DAQ-2025-002431

Small Source Registration

DAQE-EN162690001-25

{{$d1 }}

Tyson Pond
reWater, LLC, a subsidiary of Wasatch Energy Management, LLC
4092 West 3000 South
Roosevelt, UT 84066
[e-mail]

Dear Mr. Pond:

Re: Request for Evaluation of Compliance with Rule R307-401-9, UAC: Small Source Exemption
Project Fee Code: N162690001

On April 23, 2025, the Division of Air Quality (DAQ) received your request for a small source exemption
for the reWater, LLC Tap Facility. The source is located approximately six miles southeast of Duchesne
at UTM (Universal Transverse Mercator) coordinates 556,548 meters Easting and 4,438,251 meters
Northing (Datum NAD 83, Zone 12) in Duchesne County. Operations on-site include the use of one (1)
118 horsepower (Site Rating of 96 horsepower) natural gas-fired generator set and one (1) condensate
storage tank. Per the registration request, the maximum annual oil production is 1,440 barrels of oil per
year. DAQ has determined the small source exemption applies to the source, as long as the equipment and
associated processes operate as specified in the registration request.

The small source exemption does not exempt a source from complying with other applicable federal,
state, and local regulations and the current Utah Administrative Code. Based on the emissions that you
submitted to DAQ with your registration request, reWater, LLC is not required to obtain an approval
order under R307-401 for the Tap Facility. If you change your operation such that there is an increase in
emissions, we recommend that you notify us, as an approval order may be required.

As authorized by the Utah Legislature, the fee for issuing this small source exemption is a one-time filing
fee in addition to the actual time spent by the review engineer and all other staff on the project. Payment
should be sent to DAQ upon receipt of the invoice.
195 North 1950 West • Salt Lake City, UT
Mailing Address: P.O. Box 144820 • Salt Lake City, UT 84114-4820
Telephone [phone] • Fax [phone] • T.D.D. [phone]
www.deq.utah.gov
Printed on 100% recycled paper
State of Utah

SPENCER J. COX
Governor
DEIDRE HENDERSON
Lieutenant Governor

Department of
Environmental Quality

Tim Davis
Executive Director

DIVISION OF AIR QUALITY
Bryce C. Bird
Director

6 á Û Ù Û Þ
DAQE-EN162690001-25
Page 2
Thank you for registering your source with the DAQ. If you have any additional questions, please contact
Katie Andersen at [phone] or [e-mail].

Sincerely,

Bryce C. Bird
Director

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Alan D. Humpherys, Manager
New Source Review Section

BCB:ADH:KA:jg

{{#d1=date1_es_:signer1:date:format(date, "mmmm d, yyyy")}} {{#s=Sig_es_:signer1:signature}}
Katie Andersen <[e-mail]>
Tap Facility Notification Information Request
5 messages
Katie Andersen <[e-mail]>Thu, May 1, 2025 at 11:20 AM
To: [e-mail]
Cc: [e-mail], [e-mail], [e-mail]
Hello Tyson,
The Utah Division of Air Quality received your notice of tap facility on April 23rd, 2025. I have been assigned as the project
engineer to process this notification.
Based on the information submitted, I will be processing this project as a Small Source Exemption. Will you send me an
excel file that shows how you calculated the PTEs of the site? Please include any references, citations, or assumptions
you used to determine your emissions.
I look forward to working with you.
Cheers,
Katie Andersen
--

Katie Andersen
Environmental Engineer | Minor NSR Section
M: [phone]
airquality.utah.gov
Tyson Pond <[e-mail]>Mon, May 5, 2025 at 8:06 AM
To: Katie Andersen <[e-mail]>
Cc: Lynn Hadlock <[e-mail]>, Juliann Marx <[e-mail]>, BJ Hadlock
<[e-mail]>
Hi Kae,
Please find aached the following documents:
reWater Tap Facility PTE Emissions Calculaons
Tank Exported Roune Losses Table
Updated Emissions Spec Sheet for the Smaller Sized Generator
These documents were used by my Engineer Consultant for the calculaons. Let me know if you need
anything further.
Thank you for your me.
5/7/25, 12:29 PM State of Utah Mail - Tap Facility Notification Information Request
https://mail.google.com/mail/u/0/?ik=0900585596&view=pt&search=all&permthid=thread-a:r8301374870554409638&simpl=msg-a:r414701650618291…1/4
Best regards,
Tyson
Tyson Pond
[phone]
[e-mail]

From: Kae Andersen <[e-mail]>
Sent: Thursday, May 1, 2025 11:20 AM
To: Tyson Pond <[e-mail]>
Cc: Lynn Hadlock <[e-mail]>; Juliann Marx <[e-mail]>; BJ Hadlock
<[e-mail]>
Subject: [External]Tap Facility Noficaon Informaon Request

IRONSCALES couldn't recognize this email as this is the first time you received an email from this sender
kandersen @ utah.gov
[Quoted text hidden]
Confidentiality Notice--This electronic transmission and any attached documents or other writings are intended only for the person or entity to which it is
addressed and may contain information that is privileged, confidential or otherwise protected from disclosure. Any disclosure, copying, distribution or the taking
of any action concerning the contents of this communication or any attachments by anyone other than the named recipient is strictly prohibited. If you have
received this communication in error, please consider the communication and any attachments as confidential and immediately notify sender by return e-mail
and destroy the communication and any and all attachments.
Confidentiality Notice--This electronic transmission and any attached documents or other writings are intended only for the person or entity to which it is
addressed and may contain information that is privileged, confidential or otherwise protected from disclosure. Any disclosure, copying, distribution or the taking
of any action concerning the contents of this communication or any attachments by anyone other than the named recipient is strictly prohibited. If you have
received this communication in error, please consider the communication and any attachments as confidential and immediately notify sender by return e-mail
and destroy the communication and any and all attachments.
3 attachments
TANKS5.1_exported_routine_losses.xlsx
16K
M70 - Moser Emissions.pdf
87K
reWATER Tap Facility PTE Emissions Calcs 4.22.25.xlsx
3490K
Katie Andersen <[e-mail]>Wed, May 7, 2025 at 12:13 PM
To: Tyson Pond <[e-mail]>
Cc: Lynn Hadlock <[e-mail]>, Juliann Marx <[e-mail]>, BJ Hadlock
<[e-mail]>
Tyson,
5/7/25, 12:29 PM State of Utah Mail - Tap Facility Notification Information Request
https://mail.google.com/mail/u/0/?ik=0900585596&view=pt&search=all&permthid=thread-a:r8301374870554409638&simpl=msg-a:r414701650618291…2/4
Thank you for these documents.
Some additional questions for you:
Is 4092 W 3000 S Roosevelt UT 84066 the correct mailing address?
What is the relationship between WEM Operating, LLC and reWater, LLC?
Cheers,
Katie Andersen
[Quoted text hidden]
Lynn Hadlock <[e-mail]>Wed, May 7, 2025 at 12:20 PM
To: Katie Andersen <[e-mail]>, Tyson Pond <[e-mail]>
Cc: Juliann Marx <[e-mail]>, BJ Hadlock <[e-mail]>
Hi Kae,
I can help answer the relaonship queson. ReWater and WEM Operang are both owned by Wasatch Energy
Management. The two LLC's operate as separate enes, however, the employees operang both companies are
WEM Operang employees.
Rewater owns all of our midstream assets, and WEM Operang is everything upstream.
Tyson as example, is an employee of WEM Operang, but he takes care of all emissions and compliance for both
companies.
Hopefully that makes sense.
Lynn Hadlock
Utah Field Superintendent
(435-828-8091)
[e-mail]
From: Kae Andersen <[e-mail]>
Sent: Wednesday, May 7, 2025 12:13 PM
To: Tyson Pond <[e-mail]>
Cc: Lynn Hadlock <[e-mail]>; Juliann Marx <[e-mail]>; BJ Hadlock
<[e-mail]>
Subject: Re: [External]Tap Facility Noficaon Informaon Request

[Quoted text hidden]
Tyson Pond <[e-mail]>Wed, May 7, 2025 at 12:23 PM
To: Katie Andersen <[e-mail]>
Cc: Lynn Hadlock <[e-mail]>, Juliann Marx <[e-mail]>, BJ Hadlock
<[e-mail]>
Yes, that is the correct address.
Thanks!

5/7/25, 12:29 PM State of Utah Mail - Tap Facility Notification Information Request
https://mail.google.com/mail/u/0/?ik=0900585596&view=pt&search=all&permthid=thread-a:r8301374870554409638&simpl=msg-a:r414701650618291…3/4
Tyson Pond
[phone]
[e-mail]

From: Kae Andersen <[e-mail]>
Sent: Wednesday, May 7, 2025 12:13 PM
To: Tyson Pond <[e-mail]>
Cc: Lynn Hadlock <[e-mail]>; Juliann Marx <[e-mail]>; BJ Hadlock
<[e-mail]>
Subject: Re: [External]Tap Facility Noficaon Informaon Request

[Quoted text hidden]
5/7/25, 12:29 PM State of Utah Mail - Tap Facility Notification Information Request
https://mail.google.com/mail/u/0/?ik=0900585596&view=pt&search=all&permthid=thread-a:r8301374870554409638&simpl=msg-a:r414701650618291…4/4
Criteria Pollutants Maximum PTE Site-Wide Uncontrolled (tons/year)
Source EPNs VOC CO NOX SOx PM PM10 PM2.5Condensate Storage Tank TK1 1.56 ------Truck Loading - Condensate L1 0.088 ------Generator ENG-1 0.65 1.39 0.46 0.002 0.070 0.070 0.070Total2.30 1.39 0.462 0.002 0.070 0.070 0.070
Criteria Pollutants - PTE Emissions Summary
TAP FACILITY
ReWATER, LLC
HAPs Maximum Site-Wide Uncontrolled PTE (tons/year)
Source EPNs Benzene Toluene e-benzene Xylenes n-Hexane Formal-
dehyde
Acetald-
ehyde Acrolein Total HAPs
Condensate Storage Tank TK1 0.009 0.013 0.001 0.008 0.032 ---0.062
Truck Loading - Condensate L1 0.000 0.001 0.000 0.000 0.005 ---0.006
Generator ENG-1 0.006 ----0.073 0.100 0.009 0.188Total0.015 0.013 0.001 0.008 0.037 0.073 0.100 0.009 0.257lbs/year 29.68 26.48 2.07 16.36 73.37 146.87 199.88 18.84 513.55

HAPs - PTE Emissions SummaryTAP FACILITYReWATER, LLC
EPNs: Site InformationAnnual Oil Production1 BOPY 1,440 Emission Factor12(lb/bbl)Oil Production 1 BOPD 3.9 VOC Flash =2.17Operating hours hrs/yr 8,760Flare DRE %0%LP Flash Loss7 (scf/hr)10.22Molecular Weight of Flash Gas2 lb/lb-mol 38.9 Annual LP Flash Loss8 (MMSCF/yr)0.089 Flash Heat Content2 Btu/scf 1,954 Flash Emissions Heat Content9 (MMBtu/hr)0.020 FGOR2 scf/bbl 31.1 Flash Emissions Heat Content10 (MMBtu/yr)784.0
Calculated Total Emissions3
lb/hr 0.5ton/yr 2.3
Composition Data
(lb/hr)4 (ton/yr) 5 (lb/hr)6 (ton/yr)6
CO2 2.67 3.02 0.016 0.069 0.016 0.069 N2 0.012 0.000 - - - - C1 42.2 17.4 0.091 0.399 0.091 0.399 C2 14.7 11.4 0.060 0.261 0.060 0.261 C3 13.7 15.5 0.081 0.356 0.081 0.356 C4 10.5 15.7 0.082 0.359 0.082 0.359 C5 6.56 12.2 0.064 0.279 0.064 0.279 C6 0.282 5.13 0.027 0.118 0.027 0.118 C7 4.32 11.1 0.058 0.256 0.058 0.256 C8 1.26 3.70 0.019 0.085 0.019 0.085 C9 0.690 2.27 0.012 0.052 0.012 0.052 C10 0.086 0.316 0.002 0.007 0.002 0.007 Benzene 0.182 0.366 0.002 0.008 0.002 0.008 Toluene 0.220 0.520 0.003 0.012 0.003 0.012 Ethylbenzene 0.015 0.041 0.000 0.001 0.000 0.001 Xylene 0.116 0.317 0.002 0.007 0.002 0.007 N-Hexane 2.51 1.05 0.005 0.024 0.005 0.024 Volatile Organic Compds. (C3+)40.4 68.2 0.357 1.564 0.357 1.564 Totals 100 100
Control Device Emissions - No Control Device EmissionsEF (lb/MMBtu)(ton/yr)11
NOx 0.068 AP-42 Chapter 13.5 0.000CO0.310 AP-42 Chapter 13.5 0.000SOx0.000 AP-42 Table 1.4-2 0.000PM2.5 0.003 AP-42 Table 1.4-2 0.000PM103.37E-03 AP-42 Table 1.4-2 0.000
1 From WEM/reWater
3Total Emissions (lb/hr) = FGOR (scf/bbl) x bbl/day x MW (lb/lbmole)/379.4 (scf/lb-mol) / 24 hrs/day; ton/yr = lb/hr *8760/2000 4Uncontrolled Emissions (lb/hr) = Total flash losses (lb/hr) x Wt %/100
7 Hourly Flash Loss (scfh) = GOR (scf/bbl) x throughput (bbl/day) / 24 (hr/day) 8 Yearly Flash Loss (MMscf/yr) = Hourly Flash Loss (scfh) x operating hrs/yr9 Flash Emissions Heat Content (MMBtu/hr) = Flash emissions heat content (MMbtu/hr)/1,000,000 btu/Mmbtu10Flash Emissions Heat Content (MMBtu/yr)= heat content (btu/scf) * flash loss (scf/hr) * hrs/yr
Source
11Control Device Emissions = waste gas heat content (MMBTU/yr) * EF (lb/MMBTU)/2000 lb/ton)12 VOC EF (lb/bbl) = Uncontrolled emissions(ton/yr)*2000 lb/ton*/bbls/yr
Component LP Flash
mol%2 LP Flash Wt%
Pollutant Emission Factor
Uncontrolled Emissions Controlled Emissions
2From UDAQ/FIP Default Production Area Designation - no site specific analyses available
5Uncontrolled Emissions (ton/yr) = Total flash losses (ton/yr) x Wt%/1006Controlled emissions = uncontrolled emissions * (1-DRE%)
Condensate Tank Flash Emissions - EOS FGOR Method TAP FACILITYReWATER, LLC
TK-1
EPNs: TK-1
Site Information CAnnual Condensate Production/tank bbls/year 1,440 Annual Condensate Production/tank gals/year 60,480 Emission Factor (lb/bbl)Number of Condensate Tanks 1 VOC WSB =0.183Volume of Storage Tanks bbls 100 Operating hours hr/yr 8,760VRUNo 0.0876 Flare DRE %0%0.34 Molecular Weight of W&S gas1 lb/lb-mol 50.0 0.003 Reid Vapor Pressure 5.00 0.001 Heat Content3 Btu/scf 1,954 5.9 Total losses per tank2 lb/yr 349 Total losses per tank lb/hr 0.04 Total losses per tank ton/yr 0.17
(lb/hr)4 (ton/yr) 4
CO2 2.67 0.001 0.005 N2 0.000 - - C1 5.83 0.002 0.010 C2 15.9 0.006 0.028 C3 27.3 0.011 0.048 C4 20.4 0.008 0.036 C5 11.9 0.005 0.021 C6 0.496 0.000 0.001 C7 5.699 0.002 0.010 C8 3.615 0.001 0.006 C9 0.518 0.000 0.001 C10 0.258 0.000 0.000 Benzene 0.265 0.000 0.000 Toluene 0.447 0.000 0.001 Ethylbenzene 0.031 0.000 0.000 Xylene 0.315 0.000 0.001 N-Hexane 4.329 0.002 0.008 Total Volatile Organic Compounds 75.57 0.030 0.132
Control Device Emissions - No Control Device Emissions6
EF (lb/MMBtu)(tons/yr)NOx 0.068 AP-42 Chapter 13.5 0.0000CO0.310 AP-42 Chapter 13.5 0.0000SOx2.66E-04 AP-42 Table 1.4-2 0.0000PM2.5 3.37E-03 AP-42 Table 1.4-2 0.0000PM103.37E-03 AP-42 Table 1.4-2 0.0000
4 Uncontrolled emissions (lb/hr) = Total losses per tank (lb/hr)* no. tanks * stable oil vapor wt%/100
5Uncontrolled emissions (ton/yr) = Total losses per tank (ton/yr)*no. tanks* stable oil vapor wt%/1005Emissions during VRU downtime = uncontrolled emissions * VRU downtime (%)
Component
Pollutant Emission FactorSource
1From AP-42, Table 7.1-2
2From EPA TANKS5.1 Output Report3From UDAQ/FIP Emissions Inventory Default Production Area Designation - no site specific analyses available
Composition Data
Uncontrolled Emissions Stable Oil
Vapor Wt%3
6Control Device Emissions = waste gas heat content (MMBTU/yr) * EF (lb/MMBTU)/2000 lb/ton)
Vapor Density (lb/cu.ft)1
Hourly W&S loss (scf/hr) Annual W&S loss (MMscf/yr) Heat Content (MMBtu/hr) Heat Content (MMBtu/yr)
Condensate Storage Tank Working & Standing Emissions TAP FACILITYReWATER, LLC
EPN: L1
Site Information
BOPD 3.9
gal/day 166
gal/hr 6.90
True VP of Liquid Loaded (P)1 psia 6.00
MW of Vapor (M)2 lb/lb-mol 50.00
Temperature of liquid (T)3 ˚R 580
Saturation Factor (S)4 constant 0.6
Loading Losses5 (L)lb/1000 gal 3.87
Control Capture Efficiency %0%
Heat Content btu/scf 1,954
Control Efficiency %`0%
8760 hrs/yr 8760 hrs/yr 8760 hrs/yr
(lb/hr)(ton/yr) CO2 2.674 0.001 0.003
N2 0.000 - -
C1 5.827 0.002 0.007
C2 15.934 0.004 0.019
C3 27.264 0.007 0.032
C4 20.416 0.005 0.024
C5 11.911 0.003 0.014
C6 0.496 0.000 0.001
C7 5.699 0.002 0.007
C8 3.615 0.001 0.004
C9 0.518 0.000 0.001
C10 0.258 0.000 0.000
Benzene 0.265 0.000 0.000
Toluene 0.447 0.000 0.001
Ethylbenzene 0.031 0.000 0.000
Xylene 0.315 0.000 0.000
N-Hexane 4.329 0.001 0.005
Total VOCs 75.57 0.020 0.088
Control Device Emissions - No Control Device Emissions11
EF (lb/MMBtu)(tons/yr)
NOx 0.068 AP-42 Chapter 13.5 0.000CO0.310 AP-42 Chapter 13.5 0.000
SOx 2.66E-04 AP-42 Table 1.4-2 0.000PM2.5 3.37E-03 AP-42 Table 1.4-2 0.000PM103.37E-03 AP-42 Table 1.4-2 0.0001From AP-42, Figure 7.1-13
2From AP-42, Table 7.1-23 Temperature of liquids loaded = 160o F4From AP-42, Table 5.2-1, submerged loading5 From AP-42, Section 5.2, equation 1; L=12.46*SPM/T
Source
6 Emissions lb/hr = L (lb/1000 gal)*Loading rate (gal/hr)/1000 gal*wt%/100
Emissions ton/yr = emissions (lb/hr)*8760/200011Control Device Emissions = waste gas heat content (MMBTU/yr) * EF (lb/MMBTU)/2000 lb/ton)
Pollutant Emission Factor
Composition Data2 Uncontrolled
Emissions6PollutantStable Oil
Vapor Wt%
Condensate Loading EmissionsTAP FACILITYReWATER, LLC
Loading Rate
EPN: ENG-1
Engine Data Method of Emission ControlManufacturerPSI Federal StandardsModelG8.1 YesSerial Number TBD MACT Subpart ZZZZ NoManufacture Date TBDApplicationelectric genIgnition/injection timing VariableHorsepower118Site Rated Horsepower 96Fuel Consumption (Btu/hp-hr)8545Hours of operation per year 8760 Fuel ConsumptiomEngine Type 4SRB HHV 1,020 btu/scfFuel Data Fuel Cons.7,792 btu/bhp-hrFuel Heat Content1 (Btu/scf)1,020 Operating 8,760 hr/yrFuel Sulfur Content3 (grain/scf)5788.0 Fuel consumption 6,404,776 scf/yrAnnual Consumption (MMScf/yr)7.0 6,405 mscf/yrHourly Consumption (MMscf/hr)0.0008 Site Elevation 6297 ftHourly Consumption (MMBtu/hr)0.82
EF AP-42
Contaminant
Test results or
manufacturer's
EF before
control
(g/hp-hr)
Table 3.2-3
4 stroke, rich-
burn engine
emission
factors
(lb/mmBtu)
Emission
Factor
Used Units
Emissions
(lb/hr)
Emissions
(tpy)
Efficiency
of Control
Device4
( %)
Control
Emission
factor4
(g/hp-hr)
Emissions
(lb/hr)
Emissions
(tpy)Katie's results At 118 hpVOC0.10 0.0296 0.10 g/hp-hr 0.02 0.09 0.7 0.148 0.65 0.65 0.8NOx12.0 2.21 12.0 g/hp-hr 2.53 11.08 0.5 0.105 0.462 0.46 0.57CO11.5 3.72 11.5 g/hp-hr 2.42 10.62 1.5 0.316 1.385 1.39 1.71PM1020.01941 0.0194 lb/mmBtu 0.016 0.070 0.016 0.070 0.06 0.07PM2.52 0.01941 0.0194 lb/mmBtu 0.016 0.070 0.016 0.070 0.06 0.07SO20.000588 0.0006 lb/mmBtu 0.000 0.002 0.000 0.002Formaldehyde0.0205 0.0205 lb/mmBtu 0.017 0.073 0.017 0.073Benzene0.00158 0.0016 lb/mmBtu 0.001 0.006 0.001 0.006Acetaldehyde0.0279 0.0279 lb/mmBtu 0.023 0.100 0.023 0.100Acrolein0.00263 0.0026 lb/mmBtu 0.002 0.009 0.002 0.009Methanol0.00306 0.0031 lb/mmBtu 0.003 0.011 0.003 0.011Total HAPS 0.046 0.199 0.046 0.1991AP-42 Pipeline quality gas spec2PM10 EF = PM10 (filterable) + PM (Condensable); PM2.5 EF = PM2.5 (filterable) + PM (Condensable)3 Emissions (lb/hr)= EF(g/hp-hr)/454 g/lb*hp; or EF(lb/mmBTU)*fuel consumption (Btu/hp-hr)*hp/1.0*106;(tpy) = (lb/hr)*8760 hr/yr/2000 lb/ton 4 Provided by manufacturer or field adjustment5Controlled emissions are calculated using efficiency of control device (%) or controlled emission factor
NSPS Subpart JJJJJLCC Catalyst NoParameter Adjustment No
Uncontrolled Emissions3 Controls Controlled Emissions5
SCR Catalyst
Stratified ChargeAFR YesLean Burn No
No
No
Generator Engine EmissionsTAP FACILITYReWATER, LLC
NSCR Catalyst Yes
Flash Gas MW Calculator
Site-Specific Information - Enter information in yellow cells
Gas Oil Ratio1:31.07
VOC emission Factor9 = 2.17 lb voc/bblFlash Gas MW (lb/lb-mol) = 38.90Componentmole1 %Molecular grams per weight %4
hydrogen 0.0000 2.02 0 0.0000helium0.0000 4.00 0 0.0000 0.517514nitrogen0.0123 28.01 0 0.0089 2.26671CO22.6712 44.01 118 3.0223H2S0.0000 34.08 0 0.0000 68.1847methane (C1)42.1886 16.04 677 17.3999ethane (C2)14.7268 30.07 443 11.3843 0.352865propane (C3)13.6834 44.10 603 15.5120 1.545549butanes (C4)10.4800 58.12 609 15.6598pentanes (C5)6.5558 72.15 473 12.1600 0.3665benzene 0.1825 78.11 14 0.3665other hexanes (C6)2.7880 86.18 240 6.1770 0.001896toluene0.2196 92.14 20 0.5203 0.008307other heptanes (C7)4.3243 100.20 433 11.1394ethylbenzene0.0151 106.17 2 0.0412 0.0000xylenes (o, m, p)0.1160 106.17 12 0.3166other octanes (C8)1.2605 114.23 144 3.7018 0nonanes (C9)0.6895 128.26 88 2.2736 0decanes plus (C10+)0.0864 142.50 12 0.3164Totals:100.0000 38.90 3890 100.00
1From UDAQ/FIP Emissions Inventory Default Production Area Designation2 From Perry's Chemical Engineers' Handbook, 8th edition.
3Grams per 100 moles of gas = mole% * molecular wt (grams/mole;lb/lb-mol)4Weight % = grams component per 100 moles of gas (grams) / total weight of 100 moles gas (grams)5Total gas emitted (lb/hr) = flash GOR (scf/bbl)*BOPD*flash gas MW (lb/lb-mol)/379.4832 (scf/lb-mol)*24 hrs/day.
where 379.4832 scf/lb-mole = ideal gas law conversion factor6Total gas emitted (tpy) = total gas emitted (lb/hr) * ton/2000 lb * 8760 hrs/yr7VOC wt% = sum of C3 - C10+ component weight %
8 VOC (lb/hr) = VOC wt% * total gas emitted (lb/hr); VOC (tpy) = VOC wt% * total gas emitted (tpy)9 VOC emission factor (lb VOC/bbl) = VOC (tpy) * 2000 lb/ton /bbl oil (bbl/yr)
Benzene, lb/hr:Benzene, tpy:
H2S wt% =
H2S, lb/hr:H2S, tpy:
CALCULATED
Flash Gas Speciation:
VOC, tpy:
Benzene wt% =
Total gas emitted5,6
lb/hr:tpy:
VOC wt%7 =
VOC, lb/hr8:
In standard cubic feet of flash gas per barrel (SCF/bbl) of oil/condensate
produced
Barrels of Oil or Condensate per day: 3.9 Enter BOPD
Produced Natural Gas CompositionGas MW (lb/lb-mole)23.00VOC wt %29.86%68.18%Heat Content (BTU/scf)1191 1954GOR800031# of Samples Taken 67 67Mole Fraction Mole Fraction Mole Fraction Mol %Weight %CO2 0.0211 0.0267 2.6712 3.0223N20.0084 0.0001 0.0123 0.0000C10.7851 0.4219 42.1886 17.3998
C2 0.0789 0.1473 14.7268 11.3843
C3 0.0422 0.1368 13.6834 15.5120
C4 0.0239 0.1048 10.4800 15.6598
C5 0.0145 0.0656 6.5558 12.1600
C6 0.0063 0.0028 0.2820 5.1282C70.0061 0.0432 4.3243 11.1394C80.0048 0.0126 1.2605 3.7018C90.0006 0.0069 0.6895 2.2736C100.0017 0.0009 0.0864 0.3164
Benzene 0.0004 0.0018 0.1825 0.3665
Toluene 0.0007 0.0022 0.2196 0.5203
Ethylbenzene 0.0001 0.0002 0.0151 0.0412
Xylene 0.0004 0.0012 0.1160 0.3166N-Hexane 0.0047 0.0251 2.5060 1.0489
Total 1.0000 1.0000 100.0 100.0
Production Area DesignationDefaultFlash Gas Analysis
75.57%
1954
31
67Mole Fraction Mol %Wt%0.0270 2.6998 2.67380.0000 0.0000 0.00000.1614 16.1402 5.82690.2355 23.5471 15.93370.2747 27.4746 27.26370.1561 15.6087 20.41590.0734 7.3362 11.91130.0026 0.2558 0.49620.0253 2.5273 5.69880.0141 1.4064 3.61540.0018 0.1795 0.51810.0008 0.0803 0.25760.0015 0.1510 0.26540.0022 0.2158 0.44740.0001 0.0131 0.03130.0013 0.1319 0.31510.0223 2.2324 4.32941.0000 100.00 100.00

Standing Working Breathing Gas Analysis
Engine Type:PSI / HDI G8.1LNA I-6 AFR Controller:Engine ECU Integrated
Engine Displacement, L (in3):8.1 (494)Ignition System:Engine ECU-controlled timing
Engine Speed, rpm:1800 Jacket Water Outlet, °F:185
Compression Ratio:10.5:1 Jacket Water Capacity, gal:9
Combustion:4-stroke Rich Burn Lube Oil Capacity, gal:6
Aspiration:Naturally Aspirated Catalyst Housing Length, in:20.8"
Charge Air Cooler:N/A Substrate Dimensions, in:7" L x 5.66" dia (2pcs in parallel per catalyst)
Engine Dry Weight, lbs (kg):1641 (744)Exhaust Stack Height, in:96"
Engine ECU:Econtrols GCP/4G Heavy-Duty Exhaust Stack Diameter, in:3.5"
Measurement Conditions:
Fuel:Commercial-grade Natural Gas Elevation (ft above sea level):1200
Fuel Pressure at Engine Inlet:11 in H2O Inlet Air Temp (°F):77
Fuel HHV (BTU/scf):1015 Fuel Methane Number:97
Fuel LHV (BTU/scf):927 Engine Speed (rpm):1800
Power Rating
Prime Engine Power
BMEP
Fuel Consumption
Air Intake / Exhaust
Combustion Air Consumption
Exhaust Gas Mass Flow
Exhaust Gas Volumetric Flow
Exhaust Temperature
Pre-catalyst Emissions
CO
NOx
VOC
Post-catalyst Emissions
CO
NOx
VOC
CO2*
*Estimated emissions based on US EIA Carbon Dioxide Emissions Coefficient of 52.91 kg CO2 per 1 million BTU of natural gas
bhp (kWm)118 (88)112 (84)89 (66)
psi (bar)105 (7.2)100 (6.9)79 (5.5)
M70
Gaseous-fueled prime power generator
Engines used in Moser generators meet applicable EPA standards for engine performance, equipment protection, and emissions control. Emissions are controlled via an
integrated air-fuel ratio controller, precision spark timing control, three-way catalytic converters, pre- and post-catalyst EGO sensors, and closed-loop emissions control
feedback. Catalytic converter health is further monitored with pre- and post-catalyst exhaust thermocouples and pressure transducers that measure backpressure. All
units are equipped with telematics that allow operating parameters to be monitored from anywhere at any time.
Units 100%95%75%
Units 100%95%75%
Fuel Consumption (LHV)BTU/bhp-hr 7804 7891 8262
BTU/kWm-hr 10465 10572 11141
Fuel Consumption (HHV)BTU/bhp-hr 8545 8596 9000
BTU/kWm-hr 11458 11575 12198
Fuel Flow (based on LHV)
SCF/min 16.6 15.9 13.2
SCF/bhp-hr 8.42 8.51
ACF/min 153 146 122
lb/hr 781 749 624
8.91
SCF/kWm-hr 11.29 11.40 12.02
Units 100%95%75%
Units 100%95%75%
g/bhp-hr 11.5 11.5 11.5
ACF/min 589 596 548
°F 1377 1369 1333
Units 100%95%75%
g/bhp-hr < 1.5 < 1.5 < 1.5
g/bhp-hr 12 12 12
g/bhp-hr 0.1 0.1 0.1
Except as expressly set forth in a written agreement with Moser Energy Systems executed by Moser Energy Systems and the party renting/leasing the generator(s) that is the subject of this
datasheet, Moser Energy Systems shall have no liability for any representations or warranties, and Moser Energy Systems hereby expressly disclaims all statutory, oral, expressed or implied
representations and warranties with respect to the generators. In the event that such parties enter into a written agreement with respect to the generators, Moser Energy System's maximum
aggregate liability for any and all claims and losses arising out of or in connection with any breach of any representation, warranty or guarantee arising out of or in connection with the engines
in any generator shall be limited to, and in no case shall exceed, $25,000.
kg/hr 83 80 67
All representations and warranties as to performance are dependent on a written agreement with Moser Energy Systems and with the submission to Moser, and Moser’s written approval of, a
current (<6 months old) gas analysis report and updated gas analysis reports every six months thereafter. Gas supplied to generator(s) must be free of liquids and hydrogen sulfide (H2S) and
any representations or warranties as to performance shall be dependent on satisfaction of this free liquids condition.
There are a number of factors that may affect emission measurements and therefore reliance on representations as to performance. Measured emissions levels are subject to
instrumentation and equipment variability. Production tolerances in engine, generator, and other components can account for variances in data of +/-5%. Actual field test results may vary
due to factors including, but not limited to, ambient conditions, fuel quality, produced water chemical content, installation, application, and instrumentation. Excessive intake or exhaust
restriction, excessive water in the fuel, or improper engine maintenance may result in elevated emissions levels.
g/bhp-hr < 0.5 < 0.5 < 0.5
g/bhp-hr <0.7 <0.7 <0.7
Exhaust height:
96" (2017)
Tank ID Tank Type Description
Tap Facility Vertical Fixed Roof Tank 100 bbl vertical tank
City, State Company Meteorological Location
Vernal Utah, Utah WEM/reWater Salt Lake City, UT
Chemical Name Annual Standing Losses (lb/yr)Annual Rim Seal Losses (
Midcontinent Crude Oil RVP 5 0
Annual Deck Seam Losses (lb/yr)Annual Deck Fitting Los Annual Working Losses (lb/yr)
349.2321971
Annual Total Losses (lb/yr)
349.2321971
Tank ID Tank Type Description
Tap Facility Vertical Fixed Roof Tank 100 bbl vertical tank
City, State Company Chemical Name
Vernal Utah, Utah WEM/reWater Midcontinent Crude Oil RVP 5
Annual Standing Losses (lb/yr)Annual Working Losses (lb/yr)Annual Vapor Space Volume (c
0 349.2321971 354.0666014
Annual Stock Vapor Density (lb Annual Average Vapor Space Ex Annual Average Vented Vapor
0.057911585 0 0.249422927
Effective Diameter (ft)Vapor Space Outage (ft)Average Liquid Height (ft)
7.5 8.014428415 7
Roof Outage (ft)Dome Radius (ft)Shell Radius (ft)
0.514428415 7.5 3.75
Tank Cone Roof Slope (ft/ft)Annual Average Vapor Molecu Annual Average Vapor Pressure
50 7.084521124
Annual Average Liquid Surface Annual Average Ambient Temp Liquid Bulk Temperature (°R)
570 512.77 570
Tank Paint Solar Absorptance (Tank Paint Solar Absorptance (Annual Average Vapor Temper
0.42 0.42 0
Annual Average Daily Vapor Pr Breather Vent Press. Setting Ra Annual Average Vapor Pressure
0 0.06 7.084521124
Annual Average Vapor Pressure Annual Average Min. Liquid Su Annual Average Max. Liquid Su
7.084521124 570 570
Annual Average Daily Ambient Vapor Space Pressure at Norma Annual Throughput (gal/yr)
20.4 0 60480
Annual Turnovers Working Loss Turnover Factor Maximum Liquid Height (ft)
13.55466298 1 13.5
Minimum Liquid Height (ft)Working Loss Product Factor Vent Setting Correction Factor
0 0.75 0.994609628
Annual Sum of Increases in Liquid Level (ft/yr)
182.9879502
Tank ID Tank Type DescriptionCity, State Company Meteorolo Tank ShapeShell Lengt Shell Side L
Tap FacilityVertical Fix 100 bbl ve Vernal Uta WEM/reW Salt Lake C Cylinder
Shell Side 1 Shell Side 2 Shell Heigh Shell Diam Maximum Average Liq Minimum Is Tank HeaTypical Ma
14.5 7.5 13.5 7 Not Heated
Typical Ave Typical Min Number of Roof Type Vacuum Se Pressure Se Vapor Spac Is Tank Ins Is Tank Ins
Dome -0.03 0.03 0 Fully Insulated
Tank Cone Tank Dome Is Tank Equ Control De Liquid Bulk Liquid Bulk Tank Botto Cone-Shap Liquid Hee
7.5 No Contro 570 flat none
Minimum Self Suppo Number of Effective C Internal Sh Primary Se Secondary Seal Fit Deck Type
Tank ConstDeck ConstDeck SeamPanel/Shee Panel Leng Shell Color Shell Cond Roof Color Roof Condi
Beige/CreaAverage Beige/CreaAverage
ition
Tank ID Meteorolo Annual Ave Annual Ave Annual Ave Annual Ave Annual Ave January Av January Av
Tap FacilitySalt Lake C 12.62 63.3 42.9 8.3 1442 37.7 23.3
January Av January Av February A February A February A February A March Ave March Ave March Ave
6.7 596 43.1 26.9 7.2 877 53.4 34.4 8.7
March Ave April Avera April Avera April Avera April Avera May Avera May Avera May Avera May Avera
1348 60.3 40.2 9.6 1685 71.5 49 8.9 2071
June Avera June Avera June Avera June Avera July Averag July Averag July Averag July Averag August Ave
81.8 57.3 9.2 2336 92.4 66.4 8.9 2338 90.1
August Ave August Ave August Ave September September September September October Av October Av
64.9 9.6 2052 78.9 54.3 8.7 1689 64 42.2
October Av October Av November November November November December December December
8.1 1144 48.7 31.1 7.4 700 38 24.1 7.2
December Average Daily Total Insolation Factor (Btu/ft2/day)
469
Tank ID Input Type Chemical Category of L
Tap Facility Enter Annual Values Petroleum Liquids
Sum of Increases in Liquid Level Method Working Loss Turnover Factor Meth
AP-42 Calculation AP-42 Calculation
Annual Chemical Name Annual Speciation Option Annual Components to Speciate
Midcontinent Crude Oil RVP 5
Annual Throughput Annual Sum January Ch January Sp January Co January ThJanuary Su
60480
February C February S February C February T February S March Che March Spe March Com March Thro
March Sum April Chem April Speci April Comp April ThrouApril Sum o May Chem May Specia May Comp
May ThrouMay Sum o June Chem June Speci June Comp June ThrouJune Sum o July Chemi July Specia
July Compo July ThrougJuly Sum o August Che August Spe August Com August ThrAugust Sum September
September September September September October Ch October Sp October Co October ThOctober Su
November November November November November December December December December
December Sum of Increases/Decreases in Liquid Level (ft/yr)
Criteria Pollutants - Maximum PTE Site-Wide (tons/year)
Source EPNs VOC CO NOX SOx PM PM10 PM2.5
Condensate Storage Tank TK1 1.564 0.123 0.027 0.000 0.001 0.001 0.001
Truck Loading - Condensate L1 0.080 ------
Generator ENG-1 0.393 1.12 0.56 0.001 0.039 0.039 0.039Total2.037 1.24 0.588 0.001 0.040 0.040 0.040
HAPs - Maximum Site-Wide PTE (tons/year)
Source EPNs Benzene Toluene e-benzene Xylenes n-Hexane Formal-
dehyde
Acetald-
ehyde Acrolein Total HAPs
Condensate Storage Tank TK1 0.009 0.013 0.001 0.008 0.035 ---0.066
Truck Loading - Condensate L1 0.000 0.000 0.000 0.000 0.005 ---0.006
Generator ENG-1 0.003 ----0.041 0.017 0.010 0.071
Total 0.012 0.014 0.001 0.008 0.040 0.041 0.017 0.010 0.143
Potential to Emit (PTE) Emissions Summary
reWater, LLC
Tap Facility

reWater, LLC
4092 West 3000 South
Roosevelt, Utah

April 23, 2025
Bryce Bird
UDAQ Director
P.O. Box 144820
Salt Lake City, Utah 84114-4820
Dear Mr. Bird,
This notice is to inform you that reWater, LLC is planning a small tap at the coordinates
of Latitude: 40.092651, Longitude: -110.336633, into Four Point Energy's gasline to the
Moon Ranch Compressor.
We will take gas off our 12" natural gas line, run it through a 10hp gas cooler and meter,
and inject it into Four Point Energy's 6" meter. The site will have a pig receiver and an
uncontrolled 100BBL tank for liquids. The estimated throughput for the tap is 1440BBLs
of condensate per year. The site will flow daily with pigging typically done weekly. The
Tank will be unloaded as needed expected to be monthly. Additionally, the site will have
a 70hp generator set using natural gas to drive it.
The site manager will be BJ Hadlock, who can be reached at 435-790-5609. For
estimated emission rates, please refer to the PTE table sent with this letter.
Thank you for your attention to this matter.
Sincerely,

Tyson Pond
Regulatory Compliance
WEM Operating, LLC
435-828-0531