, B. C.I & C.3
Storage tank is subject to Regulation 7, Section XVII.C.2
Storage Tank is not subject to 55P5 Kb
Storage Tank is not subject to N5P5 0000
Storage Tank is not subject to MACT HH
166;
Barrels (bbl) per year
3 of 14
K:\PA\2017\17W E0136.CP1.xlsm
Condensate Storage Tank(s) Emissions Inventory
Section 07 - Initial and Periodic Sampling and Testing Requirements
Does the company use the state default emissions factors to estimate emissions?
If yes, are the uncontrolled actual or requested emissions estimated to be greater than or equal to 80 tons VOC per year?
If yes, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in PS Memo 05-01.
Does the company use a site specific emissions factor to estimate emissions?
If yes and if there are flash emissions, are the emissions factors based on a pressurized liquid sample drawn at the
facility being permitted? This sample should be considered representative which generally means site specific and
collected within one year of the application received date. However, if the facility has not been modified (e.g., no
new wells brought on-line), then it may be appropriate to use an older site -specific sample. Yes
If no, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor based on guidelines in P5 Memo 05-01.
Does the company request a control device efficiency greater than 95% for a flare or combustion device?
If yes, the permit will contain and initial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling
Section 08 - Technical Analysis Notes
Section 09 - Inventory SCC Coding and Emissions Factors
AIRS Point 0
2
Process 0 SCC Code
01
Uncontrolled
Emissions
Pollutant Factor Control % Units
PM10 0.00 0 lb/1,000 gallons condensate throughput
PM2.5 0.00 0 lb/1,000 gallons condensate throughput
NOx 0.14 0 lb/1,000 gallons condensate throughput
VOC 202.9 95 lb/1,000 gallons condensate throughput
CO 0.63 0 lb/1,000 gallons condensate throughput
Benzene 0.57 95 lb/1,000 gallons condensate throughput
Toluene 0.33 95 lb/1,000 gallons condensate throughput
Ethylbenzene 0.02 95 lb/1,000 gallons condensate throughput
' Xylene 0.10 95 lb/1,000 gallons condensate throughput
n -Hexane 3.02 95 lb/1,000 gallons condensate throughput
224 TMP 0.26 95 lb/1,000 gallons condensate throughput
4 of 14 if \PA\2017\17WE0136.CP1.xlsm
E n
8
S
T.
E
Produced Water Storage Tank(s) Emissions Inventory
Section 01- Administrative Information
'Facility AIRs ID:
County
9FOP ".
Plant
Poin
Section 02 - Equipment Description Details
Detailed Emissions Unit 400 barrel produced water storage tank
Description:
Emission Control Device
enclosed comity
Description:
Requested Overall VOC & HAP Control
Efficiency %:
Section 03 - Processing Rate Information for Emissions Estimates
Primary Emissions - Storage Tank(s)
Actual Produced Water Throughput =
Requested Permit Limit Throughput =
Potential to Emit (PTE) Produced Water
Throughput =
41,975 Barrels (bbl) per year Actual Produced Water Throughput While Emissions Controls Operating =
41.975.: Barrels (bbl) per year
41,975 Barrels (bbl) per year
Secondary Emissions - Combustion Device(s)
Heat content of waste gas= 2330Btu/scf
Volume of waste gas emitted per BBL of liquids-'
produced = ''244 scf/bbl
Actual heat content of waste gas routed to combustion device -
Request heat content of waste gas routed to combustion device =
23,864 MMBTU per year
23,864 MMBTU per year
Potential to Emit (PTE) heat content of waste gas routed to combustion device = 23,864 MMBTU per year
Section 04- Emissions Factors & Methodologies
Will this storage tank emit flash emissions?
Emission Factors
Produced Water Tank
Pollutant
Uncontrolled Controlled
(lb/bbl) (1b/bbl)
(Produced Water
Throughput)
(Produced
Water
Throughput)
VOC
Benzene
Toluene
Ethylbenzene
Xylene
n -Hexane
224 TMP
O.262;
0.007
0.022,
0.01
0.000
0.000
0.000
0.000
0.001
0.000
Control Device
Pollutant
Emission Factor Source
Uncontrolled Uncontrolled
(Ib/MMBtu) (lb/bbl)
(waste heat
combusted)
(Produced
Water
Throughput)
PM10
PM2.5
NOx
CO
0.0000
0.0000
0.0000
0.0000
Emission Factor Source
Section 05 - Emissions Inventory
Criteria Pollutants
Potential to Emit
Uncontrolled
(tons/year)
Actual Emissions
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(tons/year) (tons/year)
VOC
PM10
PM2.5
NOx
CO
5.5
5.5
0.3
5.5
0.3
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
Hazardous Air Pollutants
Potential to Emit
Uncontrolled
(tons/year)
Actual Emissions
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(tons/year) (tons/year)
Requested Permit Limits
Uncontrolled Controlled
(lbs/year) (Ibs/year)
Benzene
Toluene
Ethylbenzene
Xylene
n -Hexane
224 TMP
0.15
0.15
0.01
0.15
0.01
294
15
0.00
0.00
0.00
0.00
0.00
0
0
0.00
0.00
0.00
0.00
0.00
0
0
0.00
0.00
0.00
0.00
0.00
0
0
0.46
0.46
0,02
0.46
0.02
923
46
0.00
0.00
0.00
0.00
0.00
0
0
Section 06 - Regulatory Summary Analysis _
Regulation 3, Parts A, B
Regulation 7, Section XVII.B, C.1, C.3
Regulation 7, Section XVII.C.2
Regulation 6, Part A, NSPS Subpart 0000
(See regulatory applicability worksheet for detailed analysis)
Source requires a permit
Storage Tank is not subject to Regulation 7, Section XVII
Storage Tank is not subject to Regulation 7, Section XVII.C.2
Storage Tank is not subject to NSPS 0000
7 of 14
K:\PA\2017\17W E0136.CP1.xlsm
Produced Water Storage Tank(s) Emissions Inventory
Section 07 - Initial and Periodic Sampling and Testing Requirements
Does the company use a site specific emissions factor to estimate emissions?
If yes and if there are flash emissions, are the emissions factors based on a pressurized liquid water sample drawn a
the facility being permitted and analyzed using flash liberation analysis? This sample should be considered
representative which generally means site -specific and collected within one year of the application received date.
However, if the facility has not been modified (e.g., no new wells brought on-line), then it may be appropriate to use
an older site -specific sample.
If no, the permit will contain an "Initial Compliance" testing requirement to develop a site specific emissions factor. See PS Memo 14-03, Questions 5.9 and 5.12 for additional guidance on testing.
Does the company request a control device efficiency greater than 95% for a flare or combustion device?
If yes, the permit will contain and initial compliance test condition to demonstrate the destruction efficiency of the combustion device based on inlet and outlet concentration sampling
Section 08 - Technical Analysis Notes
Section 09 - Inventory SCC Coding and Emissions Factors
AIRS Point # Process # SCC Code
002 01 4-04-003-15 Fixed Roof Tank, Produced Water, working+breathing+flashing losses
Uncontrolled
Emissions
Pollutant Factor Control % Units
PM10 0.00 0 lb/1,000 gallons liquid throughput
PM2.5 0.00 0 lb/1,000 gallons liquid throughput
NOx 0.00 0 lb/1,000 gallons liquid throughput
VOC 6.2 95 lb/1,000 gallons liquid throughput
CO 0.00 0 lb/1,000 gallons liquid throughput
Benzene 0.17 95 lb/1,000 gallons liquid throughput
Toluene 0.00 95 lb/1,000 gallons liquid throughput
Ethylbenzene 0.00 95 lb/1,000 gallons liquid throughput
Xylene 0.00 95 lb/1,000 gallons liquid throughput
n -Hexane 0.52 95 lb/1,000 gallons liquid throughput
224 TMP 0.00 95 lb/1,000 gallons liquid throughput
8 of 14 K:\PA\2017\ 17WE0136.CP1.xlsm
Produced Water Storage Tank Regulatory Analysis Worksheet
Please note that NSPS Kb might be might be applicable for certain tanks at water management and injection facilities. If the tanks you are reviewing are at one of these facilities, please review NSPS Kb.
A and B - APEN and Permit Reouirem
heated that source is in the Non-Attai
Colorado Regulation 3 P
ATTAINMENT
N N M
0
0
0-
NON -ATTAINMENT
C
c
0
0
Colorado Re
tH
.- o
o a 2
° °
V a l7 v
N M V (0
Equipment and Prevention of Emissions
a 'N
v
o a
V
H
n
0
a
C
m
03
0
0
o-
o 0 6
v w a 3 v
m u 0 v O
o
X x x
v
c c c «
0 o g
v
O N Vv 0
00
on Control Equipm
3
F
ex
U
0
N
art OOOO. Standards of Performance for Crude Oil and Natural Gas Production. Transmission and Distribution
40 CFR. Part 60. Sub
N M a
O
O
Z
v
O
O
O
O
c
E
N
E
0
0
0
b
0
a
0
0
rea. If the tank meets both criteria, then review RACT requirements.
c
m m
2 Z
S'
c
a o
O c
O y
O
a
C C O A
E E
v a a
0 N 0
Z
m m a T
V
m
c n a
a O i i' a
W C
o C O
a Eb g
g u v
.n> v E-;; 3 0
o v O 0
N ° « v a a
c � ¢ O O n
(0 a v
m m o o O
a ca+ - o y
` `c' jO .J
n v a 0 0 8.j m
° o N 00
o ,-
o a o u N E 9
Q u o 0 0 4, `
0 u
c m o ! O
T7, -,
m `m o m> y
N L.'
m
N
O • w H m U y
Q N M IA iD n "6, 3 '0
., m a m a s `� - d
a u, vi ui ul ,n 2 c O H
1S5S2S535zeg it
g
Disclaimer
Division Information
Engineer:
Control Engineer:
Review Date:
Application Date:
Facility Identifiers
Permit No.
AIRs County #
Facility #
Point #
Kirk Bear
Stephanie Spector
5/17/2017
2/10/2017
17W E0136
123 Weld
9F0F
003
Section 01: Administrative Information
Company N Verdad Resources LLC
Source Name: Johnson 8-30N
Source Location: NENW, S31, T2N, R65W
SIC:
Elevation (feet)
1311
5006
Section 02 - Emissions Inventory Analysis
AP -42: Chapter 5.2
Equation 1
L = 12.46*S*P*M/T
L = loading losses in lb per 1000 gallons loaded
S = Saturation Factor
P = true vapor pressure of liquid loaded [psia]
M = molecular weight of vapors [lb/lb-mole]
T = temperature of bulk liquid loaded [deg. R]
1 degree Fahrenheit = 460.67 degree Rankine
Criteria Pollutants
Variables
S
P
M
T
L
0.6 Submerged loading: dedicated normal service
5.9821 psia
39.86 lb/lb-mole bbl/year
520 deg. R 166800
0.236.Ib/bbl
19.7 tpy
Non -Criteria Reportable Air Pollutants/Hazardous Air Pollutants
Componen State Defai State Defau Mass Ratio Emissions ( Are Emissions Reportable?
Benzene 0.00041 0.0004 1.025 68 Yes/No
n -hexane 0.0036 0.236 0.015254 600 Yes/No
Section 03 - Regulatory Considerations
Is this site considered an exploration and production location (e.g. well pad)? Yes/No
If yes, review the following two exemptions for applicability:
Does the operator unload less than 10,000 gallons (238 BBLs) of crude oil per day on an annual average Yes/No
If yes, this emissions point is categorically exempt from permit requirements per Regulation 3, Part B, Section II.D.1.l
Does this operator unload less than 6,750 bbls per year of condensate via splash fill or
16,308 bbls per year of condensate via submerged fill procedure? Yes/No
If yes, this emissions point is categorically exempt from permit requirements per Regulation 3, Part B, Section II.D.1.l
Is this site located in an ozone non -attainment area? Yes/No
If yes, this source is subject to Reasonably Available Control Technology (RACT) requirements under Regulation 3, Part B
Section III.D.2.a. This requirement may be met using "submerged fill" and/or vapor balance with emissions routed to an
emissions control device.
Is this facility classified as a major source of HAPs? Yes/No
If yes, evaluate if 40 CFR, Part 63, Subpart EEEE "Organic Liquids Distribution" MACT provisions apply
Does this facility involve the loading of refined crude/condensate in the form of "gasoline"? Yes/No
If yes, proceed to evaluate the following:
Is this facility classified as a "Terminal" as defined per Regulation 7, Section VI.C.2.a? Yes/No
If yes, the provisions of Regulation 7, Section VI.C.2 may apply
Is this facility classified as a "Bulk Plant" as defined per Regulation 7, Section VI.C.3.a? Yes/No
If yes, the provisions of Regulation 7, Section VI.C.3 may apply
Section 04 - SCC Coding
Pollutant Emissions Factor (lb/1,000 gallons)
VOC 3.81 lb/1,000 gallons
Benzene 0.0065 lb/1,000 gallons
n -hexane 0.058 lb/1,000 gallons
40600132: Crude Oil: Submerged Loading (Normal Service) Use if S = 0.6
40600137: Crude Oil: Splash loading (normal Service) Use if S = 1.45
40600142: Crude Oil: Submerged Loading (balanced Service) Use if S = 1.00
40600145: Crude Oil: Splash loading (Balanced Service) Use if S = 1.00 and splash loading
40600148: Crude Oil: Submerged Loading (Clean tanks) Use if S = 0.5
Equipment Description
This source vents natural gas from:
a well head separator
Emissions from this source are:
routed to an enclosed flare
Natural gas venting from a well head separator. Emissions from this source are routed to an enclosed flare.
Emission Calculation Method
EPA Emission Inventory Improvement Program Publication: Volume II, 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 = SG of gas' MW of air
Xx = mass fraction of x in gas
C = molar volume of ideal gas (379 scf/Ib-mol) at 60F and 1 atm
I
RequestedThroughput (Q) 100.0000 MMscf/yr
11415.5 scf/hr I 0.002 MMscf/d I 8.49 MMscf/mo
Vented #DIV/0!
MW 20.290 Ib/Ib-mol
Component
mole %
MW
Ibx/Ibmol
mass fraction
E
lb/hr
Ib/yr
tpy
Helium
0
4.0026
0.000
0.000
Helium
0.0
0
0.00
CO2
1.1262
44.01
0.496
0.024
CO2
14.9
130776
65.39
N2
1.127
28.013
0.316
0.016
N2
9.5
83300
41.65
methane
82.3101
16.041
13.203
0.651
methane
397.7
3483737
1741.87
ethane
8.6231
30.063
2.592
0.128
ethane
78.1
684001
342.00
propane
3.6681
44.092
1.6173
0.080
propane
48.7
426738
213.37
isobutane
0.5016
58.118
0.2915
0.014
isobutane
8.8
76918
38.46
n -butane
1.5274
58.118
0.8877
0.044
n -butane
26.7
234220
117.11
isopentane
0.3637
72.114
0.2623
0.013
isopentane
7.9
69203
34.60
n -pentane
0.394
72.114
0.2841
0.014
n -pentane
8.6
74968
37.48
cyclopentane
0.0169
70.13
0.0119
0.001
cyclopentane
0.4
3127
1.56
n -Hexane
0.0576
86.18
0.0496
0.002
n -Hexane
1.5
13098
6.55
cyclohexane
0.0092
84.16
0.0077
0.000
cyclohexane
0.2
2043
1.02
Other hexanes
0.0813
86.18
0.0701
0.003
Other hexanes
2.1
18487
9.24
heptanes
0.1091
100.21
0.1093
0.005
heptanes
3.3
28847
14.42
methylcyclohexane
0.0251
98.19
0.0246
0.001
methylcyclohexane
0.7
6503
3.25
224-TMP
0.0001
114.23
0.0001
0.000
224-TMP
0.0
30
0.02
Benzene
0.0076
78.12
0.0059
0.000
Benzene
0.2
1567
0.78
Toluene
0.0211
92.15
0.0194
0.001
Toluene
0.6
5130
2.57
Ethylbenzene
0.0019
106.17
0.0020
0.000
Ethylbenzene
0.1
532
0.27
Xylenes
0.0024
106.17
0.0025
0.000
Xylenes
0.1
672
0.34
CB+Heavies
0.0265
138.237
0.0366
0.002
O8* Heavies
1.1
9666
4.83
100 - VOC mass fraction: 0.1815 Total VOC Emissions (Uncontrolled)
annual limit assuming 95% control
Notes
485.9
24.3
Flaring Information
Equipment Description
Flare to combust low-pressure separator gas during VRU downtime.
Manufacturer
Model
Serial Number
Gas Heating Value
Throughput
1190
Btu/scf
MMBtu/yr
119000
Combustion emission factor source:
AP -42: Chapter 13.5
0.068
lb NOX/MMBtu
tpy NOX
0.31
lb CO/MMBtu
tpy CO
.4
Emissions Summary
Uncontrolled/PTE
485.9
tpy VOC
Controlled
24.3
tpy VOC
Uncontrolled
Total (Ib/yr)
Scenario A
Reportable?
Controlled Total
(Ib/yr)
Benzene
1567
Yes
78
Toluene
5130
Yes
257
Ethylbenzene
532
Yes
27
Xylenes
672
Yes
34
n -hexane
13098
Yes
655
224-TMP
30
No
2
Emission Factors for Permit
meter installed:
Modeled liquid thorughput to separator:
SCF vented gas/BBL liquid throughput:
Uncontrolled
NOX
21.07
lb/MMscf natun
CO
114.63
lb/MMscf natun
VOC
9717.49
lb/MMscf natun
Benzene
15.67
lb/MMscf natun
Toluene
51.30
lb/MMscf natura
Ethylbenzene
5.32
lb/MMscf natun
Xylenes
6.72
lb/MMscf natun
n -Hexane
130.98
lb/MMscf natun
224 -IMP
0.30
lb/MMscf natura
600 bbl/yr
0.0 scf/bbl
Controlled
NOX
21.07
lb/MMscf natun
CO
114.63
lb/MMscf natun
VOC
485.87
lb/MMscf natun
Benzene
0.78
lb/MMscf natura
Toluene
2.57
lb/MMscf natun
Ethylbenzene
0.27
lb/MMscf nature
Xylenes
0.34
lb/MMscf natura
n -Hexane
6.55
IbIMMscf nature
224-TMP
0.02
lb/MMscf natun
Regulatory Applicability
AQCC Regulation 1
I gas vented
I gas vented
I gas vented
I gas vented
1 gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
I gas vented
This source is subject to the opacity requirements for flares in Section II.A.5:'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.'
CC R AQegulation 2
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 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."
AQCC Regulation 3
Part A.
An APEN is required for this source because uncontrolled VOC emissions exceed two
tons per year in an attainment area.
Part B:
#REF!
#REF!
Is public comment
required?
yes
AQCC Regulation 7
Was the well newly constructed, hydraulically fractured, or recompleted on or after August 1, 2014?
yes
This separator is subject to Reg 7, Section XVII.G. and control requirements of Reg 7, XVII.B.2
cropdown List
Yes
No
AIR POLLUTANT EMISSION NOTICE (APEN) & Application for Construction Permit — Condensate Storage Tank(s)'
ermit Number 1 7 W G a /36, [Leave blank unless APCD has already assigned a permit & AIRS ID] Emission Source AIRS ID: / q F tC / 00f
lcility Equipment ID: Condensate Storage Tanks
Trion 01— Administrative Information
Company Name: Verdad Resources LLC
[Provide Facility Equipment ID to identify how this equipment is referenced within your organization.]
Source Name: Johnson 8-30N
Source Location NENW S31 T2N R65W
NAICS, or 1311
SIC Code:
County: Weld
Elevation: 5,006 Feet
Mailing Address: 5950 Cedar Springs Road, Suite 200 ZIP Code: 75235
Dallas, TX
,rson To Contact Mike Cuguetti Phone Number: (303) 704-8856
E-mail Address: MCugnetti@VerdadOi.com Fax Number:
xtion 03 — General Information
r existing sources, operation began on: / /
as Storage Tank is ® Exploration & Production ❑ Midstream or Downstream
.cated at (E&P) Site (Non-E&P) Site
ill this equipment be operated in any NAAQS nonattainment area? Z Yes ❑ No
actual annual average hydrocarbon liquid throughput ? 500 bbl/day? ❑ Yes Z No
► Are these condensate tanks subject to Colorado Oil and Gas Conservation Commission (COGCC) 805 series rules? If so, submit Form APCD-105.
► Are you requesting ? 6 ton/yr VOC emissions, or are uncontrolled actual emissions ? 6 ton/yr?
acral description of equipment purpose: 3 x 400 bbl steel welded tanks manifolded together for storing condensate until transported off -site
xtion 04 — Storage Tank(s) Information 14( boQ
Requested Permit Limit 11,975. bbl/year
Actual:
Average API Gravity of Sales Oil:
mk Design: Fixed Roof
orage
rank
ID
# of Liquid Manifold
Storage Vessels in
Storage Tank
Total Volume of
Storage Tank
(bbl)
Installation Date of most recent
storage vessel in storage tank
(Month/Year)
Date Of First Production
(Month/Year)
001
All three storage
400
01/2017
02/2017
002 .
tanks are
400
01/2017
02/2017
003
manifolded together.
400
01/2017
02/2017
Wells Serviced by this Storage Tank or Tank Battery (E&P Sites Only)
API Number
Name of WdI
Newly Reported Well
TBD - -
Johnson 8-30N
121
_
O
Section 02 — Requested Action (Check applicable request boxes)
® Request for NEW INDIVIDUAL permit
O Request for coverage under GENERAL PERMIT
❑ GP01 O GP08
❑ Request MODIFICATION to existing INDIVIDUAL permit (check boxes below)
O Change process or equipment O Change company name
O Change permit limit ❑ Transfer of ownership ❑ Other
❑ APEN Submittal for Permit Exempt/Grandfathered source
❑ APEN Submittal for update only (Please note blank APEN's will not be accepted)
Addl. Info. An ECD controls the tank vapors. These emissions contain both Tank and
& Notes: ECD pilot emissions. See attached calculations.
mdensate
uoughput
For new or reconstructed sources, the projected startup date is: 02 / 01 / 2017
daYsi
Normal Hours of Source Operation: '24 day week
Are Flash Emissions anticipated at these tanks
If "yes", identify the stock tank gas -to -oil ratio: 0.0255
(3 II{►6600
11,975 bbl/year cmal While Controls Operational: 41,975 bbl/year
41.43 degrees RVP of Sales Oil 8.6
Internal Floating Roof ❑ External Floating Roof ❑
FORM APCD-205
Page 1 of 2
52 weeks/
year
Yes ❑ No 4
m3/liter ��tk� '4Y
® Yes ❑ No
® Yes ❑ No
Colorado Department of Public Health and Environment
Air Pollution Control Division (APCD)This notice is valid for five
(5) years. Submit a revised APEN prior to expiration of five-year
term, or when a significant change is made (increase production, new
equipment, change in fuel type, etc).
Mail this form along with a check for $152.90 per APEN for non-
E&P, midstream and downstream sources or S152.90 for up to
five (5) APENs for E&P sources and $250 for each general permit
registration to:
Colorado Department of Public Health & Environment
APCD-SS-B1
4300 Cherry Creek Drive South
Denver, CO 80246-1530
For guidance on how to complete this APEN form:
Air Pollution Control Division: (303) 692-3150
Small Business Assistance Program (SBAP): (303) 692-3148 or
(303) 692-3175
APEN forms: http:!iuww.coloredo.govicdphc/oilgas.APENS
Application status: http:!'www.colorado.soc,cdthe'pennitstatus
Johnson 8-30N AP_Form-APCD-205-Condensate-Tanks-APEN_DRAFT.doc
358205
AIR POLLUTANT EMISSION NOTICE (APEN) & Application for Construction Permit — Condensate Storage Tank(s)1
Permit Number.
xtion 05 — Stack Information (For Midstream sites onl
Operator
Stack
ID No.
Stack Base
Elevation
(feet)
Stack Discharge
Height Above
Ground Level
(feet)
Temp.
(°F)
Flow Rate
(ACFM)
Velocity
(ft/sec)
Moisture
(%)
)irection of stack outlet (check one): ❑ Vertical 0 Vertical with obstructing raincap
:xhaust Opening Shape & Size (check one): ❑ Circular. Inner Diameter (inches) =
xtion 07 — Control Device Information
Emission Source AIRS II):
Section 06 —Stack (Sourcg, if no combustion) Location (Datum & either Lat/Long or UTM)
Horizontal Datum
(NAD27, NAD83,
WGS84)
UTM
Zone
(12 or 13)
UTM Fasting or
Longitude
(meters or degrees)
UTM Northing or
Latitude
(meters or degrees)
Method of Collection for
Location Data (e.g. map,
GPS, GoogleEarth)
104542'40.83"W
40° 0'54.06"N
Google Earth
❑ Horizontal ❑ Down
❑ Other Length (inches) =
❑ Other (Describe):
Width (inches) =
] Vapor Recovery Unit (VRU) used for control of the Storage Tank(s)
Size: Make/Model:
Requested VOC & HAP Control Efficiency: %
Annual time that VRU is bypassed (emissions vented): %
] Closed loop system used for control of the storage tank(s)
Description:
® Combustion Device used for control of the Storage Tank(s)
Rating 1.25 MMBtu/hr
Type: Enclosed Flare Make/Model Cimarron Energy Inc./ECD-2-48-210
VOC & HAP Control Efficiency: Requested: 95 %
°F
Minimum temp. to achieve requested control: 500
Constant pilot light? ® Yes El No
❑ Describe Any Other:
Manufacturer Guarantee& 98 %
Waste gas heat content 2,330 Btu/scf
Pilot burner rating: 0.11 MMBnilhr
xtion 08 — Gas/Liquids Separation Technology Information (E&P Sites Only) ^,,
What is the pressure of the final separator vessel prior to discharge to the storage tank(s)? 4.45"' D psig ��,
'lease describe the separation process between }uwell and the storage tanks: (1) 3 -phase separator (High Pressure) separates gas, condensate, and slater
xtion 09 — Emissions Inventory Info r xtion & Emission Control Information
® Emission Factor Docnmevtatlo Data year for actual calendar yr. emissions below & throughput in Sec. 04 (e.g. 2007): N/A
n attached
Pollutant
Emission Factor
Actual Calendar Year Emission'
Requested Permitted Emissions
Emission Factor
Data Source
Uncontrolled Basis
Units
Uncontrolled (Tons/Year)
Controlled (Tons/Year)
Uncontrolled (Tons/Year)
Controlled (Tons/Year)
NOx
0.068
Lb/MMBtu
N/A
N/A
N/A
1, 0(
037 t, °'(
AP42
VOC
832
Lb/bbl
N/A
N/A
196.96
7(p, (p
9.85 35, (/
E&P Tanks
CO
0.31
Lb/MMBtu
N/A
N/A
N/A
8,(.
1.70 S. (p
AP42
Benzene
0.024
Lb/bbl
N/A
N/A
1-(003
03499
2r O
ZCYJ
0.0275 Q , 1
Mass Balance
Toluene
0.014
Lb/bbl
N/A
N/A
2 335
0.3190
1 , 2r
I r-
0.0160 Q , 1
Mass Balance
Ethylbenzene
0.001
Lb/bbl
N/A
N/A
((, --)-
0.0145
O I
p
0.0007 U O
Mass Balance
Xylenes
0.004
Lb/bbl
N/A
N/A
( (01-
0.0864
O1q
3 3
0.0043 O , I
Mass Balance
n -Hexane
0.127
Lb/bbl
N/A
N/A
2 I l Q>y
2.9395
(.b , (/
Iocc?
0.1470 6, (..
Mass Balance
2,2,4-Trimethylpentane
0.011
Lb/bbl
N/A
N/A
1 i 3S
0.2602
1 .„Q
`)-2.,
0.1892 O ,!
Mass Balance
Please use the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above.
xtion 10 Applicant Certification - I hereby certify that all information contained herein and information submitted with this application is complete, true and correct. If this is a registration for
rypder g ral permit GPOI or GP08, I fgrtber certify that this source is and will be operated in full compliance with each condition of the applicable general permit
very
ggntume of Person LettrA orized to Supply ata
2 / 71 42 ) 7 Mike Cugnetti EH&S Manager
Date Name of Legally Authorized Person (Please print) Title
You may be charged an additional APEN fee for APEN re -submittal due to incorrectly filled -out APEN or missing information.
Annual emissions fees will be based on actual emissions reported here.
'rdditional Information
Required:
O
FORM APCD-205
Attach a pressurized pre -flash condensate extended liquids analysis, RVP & API analysis of the post -flash oil
Attach E&P Tanks input & emission estimate documentation (or equivalent simulation report/test results)
Attach EPA TANKS emission analysis if emission estimates do not contain working/breathing losses
Check box to request copy of draft permit prior to issuance.
Check box to request copy of draft permit prior to public notice.
Page 2 of 2 Johnson 8-30N_AP_Form-APCD-205-Condensate-Tanks-APEN_DRAFT.doc
ermitNumber: /7vt/Eto(36
acuity Equipment ID: Produced Water Tank
action 01 — Administrative Information
Company Name: Verdad Resources LLC
V�
cc<(; .
AIR POLLUTANT EMISSION NOTICE (APEN) & Application for Construction Permit — Produced Water Storage Tank(s)1 rr 7
[Leave blank unless APCD has already assigned a permit # & AIRS ID] Emission Source AIRS ID: 113 / % FCF / (1 U
[Provide Facility Equipment ID to identify how this equipment is referenced within your organization.]
Source Name: Johnson 8-30N
Source Location_ NENW S31 T2N R65W
Mailing Address: 5950 Cedar Springs Road, Suite 200
Dallas, TX
NAICS, or 1311
SIC Code.
County: Weld
Elevation: 5,006 Feet
ZIP Code: 75235
.rson To Contact Mike Cugnetti Phone Number: (303) 704-8856
E-mail Address: MCugnetti@VerdadOil.com Fax Number:
tetion 03 — General Information
tr existing sources, operation began on: / /
us Storage Tank is Exploration & Production Midstream or Downstream
scaled at r".
(E&P) Site E1 Midstream
Site
ill this equipment be operated in any NAAQS nonattainment area? ® Yes ❑ No Are Flash Emissions anticipated at these tanks
I. Are these produced water tanks located at a commercial facility that accepts oil production wastewater for processing?
► Do these storage tanks contain less than 1% by volume crude oil on an annual average basis?
► Are these produced water tanks subject to Colorado Oil and Gas Conservation Commission (COGCC) 805 series rules? If so, submit Form APCD-105.
► Are you requesting 6 ton/yr VOC emissions, or are uncontrolled actual emissions ≥ 6 ton/yr?
meral description of equipment purpose: 400 bbl fiberglass produced water tank for storing produced water until transported off -site
Section 02 — Requested Action (Check applicable request boxes)
❑ Request for NEW INDIVIDUAL permit
❑ Request for coverage under GENERAL PERMIT
❑ GP05 O GPOS
❑ Request MODIFICATION to existing INDIVIDUAL permit (check boxes below)
O Change process or equipment ❑ Change company name
O Change permit limit ❑ Transfer of ownership O Other
❑ APEN Submittal for Permit Exempt/Grandfathered source
❑ APEN Submittal for update only (Please note blank APEN's will not be accepted)
Addl. Info.
& Notes:
xtion 04 — Storage Tank(s) Information
educed Water
iroughput
ink Design:
:orage
auk
# of Liquid Manifold
Storage Vessels in
Storage Tank
Total Volume of
Storage Tank
(bbl)
Installation Date of most recent
storage vessel in storage tank
(Month/Year)
Date Of First Production
(Month/Year)
004
Single Tank
400
01/2017
02/2017
Requested Permit Limit: 41,975
Actual:
Fixed Roof
bbl/year
41,975 bbl/year
Internal Floating Roof ❑
For new or reconstructed sources, the projected startup date is: 02 / 01 / 2017
Actual While Controls Operational: 41,975
External Floating Roof O
Normal Hours of Source Operation:
bbl/year
Wells Serviced by this Storage Tank or Tank Battery (E&P Sites Only)
API Number
Name of Well
Newly Reported Well
TBD - -
Johnson 8-30N
Ca
- -
❑
- -
❑
- -
O
- -
❑
FORM APCD-207
Page 1 of 2
hours! days/ weeks/
24 day 7 week 52 year
Yes ❑ No
Yes ® No
Yes ❑ No
Yes ® No
Yes ® No
O
Colorado Department of Public Health and Environment
Air Pollution Control Division (APCD)This notice is valid for five
(5) years. Submit a revised APEN prior to expiration of five-year
term, or when a significant change is made (increase production, new
equipment, change in fuel type, etc).
Mail this form along with a check for $152.90 per APEN for non-
E&P, midstream and downstream sources or $152.90 for up to five (5) APENs for E&P sources and S250 for each generalvermit
registration to:
Colorado Department of Public Health & Environment
APCD-SS-B1
4300 Cherry Creek Drive South
Denver, CO 80246-1530
For guidance on how to complete this APEN form:
Air Pollution Control Division: (303) 692-3150
Small Business Assistance Program (SBAP): (303) 692-3148 or
(303) 692-3175
APEN forms: http://www.colorado.cov'cdpheioilgasAPENS
Application status: http:! uciw.colorado. cos !cdphe/permit tstus
Johnson 8-30N_AP Form-APCD-207-Produced Water APEN_DRAFT.doc
358206
AIR POLLUTANT EMISSION NOTICE (APEN) & Application for Construction Permit — Produced Water Storage Tank(s)'
Permit Number.
ction 05 - Stack Information (For Midstream sites onl
Operator
Stark
ID No.
Stack Base
Elevation
(feet)
Stack Discharge
Height Above
Ground Level
(feet)
Temp.
(°F)
Flow Rate
(ACFM)
Velocity
(ft/sec)
Moisture
(%)
)iteclion of stack outlet (check one): ❑ Vertical ❑ Vertical with obstructing raincap
achaust Opening Shape & Size (check one): ❑ Circular Inner Diameter (inches) =
ction 07 — Control Device Information
Emission Source AIRS ID:
Section 06 —Stack (Source, if no combustion) Location (Datum & either Lat/Long or UTM
Horizontal Datum
(NAD27, NAD83,
WGS84)
UTM
Zone
(12 or 13)
UTM Basting or
Longitude
(meters or degrees)
UTM Northing or
Latitude
(meters or degrees)
Method of Collection for
Location Data (e.g. map,
GPS, GoogteEarth)
40° 0'54.06"N
104°42'40.83"W
Google Earth
❑ Horizontal ❑ Down
❑ Other: Length (inches) =
❑ Other (Describe)
Width (inches) _
] Vapor Recovery Unit (VRU) used for control of the Storage Tank(s)
Size: Make/Model:
Requested VOC & HAP Control Efficiency: %
Annual time that VRU is bypassed (emissions vented): %
] Closed loop system used for control of the storage tank(s)
Description.
® Combustion Device used for control of the Storage Tank(s)
Rating: 1.25 MMBtu/hr
Type: Enclosed Flare Make/Model Cimarron Energy Inc../ECD-2-48-210
VOC & HAP Control Efficiency: Requested: 95 % Manufacturer Guaranteed 98 %
Minimum temp. to achieve requested control: 500 °F Waste gas heat content 2,330 Btu/scf
Constant pilot light? ® Yes O No Pilot burner rating: 0.11 MMBtu/hr
Describe Any Other:
ction OS — Gas/Liquids Separation Technology Information (E&P Sites Only)
What is the pressure of the final separator vessel prior to discharge to the storage tank(s)? 145 psig
'lease describe the separation process between the well and the storage tanks: 3 -phase separator (Heater Treater) separates oil, gas, water
ction 09 — Emissions Inventory Information & Emission Control Information
Emission Factor Documentation attached Data year for actual calendar yr. emissions below & throughput in Sec. 04 (e.q. 2007): I NA
Pollutant
Emission Factor
Actual Calendar Year Emission'
Requested Permitted Emissions
Estimation Method or
Fmission Factor
Source
Uncontrolled Basis
�, Units
Uncontrolled
(Tons/Year)
Controlled
(Tons/Year)
Uncontrolled
(Tons/Year)
Controlled
1ons/Year)
NOx
N/A
/
N/A
N/A
N/A
N/A r
N/A
N/A
VOC
0.262
lb/bbl
N/A
N/A
5.50
0.27
PS 14-03
CO
N/A
N/A
N/A
N/A
N/A
N/A
N/A
Benzene
0.007
lb/bbl
N/A
N/A
0.1469125
0.007345625
PS 14-03
Toluene
N/A
N/A
N/A
N/A
N/A
N/A
N/A
Ethylbenzene
N/A
N/A
N/A
N/A
N/A
N/A
N/A
Xylenes
N/A
N/A
N/A
N/A
N/A
N/A
N/A
n -Hexane
0.022
lb/bbl
N/A
N/A
0.461725
0.02308625
PS 14-03
?,2,4-Trimethylpentane
N/A
N/A
N/A
N/A
N/A
N/A
N/A
Please use the APCD Non -Criteria Reportable Air Pollutant Addendum form to report pollutants not listed above.
ction 10 —Applicant Certification - I hereby certify that all information contained herein and information submitted with this application is complete, true and correct If this is a registration for
ve under gene al per 't 9 '05 or GP08, I further certify that this source is and will be operated in full compliance with each condition of the applicable general ermit
� 0 'Li 1/ �l Al; k9 Cit,gne� _ S :�M P a ns
patine of Person L y orized to Supply Data Date Name of Legally Authorized Person (Please print) Title
You may be charged an additional APEN fee for APEN re -submittal due to incorrectly filled -out APEN or missing information_
Annual emissions fees will be based on actual emissions reported here.
cdditioaal Information
tegoired:
O
FORM APCD-207
Attach produced water laboratory analysis, stack test results and associated emissions calculations if you are
requesting a site specific emissions factor according to the guidance in PS Memo 14-03
Page 2 of 2
Check box to request copy of draft permit prior to issuance.
Check box to request copy of draft permit prior to public notice.
Johnson 8-30N_AP Form-APCD-207-Produced Water APEN_DRAFT doc
V ,
Eb 102017
Lonary
Sources
AIR POLLUTANT EMISSION NOTICE (APEN) & Application for Construction Permit — Hydrocarbon Liquid Loadings
Please use the Fuel Dispensing Station APEN to report emissions from service stations and fleet refueling stations.
:rmit Number: / 7 W E 0 ( 6 [Leave blank unless APCD has already assigned a permit # & AIRS ID] Emission Source AIRS ID:
lcility Equipment 1D: Condensate Loading [Provide Facility Equipment ID to identify how this equipment is referenced within your organization.)
ction 01— Administrative Information Section 02 — Requested Action (Check applicable request boxes)
Company Name: Verdad Resources LLC
Source Name: Johnson 8-30N
Source Location: NENW S31 T2N R65W
Mailing Address: 5950 Cedar Springs Road, Suite 200
NAICS, or
SIC Code:
1311
County: Weld
123 , 9Feg i 6433
Action Applies To:
✓0 Individual Permit ❑ General Permit GP07
Dallas, TX Elevation: 5,006
sson To Contact Mike Cugnetti
E-mail Address: MCugnetti@VerdadOil.com
Phone Number: (303) 704-8856 Fax Number:
ZiP Code: 75235
action 03 — General Information
ate operation began or projected startup date: 02 / 01 / 2017
meral description of equipment and purpose: Loadout for tank trucks
❑✓ Request NEW permit or newly reported emission source
❑ Request REGISTRATION for coverage under GP07 & concurrent
request for CANCELLATION of individual permit number:
❑ Request MODIFICATION to existing permit (check each box below that applies)
❑ Change process or equipment ❑ Change company name
Feet ❑ Change permit limit ❑ Transfer of ownership O Other
O Request to limit RAPs with a Federally enforceable limit on PTE
❑
Request APEN update only. Note — Emissions data must be completed. Blank APENs
will not be accepted
AddL Info. & Notes:
Normal Hours of Source Operation:
24 hours/day 7 days/week 52 weeks/year
Is this source located at an oil and gas exploration and production site?
If yes, does this source load less than 10,000 gallons of crude oil per day on an annual average, splash fill less than 6750 BBL of condensate per year
or submerge fill less than 16,308 BBL of condensate per year?
Is this source located at a facility that is considered a Major Source of Hazardous Air Pollutant (HAP) emissions?
Will this equipment be operated in any NAAQS nonattainment area? (www.colorado. ov/cdphe/ozone)
Does this source load gasoline into transport vehicles?
f "Yes", provide an applicability determination of state and federal rules.
tction 04 — Loading Information (40800 a ev ce W2.7%►?-
vduct Loaded: El Condensate ❑ Crude Oil Other:
If this APEN is being filed for vapors displaced from cargo carrier, complete the following: ((4(0600
rural Volume Loaded: Requested':—f4;9₹5 bbl/year Actual calendar year: 41,975 . bbl/year
Us product is loaded from tanks at this facility into: Tank Trucks (e.g, "rail tank cars," or "tank trucks")
• If site -specific emission factor is used to calculate emissions (Not available for GP07), complete the following:
Saturation Factor3: 1440— Average Temperature of Bulk Liquid Loaded: °F
True Vapor Pressure: -6:982* psis @ 60 °F Molecular Weight of Displaced Vapor:, -2986. Lb/lb-mol
• If this APEN is being filed for vapor losses from pressurized loading lines, complete the following4
)ads per year Requested': #/yr. Actual Calendar Year: #/yr. Product Density:
oad Line Volume': Ft3/truckload Vapor Recovery Line Volume': Ft3/truckload
'tilt may be charged an additional APEN fee for APEN re -submittal doe to incorrectly filled -out APEN or missing information.
tequested sallies will become permit limitations for individual construction permits.
'lease refer to AP -42, Table 5.2-1 for information on saturation factors (found online at, htte:%iw w'e epz.ear Ittn'ebiefisp42!c hO5',nAcc.hrm0.
sift the total volume for all lines in each category and attach your calculations of these volumes.
FORM APCD-208
Page 1 of 2
Lb/f
• Yes 0 No 0 Don't know
❑ Yes ❑ No ❑ Don't know
O Yes"
Yes"
Yes"
0 No 9 Don't know
❑ No 0 Don't know
O No ❑ Don't know
Colorado Department of Public Health and Environment
Air Pollution Control Division (APCD)
This notice is valid for five (5) years. Submit a revised APEN prior to
expiration of five-year term, or when a significant change is made"
(increase production, new equipment, change in fuel type, etc).
Mail this form along with a check for $152.90 per APEN &
$250.00 for each general permit registration to:
Colorado Department of Public Health & Environment
APCD-SS-B1
4300 Cherry Creek Drive South
Denver, CO 80246-1530
For guidance on how to complete this APEN form:
Air Pollution Control Division: (303) 692-3150
Small Business Assistance Program (SBAP): (303) 692-3148 or
(303) 692-3175
APEN forms: www.colorado.gov/cdphe/airforms
Permit status: www.colorado.gov/cdphe/permitstatus
FmmAPCD-208-HydrocarbonLiquidLoadingAPF.N-Ver.4I4-2014 (1).docx
358207
AIR POLLI TANT EMISSION NOTICE (APEN) & Application for Construction Permit — Hydrocarbon Liquid Loadings
Please use the Fuel Dispensing Station APEN to report emissions from service stations and fleet refueling stations.
Permit Number: Emission Source AIRS ID: / /
ction 05 — Stack Information (Combustion stacks must be listed here) Section 06 —Stack (Source, if no combustion) Location (Datum & either Lat/Long or UTM)
Dperator
Stack
ID No.
Stack Base
Elevation
(feet)
Stack Discharge
Height Above
Ground Level
(feet)
Temp.
(°F)
Flow Rate
(ACFM)
Velocity
(ft/sec)
Moisture
(%)
IA
lirection of stack outlet (check one): ❑ Vertical ❑ Vertical with obstructing raincap
Horizontal Datum
(NAD27, NAD83,
WGS84)
UTM
Zone
(l2 or l3)
UTM Easting or
Longitude
(meters or degrees)
UTM Northing or
Latitude
(meters or degrees)
Method of Collection for
Location Data (e.g. map,
GPS, GoogleEarth)
40° O'54.06'N
104°42'40.83"W
Google Earth
❑ Horizontal ❑ Down U Other (Describe):
.xhaust Opening Shape & Size (check one): Circular: Inner Diameter (inches) = ❑ Other: Length (inches) = Width (inches) =
ction 07 — Control Device Information
] Loading occurs using a vapor balance system.
3 Combustion Device used for control of the loadout emissions. Rating: MMBtu/br
Type: Make/Model/Serial #:
VOC & HAP Control Efficiency: Requested: % Manufacturer Guarantee&
Minimum temp. to achieve requested control: °F Waste gas heat content Btu/scf
Ca ts(ant pilot light? n Yes ❑ No Pilot bunter ratin.: MMBtu/lir
short i$— Emissions Inventory Information
0 Describe Any Other (Including VRU)
VOC & HAP Control Efficiency: Requested:
State Emission Factors (Required for general permit GP07 - Optional for individual permit)
R Condensate
n Crude Oil
VOC: 0.236
VOC: 0.104
Lbs/BBL
Lbs/BBL
Benzene:
Benzene:
0.00041 Lbs/BBL
0.00018 LbsBBL
n -Hexane:
n -Hexane:
0.0036 Lbs/BBL
0.0016 Lbs/BBL
Emission Factor Documentation attached (If using site specific emission factor) Data year for actual calendar year emissions below & throughput in Sec. 04 (e.g. 2007):
NA
Pollutant
Control Device Description
p
Control Efficiency
(% Reduction)
Emission Factor
Actual Calendar Year Emissions'
Requested Permitted
Emissions
Estimation
Method or
Primary Secondary
Uncontrolled Basis
Units
Uncontrolled
(Tons/Year)
Controlled
(Tons/Year)
Uncontrolled
(Tons/Year)
Controlled
(Tons/Year)
Emission
Factor Source
NOx
Identify in Section 07
N/A
N/A
N/A
N/A
N/A
N/A
N/A
voC
0.236
lb/bbl
NA
N/A
4.95I
V-
N/A
PS MEMO 14-02
CO
N/A
N/A
N/A
N/A
N/A
N/A
N/A
Benzene
0.0004
lb/bbl
NA
N/A(o6
4664
06
0,1 N/A
PS MEMO 14-02
n -Hexane
0.0036
lb/bbl
NA
N/AID
0.3N/A
PS MEMO 14-02
n.__._ ..._ «r.. Aprn nr...._r-,.aa.ta u.....rtohie Air Pollutant Addendum form to reoort pollutants not listed above.
'You may be charged an additional ADEN fee for APEN re -submittal doe to incorrectly filled -out APEN or mining information.
Aonoal emission fees will be based on actual emissions reported here.
Check bog to request copy of draft permit prior to issuance.
!ction 09 —Applicant Certification - I hereby certify that all information contained herein and information submitted with this application is complete, true and correct. If this is a registration
rage under general permit GP07, I further certify that this source is and will be operated in full compliance with each condition of general permit GP07. An
P1 , -44P- f.4> t�y c.
ngnature o Pets n .a y Authorized to Supply Data Date Name of Legally Authorized Person (Please print) Title
Page 2 of 2 FormAPCD 208-HydtocarbonLigoidLoadingAPEN-Ver.4-14-2014 (1).docx
M1.
t=_O�1'S7
ermit Number:
AIR POLLUTANT EMISSION NOTICE (APEN) & Application for Construction Permit — Natural Gas Venting'
[Leave blank unless APCD has already assigned a permit # & AIRS ID] Emission Source AIRS ID: / Z3 / !FP' -S / 06174
[Provide Facility Equipment ID to identify how this equipment is referenced within your organization.]
Section 02 — Requested Action (check applicable request boxes)
17►/JC0136
Lcility Equipment ID: Separator Venting
ction 01 — Administrative Information
Company Name: Verdad Resources LLC
Source Name: Johnson 8-30N
Source Location: NENW S31 T2N R65W
Mailing Address: 5950 Cedar Springs Road, Suite 200
Dallas, TX
rson To Contact: Mike Cugnetti
E-mail Address: MCugnetti@VerdadOil.com
ction 03 — General Information
ur existing sources, operation began on:
rmal Hours of Source Operation:
meral description of equipment and purpose:
ill this equipment be operated in any NAAQS nonattainment area?
ttp://www.colorado.gov/cdphe/attainment)
:ction 04 — Processing Equipment Information
>escription of Source':
] Well Head Casing
Gas/liquid Separator
] Pneumatic Pump: Make:
] Compressor Rod Packing Make:
] Blowdowns: # of events:
Description:
] Other.
24
Separator will vent produced natural gas through an enclosed emissions control device.
NAICS, or
SIC Code:
County: Weld
Elevation: 5,006 Feet
1311
ZIP Code: 75235
Phone Number. (303) 704-8856
Fax Number:
hours/day
Z Request for NEW permit or newly reported emission source
❑ Request MODIFICATION to existing permit (check -each box below that applies)
O Change fuel or equipment O Change company name
O Change permit limit O Transfer of ownership O Other
❑ Request to limit HAPs with a Federally enforceable limit on PTE
❑ Request APEN update only (check the box below that applies)
O Revision to actual calendar year emissions for emission inventory
Update 5 -Year APEN term without change to permit limits or previously
reported emissions
Additional
Info. &
Notes:
For new or reconstructed sources, the projected startup date is: 02 / 01 / 2017
7 days/week 52 weeks/year
Model:
Model:
Volume:
® Yes O No O Don't
know
Serial #:
4 of pistons:
MMscCevent
Capacity
Leak rate:
gal./min.
Scf/hr/pist
Maximum Vent Rate
(scar)
Actual Volume
(MMscfyr)
Process Parameters: -4792. 11411 43di3
Requested Volume'
(MMscf/yr)
Vent Gas Heating Value
(Bta/sef)
43:41a 100 —1.226+ i .0 dip
Vented Gas Properties:
Z Submit a tem.-sanative gas anal{rsis (including BTEX & n -Hexane) to support calculations
You will be charged an additional APEN fee if APEN is filled out incorrectly or missing information and requires re -submittal
:Only one source type may be reported per APEN.
MoleCailar WE VOC I
1 (mole %) l
Benzene Toulene
(mole %) (mole %)
Ethylbenzene Xylene n -Hexane
(mole %) (mole %) (mole %)
'39;94
212;111-94:+5.
0.716O,NA 449.2 002.
03-7 0402.4-1020.3.601 Opal
'Requested vahres will become permit limitations. Requested level shall be a "not to exceed value".
FORM APCD-211
Page 1 of 3
Colorado Department of Public Health and Environment
Air Pollution Control Division (APCD)
This notice is valid for five (5) years. Submit a revised APEN prior to
expiration of five-year term, or when a significant change is made
(increase production, new equipment, change in fuel type, etc).
Mail this form along with a check for $152.90 to:
Colorado Department of Public Health & Environment
APCD-SS-BI
4300 Cherry Creek Drive South
Denver, CO 80246-1530
For guidance on how to complete this APEN form: Air Pollution Control Division: (303) 692-3150
Small Business Assistance Program (SBAP): (303) 692-3148 or
(303)692-3175
APEN forms:http://www.colorado.gov/cdphe/oilgaspermits
Application status:http://www.colorado.gov/cdphe/permitstatus
0 Check box to request copy of draft permit prior to issuance.
Z Check box to request copy of draft permit prior to public notice.
Johnson 8-30N AP Form-APCD-211-Natural Gus-Venting-APEN.doc
358208
AIR POLLUTANT EMISSION NOTICE (APEN) & Application for Construction Permit — Natural Gas Venting'
Permit Number: Emission Source AIRS ID:
:lion 05 — Stack Information (Combustion stacks must be listed here)
tperatm
Stack
ID No.
Stack Base
Elevation
(feet)
Stack Discharge
Height Above
Ground Level
(feet)
Temp.
(°F)
Flow Rate
(ACFM)
Velocity
(ft/sec)
Moisture
(%)
irection of stack outlet (check one): ❑ Vertical ❑ Vertical with obstructing raincap
xhaust Opening Shape & Size (check one): O Circular: Inner Diameter (inches) =
ction 07 — Control Device Information
Section 06 —Stack (Source, if no combustion) Location (Datum & either Lat/Long or UTM)
Horizontal Datum
(NAD27, NAD83,
WGS84)
UTM
Zone
(12 or 13)
UTM Fasting or
Longitude
(meters or degrees)
UTM Northing or
Latitude
(meters or degrees)
Method of Collection for
T oration Data (e.g. map,
GPS, Googlelarth)
40° 0'54.06"N
104°42'40.83"W
Google Earth
O Horizontal D Down
O Other: Length (inches) _
O Other (Describe):
Width (inches) =
] VRU used for control of
Size:
Make/Model:
Requested VOC & HAP Control Efficiency:
Annual time that VRU is bypassed (emissions vented):
The VRU recycles venting emissions to:
] Describe Any Other.
® Combustion Device used for control of. VOC
Rating: 10.79 MMBtu/hr
The
Type: ECD Make/ModellSerial #: Beast/3200/328.5161
0007
VOC & HAP Control Efficiency: Requested: 95 % Manufacturer Guaranteed 98 %
Minimum temp. to achieve requested control: °F Waste gas heat content 2251 Btu/scf
Constant pilot light? ® Yes O No Pilot burner rating: 0 MMBtu/hr
ction 08 — Emissions Inventory Information & Emission Control Information
roach any emission calculations and emission factor documentation to this APEN form.
N/A
Y GIIIISSIOU
Pollutant
ractur Yucumcuuuuu aauwcu
Control Device Description
..... J.e.....
Overall
Collection
Efficiency
ate...-. .a.....
Control
Efficiency
(% Reduction)
....-.....-_r. -.__.. _ _-_e_c_. _--
Emission Factor
_ .--e - .
Actual Calendar Year
Emissions°
Requested Permitted Emissions
Estimation
Method or
Emission
Factor Source
Primary
Secondary
Uncontrolled
Basis
Units
Uncontrolled
(Tons/Year)
Controlled
(Tons/Year)
Uncontrolled
(Tons/Year)
Controlled
(Tons/Year)
VOC
ECD
N/A
95
95
78.7346
lb/Mscf
N/A
N/A
-i65z�4 1{13 4
-8.2:64.
2 44,1.
MassBalance
NOx
N/A
N/A
N/A
N/A
0.068
Ib/MMBtu
N/A
N/A
-Miss.
y, (
-3:2i+
/f, I
AP42
CO
N/A
N/A
N/A
N/A
0.31
lb/MMBtu
N/A
N/A
.NM-
I $, S
14.65
( li,c
AP42
SOx
N/A
N/A
N/A
N/A
0.6
lb/MMBtu
N/A
N/A
N/A
0.00
AP42
Benzene
ECD
N/A
95
95
0.1977
lb/Mscf
N/A
N/A
.4450.
O,a
0.208
0, 1
MassBalance
Toulene
ECD
N/A
95
95
0.0936
lb/Mscf
N/A
N/A
1.966
2.(/
0099
CO.
MassBalance
ithylbenzene
ECD
N/A
95
95
0.0347
lb/Mscf
N/A
N/A
-0,728
0,3
0:0364
U , 1
MassBalance
Xylene
ECD
N/A
95
95
0.0568
lb/Mscf
N/A
N/A
-1.1A3
0,4
0:9596
0.I
MassBalance
n -Hexane
ECD
N/A
95
95
0.7258
lb/Mscf
N/A
N/A
46-133
6, (/
4.361
0.4
MassBalance
Pl.... n.. th. APCII Non -Criteria Renortable Air Pollutant Addendum form to report pollutants not listed above.
' You will be charged an additional APEN fee if APEN is filled out incorrectly or missing information and requires re -submittal.
Annual emission fees will be based on actual emissions reported here.
ction 09 —Applicant Certification - I hereby certify that all information contained herein and information submitted with this application is complete, true and correct.
Z`7/2D 1`1
FORM APCD-211
Mike Cugnetti
Page 2 of 3
EH&S Manager
Johnson 8-30N APForm-APCD-211-Natural-Gas-Venting-APEN-doc
Hello