DAQ-2025-001248

Small Source Registration

DAQE-EN162550001-25

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Lori McClaflin
FinishWorks
3350 West Directors Row, Suite 100
Salt Lake City, UT 84104
[e-mail]

Dear Ms. McClaflin:

Re: Request for Evaluation of Compliance with Rule R307-401-9, UAC: Small Source Exemption
Project Fee Code: N162550001

On February 12, 2025, the Division of Air Quality (DAQ) received your request for a small source
exemption for FinishWorks - Coating Manufacturing Plant. The source is located at 3350 West Directors Row Suite 100, Salt Lake City, Salt Lake County. 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, FinishWorks - Coating Manufacturing Plant is not
required to obtain an approval order under R307-401. 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
Interim Executive Director

DIVISION OF AIR QUALITY
Bryce C. Bird
Director

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DAQE-EN162550001-25
Page 2

Thank you for registering your source with the DAQ. If you have any additional questions, please contact
Mr. Tim DeJulis at [phone] or [e-mail].

Sincerely,

Bryce C. Bird
Director

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Alan D. Humpherys, Manager
New Source Review Section

BCB:ADH:TD:jg

{{#d1=date1_es_:signer1:date:format(date, "mmmm d, yyyy")}} {{#s=Sig_es_:signer1:signature}}
Response Summary:
To be eligible businesses shall not do any of the follow:

1) Emit more than 5 tons per year of each of the following pollutants: Sulfur Dioxide (SO2), Carbon Monoxide (CO),
Nitrogen Oxides (NOx), Particulate Matter (PM10), Ozone (O3), or Volatile Organic Compounds (VOCs).
2) Emit more than 500 lbs/yr of any single Hazardous Air Pollutant (HAP), and emit more than 2000 lbs/yr of any
combination of HAPs
3) Emit more than 500 lbs/yr of any combination of air contaminants not listed in 1 or 2

A copy of this registration notice and worksheets are required on site to verify permit exemption status.

Please be aware a the Small Source Exemption ONLY exempts the site from the air permitting requirements of R307-
401-5 thru R307-401-8 of the Utah Administrative Code, all other air quality regulations still apply.

Q4.
Please fill out the following contact information:
Site Contact Site Owner
Name Lori McClaflin FinishWorks Derek WIlson
Mailing Address 3350 W. Directors Row 3350 W. Directors Row 7990 W 075 N
Mailing Address 2 Suite 100 Suite 100 -
City Salt Lake City Salt Lake City Shipshewana
State Utah Utah IN
Zip Code 84104 84104 46565
Phone [phone] (801)-204-4350 (260)-214-1400
Fax No Fax No Fax No Fax
Email [e-mail] [e-mail] [e-mail]

Q5. County the Site is located in:
Salt Lake County

Q6. Briefly describe the process including the end products, raw materials, and process equipment used.
FinishWorks manufactures custom wood stains, paints, and coatings for furniture, cabinet, and trim. The site operates
8 hours a day, 5 days a week. The manufacturing process consists of the tinting and blending of these materials,
quality control using a coating booth to test products, and subsequent packaging in various container sizes. Raw
materials include water, solvents, and pigments. Process equipment includes coating booths, mixers, and dispensers.

Q7. List emission units
One coating booth
Tinting, blending, and repackaging operations
Three space heaters

Q8. List any pollution control equipment
NA

Q9. Please include Annual Emission Rates calculation spreadsheet.
[Click here]

Q11. Contact Information: (person filling out form - signature will be required)
Name Derek Wilson
Title EHS Manager
Phone [phone]
Date 02/10/2025

Q10. By signing below, I hereby certify that the information and data submitted in this notice fully describes
this site and ONLY this site. The information provide is true, accurate, and complete to the best of my
knowledge. I understand that I am responsible for determining whether the site remain eligible for this
exemption before making operational or process changes in the future, and agree to notify the Division of
Air Quality when this site is not longer eligible for this exemption. (Signature of Owner/Manager)
[Click here]

Embedded Data:
N/A
Emission Summary:
Combustion Emissions Coating Booth
Emissions
Blending, Tinting, and
Packaging Emissions
Total Actual
Emissions
ton/yr ton/yr ton/yr ton/yr
PM 1E-02 0.04 0.1
PM10 1E-02 0.04 0.1
SO2 8E-04 8E-04
CO 0.11 0.1
NOx 0.13 0.1
VOC 7E-03 0.33 0.01 0.3
Total HAP 2E-03 0.08 4E-03 0.1
lead 6E-07 6E-07
toluene 4E-06 0.03 3E-04 0.0
xylene 0.07 5E-04 0.1
ethylbenzene 0.01 9E-05 0.01
formaldehyde 1E-04 0.01 4E-03 0.01
MIK 0
2-methylnaphthalene 3E-08 3E-08
3-methylcholanthrene 2E-09 2E-09
7,12- dimethylbenz(a)anthracene 2E-08 2E-08
acenaphthene 2E-09 2E-09
acenaphthylene 2E-09 2E-09
anthracene 3E-09 3E-09
benz(a)anthracene 2E-09 2E-09
benzene 3E-06 3E-06
benzo(a)pyrene 2E-09 2E-09
benzo(b)fluoranthene 2E-09 2E-09
benzo(g,h,i)perylene 2E-09 2E-09
benzo(k)fluoranthene 2E-09 2E-09
chrysene 2E-09 2E-09
dibenzo(a,h)anthracene 2E-09 2E-09
dichlorobenzene 2E-06 2E-06
fluoranthene 4E-09 4E-09
fluorene 4E-09 4E-09
hexane 2E-03 2E-03
indeno(1,2,3-cd)pyrene 2E-09 2E-09
naphthalene 8E-07 8E-07
phenanathrene 2E-08 2E-08
pyrene 6E-09 6E-09
arsenic 3E-07 3E-07
beryllium 2E-08 2E-08
cadmium 1E-06 1E-06
chromium 2E-06 2E-06
cobalt 1E-07 1E-07
manganese 5E-07 5E-07
mercury 3E-07 3E-07
nickel 3E-06 3E-06
selenium 3E-08 3E-08
Pollutant
FinishWorks - Salt Lake City, UT
2023 Actual Air Emissions Summary
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 1
Actual Emissions Summary
February 2025
Emission Summary:
lb/hr ton/yr lb/hr ton/yr lb/hr ton/yr lb/hr ton/yr
PM 4.5E-03 2E-02 0.05 0.2 0.05 0.2
PM10 4.5E-03 2E-02 0.05 0.2 0.05 0.2
SO2 3.5E-04 2E-03 4E-04 2E-03
CO 4.9E-02 2E-01 0.05 0.2
NOx 5.9E-02 3E-01 0.06 0.3
VOC 3.2E-03 1E-02 0.37 1.6 0.01 0.02 0.38 1.7
Total HAP 1.1E-03 5E-03 0.09 0.4 3.4E-03 0.01 0.10 0.4
lead 2.9E-07 1E-06 3E-07 1E-06
toluene 2.0E-06 9E-06 0.03 0.1 2.7E-04 1E-03 0.03 0.1
xylene 0.08 0.4 3.9E-04 2E-03 0.08 0.4
ethylbenzene 0.01 0.0 7.9E-05 3E-04 0.01 0.04
formaldehyde 4.4E-05 2E-04 3.2E-03 1E-02 3.3E-03 0.01 0.01 0.03
MIK 0 0
2-methylnaphthalene 1.4E-08 6E-08 1E-08 6E-08
3-methylcholanthrene 1.1E-09 5E-09 1E-09 5E-09
7,12- dimethylbenz(a)anthracene 9.4E-09 4E-08 9E-09 4E-08
acenaphthene 1.1E-09 5E-09 1E-09 5E-09
acenaphthylene 1.1E-09 5E-09 1E-09 5E-09
anthracene 1.4E-09 6E-09 1E-09 6E-09
benz(a)anthracene 1.1E-09 5E-09 1E-09 5E-09
benzene 1.2E-06 5E-06 1E-06 5E-06
benzo(a)pyrene 7.1E-10 3E-09 7E-10 3E-09
benzo(b)fluoranthene 1.1E-09 5E-09 1E-09 5E-09
benzo(g,h,i)perylene 7.1E-10 3E-09 7E-10 3E-09
benzo(k)fluoranthene 1.1E-09 5E-09 1E-09 5E-09
chrysene 1.1E-09 5E-09 1E-09 5E-09
dibenzo(a,h)anthracene 7.1E-10 3E-09 7E-10 3E-09
dichlorobenzene 7.1E-07 3E-06 7E-07 3E-06
fluoranthene 1.8E-09 8E-09 2E-09 8E-09
fluorene 1.6E-09 7E-09 2E-09 7E-09
hexane 1.1E-03 5E-03 1E-03 5E-03
indeno(1,2,3-cd)pyrene 1.1E-09 5E-09 1E-09 5E-09
naphthalene 3.6E-07 2E-06 4E-07 2E-06
phenanathrene 1.0E-08 4E-08 1E-08 4E-08
pyrene 2.9E-09 1E-08 3E-09 1E-08
arsenic 1.2E-07 5E-07 1E-07 5E-07
beryllium 7.1E-09 3E-08 7E-09 3E-08
cadmium 6.5E-07 3E-06 6E-07 3E-06
chromium 8.2E-07 4E-06 8E-07 4E-06
cobalt 4.9E-08 2E-07 5E-08 2E-07
manganese 2.2E-07 1E-06 2E-07 1E-06
mercury 1.5E-07 7E-07 2E-07 7E-07
nickel 1.2E-06 5E-06 1E-06 5E-06
selenium 1.4E-08 6E-08 1E-08 6E-08
FinishWorks - Salt Lake City, UT
Potential Uncontrolled Air Emissions Summary
Blending, Tinting, and
Packaging Emissions
Total Potential
EmissionsPollutantCombustion Emissions Coating Booth
Emissions
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 2 Potential Emissions Summary
February 2025
Basis
Temperature 30.0 C =86 F
Total Vapor Pressure 58.7 mmHg
1.1 psi
Liquid molecular weight 38.0
Vapor molecular weight 27.8
A B C
123-86-4 n-butyl acetate 17.50%116.16 5.72%7.24491 1518.3865 222.077 16.65 0.95 1.62%6.80%X
13463-67-7 titanium dioxide 17.50%79.86 8.32%0 0.00 0.00%0.00%71-36-3 butanol 6.25%74.12 3.20%7.3013 1285.0227 173.247 9.52 0.30 0.52%1.39%X
108-38-3 m-xylene 6.25%106.17 2.24%7.18115 1573.0243 226.671 11.29 0.25 0.43%1.65%X X
763-69-9 eep 6.25%146.18 1.62%7.3845 1710.719 209.847 1.79 0.03 0.05%0.26%X
95-47-6 o-xylene 6.25%106.17 2.24%7.8126 1901.373 246.882 8.82 0.20 0.34%1.29%X X106-42-3 p-xylene 1.75%106.17 0.63%7.15471 1553.9461 225.23 11.65 0.07 0.12%0.48%X X
100-41-4 ethylbenzene 1.75%106.17 0.63%7.1561 1559.5452 228.582 13.33 0.08 0.14%0.54%X X
64-17-5 ethanol 0.55%46.07 0.45%8.12875 1660.8713 238.131 86.00 0.39 0.66%1.10%X
50-00-0 formaldehyde 0.55%30.03 0.70%7.46432 1078.39 254.377 4701.17 32.70 55.74%60.30%X X39464-64-7 polyoxyethylene dinonyphenyl ether phosphate0.10%200 0.02%1.00 0.00 0.00%0.00%X
68891-21-4 surfactant 0.10%200 0.02%1.00 0.00 0.00%0.00%X
7732-18-5 water 35.20%18.01 74.22%8.05573 1723.6425 233.08 31.91 23.69 40.37%26.20%
73.80%64.25%
Total Vapor Pressure 58.7 mmHg
1.1 psi
Liquid molecular weight 38.0Vapor molecular weight 27.8
A B C123-86-4 n-butyl acetate 17.50%116.16 5.72%7.24491 1518.3865 222.077 16.65 0.95 1.62%6.80%X13463-67-7 titanium dioxide 17.50%79.86 8.32%0 0.00 0.00%0.00%
71-36-3 butanol 6.25%74.12 3.20%7.3013 1285.0227 173.247 9.52 0.30 0.52%1.39%X
108-38-3 m-xylene 6.25%106.17 2.24%7.18115 1573.0243 226.671 11.29 0.25 0.43%1.65%X X
763-69-9 eep 6.25%146.18 1.62%7.3845 1710.719 209.847 1.79 0.03 0.05%0.26%X95-47-6 o-xylene 6.25%106.17 2.24%7.8126 1901.373 246.882 8.82 0.20 0.34%1.29%X X
106-42-3 p-xylene 1.75%106.17 0.63%7.15471 1553.9461 225.23 11.65 0.07 0.12%0.48%X X
100-41-4 ethylbenzene 1.75%106.17 0.63%7.1561 1559.5452 228.582 13.33 0.08 0.14%0.54%X X
64-17-5 ethanol 0.55%46.07 0.45%8.12875 1660.8713 238.131 86.00 0.39 0.66%1.10%X50-00-0 formaldehyde 0.55%30.03 0.70%7.46432 1078.39 254.377 4701.17 32.70 55.74%60.30%X X
39464-64-7 polyoxyethylene dinonyphenyl ether phosphate0.10%200 0.02%1.00 0.00 0.00%0.00%X
68891-21-4 surfactant 0.10%200 0.02%1.00 0.00 0.00%0.00%X
7732-18-5 water 35.20%18.01 74.22%8.05573 1723.6425 233.08 31.91 23.69 40.37%26.20%73.80%64.25%
Total Vapor Pressure 108.1 mmHg
2.1 psiLiquid molecular weight 47.5
Vapor molecular weight 41.7
A B C
123-86-4 n-butyl acetate 17.50%116.16 7.16%7.24491 1518.3865 222.077 16.65 1.19 1.10%3.07%X
67-64-1 acetone 17.50%58.08 14.32%7.2996 1312.253 240.705 283.16 40.56 37.51%52.27%
13463-67-7 titanium dioxide 17.50%79.86 10.42%0 0.00 0.00%0.00%
64-17-5 ethanol 6.25%46.07 6.45%8.12875 1660.8713 238.131 86.00 5.55 5.13%5.67%X
9004-70-05 cellulose nitrate, cellulose ester 6.25%1044.57 0.28%1.00 0.00 0.00%0.07%X
71-36-3 butanol 6.25%74.12 4.01%7.3013 1285.0227 173.247 9.52 0.38 0.35%0.63%X
67-63-0 isopropanol 6.25%60.11 4.94%7.82517 1482.1331 217.413 68.34 3.38 3.12%4.50%X111-76-2 butyl cellosolve 1.75%118.18 0.70%7.96174 1928.1455 208.437 0.75 0.01 0.00%0.01%X
1623-15-0 butyl dihydrogen phosphate 0.55%154.1 0.17%0.00 0.00 0.00%0.00%
50-00-0 formaldehyde 0.55%30.03 0.87%7.46432 1078.39 254.377 4701.17 40.93 37.86%27.27%X X
100-41-4 ethylbenzene 0.55%106.17 0.25%7.1561 1559.5452 228.582 13.33 0.03 0.03%0.08%X X
7732-18-5 water 19.10%18.01 50.42%8.05573 1723.6425 233.08 31.91 16.09 14.88%6.43%
41.30%27.35%
Total Vapor Pressure 110.1 mmHg
2.1 psiLiquid molecular weight 48.7
Vapor molecular weight 41.8
A B C
123-86-4 n-butyl acetate 17.50%116.16 7.34%7.24491 1518.3865 222.077 16.65 1.22 1.11%3.08%X
67-64-1 acetone 17.50%58.08 14.69%7.2996 1312.253 240.705 283.16 41.59 37.76%52.41%
13463-67-7 titanium dioxide 17.50%79.86 10.68%0 0.00 0.00%0.00%64-17-5 ethanol 6.25%46.07 6.61%8.12875 1660.8713 238.131 86.00 5.69 5.16%5.68%X
9004-70-05 cellulose nitrate, cellulose ester 6.25%1044.57 0.29%1.00 0.00 0.00%0.07%X
71-36-3 butanol 6.25%74.12 4.11%7.3013 1285.0227 173.247 9.52 0.39 0.36%0.63%X
67-63-0 isopropanol 6.25%60.11 5.07%7.82517 1482.1331 217.413 68.34 3.46 3.14%4.52%X111-76-2 butyl cellosolve 1.75%118.18 0.72%7.96174 1928.1455 208.437 0.75 0.01 0.00%0.01%X
64742-47-8 aliphatic petroleum distillates 0.55%200 0.13%7.79056 2225.63 257.923 1.15 0.00 0.00%0.01%X
1623-15-0 butyl dihydrogen phosphate 0.55%154.1 0.17%0.00 0.00 0.00%0.00%
50-00-0 formaldehyde 0.55%30.03 0.89%7.46432 1078.39 254.377 4701.17 41.97 38.11%27.35%X X100-41-4 ethylbenzene 0.55%106.17 0.25%7.1561 1559.5452 228.582 13.33 0.03 0.03%0.08%X X12236-62-3 pigment orange 36 0.10%416.78 0.01%0.00 0.00 0.00%0.00%
39464-64-7 polyoxyethylene dinonyphenyl ether phosphate0.10%200 0.02%1.00 0.00 0.00%0.00%X
68891-21-4 surfactant 0.10%200 0.02%1.00 0.00 0.00%0.00%X
68412-53-3 alkyl phenol phosphate ester 0.10%933.4 0.01%1.00 0.00 0.00%0.00%X
7732-18-5 water 18.25%18.01 49.39%8.05573 1723.6425 233.08 31.91 15.76 14.31%6.16%
41.43%27.43%
Solid
Solid
Solid
Vapor
wt.%VOC HAP
Total:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Solid
Solid
Total:
Solid
Product chemical data for SW7004 SNOWBOUND 10SH - L42CW01679 mixture components:
Total:
Product chemical data for DIMENSIONAL WHITE 10SH - L42CW02023 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC HAP
Product chemical data for MS ULTRA WHITE CV - E29CW01410+K mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC HAP
Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor wt.%VOC HAP
Total:
Solid
FinishWorks - Salt Lake City, UT
Material Evaluation
a. The true vapor pressure of each material is evaluated using Antoine coefficients for each individual component and Raoult's law. The vapor pressure is estimated using ambient temperature as the materials are not heated during the tinting, blending, or repackaging process.
Highest Production Materials
Product chemical data for SW7103 WHITETAIL 20SH CV - E29CW02174+K mixture components:
CAS no.Component Liquid wt.%Molecularweight
xi, liquid
mole
Antoine Coefficients1
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 3 Material Evaluation
February 2025
Total Vapor Pressure 28.9 mmHg
0.6 psi
Liquid molecular weight 43.0
Vapor molecular weight 44.4
A B C
123-86-4 n-butyl acetate 17.50%116.16 6.48%7.24491 1518.3865 222.077 16.65 1.08 3.73%9.75%X
108-65-6 pm acetate 6.25%132.16 2.03%1.00 0.02 0.07%0.21%X141-78-6 ethyl acetate 6.25%88.11 3.05%7.2601 1338.5652 228.608 121.36 3.70 12.79%25.38%X
9004-70-05 cellulose nitrate, cellulose ester 6.25%1044.57 0.26%1.00 0.00 0.01%0.21%X
64-17-5 ethanol 6.25%46.07 5.83%8.12875 1660.8713 238.131 86.00 5.01 17.34%17.98%X
108-88-3 toluene 6.25%92.14 2.92%7.1366 1457.287 231.827 37.22 1.09 3.75%7.78%X X71-36-3 butanol 6.25%74.12 3.62%7.3013 1285.0227 173.247 9.52 0.35 1.19%1.99%X
1333-86-4 carbon black 6.25%12.011 22.37%0 0.00 0.00%0.00%
67-63-0 isopropanol 6.25%60.11 4.47%7.82517 1482.1331 217.413 68.34 3.05 10.56%14.29%X
64742-47-8 aliphatic petroleum distillates 6.25%200 1.34%7.79056 2225.63 257.923 1.15 0.02 0.05%0.24%X108-38-3 m-xylene 1.75%106.17 0.71%7.18115 1573.0243 226.671 11.29 0.08 0.28%0.66%X X
78-83-12 isobutanol 1.75%74.12 1.01%7.16115 1164.4309 164.392 14.83 0.15 0.52%0.87%X
64742-48-9 petroleum distillate 1.75%200 0.38%7.79056 2225.63 257.923 1.15 0.00 0.01%0.07%X
100-41-4 ethylbenzene 0.55%106.17 0.22%7.1561 1559.5452 228.582 13.33 0.03 0.10%0.25%X X106-42-3 p-xylene 0.55%106.17 0.22%7.15471 1553.9461 225.23 11.65 0.03 0.09%0.21%X X
64742-82-1 petroleum distillates 0.55%200 0.12%7.79056 2225.63 257.923 1.15 0.00 0.00%0.02%X
8052-41-3 aliphatic hydrocarbons 0.55%223.11 0.11%7.79056 2225.63 257.923 1.15 0.00 0.00%0.02%X
7732-18-5 water 18.80%18.01 44.87%8.05573 1723.6425 233.08 31.91 14.32 49.50%20.07%79.93%8.90%
Total Vapor Pressure 11.9 mmHg
0.2 psiLiquid molecular weight 84.1
Vapor molecular weight 39.4
A B C
64742-48-9 petroleum distillate 65.00%200 13.97%7.79056 2225.63 257.923 1.15 0.16 1.35%6.86%X
111-76-2 butyl cellosolve 6.25%118.18 2.27%7.96174 1928.1455 208.437 0.75 0.02 0.14%0.43%X
64-17-5 ethanol 6.25%46.07 5.83%8.12875 1660.8713 238.131 86.00 5.01 42.23%49.32%X
108-38-3 m-xylene 6.25%106.17 2.53%7.18115 1573.0243 226.671 11.29 0.29 2.41%6.47%X X1333-86-4 carbon black 1.75%12.011 6.26%0 0.00 0.00%0.00%
95-47-6 o-xylene 1.75%106.17 0.71%7.8126 1901.373 246.882 8.82 0.06 0.53%1.42%X X
106-42-3 p-xylene 1.75%106.17 0.71%7.15471 1553.9461 225.23 11.65 0.08 0.70%1.87%X X
67-63-0 isopropanol 1.75%60.11 1.25%7.82517 1482.1331 217.413 68.34 0.86 7.20%10.97%X100-41-4 ethylbenzene 1.75%106.17 0.71%7.1561 1559.5452 228.582 13.33 0.09 0.80%2.14%X X
96-29-7 methyl ethyl ketoxime 0.55%87.12 0.27%7.58369 1716.2122 212.378 3.18 0.01 0.07%0.16%X
7732-18-5 water 6.95%18.01 16.59%8.05573 1723.6425 233.08 31.91 5.29 44.58%20.35%
79.65%11.90%
Total Vapor Pressure 28.8 mmHg
0.6 psi
Liquid molecular weight 44.1Vapor molecular weight 45.3
A B C123-86-4 n-butyl acetate 17.50%116.16 6.65%7.24491 1518.3865 222.077 16.65 1.11 3.85%9.87%X
108-65-6 pm acetate 6.25%132.16 2.09%1.00 0.02 0.07%0.21%X
141-78-6 ethyl acetate 6.25%88.11 3.13%7.2601 1338.5652 228.608 121.36 3.80 13.21%25.70%X
9004-70-05 cellulose nitrate, cellulose ester 6.25%1044.57 0.26%1.00 0.00 0.01%0.21%X
64-17-5 ethanol 6.25%46.07 5.99%8.12875 1660.8713 238.131 86.00 5.15 17.90%18.21%X
108-88-3 toluene 6.25%92.14 2.99%7.1366 1457.287 231.827 37.22 1.11 3.87%7.88%X X
71-36-3 butanol 6.25%74.12 3.72%7.3013 1285.0227 173.247 9.52 0.35 1.23%2.02%X
1333-86-4 carbon black 6.25%12.011 22.96%0 0.00 0.00%0.00%64742-47-8 aliphatic petroleum distillates 6.25%200 1.38%7.79056 2225.63 257.923 1.15 0.02 0.06%0.24%X
67-63-0 isopropanol 6.25%60.11 4.59%7.82517 1482.1331 217.413 68.34 3.14 10.90%14.47%X
78-83-12 isobutanol 1.75%74.12 1.04%7.16115 1164.4309 164.392 14.83 0.15 0.54%0.88%X
108-38-3 m-xylene 1.75%106.17 0.73%7.18115 1573.0243 226.671 11.29 0.08 0.29%0.67%X X64742-48-9 petroleum distillate 1.75%200 0.39%7.79056 2225.63 257.923 1.15 0.00 0.02%0.07%X
106-42-3 p-xylene 0.55%106.17 0.23%7.15471 1553.9461 225.23 11.65 0.03 0.09%0.22%X X
100-41-4 ethylbenzene 0.55%106.17 0.23%7.1561 1559.5452 228.582 13.33 0.03 0.11%0.25%X X
39464-64-7 polyoxyethylene dinonyphenyl ether phosphate0.55%200 0.12%1.00 0.00 0.00%0.02%X68891-21-4 surfactant 0.55%200 0.12%1.00 0.00 0.00%0.02%X
64742-82-1 petroleum distillates 0.55%200 0.12%7.79056 2225.63 257.923 1.15 0.00 0.00%0.02%X
8052-41-3 aliphatic hydrocarbons 0.55%223.11 0.11%7.79056 2225.63 257.923 1.15 0.00 0.00%0.02%X
1623-15-0 butyl dihydrogen phosphate 0.10%154.1 0.03%0.00 0.00 0.00%0.00%7732-18-5 water 17.60%18.01 43.12%8.05573 1723.6425 233.08 31.91 13.76 47.85%19.03%
80.97%9.01%
Total Vapor Pressure 31.9 mmHg
0.6 psi
Liquid molecular weight 55.0
Vapor molecular weight 35.7
A B C
64742-48-9 petroleum distillate 32.50%200 8.94%7.79056 2225.63 257.923 1.15 0.10 0.32%1.81%X
111-76-2 butyl cellosolve 17.50%118.18 8.15%7.96174 1928.1455 208.437 0.75 0.06 0.19%0.64%X
123-86-4 n-butyl acetate 6.25%116.16 2.96%7.24491 1518.3865 222.077 16.65 0.49 1.55%5.04%X78-93-3 methyl ethyl ketone (MEK)6.25%72.11 4.77%7.1913 1323.0708 227.093 110.92 5.29 16.60%33.56%X
64-17-5 ethanol 6.25%46.07 7.46%8.12875 1660.8713 238.131 86.00 6.42 20.14%26.02%X
64742-95-6 aromatic hydrocarbons 1.75%200 0.48%7.79056 2225.63 257.923 1.15 0.01 0.02%0.10%X
64742-47-8 aliphatic petroleum distillates 1.75%200 0.48%7.79056 2225.63 257.923 1.15 0.01 0.02%0.10%X108-38-3 m-xylene 1.75%106.17 0.91%7.18115 1573.0243 226.671 11.29 0.10 0.32%0.96%X X
52125-53-8 propylene glycol monoethyl ether 1.75%104.15 0.92%11.2399 2832.6194 208.564 0.23 0.00 0.01%0.02%X
95-63-6 1,2,4-trimethylbenzene 1.75%120.19 0.80%7.29329 1763.3511 230.248 3.29 0.03 0.08%0.28%X
106-42-3 p-xylene 0.55%106.17 0.28%7.15471 1553.9461 225.23 11.65 0.03 0.10%0.31%X X100-41-4 ethylbenzene 0.55%106.17 0.28%7.1561 1559.5452 228.582 13.33 0.04 0.12%0.36%X X
13463-67-7 titanium dioxide 0.55%79.86 0.38%0.00 0.00 0.00%0.00%
107-98-2 propylene glycol monoethyl ether 0.55%90.12 0.34%8.0526 1764.7387 222.677 11.71 0.04 0.12%0.31%X
1333-86-4 carbon black 0.55%12.011 2.52%0.00 0.00 0.00%0.00%70851-34-2 cobalt compound 0.10%522.58 0.01%0.00 0.00 0.00%0.00%
7732-18-5 water 19.75%18.01 60.32%8.05573 1723.6425 233.08 31.91 19.25 60.41%30.51%
69.49%1.62%Total:
Solid
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC HAP
Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC HAP
Total:
Vapor
wt.%VOC HAP
Solid
Vapor
wt.%VOC HAP
Solid
Total:
Product chemical data for EBONY W/S - D22K00333 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole Antoine Coefficients1
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Pi,
component
pi, partial
pressure of
yi, vapor
mole
Product chemical data for BLACK 20SH PRECAT - L42K00293 mixture components:
Solid
Solid
Solid
Solid
Product chemical data for SW6258 TRICORN BLACK 20SH - L42K00267 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole Antoine Coefficients1
Total:
Product chemical data for ELKO TEMPLE W/S - D22N11505 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 4 Material Evaluation
February 2025
Total Vapor Pressure 108.9 mmHg
2.1 psi
Liquid molecular weight 48.0
Vapor molecular weight 41.8
A B C123-86-4 n-butyl acetate 17.50%116.16 7.23%7.24491 1518.3865 222.077 16.65 1.20 1.11%3.08%X67-64-1 acetone 17.50%58.08 14.47%7.2996 1312.253 240.705 283.16 40.97 37.63%52.34%
13463-67-7 titanium dioxide 17.50%79.86 10.52%0 0.00 0.00%0.00%
64-17-5 ethanol 6.25%46.07 6.51%8.12875 1660.8713 238.131 86.00 5.60 5.15%5.68%X
9004-70-05 cellulose nitrate, cellulose ester 6.25%1044.57 0.29%1.00 0.00 0.00%0.07%X
71-36-3 butanol 6.25%74.12 4.05%7.3013 1285.0227 173.247 9.52 0.39 0.35%0.63%X
67-63-0 isopropanol 6.25%60.11 4.99%7.82517 1482.1331 217.413 68.34 3.41 3.13%4.51%X
111-76-2 butyl cellosolve 1.75%118.18 0.71%7.96174 1928.1455 208.437 0.75 0.01 0.00%0.01%X
1623-15-0 butyl dihydrogen phosphate 0.55%154.1 0.17%0.00 0.00 0.00%0.00%50-00-0 formaldehyde 0.55%30.03 0.88%7.46432 1078.39 254.377 4701.17 41.34 37.98%27.31%X X
100-41-4 ethylbenzene 0.55%106.17 0.25%7.1561 1559.5452 228.582 13.33 0.03 0.03%0.08%X X
12236-62-3 pigment orange 36 0.10%416.78 0.01%0.00 0.00 0.00%0.00%
39464-64-7 polyoxyethylene dinonyphenyl ether phosphate0.10%200 0.02%1.00 0.00 0.00%0.00%X68891-21-4 surfactant 0.10%200 0.02%1.00 0.00 0.00%0.00%X
68412-53-3 alkyl phenol phosphate ester 0.10%933.4 0.01%1.00 0.00 0.00%0.00%X
7732-18-5 water 18.70%18.01 49.86%8.05573 1723.6425 233.08 31.91 15.91 14.61%6.30%
41.36%27.39%
Total Vapor Pressure 21.2 mmHg
0.4 psi
Liquid molecular weight 115.9
Vapor molecular weight 55.6
A B C64742-48-9 petroleum distillate 57.34%200 33.24%7.79056 2225.63 257.923 1.15 0.38 1.80%6.49%X111-76-2 butyl cellosolve 7.65%118.18 7.50%7.96174 1928.1455 208.437 0.75 0.06 0.27%0.56%X
64-17-5 ethanol 7.65%46.07 19.24%8.12875 1660.8713 238.131 86.00 16.55 78.02%64.71%X
108-38-3 m-xylene 7.65%106.17 8.35%7.18115 1573.0243 226.671 11.29 0.94 4.44%8.49%X X
13463-67-7 titanium dioxide 7.65%79.86 11.10%0.00 0.00 0.00%0.00%108-65-6 pm acetate 1.91%132.16 1.68%1.00 0.02 0.08%0.19%X
95-47-6 o-xylene 1.91%106.17 2.09%7.8126 1901.373 246.882 8.82 0.18 0.87%1.66%X X
106-42-3 p-xylene 1.91%106.17 2.09%7.15471 1553.9461 225.23 11.65 0.24 1.15%2.19%X X
67-63-0 isopropanol 1.91%60.11 3.69%7.82517 1482.1331 217.413 68.34 2.52 11.88%12.85%X100-41-4 ethylbenzene 1.91%106.17 2.09%7.1561 1559.5452 228.582 13.33 0.28 1.31%2.51%X X
64742-47-8 aliphatic petroleum distillates 0.76%200 0.44%7.79056 2225.63 257.923 1.15 0.01 0.02%0.09%X
1333-86-4 carbon black 0.76%12.011 7.38%0.00 0.00 0.00%0.00%
96-29-7 methyl ethyl ketoxime 0.76%87.12 1.02%7.58369 1716.2122 212.378 3.18 0.03 0.15%0.24%X39464-64-7 polyoxyethylene dinonyphenyl ether phosphate0.08%200 0.04%1.00 0.00 0.00%0.01%X
68412-53-3 alkyl phenol phosphate ester 0.08%933.4 0.01%1.00 0.00 0.00%0.01%X
68891-21-4 surfactant 0.08%200 0.04%1.00 0.00 0.00%0.01%X
100.00%14.85%
Total Vapor Pressure 283.2 mmHg5.5 psi
Liquid molecular weight 58.1
Vapor molecular weight 58.1
A B C
67-64-1 acetone 100.00%58.08 100.00%7.2996 1312.253 240.705 283.16 283.16 100.00%100.00%
0.00%0.00%
Total:
Total:
Product chemical data for FC-47871 GRAY FLANNEL - D22N06983 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC HAP
Product chemical data for BM WHITE DOVE 20 SH PRECAT - L42CW00787 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC
Total:
Cleaning Solvent
Product chemical data for Solvent - T84C0033 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC HAP
Solid
Solid
Solid
Solid
HAP
Solid
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 5 Material Evaluation
February 2025
Basis
a. The coating booth is
occasionally used to spray
- one production/color lab booth
b. The maximum volume sprayed onto the test material for each product QC test is:40 mL/spray
c. The coating overspray is conservatively assumed to be 50%for calculating PM emissions (percent of coating solids not applied to the test material).
One QC test is conducted for each material packaged in the tinting, repackaging, and blending line. The maximum number of containers packaged in a shift are:
Container Size (gal)Containers
mixed in a shift
Containers
mixed in a day
0.25 7 21
1 10 30
5 20 60
55 0 0
111 total sprays per 24 hours
To estimate worst case sprays per day, a safety factor of 1.25 was used to obtain maximum total sprays of 139 per day.
Max Daily Coating Usage per production area QC booth =40 mL/spray x 248 sprays/day / 3,785 mL/gal
Max Daily Coating Usage per production area QC booth =1.5 gal/day
Actual Daily Coating Usage per production area QC booth =0.4 gal/day
Max Daily Cleaning Solvent Usage:1.5 gal/day Actual 0.4 gal/day
toluene xylene ethylbenzene formaldehyde
E29CW02174+K 9.36 17.50%47.30%16.55%14.25%1.75%0.55%
E29CW01410+K 9.36 17.50%47.30%16.55%14.25%1.75%0.55%
L42CW02023 8.56 18.05%62.85%1.10%0.55%0.55%
L42CW01679 8.86 18.15%63.70%1.10%0.55%0.55%
L42K00293 8.05 6.25%74.95%9.10%6.25%2.30%0.55%
D22K00333 7.03 1.75%91.30%11.50%9.75%1.75%
L42K00267 8.01 6.35%76.05%9.10%6.25%2.30%0.55%
D22N11505 7.37 1.20%79.15%2.85%2.30%0.55%
L42CW00787 8.48 18.15%63.15%1.10%0.55%0.55%
D22N06983 7.15 8.41%91.59%13.38%11.47%1.91%
T84C0033 6.66 0.00%0.00%0.00%
g. Potential emissions are based on operating:24 hr/day Actual emissions are based on operating: 8 hr/day
7 day/week 5 day/week
365 day/yr 52 week/yr
8,760 hr/yr 2,080 hr/yr
Emission Calculations:
PM Coating emissions (lb/day)=(coating usage, gal/day) x (% overspray) x (coating density, lb/gal) x (solids content, %)
VOC Coating emissions (lb/day)=(coating usage, gal/day) x (coating density, lb/gal) x (VOC content, %)
VOC Cleaning Solvent emission (lb/day)=(cleaning solvent usage, gal/day) x (cleaning solvent density, lb/gal) x (VOC content, %)
HAP Coating emissions (lb/day)=(coating usage, gal/day) x (coating density, lb/gal) x (HAP content, %)
Potential VOC emissions (ton/yr)=(total VOC emissions, lb/day) x (365 day/yr) / (2000, lb/ton)
Emissions:
2023 Actual
Emissions
(Production
Booth)
lb/hr ton/yr ton/yr
PM 0.05 0.22 0.04
VOC 0.37 1.63 0.33
Total HAP 0.09 0.42 0.08
toluene 0.03 0.13 0.03
xylene 0.08 0.36 0.07
ethylbenzene 0.01 0.04 0.01
formaldehyde 0.003 0.01 1E-02
Code Density
(lb/gal)
VOC
(liquid wt%)
Total HAP
(liquid
wt%)
Solids (liquid
wt%)
e. It is assumed that 100% of the organics contained in the products and cleaning solvent used in the coating booth are captured by the coating booth exhaust system and exit the
stacks as air emissions. Potential emissions are calculated assuming maximum annual operation of 8,760 hr/yr.
f. The products with the highest processing rate were used to evaluate the worst case uncontrolled potential emissions for the facility. The products evaluated are listed below. (The
green highlight indicates the cleaning solvent. The red highlights indicate the products with the highest overall VOC content, highest total HAP content, and the highest individual HAPs.)
FinishWorks - Salt Lake City, UT
Air Emissions - Coating Booths
Pollutant
Uncontrolled Potential
Emissions
(Production Booth)
HAP %
d. The booth spray guns are assumed to be cleaned after each use with the solvent Acetone. It is assumed the same quantity of cleaning solvent is used as coating.
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 6 Coating Booths
February 2025
Basis
LL =12.46 * (SPM/T)
Where:
LL =loading loss, lb/1,000 gal liquid loaded
S =saturation factor (see Table 5.2-1)
P =true vapor pressure of material, psia
M =molecular weight of vapors, lb/lb-mol
T =temperature of material (at ambient conditions), ◦R
S =1.45 (splash loading: dedicated normal service)
T =30 °C
Code True Vapor
Pressure (psia)
Vapor Molecular
Weight
(lb/lb-mol)
Total VOC Total HAP toluene xylene ethylbenzene formaldehyde
E29CW02174+K 1.13 27.76 73.80%64.25%3.41%0.54%60.30%
E29CW01410+K 1.13 27.76 73.80%64.25%3.41%0.54%60.30%
L42CW02023 2.09 41.69 41.30%27.35%0.08%27.27%
L42CW01679 2.13 41.85 41.43%27.43%0.08%27.35%
L42K00293 0.56 44.41 79.93%8.90%7.78%0.88%0.25%
D22K00333 0.23 39.45 79.65%11.90%9.76%2.14%
L42K00267 0.56 45.29 80.97%9.01%7.88%0.89%0.25%
D22N11505 0.62 35.66 69.49%1.62%1.27%0.36%
L42CW00787 2.11 41.76 41.36%27.39%
D22N06983 0.41 55.55 100.00%14.85%12.34%2.51%
Emission Calculations
c. Tinting, Blending, and Repackaging
Loading Loss, LL (lb/1,000 gal)= 12.46 x 1.45 x (true vapor pressure, psia) x (vapor molecular weight, lb/lb-mol) / (temperature, °R)
Total Emissions (lb/yr)= (Loading Loss, lb/1,000 gal) x [(Production, gal/yr)/1,000]
Stack Emissions (lb glycol ether/yr)= (total emissions, lb/yr) x (vapor wt %)
Stack Emissions (lb/hr)= (total emissions, lb/yr) / (8760, hr/yr)
d. Actual production is based on one 8-hour shift/day. Potential production is based on three, 8-hour shifts/day.
e. The 2023 throughput capacity based on one shift/day is:9,695 gal/yr.The throughput capacity based on three shifts/day would be:29,085 gal/yr.
To estimate worst case throughput, a safety factor of 1.25 was used to obtain maximum throughput of 36,356 gal/yr.
VOC Total HAP toluene xylene ethylbenzene formaldehyde
E29A04201+K 1.04 37.91 27.98 24.36 0 1.29 0.21 22.86
E29B02326+K 1.04 37.91 27.98 24.36 0 1.29 0.21 22.86
E29CW05494+K 2.89 104.94 43.35 28.70 0 0.00 0.08 28.62
L41K00005A 2.95 107.30 44.45 29.43 0.00 0 0 29
B10A00546A 0.82 29.91 23.91 2.66 2.33 0 0 0
B10A00548A 0.30 10.91 8.69 1.30 0.00 1 0 0B10K00068A0.83 30.33 24.56 3 2 0 0 0
S75A00114 0.73 26.46 18.38 0.43 0 0 0 0
S75N2262A 2.91 105.86 43.78 29 0 0 0 0
S75N02880A 0.75 27.43 27.43 4.07 0 3 1 0
VOC Total HAP toluene xylene ethylbenzene formaldehyde
E29A04201+K 1.04 10.11 7.46 6.50 0 0.34 0.06 6.10
E29B02326+K 1.04 10.11 7.46 6.50 0 0.34 0.06 6.10
E29CW05494+K 2.89 27.99 11.56 7.65 0 0.00 0.02 7.63
L41K00005A 2.95 28.61 11.85 7.85 0.00 0 0 8
B10A00546A 0.82 7.98 6.38 0.71 0.62 0 0 0
B10A00548A 0.30 2.91 2.32 0.35 0.00 0 0 0
B10K00068A 0.83 8.09 6.55 1 1 0 0 0
S75A00114 0.73 7.05 4.90 0.11 0 0 0 0
S75N2262A 2.91 28.23 11.68 8 0 0 0 0
S75N02880A 0.75 7.32 7.32 1.09 0 1 0 0
Emission Summary:
lb/hr lb/yr ton/yr lb/hr lb/yr ton/yrVOC0.01 44.45 0.0 0.01 11.85 0.01
Total HAP 0.00 29.43 1E-02 4E-03 7.85 4E-03
toluene 2.7E-04 2.39 1E-03 3E-04 0.64 3E-04xylene 3.9E-04 3.39 2E-03 4E-04 0.90 5E-04
ethylbenzene 7.9E-05 0.69 3E-04 8E-05 0.18 9E-05
formaldehyde 0.00 29.34 1E-02 4E-03 7.83 4E-03
a. During the blending, tinting, and repackaging activities, material evaporates and exits the facility via the vapor extraction hoods and associated stacks. AP-42 Section 5.2, Transportation and Marketing of Petroleum Liquids, provides an equation for calculating emissions from loading petroleum liquid, equation 5.2(1), which is used to represent emissions from the FinishWorks operations.
Air Emissions - Tinting, Blending, & Repackaging
FinishWorks - Salt Lake City, UT
Maximum Potential Production
EBONY W/S
b. The products with the highest processing rate and highest HAP content were used to evaluate the worst case potential emissions for the facility. The products evaluated are listed below.
Uncontrolled Potential Emissions (lb/yr)
Code Total Emissions
(lb/yr)
Loading Loss,
LL
(lb/1,000 gal)
Vapor Composition (wt%)
Product
Pollutant
Code Total Emissions
(lb/yr)
Uncontrolled Potential Emissions
Loading Loss,
LL
(lb/1,000 gal)
2023 Actual Production
36,356
(gal/yr)
(gal/yr)
9,695
Actual Emissions
2023 Actual Emissions (lb/yr)
SW6258 TRICORN BLACK 20SH
ELKO TEMPLE W/S
BM WHITE DOVE 20SH PRECAT
FC-47871 GRAY FLANNEL
SW7103 WHITETAIL 20SH CV
MS ULTRA WHITE CV
DIMENSIONAL WHITE 10SH
SW7004 SNOWBOUND 10SH
BLACK 20SH PRECAT
FinishWorks - Salt Lake City, UTAir Emissions Calculations 7 Tinting, Blending, RepackagingFebruary 2025
Basis:
a. There are 3 heaters maintained in the Salt Lake City facility all used as space or air makeup heaters.
Burner Rating
(MMBtu/hr)
Heater 1 Reznor FT200 NG 0.20
Heater 2 Reznor FT200 NG 0.20
Heater 3 Reznor FT200 NG 0.20
Total MMBtu/hr:0.60
b. The emission units are heated with natural gas. The heat content of natural gas is: 1,020 Btu/scf
c. Potential emissions are based on operating:Actual emissions are based on operating:
24 hr/day 24 hr/day
7 day/week 7 day/week
365 day/yr 26 week/yr
8,760 hr/yr 4,368 hr/yr
d. Natural gas combustion emissions are based on the following emission factors from AP-42 Section 1.4
Emission Calculations:
Emission Factors (lb/MMBtu)= (Emission factor, lb/106 scf) / (Heat content of natural gas, 1020 Btu/scf)
Hourly Emissions (lb/hr)= (Emission factor, lb/MMBtu) x (Total heat rating, MMBtu/hr)
Annual Emissions (ton/yr)= (Hourly emissions, lb/hr) x (Annual hours of operation, hr/yr) / (2000 lb/ton)
lb/hr ton/yr lb/hr ton/yr
NOx 100 9.8E-02 5.9E-02 2.6E-01 5.9E-02 1.3E-01
CO 84 8.2E-02 4.9E-02 2.2E-01 4.9E-02 1.1E-01
SO2 0.6 5.9E-04 3.5E-04 1.5E-03 3.5E-04 7.7E-04
VOC 5.5 5.4E-03 3.2E-03 1.4E-02 3.2E-03 7.1E-03
PM 7.6 7.5E-03 4.5E-03 2.0E-02 4.5E-03 9.8E-03
PM2.5 7.6 7.5E-03 4.5E-03 2.0E-02 4.5E-03 9.8E-03
PM10 7.6 7.5E-03 4.5E-03 2.0E-02 4.5E-03 9.8E-03
HAPs
lead 5.0E-04 4.9E-07 2.9E-07 1.3E-06 2.9E-07 6.4E-07
2-methylnaphthalene 2.4E-05 2.4E-08 1.4E-08 6.2E-08 1.4E-08 3.1E-08
3-methylcholanthrene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
7,12- dimethylbenz(a)anthracene 1.6E-05 1.6E-08 9.4E-09 4.1E-08 9.4E-09 2.1E-08
acenaphthene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
acenaphthylene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
anthracene 2.4E-06 2.4E-09 1.4E-09 6.2E-09 1.4E-09 3.1E-09
benz(a)anthracene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
benzene 2.1E-03 2.1E-06 1.2E-06 5.4E-06 1.2E-06 2.7E-06
benzo(a)pyrene 1.2E-06 1.2E-09 7.1E-10 3.1E-09 7.1E-10 1.5E-09
benzo(b)fluoranthene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
benzo(g,h,i)perylene 1.2E-06 1.2E-09 7.1E-10 3.1E-09 7.1E-10 1.5E-09
benzo(k)fluoranthene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
chrysene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
dibenzo(a,h)anthracene 1.2E-06 1.2E-09 7.1E-10 3.1E-09 7.1E-10 1.5E-09
dichlorobenzene 1.2E-03 1.2E-06 7.1E-07 3.1E-06 7.1E-07 1.5E-06
fluoranthene 3.0E-06 2.9E-09 1.8E-09 7.7E-09 1.8E-09 3.9E-09
fluorene 2.8E-06 2.7E-09 1.6E-09 7.2E-09 1.6E-09 3.6E-09
formaldehyde 7.5E-02 7.4E-05 4.4E-05 1.9E-04 4.4E-05 9.6E-05
hexane 1.8E+00 1.8E-03 1.1E-03 4.6E-03 1.1E-03 2.3E-03
indeno(1,2,3-cd)pyrene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
naphthalene 6.1E-04 6.0E-07 3.6E-07 1.6E-06 3.6E-07 7.8E-07
phenanathrene 1.7E-05 1.7E-08 1.0E-08 4.4E-08 1.0E-08 2.2E-08
pyrene 5.0E-06 4.9E-09 2.9E-09 1.3E-08 2.9E-09 6.4E-09
toluene 3.4E-03 3.3E-06 2.0E-06 8.8E-06 2.0E-06 4.4E-06
arsenic 2.0E-04 2.0E-07 1.2E-07 5.2E-07 1.2E-07 2.6E-07
beryllium 1.2E-05 1.2E-08 7.1E-09 3.1E-08 7.1E-09 1.5E-08
cadmium 1.1E-03 1.1E-06 6.5E-07 2.8E-06 6.5E-07 1.4E-06
chromium 1.4E-03 1.4E-06 8.2E-07 3.6E-06 8.2E-07 1.8E-06
cobalt 8.4E-05 8.2E-08 4.9E-08 2.2E-07 4.9E-08 1.1E-07
manganese 3.8E-04 3.7E-07 2.2E-07 9.8E-07 2.2E-07 4.9E-07
mercury 2.6E-04 2.5E-07 1.5E-07 6.7E-07 1.5E-07 3.3E-07
nickel 2.1E-03 2.1E-06 1.2E-06 5.4E-06 1.2E-06 2.7E-06
selenium 2.4E-05 2.4E-08 1.4E-08 6.2E-08 1.4E-08 3.1E-08
Total HAP 1.89 1.9E-03 1.1E-03 4.9E-03 1.1E-03 2.4E-03
FinishWorks - Salt Lake City, UT
Natural Gas Fired Heaters
Facility ID
Uncontrolled Potential Emissions
Make Model Fuel Type
Controlled Actual EmissionsPollutantsEmission Factor
(lb/10^6 scf)
Final Emission
Factor (lb/MMBtu)
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 8 Heaters
February 2025
Emission Summary:
Combustion Emissions Coating Booth
Emissions
Blending, Tinting, and
Packaging Emissions
Total Actual
Emissions
ton/yr ton/yr ton/yr ton/yr
PM 1E-02 0.04 0.1
PM10 1E-02 0.04 0.1
SO2 8E-04 8E-04
CO 0.11 0.1
NOx 0.13 0.1
VOC 7E-03 0.33 0.01 0.3
Total HAP 2E-03 0.08 4E-03 0.1
lead 6E-07 6E-07
toluene 4E-06 0.03 3E-04 0.0
xylene 0.07 5E-04 0.1
ethylbenzene 0.01 9E-05 0.01
formaldehyde 1E-04 0.01 4E-03 0.01
MIK 0
2-methylnaphthalene 3E-08 3E-08
3-methylcholanthrene 2E-09 2E-09
7,12- dimethylbenz(a)anthracene 2E-08 2E-08
acenaphthene 2E-09 2E-09
acenaphthylene 2E-09 2E-09
anthracene 3E-09 3E-09
benz(a)anthracene 2E-09 2E-09
benzene 3E-06 3E-06
benzo(a)pyrene 2E-09 2E-09
benzo(b)fluoranthene 2E-09 2E-09
benzo(g,h,i)perylene 2E-09 2E-09
benzo(k)fluoranthene 2E-09 2E-09
chrysene 2E-09 2E-09
dibenzo(a,h)anthracene 2E-09 2E-09
dichlorobenzene 2E-06 2E-06
fluoranthene 4E-09 4E-09
fluorene 4E-09 4E-09
hexane 2E-03 2E-03
indeno(1,2,3-cd)pyrene 2E-09 2E-09
naphthalene 8E-07 8E-07
phenanathrene 2E-08 2E-08
pyrene 6E-09 6E-09
arsenic 3E-07 3E-07
beryllium 2E-08 2E-08
cadmium 1E-06 1E-06
chromium 2E-06 2E-06
cobalt 1E-07 1E-07
manganese 5E-07 5E-07
mercury 3E-07 3E-07
nickel 3E-06 3E-06
selenium 3E-08 3E-08
Pollutant
FinishWorks - Salt Lake City, UT
2023 Actual Air Emissions Summary
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 1
Actual Emissions Summary
February 2025
Emission Summary:
lb/hr ton/yr lb/hr ton/yr lb/hr ton/yr lb/hr ton/yr
PM 4.5E-03 2E-02 0.05 0.2 0.05 0.2
PM10 4.5E-03 2E-02 0.05 0.2 0.05 0.2
SO2 3.5E-04 2E-03 4E-04 2E-03
CO 4.9E-02 2E-01 0.05 0.2
NOx 5.9E-02 3E-01 0.06 0.3
VOC 3.2E-03 1E-02 0.37 1.6 0.01 0.02 0.38 1.7
Total HAP 1.1E-03 5E-03 0.09 0.4 3.4E-03 0.01 0.10 0.4
lead 2.9E-07 1E-06 3E-07 1E-06
toluene 2.0E-06 9E-06 0.03 0.1 2.7E-04 1E-03 0.03 0.1
xylene 0.08 0.4 3.9E-04 2E-03 0.08 0.4
ethylbenzene 0.01 0.0 7.9E-05 3E-04 0.01 0.04
formaldehyde 4.4E-05 2E-04 3.2E-03 1E-02 3.3E-03 0.01 0.01 0.03
MIK 0 0
2-methylnaphthalene 1.4E-08 6E-08 1E-08 6E-08
3-methylcholanthrene 1.1E-09 5E-09 1E-09 5E-09
7,12- dimethylbenz(a)anthracene 9.4E-09 4E-08 9E-09 4E-08
acenaphthene 1.1E-09 5E-09 1E-09 5E-09
acenaphthylene 1.1E-09 5E-09 1E-09 5E-09
anthracene 1.4E-09 6E-09 1E-09 6E-09
benz(a)anthracene 1.1E-09 5E-09 1E-09 5E-09
benzene 1.2E-06 5E-06 1E-06 5E-06
benzo(a)pyrene 7.1E-10 3E-09 7E-10 3E-09
benzo(b)fluoranthene 1.1E-09 5E-09 1E-09 5E-09
benzo(g,h,i)perylene 7.1E-10 3E-09 7E-10 3E-09
benzo(k)fluoranthene 1.1E-09 5E-09 1E-09 5E-09
chrysene 1.1E-09 5E-09 1E-09 5E-09
dibenzo(a,h)anthracene 7.1E-10 3E-09 7E-10 3E-09
dichlorobenzene 7.1E-07 3E-06 7E-07 3E-06
fluoranthene 1.8E-09 8E-09 2E-09 8E-09
fluorene 1.6E-09 7E-09 2E-09 7E-09
hexane 1.1E-03 5E-03 1E-03 5E-03
indeno(1,2,3-cd)pyrene 1.1E-09 5E-09 1E-09 5E-09
naphthalene 3.6E-07 2E-06 4E-07 2E-06
phenanathrene 1.0E-08 4E-08 1E-08 4E-08
pyrene 2.9E-09 1E-08 3E-09 1E-08
arsenic 1.2E-07 5E-07 1E-07 5E-07
beryllium 7.1E-09 3E-08 7E-09 3E-08
cadmium 6.5E-07 3E-06 6E-07 3E-06
chromium 8.2E-07 4E-06 8E-07 4E-06
cobalt 4.9E-08 2E-07 5E-08 2E-07
manganese 2.2E-07 1E-06 2E-07 1E-06
mercury 1.5E-07 7E-07 2E-07 7E-07
nickel 1.2E-06 5E-06 1E-06 5E-06
selenium 1.4E-08 6E-08 1E-08 6E-08
FinishWorks - Salt Lake City, UT
Potential Uncontrolled Air Emissions Summary
Blending, Tinting, and
Packaging Emissions
Total Potential
EmissionsPollutantCombustion Emissions Coating Booth
Emissions
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 2 Potential Emissions Summary
February 2025
Basis
Temperature 30.0 C =86 F
Total Vapor Pressure 58.7 mmHg
1.1 psi
Liquid molecular weight 38.0
Vapor molecular weight 27.8
A B C
123-86-4 n-butyl acetate 17.50%116.16 5.72%7.24491 1518.3865 222.077 16.65 0.95 1.62%6.80%X
13463-67-7 titanium dioxide 17.50%79.86 8.32%0 0.00 0.00%0.00%71-36-3 butanol 6.25%74.12 3.20%7.3013 1285.0227 173.247 9.52 0.30 0.52%1.39%X
108-38-3 m-xylene 6.25%106.17 2.24%7.18115 1573.0243 226.671 11.29 0.25 0.43%1.65%X X
763-69-9 eep 6.25%146.18 1.62%7.3845 1710.719 209.847 1.79 0.03 0.05%0.26%X
95-47-6 o-xylene 6.25%106.17 2.24%7.8126 1901.373 246.882 8.82 0.20 0.34%1.29%X X106-42-3 p-xylene 1.75%106.17 0.63%7.15471 1553.9461 225.23 11.65 0.07 0.12%0.48%X X
100-41-4 ethylbenzene 1.75%106.17 0.63%7.1561 1559.5452 228.582 13.33 0.08 0.14%0.54%X X
64-17-5 ethanol 0.55%46.07 0.45%8.12875 1660.8713 238.131 86.00 0.39 0.66%1.10%X
50-00-0 formaldehyde 0.55%30.03 0.70%7.46432 1078.39 254.377 4701.17 32.70 55.74%60.30%X X39464-64-7 polyoxyethylene dinonyphenyl ether phosphate0.10%200 0.02%1.00 0.00 0.00%0.00%X
68891-21-4 surfactant 0.10%200 0.02%1.00 0.00 0.00%0.00%X
7732-18-5 water 35.20%18.01 74.22%8.05573 1723.6425 233.08 31.91 23.69 40.37%26.20%
73.80%64.25%
Total Vapor Pressure 58.7 mmHg
1.1 psi
Liquid molecular weight 38.0Vapor molecular weight 27.8
A B C123-86-4 n-butyl acetate 17.50%116.16 5.72%7.24491 1518.3865 222.077 16.65 0.95 1.62%6.80%X13463-67-7 titanium dioxide 17.50%79.86 8.32%0 0.00 0.00%0.00%
71-36-3 butanol 6.25%74.12 3.20%7.3013 1285.0227 173.247 9.52 0.30 0.52%1.39%X
108-38-3 m-xylene 6.25%106.17 2.24%7.18115 1573.0243 226.671 11.29 0.25 0.43%1.65%X X
763-69-9 eep 6.25%146.18 1.62%7.3845 1710.719 209.847 1.79 0.03 0.05%0.26%X95-47-6 o-xylene 6.25%106.17 2.24%7.8126 1901.373 246.882 8.82 0.20 0.34%1.29%X X
106-42-3 p-xylene 1.75%106.17 0.63%7.15471 1553.9461 225.23 11.65 0.07 0.12%0.48%X X
100-41-4 ethylbenzene 1.75%106.17 0.63%7.1561 1559.5452 228.582 13.33 0.08 0.14%0.54%X X
64-17-5 ethanol 0.55%46.07 0.45%8.12875 1660.8713 238.131 86.00 0.39 0.66%1.10%X50-00-0 formaldehyde 0.55%30.03 0.70%7.46432 1078.39 254.377 4701.17 32.70 55.74%60.30%X X
39464-64-7 polyoxyethylene dinonyphenyl ether phosphate0.10%200 0.02%1.00 0.00 0.00%0.00%X
68891-21-4 surfactant 0.10%200 0.02%1.00 0.00 0.00%0.00%X
7732-18-5 water 35.20%18.01 74.22%8.05573 1723.6425 233.08 31.91 23.69 40.37%26.20%73.80%64.25%
Total Vapor Pressure 108.1 mmHg
2.1 psiLiquid molecular weight 47.5
Vapor molecular weight 41.7
A B C
123-86-4 n-butyl acetate 17.50%116.16 7.16%7.24491 1518.3865 222.077 16.65 1.19 1.10%3.07%X
67-64-1 acetone 17.50%58.08 14.32%7.2996 1312.253 240.705 283.16 40.56 37.51%52.27%
13463-67-7 titanium dioxide 17.50%79.86 10.42%0 0.00 0.00%0.00%
64-17-5 ethanol 6.25%46.07 6.45%8.12875 1660.8713 238.131 86.00 5.55 5.13%5.67%X
9004-70-05 cellulose nitrate, cellulose ester 6.25%1044.57 0.28%1.00 0.00 0.00%0.07%X
71-36-3 butanol 6.25%74.12 4.01%7.3013 1285.0227 173.247 9.52 0.38 0.35%0.63%X
67-63-0 isopropanol 6.25%60.11 4.94%7.82517 1482.1331 217.413 68.34 3.38 3.12%4.50%X111-76-2 butyl cellosolve 1.75%118.18 0.70%7.96174 1928.1455 208.437 0.75 0.01 0.00%0.01%X
1623-15-0 butyl dihydrogen phosphate 0.55%154.1 0.17%0.00 0.00 0.00%0.00%
50-00-0 formaldehyde 0.55%30.03 0.87%7.46432 1078.39 254.377 4701.17 40.93 37.86%27.27%X X
100-41-4 ethylbenzene 0.55%106.17 0.25%7.1561 1559.5452 228.582 13.33 0.03 0.03%0.08%X X
7732-18-5 water 19.10%18.01 50.42%8.05573 1723.6425 233.08 31.91 16.09 14.88%6.43%
41.30%27.35%
Total Vapor Pressure 110.1 mmHg
2.1 psiLiquid molecular weight 48.7
Vapor molecular weight 41.8
A B C
123-86-4 n-butyl acetate 17.50%116.16 7.34%7.24491 1518.3865 222.077 16.65 1.22 1.11%3.08%X
67-64-1 acetone 17.50%58.08 14.69%7.2996 1312.253 240.705 283.16 41.59 37.76%52.41%
13463-67-7 titanium dioxide 17.50%79.86 10.68%0 0.00 0.00%0.00%64-17-5 ethanol 6.25%46.07 6.61%8.12875 1660.8713 238.131 86.00 5.69 5.16%5.68%X
9004-70-05 cellulose nitrate, cellulose ester 6.25%1044.57 0.29%1.00 0.00 0.00%0.07%X
71-36-3 butanol 6.25%74.12 4.11%7.3013 1285.0227 173.247 9.52 0.39 0.36%0.63%X
67-63-0 isopropanol 6.25%60.11 5.07%7.82517 1482.1331 217.413 68.34 3.46 3.14%4.52%X111-76-2 butyl cellosolve 1.75%118.18 0.72%7.96174 1928.1455 208.437 0.75 0.01 0.00%0.01%X
64742-47-8 aliphatic petroleum distillates 0.55%200 0.13%7.79056 2225.63 257.923 1.15 0.00 0.00%0.01%X
1623-15-0 butyl dihydrogen phosphate 0.55%154.1 0.17%0.00 0.00 0.00%0.00%
50-00-0 formaldehyde 0.55%30.03 0.89%7.46432 1078.39 254.377 4701.17 41.97 38.11%27.35%X X100-41-4 ethylbenzene 0.55%106.17 0.25%7.1561 1559.5452 228.582 13.33 0.03 0.03%0.08%X X12236-62-3 pigment orange 36 0.10%416.78 0.01%0.00 0.00 0.00%0.00%
39464-64-7 polyoxyethylene dinonyphenyl ether phosphate0.10%200 0.02%1.00 0.00 0.00%0.00%X
68891-21-4 surfactant 0.10%200 0.02%1.00 0.00 0.00%0.00%X
68412-53-3 alkyl phenol phosphate ester 0.10%933.4 0.01%1.00 0.00 0.00%0.00%X
7732-18-5 water 18.25%18.01 49.39%8.05573 1723.6425 233.08 31.91 15.76 14.31%6.16%
41.43%27.43%
Solid
Solid
Solid
Vapor
wt.%VOC HAP
Total:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Solid
Solid
Total:
Solid
Product chemical data for SW7004 SNOWBOUND 10SH - L42CW01679 mixture components:
Total:
Product chemical data for DIMENSIONAL WHITE 10SH - L42CW02023 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC HAP
Product chemical data for MS ULTRA WHITE CV - E29CW01410+K mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC HAP
Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor wt.%VOC HAP
Total:
Solid
FinishWorks - Salt Lake City, UT
Material Evaluation
a. The true vapor pressure of each material is evaluated using Antoine coefficients for each individual component and Raoult's law. The vapor pressure is estimated using ambient temperature as the materials are not heated during the tinting, blending, or repackaging process.
Highest Production Materials
Product chemical data for SW7103 WHITETAIL 20SH CV - E29CW02174+K mixture components:
CAS no.Component Liquid wt.%Molecularweight
xi, liquid
mole
Antoine Coefficients1
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 3 Material Evaluation
February 2025
Total Vapor Pressure 28.9 mmHg
0.6 psi
Liquid molecular weight 43.0
Vapor molecular weight 44.4
A B C
123-86-4 n-butyl acetate 17.50%116.16 6.48%7.24491 1518.3865 222.077 16.65 1.08 3.73%9.75%X
108-65-6 pm acetate 6.25%132.16 2.03%1.00 0.02 0.07%0.21%X141-78-6 ethyl acetate 6.25%88.11 3.05%7.2601 1338.5652 228.608 121.36 3.70 12.79%25.38%X
9004-70-05 cellulose nitrate, cellulose ester 6.25%1044.57 0.26%1.00 0.00 0.01%0.21%X
64-17-5 ethanol 6.25%46.07 5.83%8.12875 1660.8713 238.131 86.00 5.01 17.34%17.98%X
108-88-3 toluene 6.25%92.14 2.92%7.1366 1457.287 231.827 37.22 1.09 3.75%7.78%X X71-36-3 butanol 6.25%74.12 3.62%7.3013 1285.0227 173.247 9.52 0.35 1.19%1.99%X
1333-86-4 carbon black 6.25%12.011 22.37%0 0.00 0.00%0.00%
67-63-0 isopropanol 6.25%60.11 4.47%7.82517 1482.1331 217.413 68.34 3.05 10.56%14.29%X
64742-47-8 aliphatic petroleum distillates 6.25%200 1.34%7.79056 2225.63 257.923 1.15 0.02 0.05%0.24%X108-38-3 m-xylene 1.75%106.17 0.71%7.18115 1573.0243 226.671 11.29 0.08 0.28%0.66%X X
78-83-12 isobutanol 1.75%74.12 1.01%7.16115 1164.4309 164.392 14.83 0.15 0.52%0.87%X
64742-48-9 petroleum distillate 1.75%200 0.38%7.79056 2225.63 257.923 1.15 0.00 0.01%0.07%X
100-41-4 ethylbenzene 0.55%106.17 0.22%7.1561 1559.5452 228.582 13.33 0.03 0.10%0.25%X X106-42-3 p-xylene 0.55%106.17 0.22%7.15471 1553.9461 225.23 11.65 0.03 0.09%0.21%X X
64742-82-1 petroleum distillates 0.55%200 0.12%7.79056 2225.63 257.923 1.15 0.00 0.00%0.02%X
8052-41-3 aliphatic hydrocarbons 0.55%223.11 0.11%7.79056 2225.63 257.923 1.15 0.00 0.00%0.02%X
7732-18-5 water 18.80%18.01 44.87%8.05573 1723.6425 233.08 31.91 14.32 49.50%20.07%79.93%8.90%
Total Vapor Pressure 11.9 mmHg
0.2 psiLiquid molecular weight 84.1
Vapor molecular weight 39.4
A B C
64742-48-9 petroleum distillate 65.00%200 13.97%7.79056 2225.63 257.923 1.15 0.16 1.35%6.86%X
111-76-2 butyl cellosolve 6.25%118.18 2.27%7.96174 1928.1455 208.437 0.75 0.02 0.14%0.43%X
64-17-5 ethanol 6.25%46.07 5.83%8.12875 1660.8713 238.131 86.00 5.01 42.23%49.32%X
108-38-3 m-xylene 6.25%106.17 2.53%7.18115 1573.0243 226.671 11.29 0.29 2.41%6.47%X X1333-86-4 carbon black 1.75%12.011 6.26%0 0.00 0.00%0.00%
95-47-6 o-xylene 1.75%106.17 0.71%7.8126 1901.373 246.882 8.82 0.06 0.53%1.42%X X
106-42-3 p-xylene 1.75%106.17 0.71%7.15471 1553.9461 225.23 11.65 0.08 0.70%1.87%X X
67-63-0 isopropanol 1.75%60.11 1.25%7.82517 1482.1331 217.413 68.34 0.86 7.20%10.97%X100-41-4 ethylbenzene 1.75%106.17 0.71%7.1561 1559.5452 228.582 13.33 0.09 0.80%2.14%X X
96-29-7 methyl ethyl ketoxime 0.55%87.12 0.27%7.58369 1716.2122 212.378 3.18 0.01 0.07%0.16%X
7732-18-5 water 6.95%18.01 16.59%8.05573 1723.6425 233.08 31.91 5.29 44.58%20.35%
79.65%11.90%
Total Vapor Pressure 28.8 mmHg
0.6 psi
Liquid molecular weight 44.1Vapor molecular weight 45.3
A B C123-86-4 n-butyl acetate 17.50%116.16 6.65%7.24491 1518.3865 222.077 16.65 1.11 3.85%9.87%X
108-65-6 pm acetate 6.25%132.16 2.09%1.00 0.02 0.07%0.21%X
141-78-6 ethyl acetate 6.25%88.11 3.13%7.2601 1338.5652 228.608 121.36 3.80 13.21%25.70%X
9004-70-05 cellulose nitrate, cellulose ester 6.25%1044.57 0.26%1.00 0.00 0.01%0.21%X
64-17-5 ethanol 6.25%46.07 5.99%8.12875 1660.8713 238.131 86.00 5.15 17.90%18.21%X
108-88-3 toluene 6.25%92.14 2.99%7.1366 1457.287 231.827 37.22 1.11 3.87%7.88%X X
71-36-3 butanol 6.25%74.12 3.72%7.3013 1285.0227 173.247 9.52 0.35 1.23%2.02%X
1333-86-4 carbon black 6.25%12.011 22.96%0 0.00 0.00%0.00%64742-47-8 aliphatic petroleum distillates 6.25%200 1.38%7.79056 2225.63 257.923 1.15 0.02 0.06%0.24%X
67-63-0 isopropanol 6.25%60.11 4.59%7.82517 1482.1331 217.413 68.34 3.14 10.90%14.47%X
78-83-12 isobutanol 1.75%74.12 1.04%7.16115 1164.4309 164.392 14.83 0.15 0.54%0.88%X
108-38-3 m-xylene 1.75%106.17 0.73%7.18115 1573.0243 226.671 11.29 0.08 0.29%0.67%X X64742-48-9 petroleum distillate 1.75%200 0.39%7.79056 2225.63 257.923 1.15 0.00 0.02%0.07%X
106-42-3 p-xylene 0.55%106.17 0.23%7.15471 1553.9461 225.23 11.65 0.03 0.09%0.22%X X
100-41-4 ethylbenzene 0.55%106.17 0.23%7.1561 1559.5452 228.582 13.33 0.03 0.11%0.25%X X
39464-64-7 polyoxyethylene dinonyphenyl ether phosphate0.55%200 0.12%1.00 0.00 0.00%0.02%X68891-21-4 surfactant 0.55%200 0.12%1.00 0.00 0.00%0.02%X
64742-82-1 petroleum distillates 0.55%200 0.12%7.79056 2225.63 257.923 1.15 0.00 0.00%0.02%X
8052-41-3 aliphatic hydrocarbons 0.55%223.11 0.11%7.79056 2225.63 257.923 1.15 0.00 0.00%0.02%X
1623-15-0 butyl dihydrogen phosphate 0.10%154.1 0.03%0.00 0.00 0.00%0.00%7732-18-5 water 17.60%18.01 43.12%8.05573 1723.6425 233.08 31.91 13.76 47.85%19.03%
80.97%9.01%
Total Vapor Pressure 31.9 mmHg
0.6 psi
Liquid molecular weight 55.0
Vapor molecular weight 35.7
A B C
64742-48-9 petroleum distillate 32.50%200 8.94%7.79056 2225.63 257.923 1.15 0.10 0.32%1.81%X
111-76-2 butyl cellosolve 17.50%118.18 8.15%7.96174 1928.1455 208.437 0.75 0.06 0.19%0.64%X
123-86-4 n-butyl acetate 6.25%116.16 2.96%7.24491 1518.3865 222.077 16.65 0.49 1.55%5.04%X78-93-3 methyl ethyl ketone (MEK)6.25%72.11 4.77%7.1913 1323.0708 227.093 110.92 5.29 16.60%33.56%X
64-17-5 ethanol 6.25%46.07 7.46%8.12875 1660.8713 238.131 86.00 6.42 20.14%26.02%X
64742-95-6 aromatic hydrocarbons 1.75%200 0.48%7.79056 2225.63 257.923 1.15 0.01 0.02%0.10%X
64742-47-8 aliphatic petroleum distillates 1.75%200 0.48%7.79056 2225.63 257.923 1.15 0.01 0.02%0.10%X108-38-3 m-xylene 1.75%106.17 0.91%7.18115 1573.0243 226.671 11.29 0.10 0.32%0.96%X X
52125-53-8 propylene glycol monoethyl ether 1.75%104.15 0.92%11.2399 2832.6194 208.564 0.23 0.00 0.01%0.02%X
95-63-6 1,2,4-trimethylbenzene 1.75%120.19 0.80%7.29329 1763.3511 230.248 3.29 0.03 0.08%0.28%X
106-42-3 p-xylene 0.55%106.17 0.28%7.15471 1553.9461 225.23 11.65 0.03 0.10%0.31%X X100-41-4 ethylbenzene 0.55%106.17 0.28%7.1561 1559.5452 228.582 13.33 0.04 0.12%0.36%X X
13463-67-7 titanium dioxide 0.55%79.86 0.38%0.00 0.00 0.00%0.00%
107-98-2 propylene glycol monoethyl ether 0.55%90.12 0.34%8.0526 1764.7387 222.677 11.71 0.04 0.12%0.31%X
1333-86-4 carbon black 0.55%12.011 2.52%0.00 0.00 0.00%0.00%70851-34-2 cobalt compound 0.10%522.58 0.01%0.00 0.00 0.00%0.00%
7732-18-5 water 19.75%18.01 60.32%8.05573 1723.6425 233.08 31.91 19.25 60.41%30.51%
69.49%1.62%Total:
Solid
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC HAP
Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC HAP
Total:
Vapor
wt.%VOC HAP
Solid
Vapor
wt.%VOC HAP
Solid
Total:
Product chemical data for EBONY W/S - D22K00333 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole Antoine Coefficients1
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Pi,
component
pi, partial
pressure of
yi, vapor
mole
Product chemical data for BLACK 20SH PRECAT - L42K00293 mixture components:
Solid
Solid
Solid
Solid
Product chemical data for SW6258 TRICORN BLACK 20SH - L42K00267 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole Antoine Coefficients1
Total:
Product chemical data for ELKO TEMPLE W/S - D22N11505 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 4 Material Evaluation
February 2025
Total Vapor Pressure 108.9 mmHg
2.1 psi
Liquid molecular weight 48.0
Vapor molecular weight 41.8
A B C123-86-4 n-butyl acetate 17.50%116.16 7.23%7.24491 1518.3865 222.077 16.65 1.20 1.11%3.08%X67-64-1 acetone 17.50%58.08 14.47%7.2996 1312.253 240.705 283.16 40.97 37.63%52.34%
13463-67-7 titanium dioxide 17.50%79.86 10.52%0 0.00 0.00%0.00%
64-17-5 ethanol 6.25%46.07 6.51%8.12875 1660.8713 238.131 86.00 5.60 5.15%5.68%X
9004-70-05 cellulose nitrate, cellulose ester 6.25%1044.57 0.29%1.00 0.00 0.00%0.07%X
71-36-3 butanol 6.25%74.12 4.05%7.3013 1285.0227 173.247 9.52 0.39 0.35%0.63%X
67-63-0 isopropanol 6.25%60.11 4.99%7.82517 1482.1331 217.413 68.34 3.41 3.13%4.51%X
111-76-2 butyl cellosolve 1.75%118.18 0.71%7.96174 1928.1455 208.437 0.75 0.01 0.00%0.01%X
1623-15-0 butyl dihydrogen phosphate 0.55%154.1 0.17%0.00 0.00 0.00%0.00%50-00-0 formaldehyde 0.55%30.03 0.88%7.46432 1078.39 254.377 4701.17 41.34 37.98%27.31%X X
100-41-4 ethylbenzene 0.55%106.17 0.25%7.1561 1559.5452 228.582 13.33 0.03 0.03%0.08%X X
12236-62-3 pigment orange 36 0.10%416.78 0.01%0.00 0.00 0.00%0.00%
39464-64-7 polyoxyethylene dinonyphenyl ether phosphate0.10%200 0.02%1.00 0.00 0.00%0.00%X68891-21-4 surfactant 0.10%200 0.02%1.00 0.00 0.00%0.00%X
68412-53-3 alkyl phenol phosphate ester 0.10%933.4 0.01%1.00 0.00 0.00%0.00%X
7732-18-5 water 18.70%18.01 49.86%8.05573 1723.6425 233.08 31.91 15.91 14.61%6.30%
41.36%27.39%
Total Vapor Pressure 21.2 mmHg
0.4 psi
Liquid molecular weight 115.9
Vapor molecular weight 55.6
A B C64742-48-9 petroleum distillate 57.34%200 33.24%7.79056 2225.63 257.923 1.15 0.38 1.80%6.49%X111-76-2 butyl cellosolve 7.65%118.18 7.50%7.96174 1928.1455 208.437 0.75 0.06 0.27%0.56%X
64-17-5 ethanol 7.65%46.07 19.24%8.12875 1660.8713 238.131 86.00 16.55 78.02%64.71%X
108-38-3 m-xylene 7.65%106.17 8.35%7.18115 1573.0243 226.671 11.29 0.94 4.44%8.49%X X
13463-67-7 titanium dioxide 7.65%79.86 11.10%0.00 0.00 0.00%0.00%108-65-6 pm acetate 1.91%132.16 1.68%1.00 0.02 0.08%0.19%X
95-47-6 o-xylene 1.91%106.17 2.09%7.8126 1901.373 246.882 8.82 0.18 0.87%1.66%X X
106-42-3 p-xylene 1.91%106.17 2.09%7.15471 1553.9461 225.23 11.65 0.24 1.15%2.19%X X
67-63-0 isopropanol 1.91%60.11 3.69%7.82517 1482.1331 217.413 68.34 2.52 11.88%12.85%X100-41-4 ethylbenzene 1.91%106.17 2.09%7.1561 1559.5452 228.582 13.33 0.28 1.31%2.51%X X
64742-47-8 aliphatic petroleum distillates 0.76%200 0.44%7.79056 2225.63 257.923 1.15 0.01 0.02%0.09%X
1333-86-4 carbon black 0.76%12.011 7.38%0.00 0.00 0.00%0.00%
96-29-7 methyl ethyl ketoxime 0.76%87.12 1.02%7.58369 1716.2122 212.378 3.18 0.03 0.15%0.24%X39464-64-7 polyoxyethylene dinonyphenyl ether phosphate0.08%200 0.04%1.00 0.00 0.00%0.01%X
68412-53-3 alkyl phenol phosphate ester 0.08%933.4 0.01%1.00 0.00 0.00%0.01%X
68891-21-4 surfactant 0.08%200 0.04%1.00 0.00 0.00%0.01%X
100.00%14.85%
Total Vapor Pressure 283.2 mmHg5.5 psi
Liquid molecular weight 58.1
Vapor molecular weight 58.1
A B C
67-64-1 acetone 100.00%58.08 100.00%7.2996 1312.253 240.705 283.16 283.16 100.00%100.00%
0.00%0.00%
Total:
Total:
Product chemical data for FC-47871 GRAY FLANNEL - D22N06983 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC HAP
Product chemical data for BM WHITE DOVE 20 SH PRECAT - L42CW00787 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC
Total:
Cleaning Solvent
Product chemical data for Solvent - T84C0033 mixture components:
CAS no.Component Liquid wt.%Molecular
weight
xi, liquid
mole
Antoine Coefficients1 Pi,
component
pi, partial
pressure of
yi, vapor
mole
Vapor
wt.%VOC HAP
Solid
Solid
Solid
Solid
HAP
Solid
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 5 Material Evaluation
February 2025
Basis
a. The coating booth is
occasionally used to spray
- one production/color lab booth
b. The maximum volume sprayed onto the test material for each product QC test is:40 mL/spray
c. The coating overspray is conservatively assumed to be 50%for calculating PM emissions (percent of coating solids not applied to the test material).
One QC test is conducted for each material packaged in the tinting, repackaging, and blending line. The maximum number of containers packaged in a shift are:
Container Size (gal)Containers
mixed in a shift
Containers
mixed in a day
0.25 7 21
1 10 30
5 20 60
55 0 0
111 total sprays per 24 hours
To estimate worst case sprays per day, a safety factor of 1.25 was used to obtain maximum total sprays of 139 per day.
Max Daily Coating Usage per production area QC booth =40 mL/spray x 248 sprays/day / 3,785 mL/gal
Max Daily Coating Usage per production area QC booth =1.5 gal/day
Actual Daily Coating Usage per production area QC booth =0.4 gal/day
Max Daily Cleaning Solvent Usage:1.5 gal/day Actual 0.4 gal/day
toluene xylene ethylbenzene formaldehyde
E29CW02174+K 9.36 17.50%47.30%16.55%14.25%1.75%0.55%
E29CW01410+K 9.36 17.50%47.30%16.55%14.25%1.75%0.55%
L42CW02023 8.56 18.05%62.85%1.10%0.55%0.55%
L42CW01679 8.86 18.15%63.70%1.10%0.55%0.55%
L42K00293 8.05 6.25%74.95%9.10%6.25%2.30%0.55%
D22K00333 7.03 1.75%91.30%11.50%9.75%1.75%
L42K00267 8.01 6.35%76.05%9.10%6.25%2.30%0.55%
D22N11505 7.37 1.20%79.15%2.85%2.30%0.55%
L42CW00787 8.48 18.15%63.15%1.10%0.55%0.55%
D22N06983 7.15 8.41%91.59%13.38%11.47%1.91%
T84C0033 6.66 0.00%0.00%0.00%
g. Potential emissions are based on operating:24 hr/day Actual emissions are based on operating: 8 hr/day
7 day/week 5 day/week
365 day/yr 52 week/yr
8,760 hr/yr 2,080 hr/yr
Emission Calculations:
PM Coating emissions (lb/day)=(coating usage, gal/day) x (% overspray) x (coating density, lb/gal) x (solids content, %)
VOC Coating emissions (lb/day)=(coating usage, gal/day) x (coating density, lb/gal) x (VOC content, %)
VOC Cleaning Solvent emission (lb/day)=(cleaning solvent usage, gal/day) x (cleaning solvent density, lb/gal) x (VOC content, %)
HAP Coating emissions (lb/day)=(coating usage, gal/day) x (coating density, lb/gal) x (HAP content, %)
Potential VOC emissions (ton/yr)=(total VOC emissions, lb/day) x (365 day/yr) / (2000, lb/ton)
Emissions:
2023 Actual
Emissions
(Production
Booth)
lb/hr ton/yr ton/yr
PM 0.05 0.22 0.04
VOC 0.37 1.63 0.33
Total HAP 0.09 0.42 0.08
toluene 0.03 0.13 0.03
xylene 0.08 0.36 0.07
ethylbenzene 0.01 0.04 0.01
formaldehyde 0.003 0.01 1E-02
Code Density
(lb/gal)
VOC
(liquid wt%)
Total HAP
(liquid
wt%)
Solids (liquid
wt%)
e. It is assumed that 100% of the organics contained in the products and cleaning solvent used in the coating booth are captured by the coating booth exhaust system and exit the
stacks as air emissions. Potential emissions are calculated assuming maximum annual operation of 8,760 hr/yr.
f. The products with the highest processing rate were used to evaluate the worst case uncontrolled potential emissions for the facility. The products evaluated are listed below. (The
green highlight indicates the cleaning solvent. The red highlights indicate the products with the highest overall VOC content, highest total HAP content, and the highest individual HAPs.)
FinishWorks - Salt Lake City, UT
Air Emissions - Coating Booths
Pollutant
Uncontrolled Potential
Emissions
(Production Booth)
HAP %
d. The booth spray guns are assumed to be cleaned after each use with the solvent Acetone. It is assumed the same quantity of cleaning solvent is used as coating.
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 6 Coating Booths
February 2025
Basis
LL =12.46 * (SPM/T)
Where:
LL =loading loss, lb/1,000 gal liquid loaded
S =saturation factor (see Table 5.2-1)
P =true vapor pressure of material, psia
M =molecular weight of vapors, lb/lb-mol
T =temperature of material (at ambient conditions), ◦R
S =1.45 (splash loading: dedicated normal service)
T =30 °C
Code True Vapor
Pressure (psia)
Vapor Molecular
Weight
(lb/lb-mol)
Total VOC Total HAP toluene xylene ethylbenzene formaldehyde
E29CW02174+K 1.13 27.76 73.80%64.25%3.41%0.54%60.30%
E29CW01410+K 1.13 27.76 73.80%64.25%3.41%0.54%60.30%
L42CW02023 2.09 41.69 41.30%27.35%0.08%27.27%
L42CW01679 2.13 41.85 41.43%27.43%0.08%27.35%
L42K00293 0.56 44.41 79.93%8.90%7.78%0.88%0.25%
D22K00333 0.23 39.45 79.65%11.90%9.76%2.14%
L42K00267 0.56 45.29 80.97%9.01%7.88%0.89%0.25%
D22N11505 0.62 35.66 69.49%1.62%1.27%0.36%
L42CW00787 2.11 41.76 41.36%27.39%
D22N06983 0.41 55.55 100.00%14.85%12.34%2.51%
Emission Calculations
c. Tinting, Blending, and Repackaging
Loading Loss, LL (lb/1,000 gal)= 12.46 x 1.45 x (true vapor pressure, psia) x (vapor molecular weight, lb/lb-mol) / (temperature, °R)
Total Emissions (lb/yr)= (Loading Loss, lb/1,000 gal) x [(Production, gal/yr)/1,000]
Stack Emissions (lb glycol ether/yr)= (total emissions, lb/yr) x (vapor wt %)
Stack Emissions (lb/hr)= (total emissions, lb/yr) / (8760, hr/yr)
d. Actual production is based on one 8-hour shift/day. Potential production is based on three, 8-hour shifts/day.
e. The 2023 throughput capacity based on one shift/day is:9,695 gal/yr.The throughput capacity based on three shifts/day would be:29,085 gal/yr.
To estimate worst case throughput, a safety factor of 1.25 was used to obtain maximum throughput of 36,356 gal/yr.
VOC Total HAP toluene xylene ethylbenzene formaldehyde
E29A04201+K 1.04 37.91 27.98 24.36 0 1.29 0.21 22.86
E29B02326+K 1.04 37.91 27.98 24.36 0 1.29 0.21 22.86
E29CW05494+K 2.89 104.94 43.35 28.70 0 0.00 0.08 28.62
L41K00005A 2.95 107.30 44.45 29.43 0.00 0 0 29
B10A00546A 0.82 29.91 23.91 2.66 2.33 0 0 0
B10A00548A 0.30 10.91 8.69 1.30 0.00 1 0 0B10K00068A0.83 30.33 24.56 3 2 0 0 0
S75A00114 0.73 26.46 18.38 0.43 0 0 0 0
S75N2262A 2.91 105.86 43.78 29 0 0 0 0
S75N02880A 0.75 27.43 27.43 4.07 0 3 1 0
VOC Total HAP toluene xylene ethylbenzene formaldehyde
E29A04201+K 1.04 10.11 7.46 6.50 0 0.34 0.06 6.10
E29B02326+K 1.04 10.11 7.46 6.50 0 0.34 0.06 6.10
E29CW05494+K 2.89 27.99 11.56 7.65 0 0.00 0.02 7.63
L41K00005A 2.95 28.61 11.85 7.85 0.00 0 0 8
B10A00546A 0.82 7.98 6.38 0.71 0.62 0 0 0
B10A00548A 0.30 2.91 2.32 0.35 0.00 0 0 0
B10K00068A 0.83 8.09 6.55 1 1 0 0 0
S75A00114 0.73 7.05 4.90 0.11 0 0 0 0
S75N2262A 2.91 28.23 11.68 8 0 0 0 0
S75N02880A 0.75 7.32 7.32 1.09 0 1 0 0
Emission Summary:
lb/hr lb/yr ton/yr lb/hr lb/yr ton/yrVOC0.01 44.45 0.0 0.01 11.85 0.01
Total HAP 0.00 29.43 1E-02 4E-03 7.85 4E-03
toluene 2.7E-04 2.39 1E-03 3E-04 0.64 3E-04xylene 3.9E-04 3.39 2E-03 4E-04 0.90 5E-04
ethylbenzene 7.9E-05 0.69 3E-04 8E-05 0.18 9E-05
formaldehyde 0.00 29.34 1E-02 4E-03 7.83 4E-03
a. During the blending, tinting, and repackaging activities, material evaporates and exits the facility via the vapor extraction hoods and associated stacks. AP-42 Section 5.2, Transportation and Marketing of Petroleum Liquids, provides an equation for calculating emissions from loading petroleum liquid, equation 5.2(1), which is used to represent emissions from the FinishWorks operations.
Air Emissions - Tinting, Blending, & Repackaging
FinishWorks - Salt Lake City, UT
Maximum Potential Production
EBONY W/S
b. The products with the highest processing rate and highest HAP content were used to evaluate the worst case potential emissions for the facility. The products evaluated are listed below.
Uncontrolled Potential Emissions (lb/yr)
Code Total Emissions
(lb/yr)
Loading Loss,
LL
(lb/1,000 gal)
Vapor Composition (wt%)
Product
Pollutant
Code Total Emissions
(lb/yr)
Uncontrolled Potential Emissions
Loading Loss,
LL
(lb/1,000 gal)
2023 Actual Production
36,356
(gal/yr)
(gal/yr)
9,695
Actual Emissions
2023 Actual Emissions (lb/yr)
SW6258 TRICORN BLACK 20SH
ELKO TEMPLE W/S
BM WHITE DOVE 20SH PRECAT
FC-47871 GRAY FLANNEL
SW7103 WHITETAIL 20SH CV
MS ULTRA WHITE CV
DIMENSIONAL WHITE 10SH
SW7004 SNOWBOUND 10SH
BLACK 20SH PRECAT
FinishWorks - Salt Lake City, UTAir Emissions Calculations 7 Tinting, Blending, RepackagingFebruary 2025
Basis:
a. There are 3 heaters maintained in the Salt Lake City facility all used as space or air makeup heaters.
Burner Rating
(MMBtu/hr)
Heater 1 Reznor FT200 NG 0.20
Heater 2 Reznor FT200 NG 0.20
Heater 3 Reznor FT200 NG 0.20
Total MMBtu/hr:0.60
b. The emission units are heated with natural gas. The heat content of natural gas is: 1,020 Btu/scf
c. Potential emissions are based on operating:Actual emissions are based on operating:
24 hr/day 24 hr/day
7 day/week 7 day/week
365 day/yr 26 week/yr
8,760 hr/yr 4,368 hr/yr
d. Natural gas combustion emissions are based on the following emission factors from AP-42 Section 1.4
Emission Calculations:
Emission Factors (lb/MMBtu)= (Emission factor, lb/106 scf) / (Heat content of natural gas, 1020 Btu/scf)
Hourly Emissions (lb/hr)= (Emission factor, lb/MMBtu) x (Total heat rating, MMBtu/hr)
Annual Emissions (ton/yr)= (Hourly emissions, lb/hr) x (Annual hours of operation, hr/yr) / (2000 lb/ton)
lb/hr ton/yr lb/hr ton/yr
NOx 100 9.8E-02 5.9E-02 2.6E-01 5.9E-02 1.3E-01
CO 84 8.2E-02 4.9E-02 2.2E-01 4.9E-02 1.1E-01
SO2 0.6 5.9E-04 3.5E-04 1.5E-03 3.5E-04 7.7E-04
VOC 5.5 5.4E-03 3.2E-03 1.4E-02 3.2E-03 7.1E-03
PM 7.6 7.5E-03 4.5E-03 2.0E-02 4.5E-03 9.8E-03
PM2.5 7.6 7.5E-03 4.5E-03 2.0E-02 4.5E-03 9.8E-03
PM10 7.6 7.5E-03 4.5E-03 2.0E-02 4.5E-03 9.8E-03
HAPs
lead 5.0E-04 4.9E-07 2.9E-07 1.3E-06 2.9E-07 6.4E-07
2-methylnaphthalene 2.4E-05 2.4E-08 1.4E-08 6.2E-08 1.4E-08 3.1E-08
3-methylcholanthrene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
7,12- dimethylbenz(a)anthracene 1.6E-05 1.6E-08 9.4E-09 4.1E-08 9.4E-09 2.1E-08
acenaphthene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
acenaphthylene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
anthracene 2.4E-06 2.4E-09 1.4E-09 6.2E-09 1.4E-09 3.1E-09
benz(a)anthracene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
benzene 2.1E-03 2.1E-06 1.2E-06 5.4E-06 1.2E-06 2.7E-06
benzo(a)pyrene 1.2E-06 1.2E-09 7.1E-10 3.1E-09 7.1E-10 1.5E-09
benzo(b)fluoranthene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
benzo(g,h,i)perylene 1.2E-06 1.2E-09 7.1E-10 3.1E-09 7.1E-10 1.5E-09
benzo(k)fluoranthene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
chrysene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
dibenzo(a,h)anthracene 1.2E-06 1.2E-09 7.1E-10 3.1E-09 7.1E-10 1.5E-09
dichlorobenzene 1.2E-03 1.2E-06 7.1E-07 3.1E-06 7.1E-07 1.5E-06
fluoranthene 3.0E-06 2.9E-09 1.8E-09 7.7E-09 1.8E-09 3.9E-09
fluorene 2.8E-06 2.7E-09 1.6E-09 7.2E-09 1.6E-09 3.6E-09
formaldehyde 7.5E-02 7.4E-05 4.4E-05 1.9E-04 4.4E-05 9.6E-05
hexane 1.8E+00 1.8E-03 1.1E-03 4.6E-03 1.1E-03 2.3E-03
indeno(1,2,3-cd)pyrene 1.8E-06 1.8E-09 1.1E-09 4.6E-09 1.1E-09 2.3E-09
naphthalene 6.1E-04 6.0E-07 3.6E-07 1.6E-06 3.6E-07 7.8E-07
phenanathrene 1.7E-05 1.7E-08 1.0E-08 4.4E-08 1.0E-08 2.2E-08
pyrene 5.0E-06 4.9E-09 2.9E-09 1.3E-08 2.9E-09 6.4E-09
toluene 3.4E-03 3.3E-06 2.0E-06 8.8E-06 2.0E-06 4.4E-06
arsenic 2.0E-04 2.0E-07 1.2E-07 5.2E-07 1.2E-07 2.6E-07
beryllium 1.2E-05 1.2E-08 7.1E-09 3.1E-08 7.1E-09 1.5E-08
cadmium 1.1E-03 1.1E-06 6.5E-07 2.8E-06 6.5E-07 1.4E-06
chromium 1.4E-03 1.4E-06 8.2E-07 3.6E-06 8.2E-07 1.8E-06
cobalt 8.4E-05 8.2E-08 4.9E-08 2.2E-07 4.9E-08 1.1E-07
manganese 3.8E-04 3.7E-07 2.2E-07 9.8E-07 2.2E-07 4.9E-07
mercury 2.6E-04 2.5E-07 1.5E-07 6.7E-07 1.5E-07 3.3E-07
nickel 2.1E-03 2.1E-06 1.2E-06 5.4E-06 1.2E-06 2.7E-06
selenium 2.4E-05 2.4E-08 1.4E-08 6.2E-08 1.4E-08 3.1E-08
Total HAP 1.89 1.9E-03 1.1E-03 4.9E-03 1.1E-03 2.4E-03
FinishWorks - Salt Lake City, UT
Natural Gas Fired Heaters
Facility ID
Uncontrolled Potential Emissions
Make Model Fuel Type
Controlled Actual EmissionsPollutantsEmission Factor
(lb/10^6 scf)
Final Emission
Factor (lb/MMBtu)
FinishWorks - Salt Lake City, UT
Air Emissions Calculations 8 Heaters
February 2025