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### DEPARTMENT OF ENVIRONMENTAL QUALITY DIVISION OF AIR QUALITY

Nonnan H. Bangerter Governor ,;. 1950 West NOrth TemOle "eoly to: S;ate oi Utah Kenneth L. Alkema

_ Salt Lake City. Ulah D,YISlon or Air Quality ExecutJVf: Director (8011 536·4000 Department of Envrronmenta! Ouailty F. Burnell Cordner Director at (80 , ) 536-4099 Fax Sail Lake City. Utah 84114-4820 

### DAQE-167-92 February 19, 1992

James R. Van orman Director, Environmental Management office Department of the Air Force Headquarters Ogden Air Logistics Center (AFLC) Hill Air Force Base, Utah 84056

.Re: Approval Order for JP-4 Tank Throughput Limitations

Dear Mr. Van Orman:

Thts amended AO is being issued to update and combine the AOs dated January 3, 1989 and July 29, 1991. The JP-4 tank throughput limitations are combined to give one throughput limit for all four tanks. The re-worded throughput limitations give more flexibility and do not allow an increase in total throughput. The above-referenced project has been evaluated and found to be consistent with the requirements of the Utah Air Conservation Regulations (UACR) and the Utah Air Conservation Act. This air quality AO authorizes the project with the following conditions and failure to comply with any of the conditions may constitute a violation of this order: 1. This AO shall replace the AO's issued to Hill Air Force Base on July 29, 1991 and January 3, 1989. 2. The approved facilities. shall consist of the following equipment:. A. Two steam generators, a total heat input rate of 120.3 MMBTU/hr with natural gas as primary fuel with a standby diesel fuel (116.5 MMBTU/hr) at building 260; B. Dual seals for JP-4 storage tanks 10873, 10885, 10861 and 10862; C. TwO mobile waste hydraulic fluid reclamation units based at Building 514; D. Paint spray booth and two lab hoods at the Building 5N; E. Lab Hoods



### 4.2.4-744

Pr:nlec on recycleo oaDer

### F. Nine Turboclean chambers, or equivalent, for the paint spray hangar at Building 220

- In addition, water reducible primer or low VOC primer shall be substituted for solvent base primer, and a high volume low pressure (HVLP) type spray gun shall replace the conventional paint spray gun. Equivalency shall be determined by the Executive Secretary. 3. Visible emissions from any point or fugitive emission source associated with the emission points listed in this AO shall not exceed 10\ opacity. opacity observation of emissions from stationary sources shall be conducted in accordance with 40 CFR 60, Appendix A, Method 9. 4. The following operating limits shall not be exceeded without prior approval in accordance with R446-1-3.1, UAC: A. Steam generators, Building 260 1) 465.7 X 

### 10 9 

### BTU from natural gas per 12-month period 2) 108.3 x 10 6 

### BTU from natural gas per hour 3) 50.1 x 10 9 

### BTU from diesel fuel per 12-month period 4) 116.5 x 10 6 

### BTU from diesel fuel per hour 5) 4,300 hours per 12-month period B. Storage tanks 10873, 10885, 10861 and 10862

- total combined JP-4 throughput for all four tanks shall not exceed 1,260,000 barrels per 12-month period and shall be determined by summing individual tank throughputs F. Hydraulic fluid waste reclamation units, Building 514 1) 30,000 gallons of total fluid per 12-month period 2) 8 hours per day 3) 2,080 hours per 12-month period Compliance with the annual limitations shall be qetermined on a rolling 12-month total. Based on the first day of each month a new 12-month total shall be calculated using the previous 12 months. Records of usage, operation, and production shall be kept for all periods when the plant/equipment is in operation. Records of usage, operation, and production shall be made available to the Executive Secretary or his representative upon request, and shall include a period of two years ending with the date of the request. Fuel consumption for steam generators shall be determined by examination of fuel meter records. Storage tank throughputs shall be determined by examination of tank throughput records, which shall be kept on a daily basis. Hydraulic fluid waste reclamation unit throughput shall be determined by examination of usage records, which shall be kept on a daily basis. Hours of operation shall be determined by supervisor monitoring and maintaining of an operations log. 5. The owner/operator shall comply with R446-1-4.9.1(c), UAC for controlling emissions form storage tanks 10861, 10862, 10873 and 10885.
6. In addition to the requirements of this AO, all provisions of 40 CFR 60, NSPS Subparts A and Ka apply to storage tanks.



### 4.2.4-745

### 7. The condenser at the final point of each of the hydraulic fluid waste reclamation units shall operate during the operation of hydraulic fluid waste reclamation units. If the condenser is out of service, the hydraulic fluid waste reclamation units shall not be used until the condenser has been returned to service. The hydraulic waste reclamation equipment shall be operated for maximum solvent recovery at all times. The condenser shall be capable of recovering no less than 75% of solvents from the fluid. Records of solvent recovery shall be kept for all periods when the hydraulic fluid waste reclamation units are in operation. Demonstration of the 75% recovery shall be made by monitoring the solvent input and solvent recovery over a specified period of time acceptable to the Executive Secretary and calculating the percent recovery. A compliance demonstration shall be performed if directed by the Executive Secretary. Records of the amount of solvent recovered shall be kept for all periods when the hydraulic fluid waste reclamation units are in operation. The record shall include the following items: A. Date; B. Unit usage (start and end times); C. Total hydraulic fluid waste processed; D. Amount solvent recovered. 8. The owner/operator shall use only natural gas as a primary fuel and #2 diesel fuel as a backup fuel in the steam generators. If any other fuel is to be used, an AO shall be required in accordance with R446-1-3.1, UAC. Natural gas consumption shall not exceed 465.7 x 10 8 

### scf per 12­ month period, and diesel fuel consumption shall not exceed 5% of the annual fuel used in the boilers without prior approval in accordance with R446-1-3.1, UAC. Compliance with the**l~itations** 

### shall be determined on a rolling 12-month total. Based on the first day of each month a new 12-month total shall be calculated using the previous 12 months. Records of fuel consumption shall be kept for all periods when the plant is in operation. Records of fuel consumption shall be made available to the Executive Secretary upon request, and shall include a period of two years ending with the date of the request. Fuel consumption shall be determined by examination of fuel meter records and fuel bills. 9. The sulfur content of any diesel fuel burned shall not exceed 0.50% bv weight as determined by ASTM Method 0-4294-89. The sulfur content shall be tested if directed by the Executive Secretary. 10. The paint spray booth at Building 5N shall be equipped with a set of paint arrestor particulate filters (or equivalent) to control particulate emissions. All air exiting the booth shall pass through this control system before being vented into the atmosphere. Equivalency shall be determined by the Executive Secretary.
11. 

### The paint spray hangar at Building 220 shall be equipped with 2 

### water wall (or equivalent) to control particulate emissions.**A~l** 

### air exiting the booth shall pass through this control system 

## .-.,. before being vented to the atmosphere. Equivalency shall be determined by the Executive Secretary. 

### 4.2.4-746

### 12. Emissions of 

## vec from the paint spray booth and the two lab hoods in Building SN shall not exceed a total of 2.37 tons per l2-month period without prior approval in accordance with R446-1-3.1, UAC. Compliance with the limitation shall be determined on a rolling 12-month total. Based on the first day of each month a new 12­ month total shall be calculated using the previous l2 months. The building emissions of VOC shall be determined by maintaining a record of paints, thinners and cleaning agents used. The record shall include the following data for each item used: A. Name of paint or thinner B. Weight in pounds per gallon C. Percent 

## vec by weight D. Amount used on a daily basis Records of consumption shall be kept for all periods when the plant is in operation. Records of consumption shall be made available to the Executive Secretary upon request, and shall include a period of two years ending with the date of the request.

vee emissions shall be determined by the following manner: 

## vee 

## = (% 

### Volatile by weight 

### I 100) 

### * (Density lb/gal) 

### * (Gallons consumed) / (2,000 lb/ton) The 

## vec content in pounds for each individual item or surface coating used shall be calculated, and then the total of all items shall be summed, such that the cumulative total shall not exceed the 2.37 tons per l2-month period as specified. 13. Emissions of 

## vee from the paint spray hangar in Building 220 

### shall not exceed 17.2 tons per 12-month period without prior approval in accordance with R446-1-3.l, UAC. compliance with the limitation shall be determined on a rolling l2-month total. Based on the first day of each month a new l2-month total shall be calculated using the previous 12 months. The building emissions of 

## vee shall be determined by maintaining a record of paints and thinners used. The record shall include the following data for each item used: A. Name of paint or thinner B. Weight in pounds per gallon C. Percent 

## vee by weight D. Amount used on a daily basis Records of consumption shall be kept for all periods when the plant is in operation. Records of consumption shall be made available to the Executive Secretary upon request, and shall include a period of two years ending with the date of the request. VOC emissions shall be determined by the following manner:

vee 

## = (% 

### Volatile by weight 

### I 100) 

### * (Density lb/gal) 

### * (Gallons Consumed) / (2,000 lb/ton) The vee content in pounds for each individual item or surface coating used shall be calculated, and then the total of all items shall be summed, such that the cumulative total shall not exceed the 17.2 tons per 12-month period as specified.



# -- \ 

### 4.2.4-747

### 14. The owner/operator shall operate a solvent cleaning operation under the lab hoods according to the following: A. Covers shall remain closed at all times except during actual loading, unloading, or transfer operations. The covers shall be designed so that they can easily be operated with one**hand~**

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### a.ll d=ipping ceaEes; C. Waste or used solvent shall be stored in covered containers and disposed by a method which prevents its emission into the atmosphere in accordance with**R446-1-4.9.4.A(3)~** 

### D. Tanks, containers, and all associated equipment shall be maintained in good operating condition and leaks shall be repaired**immediately~** 

### E. Written procedures for the operation and maintenance of the solvent cleaning equipment shall be posted in an accessible and apparent location near the**equipment~** 

### F. The requirements of R446-1-4.9.4.A, UAC shall apply to this operation as applicable. 15. A copy of this AO shall be posted on site and shall be available to the employees who operate the air emission producing equipment. All employees who operate the air emission producing equipment shall receive instruction as to their responsibilities in operating the equipment in compliance with all of the relevant conditions. 16. All installations and facilities authorized by this Approval Order shall be adequately and properly maintained. The owner/operator shall comply with R446-1-3.5 and 4.7, UAC. R446-1-3.5, UAC addresses emission inventory reporting requirements. R446-1-4.7, UAC addresses unavoidable breakdown reporting requirements. The owner/operator shall calculate/estimate the excess emissions whenever a breakdown occurs. The sum total of excess emissions shall be reported to the Executive Secretary for each calendar year no later than January 31 of the following year. Any future modifications to the equipment approved by this order must also be approved in accordance with R446-l-3.1.1, UAC. This AO in no way releases the owner or operator from any liability for compliance with all other applicable federal, state, and local regulations including the Utah Air Conservation Rules. Sincerely,

# Ft-~~utive Secretary Utah Air Quality Board FBC:DC:cl

cc: EPA Region VIII, Hike Owens Davis County Health**Depar~ment**



### 4.2.4-748

## DEPARTMENT OF THE AIR FORCE HEADQUARTERS OGDEN AIR LOGISTICS CENTER (AFLC) 

# FEB 0 5 i392 HILL AIR FORCE BASE. UTAH 84056·5990 

# Air Quality 

# s FEB**r~~** 

# .

F. Burnell Cordner Department of Environmental Quality Division of Air Quality 1950 West North Temple Salt Lake City UT**84114-48~** 

### Re: Approval Orders # 

### DAQE-540-91, 29 Jul 91, and # 

### BAQE-757-88, 3 Jan 89, Vapor Seals for JP-4 Storage Tanks
Dear Mr Cordner 

## In reference to the above approval orders, we request the following changes:

g. 

### Combine the above two approval orders and delete any**~eference** 

### to a refrigeration unit on the vapor degreaser (BAQE-757-88) in Bldg 507 since this process has been discontinued since spring 90. 

### Please delete this source.

I 

# rbJ Combine throughputs of JP-4 storage tanks 10861, 10862, 10873, and

## 10~ to give an annual throughput of 1.26 x

## 1~ barrels. Currently, these tanks have individual throughput limits. With the outage of Chevron's JP-4 storage tanks, it's extremely difficult to receive a large inventory without transferring fuel between the tanks. This leads to throughput exceedence on an individual tank basis. However, the combined throughput for the overall tank farm is under the combined throughput limits. Our records CAtch 1) show that due to the above, throughput for the JP-4 tank 10885 was exceeded by 25,788 barrels on 1 Dec 91. For the tank farm as a whole, we were under the limits by 286,610 barrels. Similarly, on 1 Jan 92, 

### the throughput for tank 10885 was exceeaeo by 

### 6,717 barrels ana overall we were under**~ne** 

### limits by 267,387 barrels. Allowing us to combine the throughput will glve us more freedom in fuel management while staying under the overall limit.
We request your**concur~ence** 

### Dr comments in this matter. If 

### you have any questions, please feel free to contact Jay Gupta at 777-4618.

1 

### Atch 

## JAMES R. V AN ORMAN Throughput Volumes for 

## Director 01 Environmental**~}anagem2~t** 

### 1 

### Dec 90

- 30 

### Nov 91 

## & 1 

### Jan 91

- 31 

### Dec 91



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### 4.2.4-755

### BAQE-235-91**~,**



### Don RobEinsen**'1'hrouqh~** 

## Proal Dale Chapman, Environmental Engineer**~~** 

## oatet February 13, 1992 Hill Air Force Base request for Approval Order changes

On February 5, 1992 the Division received a letter from Hill Air Force Base requesting changes to two of their existing approval orders. These changes include:



## a. Remove the perchloroethylene vapor degreaser and associated vapor chiller (this equipment has been removed) from approval order dated January 3, 1989 b. Combine the approval orders dated July 29, 1991 and January 3, 1989.



## c. Combine the JP-4 tank throughput limitations to give an annual throughput for all four tanks combined. Present approval order conditions limit throughput by ind-i vidual tank. There will not be an emission increase as a result of these changes. Therefore a Notice of Intent for these changes is not necessary. The revised approval and the current approval orders are attached for your review. By combining the two listed Approval Orders all of the four JP-4 storage tanks will be included on one permit. This is the most logical grouping and is consistent with other approval order groupings issued by the Division. Existing approval orders for the four JP-4 tanks limit throughput for each tank (condition 10 and SD existing AO). The total permitted throughput for all four tanks is presently 1,260,000 barrels per year. ...-..,

42.4-756-


### ..



### working losses from organic storage tanks are dependent upon the total number of turnovers (total throughput)r not the specific tank that is used. Therefore combined throughput limitations can be made for the four JP-4 tanks without changing the potential emissions from working losses. There should be no confusion about the meaning of "total combined throughput" for these tanks. The total combined tank throughput is the sum of individual tank throughputs. Calculation of the throughput in this manner accounts for the transfer of fuel between tanks (ie: not just the flow into or out of the tank farm). I have included condition 4b on the attached "revised" approval order which is intended to clarify the meaning of total combined throughput for these four tanks. Individual tank throughput is measured and recorded daily (condition 4F) r 

### but throughput limits are for the sum of all four tanks. All other conditions were taken from the current approval orders

.

...-,
.....



### 4.2.4-757

# '-

... 

# -- - 

# ­ DEPARTMENT OF HEALTH BAQE-324-90 

## DIVISION OF ENVIRONMENTAL HEALTH
);onn&n H. BURn.er 8u t eau 01 Air Qualltv ljowPftOr 288 Nonn 1460 West .:luz.nne Dando,.. M.D

.. M.P.H. PO 80x 16690 KrnneLh L.. Alkema

. 

# , San Lake Cllv ulan 841 16·0690 O'f"ftIDF .j IB01l5J8-<il08 

### May 23. 1990

Newspaper Agency Salt Lake Tribune Legal Advertising Department 157 Regent Street Salt Lake City, Utah 84111
Gentlemen:
This letter will confirm the authorization to publish the attached NOTICE in the Salt Lake Tribune and Deseret News on May 26, 1990. 

### Please mail the invoice and affidavit of publication to the Utah S ta te Department of Health, Division of Environmental Health. Bureau of Air Quality, 

## P.o. Box 16690. 

### Salt Lake City. Utah 84110-0690. Sincerely, 

# "\ }'\ 7-4 " /\.. (',**-',~** 

## '-
,

i \ . fl· \..,. / I**-.~** 

# -
.. .." 

### Carol Holmes Office Technician Bureau of Air Quality
Enclosure



### 4.2.4-758

### NOTICE
The following notice of**~~tent t~**  

### construc:, submitted in accordance with
Section 3.1, 

### Utah Air Conservation Regulations, has Jeen received for
consideration by the Executive Secretary, Utah Air Conservation Committee:
1. Utah Fuel Company, modification to coal storage facility at Skyline Coal Mine, Carbon**Coun~y** 

### CDS A2


### Increased emissions for this modification are calculated at the following values:
0.02 

### ton/yr**Par~ic'..llate** 

### 0.05 

### tonlyr
2.**Departmen~** 

### of the Air Force, installation of steam boilers, vapor seals for J?-4 

### storage tanks, waste hydraulic fluid reclamation units, a pain: spray booth, lab hoods, and a paint spray hangar

at Hill AFB, Davis County, CDS A 

### Increased emissions for these modifications are currently
calculated at the following values:
Part.ic'..llate 1. 

### 34 

### tons/yr
PM lO 

### 1.34 

### tons/yr
S02 10.79 

### tons!yr
NO x 

### 8.31 

### tons/yr
CO 8.60 

### tons/yr
VOC 21.47 

### tons/yr
The engineering evaluations and air quality impact analyses has been completed and no adverse air**~uality** 

### impacts are expected. :t is the intent
of the Executive Secretary to approve the constr'..lction projects.
The construction proposal and estimates of the effect on local air quality

are available for public inspection and comment at the Bureau of Air 

### Quality,
Utah State Department of Health, 288 

### North 1460 

### West, Salt Lake City. 

### 4.2.4-759 1

# .­ Utah 84116-0690. Written comments received by the Bureau. 288 North 1460
West. P.O. Box 16690. Salt Lake City. Utah 84116-0690, on or before June**~8, ~990**  

### will be considered in making the final decision on the approval or disapproval of the proposed construction.
If anyone so requests within 15 days or publication of notice. a hearing will
be held in the area of the proposed construction. installation. modification.
relocation. or establishment.
Date of Notice: May 26. 1990



### 4.2.4-760

2

### UTAH BUREAU OF AIR QUALITY NEW/MODIFIED SOURCE PLAN REVIEW

## ,~Ot-'::J~ NaeieR-G. 

### Currier Director, Environmental Mgt Office Department of the Air Force Headquarters Ogden Air Logistics Center (AFLC) Hill Air Force Base, Utah 84056 RE: 5 Projects

- Installation of Steam Boilers, Vapor Seals for JP-4 Storage Tanks, Waste Hydraulic Fluid Reclamation Units, a Paint Spray Booth, Lab Hoods, and a Paint Spray Hangar at the Hill AFB, Davis County, CDS A DATE: April 23, 1990 NOTICES OF INTENT DATED: November 7, 1989, January 19, 1989, August 9, 1989 July 18, 1898, 1989, and November :22, 

### 1989 respectively PLANT CONTACT: Jay Gupta PHONE NUMBER: 777

- 7651 PLANT LOCATION: Hill Air Force Base, Davis County FEES: Filing Fee $ 100.00 Review Engineer

- Consultant $6,660.50 Consultant $ 000.00 Modeler

- 00 hours at $18.07/hour $ 000.00 Computer Usage Fee $ 000.00 Notice to Paper $ 24.00 Travel

- 00 miles at $0.23/mile 000 00 y 

### Total $6,784. 

### SO Review Completed By Tetra Tech/L.Carl Broadhead 

## r0 APPROVALS: Engineering Unit Manager 

# OK 

# s-/sht?

c 

### Technical Evaluation Section Manager

__

# ~)~11~~.**~\42~'~_':~0~tJ~\~_~~/~t~O~!~'~1°~Z_'** __ I 

# t BACT and Approval Order Coordination with Source (Date/Contact and Agree or Disagree) 5-1-90 I 

### Bill / bv Carl B"



### 4.2.4-761

### I. 

### DESCRIPTION OF PROPOSAL
The Department of the Air Force has filed notices of intent dated November 

### i, 1988, January 19. 1989, June 16, 1989, August 11, 1989, August 30, 1989, and November 22, 1989. They are proposing to install, modify, and operate steam boilers, vapor seals for JP-4 storage tanks, waste hydraulic fluid reclamation 

### units, a paint spray booth, lab hoods, and a paint sp;-ay hangar, respective to those dates. The description of each notice of intent is as follows:

1. 

### Steam boilers, consisting of two (2) 100,000 pounds per hour, 120 psig packaged steam boilers in total heat input rate of 120.328 million Btu per hour for natural gas combustion (primary fuel) with a standby diesel fuel (116.542 million Btu per hour), to expand the existing steam plant. The location of this expansion will be in Building 260 at Hill Air Force Base. The steam generators are equipped with a flue gas recirculation system which is designed to recirculate 20 percent of exhaust gas resulting in 60 percent reduction in NOx emissions. The flue gas recirculation system is designed to operate only for natural gas combustion, not for the standby diesel fuel combustion. The steam generators are also equipped with an economizer system for an exhaust gas heat recovery. In addition. this expansion replaces 3n existing 180 gallons per minute boiler feedwater pump with a new 600 gallons per minute pump. To account for emissions from standby diesel fuel combustion in total boiler emissions, the diesel fuel utilization is assumed to be 10 percent 

### (%) of annual boiler operation. The use of diesel fuel is dependent upon the availability of natural gas. The following numbers describe the operation:
A. 

### Annual operating hours 4300 hours per year; 

## B. Total boiler capacity

- 120.328 million Btu per hour for natural gas combustion; 116.542 million Btu per hour for diesel fuel combustion; 

## C. Diesel fuel utilization 10 percent of annual boiler operation; 

## D. Flue gas recirculation 20 percent: 

## E. Nox emissions

­ 18 ppm at 100 percent boiler capacity for natural 

### gas combustion; 25 

### ppm at 25 

### percent boiler capacity for natural gas combustion: 

### F. Volume of each boiler

- 1900 cubic feet.
2. Vapor seals for JP-4 storage tanks, consisting of dual seals for tank number 10873 and 10885, to reduce fugitive VOC emissions from the tank. The location of these tanks is the tank farm at Hill Air Force Base. The installation of dual seals results in hydrocarbon emission reduction at a rate of 0.17 pound per hour or 0.73 ton per year which are requested to be banked for future offset credits.
The tank 10885 is currently operating under an approval order issued on February 15, 1978. Tank capacity is 55,000 barrels with a dimension of 93 feet diameter and 52 feet height. The proposed modification for this tank is to replace the existing aluminum pan with a ncw stecl pan and the existing single rolled rubber sectional seal with a dual seal mounted one above the other.
Tank 10873 capacity is 25,000 barrels with a dimension of 63 feet diameter and 50 feet 3 inches height. The proposed modification for this tank is to replace the existing foam log seal with a dual seal mounted one above the other.
For both tanks, the new primary seal will be a resilient foam log with impregnated fabric. The secondary seal will be rim mounted, weather guard, continuous tip, complete with



### 4.2.4-762

### compression channel, compression plate, plate gasketing and ground shunt. Seals extend continuously from the floating roof to the tank wall.
The following numbers describe the operation:
A. Annual operating hours

- 8760 hours per year B. Annual throughput

- 660,000 barrels for tank 10885 300,000 barrels for tank 10873 C. Reid vapor pressure - 3 psia
3. Bldg 514, Waste hydraulic fluid reclamation units, conslstmg of two portable hydraulic f1uid reclamation units manufactured by Pall Corporation or equivalent complete 'With vacuum process chamber, controls, and condensers, to reclaim solvent from the fluid and hence reduce hazardous wastes. This project is part of the Air Force Base Hazardous Waste Minimization Program's intent to reduce its hazardous waste disposal. These units will be initially installed in Building 514. At later time, these units will be deported to and utilized in the other locations in effort to reclaim and reduce hazardous wastes from the other locations in the base This project will reduce 95 percent of contaminants in the hydraulic f1uid waste. The contaminants of hydraulic fluid waste consist of 1,1,1 trichlorethane, freon 113, and lP-4 jet fuel. The reclamation process involves a vaporization of contaminants and then vapor condensation at the water cooled condenser. The hydraulic fluid waste contains 15 percent contamination. The condenser in the unit will recover· 95 percent of the vapor solvents. The recovered solvents will be recycled for reuse. Total process rate is 30,000 gallons of waste per year or 4,500 gallons of contaminants per year. The following numbers describe the operation:
A. Annual operating hours

- 2080 hours per year B. Annual throughput


# - 30,000 gallons C. 

### Exhaust VOC concentration

- 2.5 ppmv 

## D. Exhaust flow rate

- 20,000 cubic feet per minute 

### E. Stack height



## - 25 feet.
4. Bldg 5N, Paint spray booth and lab hoods, consisting of a 4 feet by 4 feet spray booth with the open face and two (2) 9 square feet lab hoods with the open face, to use circuit board repair and the application of conformal coating on circuit cards and to clean printed circuit boards using organic solvents. The location of this installation \vill be in Building 5 Bay K The paint spray booth is relocated from Building 214. Workload for the spray booth from Building 214 has been transferred to Building 100. The booth is equipped with dry paint arrestor filters, an exhaust fan and an 18-inch diameter vent. The hood is equifJped with exhaust plenum, fan and vent. The exhaust vents from jab hoods are combined into one (1) 

### exhaust stream. 85 percent of the solvent will be recovered and recycled. The following numbers describe the operation:
A. Annual operating hours

- 2080 hours per year
B. Annual usage rate 50 gallons per year of urethane compound 5 gallons per year of miscellaneous paint 300 gallons per year of xylene cleaning solvents

100 galJons per year of an aliphatic cleaning solvents 300 gallons per year of Isopropyl JJcohol clc3.;Jing SiJo·.**::~s** 

# c. Exhaust face velocity 100 

### feet per minute


### 3 

### 4.2.4-763D. Exhaust flow rate

- 1,600 cubic feet per minute for the spray booth 1,850 cubic feet per minute for the lab hoods (in total)
E. Stack height



## - 30 feet for the spray booth 

### 25 feet for the lab hoods.
5. Bldg 220 Paint spray hangar, consisting of modular turboclean chambers complete v,lth pumps; nozzles, associated piping, controls and sludge disposal, to modify the existing paint spray hangar. This modification is required for a replacement of corroded existing paint hangar waterfall troughs and pipings. The location of this modification 

### will be in Building 220. The aircraft paint hangar in Building 220 is 

### in existence since the 50's which does not have an air quality permit nor does it require one. In conjunction v.ith this modification, Department of the Air Force also proposes to substitute solvent base primer v,lth water reducible primer and to replace the conventional type spray gun v.ith a high volume low pressure (HVLP) type spray gun. The primer substitution and spray gun replacement will result in reductions for VOC emissions due to less solvent contained in the water reducible primer and an increase in paint transfer efficiency. The solvent content for the water reducible primer is 2.8 pounds per gallon versus 5.8 pounds per gallon for the solvent based primer. In addition, HVLP spray gun transfers efficiency is 60 to 70 percent whereas 30 to 40 percent for the conventional spray gun. The modified paint spray hangar can accommodate up to three aircrafts for painting at one time by splitting the painting areas into three using movable partitions. There will be a total of 

### 9 units including 2 exhaust fans [Ier unit. The follov.ing numbers describe the operation:
A. Annual operating hours

- 2080 hours per year
B. Annual usage rate

- 4600 gallons per year of polyurethane compound 1600 gallons per year of water reducible primer 625 gallons per year of nitrocellulose lacquer 650 gallons per year of miscellaneous


### C. Exhaust face velocity

- 100 feet per minute
D. Exhaust flow rate

- 18,500 cubic feet per minute per fan 333,000 cubic feet per minute in total


### E. Stack height - 52 feet.

II. EMISSION SUMMARY
The total emissions from sources listed in this Approval Order will be as follows: This is not a total for all sources at Hill Air Force Base. The current allowable permited emiSSIons
are not totaled at this time.
Particulate 1.34 tons/year PM,o 1.34 tons/year 

## SD.? 10.79 tons/year 

## NO. 8.31 tons/year CO 

### S.lin cons/year VOC 21. 4 7 t ons/year



### 4.2.4-764

### Hill requested banking of the emissions from the JP-4 tanks but the overal emissions from this group of sources consumed those emissions and so the banking of emissions is denied.
III. BEST AVAILABLE CONTROL TECHNOLOGY (BACf) ANALYSIS
BACf 

### will be required at all emission points. This includes the following points:
A. Boiler plant B. JP-4 storage tanks 

## C. Waste hydraulic fluid reclamation D. Paint spray booth and lab hoods E Paint spray hangar. Boiler plant
Sox and Nox emissions from the boiler plant expansion are of the highest concern.
In the event natural gas 

### is not available to Hill AFB, Department of the Air Force proposed to use the diesel fuel as standby fuel. The diesel fuel combustion contributes the majority of boiler's Sox emissions due to the high sulfur content. 10 percent of annual operating hours using diesel fuel is assumed for accounting diesel fuel combustion emissions in total boiler emissions. These Sox emissions can be eliminated or significantly reduced by utilizing as much natural gas as possible.
Various control technologies can be utilized in effort to minimize the Nox emissions from the combustion process. Control technologies are Low-Nox designed burner, flue gas recirculations, selective catalytic reduction, and selective non-catalytic reduction. Implementation of these control technologies are often not economically practical. For example, initial capital cost for selective catalytic reduction is $6,525 per million Btu-hr in 1981 dollars. In addition, operating cost for selective catalytic reduction is $870 per million Btu-hr in 1981 dollars.
The Department of the Air Force has proposed 20 percent flue gas recirculation in part of the proposed boiler plant expansion which result in 60 percent NOx emission reductions for natural gas combustion. Based on manufacture guarantee, NOx emission is 0.028 lb/million Btu, 18 ppm.
The proposed flue gas recirculation is considered as BACf. Boiler and flue gas recirculation must be properly maintained and operated in good working condition, ensuring the proposed reductions. Properly maintained and operated boiler 

### will also be beneficial to VOC and CO emissions. For diesel fuel combustion, use of fuel which meets the sulfur standards established in the UACR is required. , For fuel oils the standard is 05 

### % by 

### wt. Natural gas must be utilized in maximum; natural gas must be used as fuel whenever natural gas ,is made available at the Hill AFB.
The proposed firing of natural gas with restricted use of diesel fuel is recommended as having applied Bact for minimum emissions.
lP-4 storage tanks
lP-4 storage tanks, 10873 and 10885, are currently equipped with a single seal. In efforts to 

### reduce VOC emissions from JP-4 storage tanks for the future offset credits, the Department of the Air Force voluntarily proposed an installation of dual seals. This modification 

### is similar to a modification already made on JP-4 storage tank 10861 and 10862. The VOC reduction from the storage tanks and the hanger 221 paint booth is less than the total emissions from all sources so there are no emissions reductions of VOCs to bank.

.



### 5 

### 4.2.4-765

### BACT for the JP-4 storage tanks is proper installation, maintenance, and operation of dual seals on the lP-4 storage tanks. Dual seals must be properly maintained and kept in good condition at all times to prevent excess emissions from the lP-4 storage tanks.
These seals are recommended to be approved as having applied BACT.

Waste hydraulic fluid reclamation
A condenser for recovering 95 percent of the solvents removed from the fluid is proposed in a parr of this project. This 

### is considered as BACT for the waste hydraulic fluid reclamation. No other options were reviewed.
This process is recommended as having applied BACT.
Paint spray booth and lab hoods
VOC emISSIOns from the paint spray booth and parts cleaning under the lab hoods can be further controlled through a carbon adsorption unit. Installation of the carbon adsorption unit is not economically practical, especially with modest VOC emissions; 0.18 lb per hour for paint spray booth and 0.29 lb per hour for the lab hoods. Cost effectiveness was calculated by Hill AFB to be $48,900 per ton of 

## vec emissions. Recommended BACT for paint spray booth and lab hoods is the minimization of emissions through good operating**pra~tice.** As 

### proposed, 85 percent of solvent use in the lab should be recovered and recycled. The dip tank covers shall remain closed at all times except during actual loading, unloading or transfer operations. Parts shall be completely drained in the internal draining rack until all dripping ceases. Waste or used solvent shall be stored in covered containers and disposed of by a method which prevents its emission into the atmosphere. Tanks, .-" containers and all associated equipment shall be maintained in good operating condition and leaks shall be repaired promptly. Written procedures for the operation and maintenance of the solvent cleaning equipment are posted in an accessible and apparent location near the equipment. Paint particulate emissions from the spray booth is controlled by dry filters. All air exiting the booth shall pass through this control system before being vented into the atmosphere. The dry filter must be properly maintained and kept in good condition at all times.
The installation of filters and a limitation on the amount of paint used IS recommended as having applied BACT.
Paint spray hangar
VOC emissions from the paint spray hangar can be further reduced through a carbon adsorption unit. Installation of a carbon adsorption unit is not economically practical. Cost effectiveness was calculated by Hill AFB to be $52,480 per ton of VOC emissions and_ is considered an exceSSIve cost.
As BACT for this project, the Department of the Air Force proposed a substitution of high solvent content epoxy polyamide primer with low solvent content water reducible primer. In addition, the conventional paint spray gun is replaced with high transfer efficiency "High Volume Low Pressure" paint spray 

### gun. The paint substitution will result in 2.4 tons 

## vec emissions reduction per year.
The recommended BACT for a paint spray hangar is the use of low-VOC solvent paints and high transfer efficiency paint spray gun; this BACT control measure is already included in the proposed modification. No other options for 

## voe emissions were reviewed. Paint particulate emissions from the spray hangar is controlled by water falls. All air exiting the booth shall pass through this control

. -...


### 6 

### 4.2.4-766

### system before being vented into the atmosphere.

IV. APPLICABLE UTAH AIR CONSERVATION REGULATIONS (UACR)
These notices of intent are for modifications to an existing installation. It is nor a major modification. The following federal and state regulations have been examined to determine their applicability ro this nouce of intent:
1. 

### Section 3.1.1, UACR

- Notice of intent required for modifications. This regulation applies.
2. Section 3.1.8, UACR

- Application of best available control technology (BACT) required at all emission points. This regulation applies.
3. Section 3.1.9, UACR

- Rules for relocation of temporary sources. This source is a permanent source. Therefore, this regulation does nor apply.
4. Section 3.1.10. UACR

- Additional information requirements for a major new source or major modification which emits precursors of ozone and impact an area of nonattainment for ozone. Notices of intent do not represent a major new source or a major modification. Therefore, this regulation does not apply.


### 5. Section 3.2, UACR

- Particulate emission limitations for existing sources which are located 

### in a non-attainment area. The existing installation is listed in this regulation for 36 boilers with a limitation of 20% opacity. Therefore, this regulation does apply.
6. Section 3.3.1, UACR

- Emission limitation for a new source which is located in a non-attainment area or which impact a non-attainment area. These notices of intenr do not represent a new major source, but additional new sources at an existing installation and minor modifications. Therefore, this regulation will apply.
7. Section 3.3.2, UACR

- Review requirements for new major sources or major modifications which are located in a non-attainment area or which impact a non

### attainment area. Notices of intent do not represent a new 

### major source or a 

### major modification. Therefore, this regulation will not apply.
8. Section 3.5, UACR

- Emission inventory reporting requirements. This regulation requires any source which emits 

### 25 tons or more per year of any pollutant 

### ro submir an emission inventory to the Bureau of Air Quality every year. This source musr comply with this regulation.
9. Section 3.6.5(b), UACR

- Prevention of significant deterioration (PSD) review requirements for new major sources or major modifications. Notices of intent do nor represent a major source or a major modification under PSD rules. Therefore, rhis regulation does nor apply.



# -,­ 10. Section 3.8, UACR

- Stack height rule. This regulation limits the creditabk height cf stacks to that**heigh~** 

### determined to 

### b:**go~d er:g:ncc~in;**  

### practic:.**T!~c L::~::::..:!2.S**  7 

### 4.2.4-767used to determine good engineering practice are found in 40 CFR 51.1. A de minim us height of 65 meters (213.2 feet) is allowed. These notices of intent do not have stacks which exceed 65 meters in height. It is in compliance with this regulation.
11. Section 3.11, UACR

- Visibility screening analysis requirements. This regulation requires all new major sources or major modifications to undergo a visibility screening analysis to determine visibility impact on any mandatory Class I area. Notices of intent do not represent a new major source or a major modification under UACR rules. Therefore, this regulation does not apply.
12. Section 4.1.2, UACR

- 20% opacity limitation at all emission points unless a more stringent limitation 

### is required by New Source Performance Standards (NSPS) or BACT or National Emission Standards for Hazardous Air Pollutants (NESHAPS). BACT will require a lower limitation than 

### 20%, therefore, this regulation does not apply.
13. Section 4.1.9, UACR

- EPA Method 9 to be used for visible emission observations. This regulation applies.
14. Section 4.2.1, UACR

- Sulfur content limitations in oil and coal used for combustion

.

. This source burns fuel oil. The limitation is 0.85 pounds of sulfur per 1cP BTU heat input. This regulation applies, howevcr, BACT for diesel oil limits sulfur to a lower value. 

### 15. Section 4.7, UACR

- Unavoidable breakdo\\'I1 reporting requirements. This regulation applies.
16. Section 4.9, UACR

- Review requirements for volatile organic compound (VOC)
sources located in a non-attainment area for ozone. This regulation covers the following processes:
A. Petroleum liquid storage B. Petroleum liquid transfer/storage 

### C. Control of hydrocarbon emiSSions In refineries 1) vacuum producing systems 2) wastewater separators 3) process unit turnaround 4) catalytic cracking units 5) safety pressure relief valves 6) leaks from petroleum refinery equipment D. Degreasing and solvent cleaning operations 1) cold cleaning facilities 2) open top vapor degreasers 

### 3) conveyorized degreasers E. Cutback asphalt F. VOC used for various processes 1) paper coating 2) fabric and vinyl coating 

### 3) metal furniturc coating 

### 4) large 3f)f)liancc surfac**~o3ting** 5) magnct wire coating 6) 

### QaL wood 

### ..:ua'ing


### 8 

### 4.2.4-768

### 7) misc. metal parts and products 8) graphic arts 

### G. Synthesized pharmaceutical manufacturing 

### H. Perchlorethylene dry cleaning plants.
This source is located in a non-attainment area for ozone as defined in the State Implementation Plan. The proposed modification includes petroleum liquid storage and cold solvent cleaning which are subject to this regulation. The provisions pertaining to petroleum liquid storage applies to Subpart Kb to 

### the proposed modification due to the true vapor pressure of stored liquid 1.3 psia. This regulation applies for the cold solvent cleaning operation. This source must comply 'With this regulation.
17. Section 5, UACR

- Emergency episode requirements. This regulation applies.
18. National Emission Standards for Hazardous Air Pollutants (NESHAPS)

- There IS 

### no NESHAPS for these notices of intent.
19. National Ambient Air Quality Standards (NAAQS)

- This source is located in a nonattainment area for ozone. The Bureau of Air Quality guidelines do not call for this source to be modeled for any pollutants. The Bureau has found through experience that, because of the small increase in quantity of emissions involved and the conservative predictions made by modeling, a source or emission point of this small increase is very unlikely to cause a new violation of the NAAQS.
20. New Source Performance Standards (NSPS)

- The NSPS which apply to these notices of intent is the NSPS Kb for petroleum liquids storage vessels. The vapors pressure and capacity parts of Kb make it applicable to the storage tanks.

V. RECOMMENDED APPROVAL ORDER CONDITIONS

1. 

### Department of the Air Force, located at Hill Air Force Base, shall install. modify, and operate the steam generators, dual vapor seals on JP-4 storage tank 10873 and 10885, waste hydraulic fluid reclamation units, a paint spray booth, lab hoods, .and a paint spray hangar according to the information submitted in the notices of intent dated November 7, 1988, January 19, 1989, June 16, 1989, August 11, 1989, August 30, 1989, and November 22, 1989, respectively, and the additional information submitted to the Executive Secretary dated February 2, 1989, January 10, 1990.
2. The approved installation shall consist of the following equipment:
A. 

### Two (2) steam generators, a total heat input rate of 120.328 million Btu/hr with natural gas as primary fuel with a standby diesel fuel (116.542 million Btu/hr) at the Building 260;
B. 

### Dual seals for JP-4 storage tank 10873 and 10885;


## c. ,We) 

### (2) waste hydraulic fluid reclamation units at the Building 514;


### .:J.**:';;.:::~** 

### 3p:-ay oooth and two (2) lab hoods at the Building 5 N;

9 

### 4.2.4-769

## E. Nine (9) Turboclean chambers for the paint spray hangar at Building 220. In addition, 

## .­ solvent base primer shall be substituted for water reducible primer and a high volume low pressure (HVLP) type spray gun shall replace the conventional paint spray gun.

3. VISible emISSIOns from any point or fugitive emission source associated with the installation shall not exceed 10% opacity. Opacity observation of emissions from stationary sources shall 

### be conducted 

### in accordance with 40 CFR 

### 60, Appendix A, Method 9.
4. The following operation limits shall not be exceeded without prior approval In 

### accordance with Section 3.1, UACR:
A. Steam generators


### 1. 

### 465.7 billion Btu of natural gas per 12 month period 2. 

### 1083 million Btu of natural gas per hour 3. 50.1 billion Btu of diesel fuel per 12 month period 4. 116.5 million Btu of diesel fuel per hour 5. 4,300 hours per 12 month period


### B. JP-4 storage tank 

### 10873
1. 300,000 barrels per 12 month period 2. 24 hours per day 3. 

### 8,760 hours per 12 month period


## c. JP-4 storage tank 

### 10885
1. 660,000 barrels per 12 month period 2. 24 hours per day 3. 

### 8,760 hours per 12 month period
D. Hydraulic fluid waste reclamation units


### 1. 30,000 gallons of total fluid per 12 month period 2. 8 hours per day 3. 2,080 hours per 12 month period
E. Paint spray booth


### 1. 50 gallons of urethane per 12 month period 2. 5 gallons of miscellaneous per 12 month period 3. 8 hours per day 4. 2,080 hours per 12 monlh period
F. Lab hoods


### 1. 200 gallons of xylene per 12 month period 2. 100 gallons of naphtha aliphatic per 12 month period 3. 

### 300 gallons of isopropyl alcohol per 12 month period 4. 

### 8 hours per day 

### 5. 2,080 hours per 12 mc::.th period

10


### 4.2.4-770

### G. Paint spray hangar
1. 

### 4600 gallons of polyurethane per 12 month period 2. 1600 gallons of water reducible primer per 12 month period 3. 625 gallons of nitrocellulose lacquer per 12 month period 4. 650 gallons of miscellaneous per 12 month period 5. 8 hours per day 6. 2,080 hours per 12 month period. Compliance with the limitation shall be determined on a rolling monthly total. On the first day of each month a new 12-month total shall be calculated using the previous 12 months. Records of production shall be kept for all periods when the plant is in operation. Records of production shall be made available to the Executive Secretary or his representative upon request, and shall include a period of two years ending with the date of the request. Fuel consumption for steam generators shall be determined by the use of records from a fuel meter. VOC emissions shall be determined by maintaining a record of paints, solvents, and lP-4 

### fuel used. The records shall be kept on a daily basis. Hours of operation shall be determined by supervisor monitoring and maintaining of an operations log.
5. The condenser at the final point of hydraulic fluid waste reclamation units shall be in operation during the operation of hydraulic fluid waste reclamation units. 

### If the condenser is out of service, the hydraulic fluid waste reclamation units shall not be used until the condenser has been returned to service. The condenser shall be capable of recovering 95 percent of solvents from the fluid. Records of solvent recovery shall be kept for all periods when the hydraulic fluid waste reclamation units are in operation. The record shall include the following items:
A. 

### Date B. Unit usage (start and end times) C. 

### Total hydraulic fluid waste processed D. Amount solvent recovered.
Records of treatment shall be made available to the Executive Secretary upon request and shall include a period of time equal to the entire duration of the project.
6. The owner/operator shall use only natural gas as a primary fuel and #2 diesel fuel as a backup fuel in the steam generators. If any other fuel is to be used, an approval order shall be required in accordance with Section 3.1, UACR. Natural gas consumption shall not exceed 465.7 million frJ of natural gas per 12 month period and diesel fuel consumption shall nO[ exceed 5% of the annual fuel used in the boilers without prior approval in accordance with Section 3.1, UACR. Compliance with the limitation shall be determined on a rolling monthly total. On the fIrst day of each month a new 12-month total shall be calculated using the previous 12 months. Records of fuel consumption shall be kept for all periods when the plant is 

### in operation. Records of fuel consumption shall be made available to the Executive Secretary upon request, and shall include a period of two years ending with the date of the request. Fuel consumption shall be determined by the use of records from the fuel meter.
7. The sulfur content of any diesel fuel burned shall not exceed 0.5 

### % by weight of sulfur determined by ASTM Method D-4294-89. The sulfur content shall be tested if directed bv the Executive Secretary.
8. The paint spray booth at Building 5N shall be equipped with a set of paint arrestor particulate

11


### 4.2.4-771

# - m.ters to control particulate emISSIons. All 

### air exiting the booth shall pass through this control system before being vented into the atmosphere.

9. 

### The paint spray hangar at Building 220 

### shall be equipped with a water wall to control particulate emissions. All 

### air exiting the booth shall pass through this control system before being vented to the atmosphere.
10. The following density and volatile organic content of paint shall not be exceeded without prior approval in accordance with Section 3.1, 

### UACR:
A. 

### Paint spray booth
Paint Density 

### Clbs/gallon) 

## vec (% 

### bv Vol) Urethane 

### 8.5 

### 80 Miscellaneous 6.0 

### 100
B. Paint spray hangar
Paint Density Clbs 

### Iga lion) 

## vec Clbs/gallon) Polyurethane 9.2 4.7 

### Epoxy Polyamide Primer 

### 10.5 5.8 Water Reducible Primer 

### 8.9 2.8 

### Nitrocellulose 

### 8.0 4.8 Miscellaneous 9.0 6.0


### These parameters shall be tested 

### if directed by the Executive Secretary using the appropriate ASTM method or another method approved by the Executive Secretary.
11. The owner/operator shall operate a solvent cleaning operation under the lab hoods in the following manners:


### A. Cover shall remain closed at all times except during actual loading, unloading or transfer operations;


### B. Parts shall be completely drained 

### in the internal draining rack until all dripping ceases;


### C. Waste or used solvent shall be stored in covered containers and disposed of by a method which prevents its emission into the atmosphere;
D. Tanks, containers and all associated equipment are maintained In 

### good operating condition and leaks are repaired immediately; and
E. Written procedures for the operation and maintenance of the solvent cleaning equipment are posted in an accessible and apparent location near the equipment.
12. Eighteen months from the date of this approval order the Executive Secretary shall be notified in writing of the status of construction of these projects unless the construction is com plete and operation has commenced.
13. A copy of this approval order shall be maintained on-site and available to the operators of the equipment.


### 12 

## 4.2.4-772

### 14. 

### All installations and facilities authorized by 

### this approval order shall be adequately and properly maintained.
15. The Executive Secretary shall be notified 

### in writing upon start-up of the installations, as an initial compliance inspection is required. Any future modifications to the equipment approved by this order must also be approved In 

### accordance with Section 3.1.1, UACR.
This approval order in no way releases the owner or operat<;>r from any liability for compliance v.;th all other applicable federal, state, and local regulations including the Utah Air Conservation Regulations.
"Allowable emissions" as defined in Section 1.12, UACR, for point sources listed 

### in this Approval Order are calculated at 1.34 tons/yr for particulates, 1.34 tons/yr for PM,o, 10.79 tons/yr for**S~,** 

### 8.31 tons/yr for NO., 8.60 tons/yr for CO, and 21.47 tons/yr for VOC. These calculations are for the purposes of determining the arplicabiliry of PSD and non-attainment area major source requirements of the UACR. They are not to be used for purposes of determining compliance.
LCB /Hill-ALL.ENG

13 

### 4.2.4-773.OLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: DATE: TIME: NET FEB-21-90 10:07 AM

SOURCE: NET EMISSION INCREASE ESTIMATE COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

SOURCE 

### voe NOX SOX 

### eo PM10 TSP UNIT

PRE-MODIFICATION •.•••••.•.••.• POST-MODIFICATION .••••.•..••.. 22.52 21.47 2.64 8.31 3.43 10.79 2.73 8.60 0.43 1.34 0.43 1.34 TONS/YR TONS/YR

NET EMISSION INCREASE ••...•.•. ·1.05 5.67 7.36 5.87 0.91 0.91 TONS/YR

SOUCE INCLUDED: TOTAL PRE-MODIFICATION EMISSION ESTIMATE TOTAL POST-MODIFICATION EMISSION ESTIMATE



# -

-
4.2.4-774.wLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: DATE: TIME: NET ,EB-21-90 10:07 AM

SOURCE: TOTAL PRE-MODIFICATION COMPANY NAME: DEPT. OF THE AIR LOCATION: HILL AFB EMISSION FORCE ESTIMATE

SOURCE VOC NOX SOX CO PM10 TSP UNIT

REPLACEMENT BOILERS

- 260 ...•.. SEALS ON JP-4 TANKS .•.•..••....**~ASTE** HYD FLUID RECLAIM -514 ••. CLEANING HOODS/PAINT BOOTH

- 5N PAINT HANGER MODIFICATION

- 220 0.21 2.32 0.00 0.00 19.99 2.64 3.43 2.73 0.43 0.43 TONS/YR TONS/YR TONS/YR TONS/YR TONS/YR

TOTAL .........••..•..•....••.. 22.52 2.64 3.43 2.73 0.43 0.43 TONS/YR

SOUCE INCLUDED:**~ACEMENT** BOILERS

- 260**~S** ON JP-4 TANKS

wASTE HYD FLUID RECLAIM -514 CLEANING HOODS/PAINT BOOTH

- 5N PAINT HANGER MODIFICATION

- 220



### 4.2.4-775

# -

JLLED AND UNCONTROLLED EMISSION ESTIHATES FOR: FILE: DATE: TIME: NET FEB·21·9D 10:07 AM

SOURCE: TOTAL POST-MODIFICATION EMISSION COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB ESTIMATE

SOURCE VOC NOX SOX CO PM10 TSP UNIT

REPLACEMENT BOILERS' 260 ••.... SEALS ON JP-4 TANKS .••...•.••.• WASTE HYD FLUID RECLAIM -514

... CLEANING HOODS/PAINT BOOTH

- 5N PAINT HANGER MODIFICATION

- 220 0.67 1.59 1.13 0.49 17.59 8.31 10.79 8.60 1.34 1.34 TONS/YR TONS/YR TONS/YR TONS/YR TONS/YR

TOTAL .....•.•..•......•.•••... 21.47 8.31 10.79 8.60 1.34 1.34 TONS/YR

SOUCE INCLUDED:

REPLACEMENT BOILERS

- 260

, ON JP-4 TANKS

HYD FLUID RECLAIM ·514 CLEANING HOODS/PAINT BOOTH

- 5N PAINT HANGER MODIFICATION

- 220 

# .-.

..



### 4.2.4-776ROLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: DATE: TIME: BOILER FEBUARY 20, 12:10 PM 1990

SOURCE: TOTAL EMISSION ESTIMATE (90"4 NATURAL COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- STEAM PLANT GAS**~ITH** 10% DIESEL FUEL FIRED)

CONTROLLED UNCONTROLLED

POLLUTANT LBS/HR HOORLY GRAMS/SEC TONS/YR ANNUAL GRAMS/SEC % CNTRL LBS/HR TONS/YR
TOTAL PARTICULATE ••••••.•••. PM-10

............................................ SOx ..........••.•.•••••••.•. NOx •••....•.•••••••••••••.•. CO •.••..•.•.•..••••..••••••• VOC, NON·METHANE .•••.••••••. 

### vec, METHANE. .•..••••...•••. 2.27 2.27 99.13 20.02

8.37 0.50 0.40 0.29 0.29 12.49 2.52 1.06 0.06 0.05 1.34 1.34 10.79 8.31 8.60 0.67 0.70 0.04 0.04 0.31 0.24 0.25 0.02 0.02 0.00 0.00 0.00 60 OR 0 0.00 0.00 0.00 2.27 2.27 99.13 20.02

8.37 0.50 0.40 1.34 1.34 10.79 8.31 8.60 0.67 0.70

SOURCE: NATURAL GAS DIESEL FUEL FIRED FIRED BOILER BOILER (90%) (10%)



### 4.2.4-777JLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: DATE: TIME: BOILER FEBUARY 20, 12:10 PM 1990

SOURCE: NATURAL GAS FIRED BOILER (90X) COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

. STEAM PLANT

CONTROLLED UNCONTROLLED

POLLUTANT LBS/HR HOURLY GRAMS/SEC TONS/YR ANNUAL GRAMS/SEC % CNTRL LBS/HR TONS/YR
TOTAL PARTICULATE ••••••••••• PM·10



### ........................................... SOx •••....•..••.•••.••..•... NOx ••••.•••.•...•••••••••••• CO •••....•••.••....••.••.... VOC, NON-METHANE •••.•••••••. VOC, METHANE .....••..•••.••• 0.60 0.60 0.07 3.37 4.21 0.34 0.36 0.08 0.08 C.Ol 0.42 0.53 0.04 0.05 1. 16 1.16 0.14 6.52 8.15 0.65 0.70 0.03 0.03 0.00 0.19 0.23 0.02 0.02 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.60 0.60 0.07 3.37 4.21 0.34 0.36 1. 16 1. 16 0.14 6.52 8.15 0.65 0.70

AP-42 FOURTH EDITION SEPT. 1985 VOLUME SECTION 1 EXTERNAL COMBUSTION SOURCES**'~TURAL** GAS COMBUSTION 1.4-1 UNCONTROLLED EMISSION FACTORS**~uc~** TYPE: NATURAL GAS FOR NATURAL GAS COMBUSTION

EMISSION FACTOR IN LB PER MILLION CUBIC FEET
TOTAL PARTICULATE ..•........ PM- 10 .........••..•.•...... SOx •..............•......... NOx •.•..•..........•••.•..•. CO •..............•.•.•••.••• VOC, NON-METHANE ...•.•..•••. VOC, METHANE ••..••••.••••.•• 5.0'0 5.00 0.60 0.03 35.00

2.80 3.00 LB/MM LB/MM LB/MM LB/MM LB/MM LB/MM LB/MM FT3 FT3 FT3 BTU FT3 FT3 FT3 TABLE 1.4-' TABLE 1.4-1 TABLE 1.4-1 BOILER MANUF. TABLE 1.4-1 TABLE 1.4-1 TABLE 1.4-1
TOTAL POYER RATING •.••.•.• HOURLY FUEL CONSUMPTION

... ANNUAL FUEL CONSUMPTION •.. OPERATING FACTOR

. 120328.00 0.12 465.67

90 K BTU/HR MM FT3/HR MM FT3/YR

% FROM NOI (TOTAL POYER RATINGl/(1000 BTU/FT3)/(MM) (TOTAL POYER RATINGl/(1000 BTU/FT3)/(MMl* (ANNUAL OPERATING HOURl*(OPERATING FACTOR) FROM NOI, DEPENDING ON THE AVAILABILITY OF NATURAL GAS
HOURS OF OPERATION

HOURS PER DAy ....••..•.•.. DAYS PER YEEK •.•.•.•...••. YEEKS PER yEAR

. HOURS PER yEAR ........•... 4300.00 HRS/DAY DAYS/YEEK IJEEKS/YR

HRS/YR FROM NOI



# -

4.2.4-778)LLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: BOILER DATE: FEBUARY 20, 1990 TIME: 12: 10 PM

SOURCE: DIESEL FUEL FIRED BOILER (10%) COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

. STEAM PLANT

CONTROLLED UNCONTROLLED
HOURLY ANNUAL POLLUTANT LBS/HR GRAMS/SEC TONS/YR GRAMS/SEC 

### % CNTRL LBS/HR TONS/YR
TOTAL PARTICULATE •••••.••.•• 1.66 0.21 0.18 0.C1 0.00 1.66 0.18 PM-10

.......................................... 1.66 0.21 0.18 0.01 0.00 1.66 0.18 SOx ......•...........•....•. 99.06 12.48 10.65 0.31 0.00 99.06 10.65 NOx ..•.•.••...••.••..•..••.• 16.65 2. I0 1.79 0.05 0.00 16.65 1. 79 CO .•.....• : ..•••.••••..•.••. 4.16 0.52 0.45 0.01 0.00 4.16 0.45 VOC, NON-METHANE .........•.. 0.17 0.02 0.02 0.00 0.00 O. i 7 0.02 VOC, METHANE. .....•...•••••. 0.04 0.01 0.00 0.00 0.00 0.04 0.00

AP-42 FOURTH EDITION SEPT. 1985 VOLUME SECTION 1 EXTERNAL COMBUSTION SOURCES ,'--­ 'UEL OIL COMBUSTION 1.3-1 UNCONTROLLED EMISSION FACTORS FOR FUEL OIL COMBUSTION

.• L TYPE: DIESEL FUEL #2

EMISSION FACTOR IN LB PER THOUSAND GAL
TOTAL PARTICULATE. •........• 2.00 LB/K GAL TABLE 1.3-1 PM -1 0 .•••.••••••••••.•••••• 2.00 LB/K GAL TABLE 1.3-1 SOx .................•....... 0.85 LB/MM BTU SECTION 4.2 OF UACR NOx ;
. 20.00 LB/K GAL TABLE 1.3-1 CO ...........•.••..•........ 5.00 LB/K GAL TABLE 1.3-1 voe, NON-METHANE ••..•......• 0.20 LB/K GAL TABLE 1.3-1 VOC, METHANE.

. 0.05 LB/K GAL TABLE 1.3-1

TOTAL POI.JER RATING .•.•.•.. 116542.00 K BTU/HR FROM NOI HOURL Y FUEL CONSUMPTION •.. 0.83 K GAL/HR (TOTAL POI.JER RATING)/(0.14 MM BTU/GAL)/(1000) ANNUAL FUEL CONSUMPT I ON •.• 178.98 K GAL/YR (TOTAL POI.JER RATING)/(0.14 MM BTU/GAL)/(1000)* (ANNUAL OPERATING HOUR)*(OPERATING FACTOR) OPERATING FACTOR .••....... 5 % FROM NOI, DEPENDING ON THE AVAILABILITY OF NATURAL GAS
HOURS OF OPERATION

HOURS PER DAy

............. HRS/DAY DAYS PER IJEEK ....•........ DAYS/IJEEK IJEEKS PER yEAR ........•... IJEEKS/YR HOURS PER yEAR

............ 4300.0C HRS/YR FROM NOI



## 4.2.4-779**~OLLED** AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: DATE: TIME: JP-4 FEB-14-90 9:00 AM

SOURCE: NET EMISSION ESTIMATE COMPANY NAME: DEPT. OF THE AIR LOCATION: HILL AFB

- TANK FARM FORCE

CONTROLLED UNCONTROLLED

POLLUTANT LBS/HR HOURLY GRAMS/SEC TONS/YR ANNUAL GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC VOC non non METHANE MATHANE (PRE-MOO) " (POST-MOO)

. 0.53 0.36 0.07 0.05 2.32 1.59 0.07 0.05 0.00 0.00 0.53 0.36 2.32 1.59
NET EMISSION -0.17 -0.02 -0.73 -0.02 0.00 -0. '7 -0.73

SOUCE INCLUDED: TOTAL PRE-MODIFICATION EMISSION ESTIMATE TOTAL POST-MODIFICATION EMISSION ESTIMATE



### 4.2.4-780**~OLLED** AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: DATE: TIME: JP-4 FEB-14-90 9:00 AM

SOURCE: TOTAL PRE-MODIFICATION COMPANY NAME: DEPT. OF THE AIR LOCATION: HILL AFB

- TANK FARM EMISSION FORCE ESTIMATE

CONTROLLED UNCONTROLLED

POLLUTANT LBS/HR HOURLY GRAMS/SEC TONS/YR ANNUAL GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 0.53 0.07 2.32 0.07 0.00 0.53 2.32

SauCE INCLUDED:
TANK 10873

- SINGLE SEAL TANK 10885

- SINGLE SEAL



### 4.2.4-781.OLLED AND UNCONTROLLED EMISSION ESTIMATES FOR:

SOURCE: TANK 10873

- SINGLE SEAL COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- TANK FARM

HOURLY POLLUTANT LBS/HR GRAMS/SEC
VOC 

### non METHANE 0.12 0.02

AP-42 FOURTH EDITION SEPT. 1985 VOLUME SECTION 4 EVAPORATION LOSS SOURCES 4.3 STORAGE OF ORGANIC LIQUIDS EQUATION 3 TOTAL LOSSES FROM FLOATING ROOF TANKS PAINT TYPE: INTERNAL FLOOTING ROOF

LBS/YR = EOUATION 3 FROM PG. 4.3-15
LOSS ...•..•••..•.•••• 1090.55 LBS/YR
LR (RIM SEAL LOSS) 

## = EQUATION 4 FROM PG. 4.3'16
LR •..••...•.•..•••• .••••••• 418.53 LBS/YR
KS ....•••••••.••••..•• 3.00

V ••••••••••••••••••••• 8.00 MPH 

### n
. 0.00 P ••••••••••••••••••••• 0.03

D ••••••••••••••••••••• 63.00 FEET MV •......• ....••

_ ..
_ .. 80.00 LB/LB-MOLE KC •.••...•••.•••.••••
. 1.00
LIJ .•.••.••••..•••.•.••• •..• 43

_ 11 LBS/YR



### o
..
_ ............•••... 300000.00 BBL/YR C ••••••••••••••••••••• 0.0015 bbl/ft 2 IJL . _ ......•••.

_ ..•.... 6.40 LBS/GAL D ••••••••••••••••

_ •••• 63.00 FEET NC ...•..•.•••.•.•• ..•. 0.00 Fe •.

_ ••••••••••••••••• 1.00

L r ...............•.•.••...• 628.91 LBS/YR

FF ••••••••••••••

_ ••••• 284.00 LB-M/FT YR 

# -
FILE: JP-4 DATE: FEB-14'90 TIME: 9:00 AM

CONTROLLED UNCONTROLLED
ANNUAL TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR
0.55 0.02 0.00 0.12 0.55

LR+LIJ+LF+LD

SEAL FACTOR (LS-MOLE/CFT"(MI/HR)'N"YR», FRO"'. TAaLE 4.3-4

­ LIQUID MOUNTEO RESILIENT SEAL IJITH RIM MOUNTED SECONDARY SEAL AVERAGE IJIND SPEED AT TANK SITE, FROM NOI SEAL RELATED IJIND SPEED EXPONENT (PT/PA)/CC1+Cl-PT/PA)AO.5)A2) PT 

## = TRUE VAPOR PRESSURE (1.3 PSIA), FROM FIGURE 4.3-6 PA 

## = AVERAGE ATMOSPHERIC PRESSURE C12.4 PSIA), FROM NOI TANK DIAMETER, FRMO NOI AVERAGE VAPOR MOLECULAR IJEIGHT, FROM NOTE 1 OF EQUATION PRODUCT FACTOR, FROM NOTE 3 PG. 4.3-16 «0.943)"O"C"IJL/D)"(1+(NC"FC/D»
THROUGHPUT (bbl/year), FROM NOI SHELL CLINGAGE FACTOR (bbl/l000 ft2), AP-42 TABLE 4_3-5 AVERAGE ORGANIC LIQUID DENSITY (LB/GAL), FROM AP-42, TABLE 4.3,2 TANK DIAMETER, FRMO NOI NUMBER OF COLUMN, NOTE 3 PG. 4.3-19 EFFECTIVE COLUMN DIAMETER, NOTE 4 PG. 4.3-19
FF"D"P"MV"KC
TOTAL DECK FITTING LOSS FACTOR


### 4.2.4-782p .••••••••••••••••••••

MV .•.•••••••.•.••..... KC 0.03

80.00

1.00 L8/L8-MOLE (LB-MOLE/FEET YEAR), FROM NOI (NF1*KF1)+(NFZ*KFZ) ••.. + (NFN*KFN) (PT/PA)/«1+(1-PT/PA)AO.5)AZ) PT 

## = TRUE VAPOR PRESSURE (1.3 PSIA), FROM FIGURE 4.3-6 PA 

## = AVERAGE ATMOSPHERIC PRESSURE (1Z.4 PSIA), FROM NOI AVERAGE VAPOR HOLECULAR WEIGHT, FROM NOTE 1 OF EQUATION PRODUCT FACTOR, FROM NOTE 3 PG. 4.3-16
LD ••.•....•••..••••••••••.• 0.00 LBS/YR
KD .••..••.•.••..•••.•.

SD ...•..•.........••.. 

### o ...........•..•...... P •••••••••••••••••••••

MV ......•......•...... KC 0.00

O.ZO 93.00

0.03

80.00

1.00 L8-M/FT YR

FT/FT2 FEET

L8/L8-HOLE DECK SEAM LOSS PER UNIT SEAM LENGTH FACTOR WELDED DECK (LB'MOLE/FEET YEAR), FROM Ap·4Z, PG. 4.3-Z5 DECK SEAM LENGTH FACTOR (FT/FTZ), FROM AP-4Z, FG. 4.3-25 TANK DIAMETER, FRMO NOI (PT/PA)/«1+(1-PT/PA)AO.5)AZ) PT = TRUE VAPOR PRESSURE (1.3 PSIA), FROM FIGURE 4.3,6 PA 

### = AVERAGE ATMOSPKERIC PRESSURE (1Z.4 PSIA), FROM NOI AVERAGE VAPOR MOLECULAR WEIGHT, FROM NOTE 1 OF EQUATION PRODUCT FACTOR, FROM NOTE 3 PG. 4.3-16

HOURS OF OPERATION
HOURS PER DAy· ..•.•••.•..... DAYS PER**~EEK** ..•..••••.•.•.**~EEKS** PER YEAR .•.•••••..•.. ".-., PER YEAR

. 24 7 5Z 8736 HOURS/DAY DAYSNEEK WEEKS/YEAR HOURS/YEAR FRCt1 NOI FRCt1 NOI FRCt1 NO! (HOURS/DAY)*(DAYS/WEEK)*(IJEEKS/YEAR)

•
. 

# ",,­

4.2.4-783,LLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: JP-4 OATE: FEB-14-90 TIME: 9:00 AM

SOURCE: TANK 10885

- SINGLE SEAL COMPANY NAME: OEPT. OF THE AIR FORCE LOCATION: HILL AFB

- TANK FARM
CONTROLLED UNCONTROLLED
HOURL Y ANNUAL POLLUTANT LBS/HR GRAMS/SEC TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 0.41 0.05 1. 78 0.05 0.00 0.41 1.78

Ap·42 FOURTH EDITION SEPT. 1985 VOLUME SECTION 4 EVAPORATION LOSS SOURCES 4.3 STORAGE OF ORGANIC LIQUIDS EQUATION 3 TOTAL LOSSES FROM FLOATING ROOF TANKS PAINT TYPE: INTERNAL FLOOTING ROOF

LBS/YR 

## = EQUATION 3 FROM PG. 4.3-15
LOSS •.•••••••.

_ •••••• 3550.32 LBS/YR LR+LI./+LF+LD
LR (RIM SEAL LOSS) 

## = EQUATION 4 FROM PG. 4.3-16
LR •••.•••.•••.••••••••••••• 1379.83 LBS/YR**KS*V~n*P*D*HV*KC** KS ....•••..•••••..•••• 6.70 SEAL FACTOR**(LB-MOLE/(FT*(MI/HR)~N*YR»,** FROH TABLE 4.3·4

­ LIQUID HOUNTED RESILIENT SEAL \.11TH RIM MOUNTED SECONDARY SEAL V ••••••••••••••••••••• 8.00 MPH AVERAGE \.lIND SPEED AT TANK SITE, FROM NOI
n ••.•.•••• ••

_ •••

_ •• 0.00 SEAL RELATED \.ICND SPEED EXPONENT P ••.•••••••••••••••••• 0.03**(PT/PA)/«1+(1-PT/PA)~0.5)~2)** PT 

## = TRUE VAPOR PRESSURE (1.3 PSIA), FROM FIGURE 4.3-6 PA 

## = AVERAGE ATMOSPHERIC PRESSURE (12.4 PSIA), FROM NOI D ••••••••••••••••••••• 93.00 FEET TANK DIAMETER, FRMO NOI MV

....
_ .•••.

_ ..••••••• 80.00 LB/LB-MOLE AVERAGE VAPOR MOLECULAR \.lEIGHT, FROM NOTE 1 OF EQUATION KC ....••••••••••••••.• 1.00 PROOUCT FACTOR, FROM NOTE 3 PG. 4.3-16

UJ .••.•••.••••••• _. _ ••••.•• 64.25 LBS/YR «0.943)*Q*C*\.IL/D)*(1+(NC*FC/D»

Q ••• - •••••••••

_ ••••••• 660000.00 BBL/YR THROUGHPUT (bbl/year), FROM NOI C ••••••••••••••••••••• 0.0015 bbl/ft 2 SHELL CLINGAGE FACTOR (bbl/100D ft2), AP-42 TABLE 4.3-5 I./L ....•.•••.•••.•.•.•. 6.40 LBS/GAL AVERAGE ORGANIC LIQUID DENSITY (LB/GAL), FROM AP-42, TABLE 4.3-2 D •••••••••• _• _ ••••

_ ••• 93.00 FEET TANK DIAMETER, FRHO NOI NC ...•..••.....••••.•. 0.00 NUMBER OF COLUMN, NOTE 3 PG. 4.3-19 FC .•...•..•••••••.•••. 1.00 EFFECTIVE COLUMN DIAMETER, NOTE 4 PG. 4.3-19

LF ••••••••••••••••••••••••• 803.85 LBS/YR FF*D*P*MV*KC

.= F •••••••••••••••••••• 363.00 LB-M/FT YR TOTAL DECK FITTING LOSS FACTOR



### 4.2.4-784P •••••••••••••••••••••

MV .....•.••••••••.••.. KC
LO .•••••.••••••••••••.....•
KD •••.•••••.••••••••••



### so •••••••••••••••••••• 

### o ••..••••••.•••••.••.• P •••••••••••••••••••••

MV •••••••••••••••••••• KC .•..••••••••••.•....

HOURS OF OPERATION
HOURS PER DAy •.••.••••••.•
. DAYS PER IJEEK ••••.••.•••.•• IJEEKS PER YEAR ••••••.••••••

.. - .. .,S PER YEAR ••••.•.•.••.. ,"'---'.'. 0.03

80.00

1.00
1302.40
0.34
0.20 93.00

0.03

80.00

1.00

24

7 52 8736 LB/LB-MOLE

LBS/YR
LB-M/FT YR
FT/FT2 FEET

LB/LB-MOLE

HOURS/DAY OAYS/IJEEK IJEEKS/YEAR HOURS/YEAR (LS-MOLE/FEET YEAR), FROM NOI (NF1*KF1)+(NF2*KF2) •••• + (NFN*KFN) (PT/PA)/«1+(1-PT/PA)AO.5)A2) PT 

## = TRUE VAPOR PRESSURE (1.3 PSIA), FROM FIGURE 4.3-6 PA 

## = AVERAGE ATMOSPHERIC PRESSURE (12.4 PSIA), FROM NOI AVERAGE VAPOR MOLECULAR \.lEIGHT, FROM NOTE 1 OF EQUATION PRODUCT FACTOR, FROM NOTE 3 PG. 4.3-16

DECK SEAM LOSS PER UNIT SEAM LENGTH FACTOR (LS-MOLE/FEET YEAR), FROM Ap·42, PC. 4.3-25 DECK SEAM LENGTH FACTOR (FT/FT2), FROM AP-42, PG_ 4.3-25 TANK DIAMETER, FRMO NOI (PT/PA)/«1+(1-PT/PA)AO.5)A2) PT 

## = TRUE VAPOR PRESSURE (1.3 PSIA), FROM FIGURE 4.3-6 PA 

## = AVERAGE ATMOSPHERIC PRESSURE (12.4 PSIA), FROM NOI AVERAGE VAPOR MOLECULAR IJEIGHT, FROM NOTE 1 OF EQUATION PRODUCT FACTOR, FROM NOTE 3 PG. 4.3-16

FROM NOI FROM NOI FROM NOI (HOURS/DAY)*(DAYS/IJEEK)*(IJEEKS/YEAR)



### 4.2.4-785**~OLLED** AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: DATE: TIME: 

## o o o

SOURCE: TOTAL POST-MODIFICATION EMISSION COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- TANK FARM ESTIMATE

CONTROLLED UNCONTROLLED

POLLUTANT LBS/HR HOORLY GRAMS/SEC TONS/YR ANNUAL GRAMS/SEC %**C~TRL** LBS/HR TONS/YR
VOC non METHANE 0.36 0.05 1.59 0.05 0.00 0.36 1.59

SauCE INCLUDED:
TANK 10873

- DUAL SEAL TANK 10885

- DUAL SEAL



### 4.2.4-786JLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: JP-4 DATE: FEB-14-90 TIME: 9:00 AM

SOURCE: TANK 10873

- DUAL SEAL COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- TANK FARM
CONTROLLED UNCONTROLLED
HOURLY ANNUAL POLLUTANT LBS/HR GRAMS/SEC TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR

VOC non METHANE 0.09 0.01 0.40 0.01 0.00 0.09 0.40

AP-42 FOURTH EDITION SEPT. 1985 VOLUME SECTION 4 EVAPORATION LOSS SOURCES 4.3 STORAGE OF ORGANIC LIQUIDS EQUATION 3 TOTAL LOSSES FROM FLOATING ROOF TANKS PAINT TYPE: INTERNAL FLooTING ROOF

LBS/YR 

### = EQUATION 3 FROM PG. 4.3,15
LOSS .•••••.•••••••••• 791.15 LBS/YR LR+L'oJ+LF+LD (RIM SEAL LOSS) = EQUATION 4 FROM PG. 4.3-16
LR ....•..•.••.••.••..•..•.• 223.22 LBS/YR KS*VAn*P*D*MV*KC
KS .•...•...•.•...•.••• 1.60 SEAL FACTOR (LB-MOLE/(FT*(MI/HR)AN*YR», FROM TABLE 4.3-4

­ LIQUID MOUNTED RESILIENT SEAL**~ITH** RIM MOUNTED SECONDARY SEAL V ••••••••••••••••••••• 8.00 MPH AVERAGE 'WIND SPEED AT TANK SITE, FROM NOI
n
. 0.00 SEAL RELATED**~IND** SPEED EXPONENT P ••••••••••••••••••••
_ 0_03 (PT/PA)/(1+(1-PT/PA)AO.5)AZ) PT = TRUE VAPOR PRESSURE (1.3 PSIA), FROM FIGURE 4.3-6 PA 

## = AVERAGE ATMOSPHERIC PRESSURE (12.4 PSIA), FROM NOI D ••••••••••••••••••••• 63.00 FEET TANK DIAMETER, FRMO NOI MV ..............•..••. 80.00 LB/LB-MOLE AVERAGE VAPOR MOLECULAR**~EIGHT,** FROM NOTE 1 OF EQUATION KC .•......••.......•.. 1.00 PRODUCT FACTOR, FROM NOTE 3 PG. 4.3-16
L'W

_ _ . 43.11 LBS/YR «0.943)*Q*C*'WL/D)*(1+(NC*FC/D»

Q

. 300000.00 BBL/YR THROUGHPUT (bbL/year), FROM NOI C ••••••••••••••••••••• 0.0015 bbL/ft 2 SHELL CLINGAGE FACTOR (bbL/1000 ft2), AP-42 TABLE 4.3-5 'WL •.....•........•.... 6.40 LBS/GAL AVERAGE ORGANIC LIQUID DENSITY (LB/GAL), FROM AP-42, TABLE 4.3-2 D ••••••••••••••••••••• 63.00 FEET TANK DIAMETER, FRMO NOI NC ............•....... 0.00 NUMBER OF COLUMN, NOTE 3 PG. 4.3-19 FC ............•••..•.. 1.00 EFFECTIVE COLUMN DIAMETER, NOTE 4 PG. 4.3-19
LF ...............•.•...•... 524.83**~BS/YR** FF*D*P*MV*KC

F F

.. 237.00 LB'M/FT YR TOTAL DECK FITTING LOSS FACTOR 

### 4.2.4-787P .••••••••••••••••••••

MV .....•••••••••.••••• KC 0_03

80.00

1.00 LB/LB-MOLE (LB-MOLE/FEET YEAR), FROM NOI (NF1*KF1)+(NF2*KF2) •••• + (NFN*KFN) (PT/PA)/((1+(1-PT/PA)AO.5)A2) PT 

## = TRUE VAPOR PRESSURE (1.3 PSIA), FROM FIGURE 4.3-6 PA = AVERAGE ATMOSPHERIC PRESSURE (12.4 PSIA), FROM NOI AVERAGE VAPOR MOLECULAR**~EIGHT,** FROM NOTE 1 OF EQUATION PRODUCT FACTOR, FROM NOTE 3 PG. 4.3-16 1·

LD .•••.•.•••••••••.•••••••• 0.00 LBS/YR
KD ••.•••••••••••••••.•



### so •...•••••••••••••••• 

### o ........•••...•••••.. P •••••••••••••••••••••

MV ...••••••••••••••••. KC 0.00

0.20 63.00

0.03

80.00

1.00 LB-M/FT YR

FT /FT2 FEET

LB/LB·MOLE DECK SEAM LOSS PER UNIT SEAM LENGTH FACTOR \lElDEO SEAM (LB-MOLE/FEET YEAR), FROM AP-42, PG. 4.3-25 OECK SEAM LENGTH FACTOR (FT/FT2), FROM AP-42, PG. 4.3-25 TANK DIAMETER, FRMO NOI (PT/PA)/((1+(1-PT/PA)AO.5)A2) PT 

### = TRUE VAPOR PRESSURE (1.3 PSIA), FROM FIGURE 4.3-6 PA 

## = AVERAGE ATMOSPHERIC PRESSURE (12.4 PSIA), FROM NOI AVERAGE VAPOR MOLECULAR**~EIGHT,** FROM NOTE 1 OF EQUATION PRODUCT FACTOR, FROM NOTE 3 PG. 4.3-16

HOURS OF OPERATION
HOURS PER DAY .•.......•••.. DAYS PER**~EEK** .••.•••••••••. ,"",cKS PER YEAR ..••••••••••• ) PER YEAR •••.••••••••• 24 7 52 8736 HOURS/DAY**DAYS/~EEK ~EEKS/YEAR**  HOURS/YEAR FROM NO! FROM NOI FROM NOI**(HOURS/DAY)*(DAYS/\lEEK)*(~EEKS/YEAR)** 

# -

4.2.4-788JLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: Jp-4 DATE: FEB-14-90 TIME: 9:00 AM

SOURCE: TANK 10885

- DUAL SEAL COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- TANK FARM
CONTROLLED UNCONTROLLED
HOURLY ANNUAL POLLUTANT LBS/HR GRAMS/SEC TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 0.27 0_03 1.20 0.03 0.00 0.27 1.20

AP-42 FOURTH EDITION SEPT. 1985 VOLUME 1 SECTION 4 EVAPORATION LOSS SOURCES 4.3 STORAGE OF ORGANIC LIQUIDS EQUATION 3 TOTAL LOSSES FROM FLOATING ROOF TANKS PAINT TYPE: INTERNAL FLOOTING ROOF

LBS/YR 

## = EQUATION 3 FROM PG. 4.3-15
LOSS .•••••••••..•••.. 2395.92 LBS/YR LR+LI.'+LF+LD (RIM SEAL LOSS) 

## = EQUATION 4 FROM PG. 4.3-16
LR .........••..• •..•..•.•.• 329.51 LBS/YR**KS"V~n"P"D"MV"I(C** KS ....•...••••.•.•...• 1.60 SEAL FACTOR**(LB-MOLE/(FT"(MI/HR)~N"YR»,** FROM TABLE 4.3'4

­ LIQUID MOUNTED RESILIENT SEAL IIITH RIM MOUNTED SECONDARY SEAL 

### v ...........•......... 8.00 MPH AVERAGE I.'IND SPEED AT TANK SITE, FROM NOI
n .•.•••.••••••••.••••• 0.00 SEAL RELATED IIIND SPEED EXPONENT P ••••••••••••••••••••• 0.03**(PT/PA)/«1+(1-PT/PA)~0.5)~2)** PT 

## = 'TRUE VAPOR PRESSURE (1.3 PSIA), FROM FIGURE 4.3-6 PA 

## = AVERAGE ATMOSPHERIC PRESSURE (12.4 PSIA), FROM Nor 

### o
. 93.00 FEET TANK DIAMETER, FRMO NOI MV ......••.•• .•...•... 80.00 LB/LB-MOLE AVERAGE VAPOR MOLECULAR I.'EIGHT, FROM NOTE 1 OF EQUATION ICC .......•.. ..•...•... 1.00 PRODUCT FACTOR, FROM NOTE 3 PG. 4.3-16
LII •........••..••.••.....•
. 64.25 LBS/YR «0.943)"Q"C"IIL/D)"C1+(NC"FC/D»

Q ••••••••••••••••••••• 660000.00 BBL/YR THROUGHPUT (bbl/year), FROM NOI C ••••••••••••••••••••• 0.0015 bbl/ft 2 SHELL CLlNGAGE FACTOR (bbl/1000 ft2), AP-42 TABLE 4.3·5 ilL •••••••••••••••••••• 6.40 LBS/GAL AVERAGE ORGANIC LIQUID DENSITY (LB/GAL), FROM AP-42, TABLE 4.3,2 D ••••••••••••••••••••• 93.00 FEET TANK DIAMETER, FRMO NOI NC _ . 0.00 NUMBER OF COLUMN, NOTE 3 PG. 4.3-19 FC

.. _ _ ...•... .•.•.• 1.00 EFFECTIVE COLUMN DIAMETER, NOTE 4 PG. 4.3'19
LF

_ ..••....... 699.77 LBS/YR FF"D"P"MV"ICC

: F •••••••

_ •••••••••••• 316.00 LB-M/FT YR TOTAL DECK FITTING LOSS FACTOR


### 4.2.4-789P •••••••••••••••••••••

MV ...••.•.•.••••.••••. KC
LD ...••...••.•.••.•. •.•...•
KD •••.•••••••••••••••.


### so .•••••••••.••••••••• 

### o ..•..••..••.•... .•... P •••••••••••••••••••••

MV •....•....••..••• ..• KC

HOURS OF OPERATION
HOURS PER DAY ••••••••••.••• DAYS PER UEEK •.••.••.•..•
..**~JrrKS** PER YEAR •••••••••••••

. PER YEAR ....•....••.. 0.03

80.00

1.00
1302.40
0.34
0.20 93.00

0.03

80.00

1.00

24

7 52 8736 LB/LB-MOLE

LBS/YR
LB-M/FT YR
FT/FT2 FEET

LB/LB'MOLE

HOURS/DAY DAYS/UEEK UEEKS/YEAR HOURS/YEAR (LB-MOLE/FEET YEAR), FROM NOl (NF1*KF1)+(NF2*KF2) •... + (NFN*KFN) (PT/PA)/«1+(1-PT/PA)AO.5)A2) PT = TRUE VAPOR PRESSURE (1.3 PSlA), FROM FIGURE 4.3-6 PA = AVERAGE ATMOSPHERIC PRESSURE (12.4 PSIA), FROM NOI AVERAGE VAPOR MOLECULAR UEIGHT, FROM NOTE 1 OF EQUATION PRODUCT FACTOR, FROM NOTE 3 PG. 4.3-16

DECK SEAM LOSS PER UNIT SEAM LENGTH FACTOR (LB-MOLE/FEET YEAR), FROM AP-42, PG. 4.3-25 DECK SEAM LENGTH FACTOR (FT/FT2), FROM AP-42, PG. 4.3-25 TANK DIAMETER, FRMO NOI (PT/PA)/«1+(1-PT/PA)AO.5)A2) PT 

### = TRUE VAPOR PRESSURE (1.3 PSIA), FROM FIGURE 4.3-6 PA 

## = AVERAGE ATMOSPHERIC PRESSURE (12.4 PSlA), FROM NOZ .AVERAGE VAPOR MOLECULAR UEIGHT, FROM NOTE 1 OF EQUATION PRODUCT FACTOR, FROM NOTE 3 PG. 4.3-16

FROM NOI FROM NOl FROM NOl (HOURS/DAY)*(DAYS/UEEK)*(UEEKS/YEAR)



### 4.2.4-790,OLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: DATE: TIME: S14 FES-14-90 9:00 AM

SOURCE: HYDRAULIC FLUID WASTE RECLAMATION UNITS COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING S14
CONTROLLED UNCONTROLLED

POLLUTANT LSS/HR HOURLY GRAMS/SEC TONS/YR ANNUAL GRAMS/SEC % CNTRL LBS/HR TONS/YR

VOC non METHANE 1.D8 0.14 1.13 0.03 9S.00 21.63 22.S0

ION FACTORS (IN LBS/GAL) COMMENTS

VOC non METHANE ••••...•....•.• .•••••• 10.00 LBS/GAL FROM NOI

TOTAL WASTE FLUID PROCESSED IN YEAR

.. 30000.00 GAL/YR FROM NOI. TOTAL IJASTE FLUID INCLUDED CONTAMINATION AND OTHER FLUIDS PERCENTAGE OF CONTAMINATION
........... 1S.00 % FROM NOI

CONTAMINATION PROCESSED IN HOUR 2.16 GAL/HR (CONTAMINATION PROCESSED IN YEAR)/(ANNUAL OPERATING HOURS) CONTAMINATION PROCESSED IN YEAR 4S00.00 GAL/YR (TOTAL IJASTE FLUID PROCESSSED IN YEAR)* (PERCENTAGE OF CONTAMINANTS)

HOURS OF OPERATION
HOURS PER DAY 8 HOURS/DAY FROM NOI**~AYS** PER WEEK 5 DAYS/WEEK FROM NOI WEEKS PER YEAR 52 IJEEKS/YEAR FROM NOI .• - ) PER YEAR 2080 HOURS/YEAR (HOURS/DAY)*(DAYS/IJEEK)*(IJEEKS/YEAR)



### 4.2.4-791.OLLED AND UNCONTROLLED EHISSION ESTIMATES FOR: FILE: 514

DATE: TIME: FEB-14-90 9:00 AM

SOURCE: VOC PPM CALC. FOR HYDRALIC FLUID COMPANY NAME:' DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 514 WASTE RECLAMATION UNITS

POLLUTANT VOC
LB/HR ...........•...

_ .•.
_ LBS/LB MOLE

_ ..•.
_ CONSTANT _. _ .

.

. 1.08 139.00
60.00 FROM CALCS ABOVE LBS/LB MOLE
MIN/HR
FLOIJ RATE ..........•.•..........•.•.. CONSTANT .......•..••••............... 20000.00 0.00259 DSCF/MIN LB MOL/DSCF
LB/MIN 

## = (LB/HR)/(60 MIN.HR)
0.02
PPM (LB/MIN)/«DSCF/HIN)(LB HOLE/DSCF)(LB/LB**MOLE)(1/lX10~6))** 2.50 PPMV



### 4.2.4-792JLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: DATE: TIME: 5N FEB-14-90 9:00 AM

SOURCE: TOTAL PAINT SPRAY BOOTH EMISSION COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 5N ESTIMATE

CONTROLLED UNCONTROLLED

POLLUTANT LBS/HR HOURLY GRAMS/SEC TONS/YR ANNUAL GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 0.18 0.02 0.18 0.01 85.00 0.18 0.18

SOUCE INCLUDED:
URETHANE MI SCELLANEOUS



### 4.2.4-793JLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: 5N DATE: FEB-14-90 TIME: 9:00 AM

SOURCE: URETHANE COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

. BUILDING 5N
CONTROLLED UNCONTROLLED
HOURLY ANNUAL POLLUTANT LBS/HR GRAMS/SEC TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 0.16 0.02 0.17 0.00 0.00 0.16 0.17

AP-42 FOURTH EDITION SEPT. 1985 VOLUME SECTION 4 EVAPORATION LOSS SOURCES 4.2 SURFACE COATING TABLE 4.2.2.1-1 VOC EMISSIONS FOR UNCONTROLLED SURFACE COATING PAINT TYPE: CONVENTIONAL**~L** OF VOC 

## = VOC, vol % FROM PG. 4.2.2.1-3 COMMENTS
VOC non METHANE •••••.••.••• 6.80 LBS/GAL V(%)*(COATING DENSITY)/100 V(%) •...•••••••.•••••• 80.00 % FROM NOI COATING DENSITy .•.•••• 8.50 LBS/GAL FROM NOI

GALlHR 0.02 GAL/HR (GAL/YR)/(HOURS/DAY)/(DAYS/UEEK)/(UEEKS/YR) GAL/YR 50.00 GAL/YR FROM NOI

HOURS OF OPERATION
HOURS PER DAY ..•.....•. ••.. 8 HOURS/DAY FROM NOI DAYS PER UEEK ...•.... .••... 5 DAYS/UEEK FROM NOI UEEKS PER YEAR

. 52 UEEKS/YEAR FROM NOI HOURS PER YEAR •............ 2080 HOURS/YEAR (HOURS/OAY)*(OAYS/UEEK)*(UEEKS/YEAR)



### 4.2.4-794JLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: 5N DATE: FEB-14-90 TIME: 9:00 AM

SOURCE: MISCELLANEOUS COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 5N

CONTROLLED UNCONTROLLED
HOORLY ANNUAL POLLUTANT LBS/HR GRAMS/SEC TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 0.01 0.00 0.01 0.00 0.00 0.01 0.01

LBS/GAL OF VOC 

## = VOC CONTENTS OF COATING COMMENTS
VOC non METHANE 6.00 LBS/GAL FROM NOI
VOC CONTENT •........... 6.00 LBS/GAL FROM NOI

GAL/HR 0.00 GAL/HR (GAL/YR)/(HOORS/DAY)/(DAYS/WEEK)/(IJEEKS/YR) GAL/YR 5.00 GAL/YR FROM NOI

HOURS OF OPERATION
HOURS PER DAy .........•.... 8 HOURS/DAY FROM'NOI DAYS PER WEEK .....•...••... 5 DAYS/WEEK FROM NOI WEEKS PER YEAR ....•....••.. 52 IJEEKS/YEAR FROM NOI HOURS PER YEAR

. 2080 HOORS/YEAR (HOORS/DAY)*(DAYS/IJEEK)*(IJEEKS/YEAR)



### 4,2.4-795OLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: DATE: TIME: 5N FEB-14-90 9:00 AM

SOURCE: TOTAL LAB HOODS EMISSION ESTIMATE COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 5N
CONTROLLED UNCONTROLLED

POLLUTANT LBS/HR HCURLY GRAMS/SEC TONS/YR ANNUAL GRAMS/SEC t CNTRL LBS/HR TONS/YR
VOC non METHANE 0.29 0.04 0.31 0.01 85.00 1.97 2.04

SOUCE INCLUDED:
XYLENE NAPTHA ALIPHATIC ISOPROPHYL ALCOHOL



### 4.2.4-796JLLED AND UNCONTROLLED EMISSION ESTIMATES FOR:

SOURCE: XYLENE COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 5N

HOURLY POLLUTANT LBS/HR GRAMS/SEC
VOC non METHANE 0.01 O. "

LBS/GAL OF VOC = SOLVENT DENSITY,

VOC non METHANE •.....•..... 7.34 lBS/GAL
SOLVENT DENSiTy ..•..... 7.34 LBS/GAL

,{ 

## . 0.10 GAL/HR ""L/YR 200.00 GAL/YR

HOURS OF OPERATION
HOURS PER DAy ..•...••.• .•.. 8 HCXJRS/DAY DAYS PER WEEK •••••••••..... 5 DAYS/WEEK WEEKS PER YEAR ..•.....•.... 52 WEEKS/YEAR HOURS PER YEAR ........•••.. 2080 HOURS/YEAR FILE: 5N DATE: FEB'14-90 TIME: 9:00 AM

CONTROLLED UNCONTROLLED
ANNUAL TONS/YR GRAMS/SEC**~:** CNTRL LBS/HR TONS/YR 

### 0." 0.00 85.00 0.71 0.73

COMMENTS
SOLVENT DENSITY
FROM CHEMICAL ENGINEERING HANDBOOK

(GAL/YR)/(HOURS/DAY)/(DAYS/WEEK)/(WEEKS/YR) FROM NOI

FROM NO! FROM NO! FROM NO! (HCXJRS/DAY)*(DAYS/WEEK)*(WEEKS/YEAR)



### 4.2.4-797JLLED AND UNCONTROLLED EMISSION ESTIMATES FOR:

SOURCE: NAPTHA ALIPHATIC COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 5N

HOURLY POLLUTANT LBS/HR GRAMS/SEC
VOC non METHANE 0.05 0.01

LBS/GAL OF VOC 

# = SOLVENT DENSITY

VOC non METHANE 6.40 LBS/GAL
SOLVENT DENSITy .••••••• 6.40 LBS/GAL

0.05 GAL/HR 100.00 GAL/YR

HOURS OF OPERATION
HOURS PER DAy .••••••••..••• 8 HOURS/DAY DAYS PER IJEEK ....••.•••.... 5 DAYS/IJEEK IJEEKS PER YEAR .••....... •.. 52 IJEEKS/YEAR HOURS PER YEAR .......•..•.• 2080 HOURS/YEAR FILE: 5N DATE: FEB-14-90 TIME: 9:00 AM

CONTROLLED UNCONTROLLED
ANNUAL TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR
0.05 0.00 85.00 0.31 0.32

COMMENTS
SOLVENT DENSITY
FROM AP-42 TABLE 4.3-2, JET NAPTHA

(GAL/YR)/(HOURS/DAY)/(DAYS/IJEEK)/(IJEEKS/YR) FROM NOI

FROM NOI FROM NOI FROM NOI (HOURS/DAY)-(DAYS/IJEEK)-(IJEEKS/YEAR)



### 4.2.4-798)LLED AND UNCONTROLLED EMISSION ESTIMATES FOR:

SOURCE: ISOPROPHYL ALCOHOL COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 5N

HOURLY POLLUTANT LBS/HR GRAMS/SEC
VOC non METHANE 0.14 0.02

LBS/GAL OF VOC 

## = SOLVENT DENSITY

VOC non METHANE .•..•..... •. 6.60 LBS/GAL
SOLVENT DENSiTy •.....•. 6.60 LBS/GAL

0.14 GAL/HR _/YR 300.00 GAL/YR

HOURS OF OPERATION
HOURS PEK DAY ......•.•..... 8 HOURS/DAY DAYS PER**~EEK** ......•..•.•.. 5 DAYS/IJEEK**~EEKS** PER YEAR •.•...••
..... 52 IJEEKS/YEAR HOURS Pb< YEAr<

. .::060 HOURS/YEAR FILE: 5N DATE: FEB·14·90 TIME: 9:00 AM

CONTROLLED UNCONTROLLED
ANNUAL TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR
0.15 0.00 85.00 0.95 0.99

COMMENTS
SOLVENT DENSITY
FROM CHEMICAL ENGINEERING HANDBOOK**(GAL/YR)/(HOURS/DAY)/(DAYS/~EEK)/(~EEKS/YR)** FROM NOI

FROM NOI FROM NOI FROM NOI (HOURS/DAY)-(DAYS/IJEEK)-(IJEEKS/YEAR)



### 4.2.4-799

# -- ;OLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: DATE: TIME: 220 FEB- 14-90 9:00 AM

SOURCE: NET EMISSION ESTIMATE COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 220
CONTROLLED UNCONTROLLED

POLLUTANT LBS/HR HOORLY GRAMS/SEC TONS/YR ANNUAL GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC VOC non non METHANE MATHANE (PRE-MOO) " (POST-MOO) • 19.22 16.91 2.42 2.13 19.99 17.59 0.57 0.51 0.00 0.00 19.22 16.91 19.99 17. ,9
NET EMISSION -2.31 -0.29 -2.40 -0.07 0.00 -2.31 -2.40

SauCE INCLUDED: TOTAL PRE-MooIFICATION EMISSION ESTIMATE TOTAL POST-MooIFICATION EMISSION ESTIMATE



# -

-
4.2.4-800,(OLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: DATE: TIME: 220 FEB-14-90 9:00 AM

SOURCE: TOTAL PRE-MODIFICATION EMISSION ESTIMATE COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 220
CONTROLLED UNCONTROLLED

POLLUTANT LBS/HR HOURLY GRAMS/SEC TONS/YR ANNUAL GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 19.22 2.42 19.99 0.57 0.00 19.22 19.99

SOUCE INCLUDED:
POLYURETHANE EPOXY POLYAMIDE PRIMER NITROCELLULOSE LACQUER MISCELLANEOUS (1600 AND 375 GALLONS/YEAR)



### 4.2.4-801JLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: 220 DATE: FEB-14-90 TIME: 9:00 AM

SOURCE: EPOXY POLYAMIDE PRIMER COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 220

CONTROLLED UNCONTROLLED
HOORLY ANNUAL POLLUTANT LBS/HR GRAMS/SEC TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 4.46 0.56 4.64 0.13 0.00 4.46 4.64

AP-42 FOURTH EDITION SEPT. 1985 VOLUME SECTION 4 EVAPORATION LOSS SOURCES 4.2 SURFACE COATING TABLE 4.2.2.1-1 VOC EMISSIONS FOR UNCONTROLLED SURFACE COATING PAINT TYPE: CONVENTIONAL

LBS/GAL OF VOC 

## = VOC CONTENTS OF COATING COMMENTS
VOC non METHANE ....••...... 5.80 LBS/GAL FROM NOI

V(%) •••••••••••••••••• % COATING DENSITy .•••••. 10.50 LBS/GAL FROM NOI

GAL/HR 0.77 GAL/HR**(GAL/YR)/(HOURS/DAY)/(DAYS/~EEK)/(~EEKS/YR)** GAL/YR 1600.00 GAL/YR FROM NOI

HOURS OF OPERATION
HOURS PER DAY ....•..••..... 8 HOURS/DAY FROM NO! DAYS PER**~EEK** .......•...... 5**DAYS/~EEK** FROM NO!**~EEKS** PER YEAR ••..•••••.••• 52**~EEKS/YEAR** FROM NOI HOURS PER YEAR ...••••••...• 2080 HOURS/YEAR**(HOURS/DAY)*(DAYS/~EEK)*(~EEKS/YEAR)**



### 4.2.4-802.OLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: DATE: TIME: 220 FEB-14-90 9:00 AM

SOURCE: TOTAL POST-MODIFICATION EMISSION ESTIMATE COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

. BUILDING 220
CONTROLLED UNCONTROLLED

POLLUTANT LBS/HR HOORLY GRAMS/SEC TONS/YR ANNUAL GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 16.91 2.13 17.59 0.51 0.00 16.91 17.59

SOUCE INCLUDED:
POLYURETHANE EPOXY POLYAMIDE PRIMER (375 GALLONS/YEAR)**~ATER** REDUCIBLE PRIMER NITROCELLULOSE LACQUER MISCELLANEOUS



### 4.2.4-803JLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: 220 DATE: FEB-14-90 TIME: 9:00 AM

SOURCE: POLYURETHANE COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 220
CONTROLLED UNCONTROLLED
HOURL Y ANNUAL POLLUTANT LBS/HR GRAMS/SEC TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 10.39 1.31 10.81 0.31 0.00 10.39 10.81

AP-42 FOURTH EDITION SEPT. 1985 VOLUME SECTION 4 EVAPORATION LOSS SOURCES 4.2 SURFACE COATING TABLE 4.2.2.1-1 VOC EMISSIONS FOR UNCONTROLLED SURFACE COATING PAINT TYPE: CONVENTIONAL**~L** OF VOC 

## = VOC CONTENTS OF COATING COMMENTS
VOC non METHANE •••••••••••• 4.70 LBS/GAL FROM NOI

V(%) •••••••••••••••••• % COATING DENSiTy ••••••• 9.20 LBS/GAL FROM NOI

GAL/HR 2.21 GAL/HR**(GAL/YR)/(HOURS/DAY)/(DAYS/~EEK)/(~EEKS/YR)** GAL/YR 4600.00 GAL/YR FRO'1 NOI

HOURS OF OPERATION
HOURS PER DAy ....•..•. •.••. 

## -s HOURS/DAY FRO'1 NOI DAYS PER**~EEK** .••.•••••••••• 5**DAYS/~EEK** FROM NOI IIEEKS PER YEAR .....•••••..• 52**~EEKS/YEAR** FROM NOI HOURS PER YEAR ••.....•.•
... 2080 HOURS/YEAR**(HOURS/DAY)~(DAYS/~EEK)~(UEEKS/YEAR)**



## .-..,

..


### 4.2.4-804JLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: 220 DATE: FEB-i4-90 TIME: 9:00 AM

SOURCE: EPOXY POLYAMIDE PRIMER COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 220

CONTROLLED UNCONTROLLED
HOORLY ANNUAL POLLUTANT LBS/HR GRAMS/SEC TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 1.05 0.13 1.09 0.03 0.00 1.05 , .09

Ap·42 FOURTH EDITION SEPT. 1985 VOLUME 1 SECTION 4 EVAPORATION LOSS SOURCES 4.2 SURFACE COATING TABLE 4.2.2.1-1 VOC EMISSIONS FOR UNCONTROLLED SURFACE COATING PAINT TYPE: CONVENTIONAL**_~/GAL** OF VOC 

## = VOC CONTENTS OF COATING COMMENTS
VOC non METHANE ••••.•••••.. 5.80 LBS/GAL FROM NOI

V(%) •••••••••••••••••• % COATING DENSiTY ......• 10.50 LBS/GAL F.<OM NO]

GAL/HR 0.18 GAL/HR (GAL/YR)/(HOURS/DAY)/(DAYS/WEEK)/(WEEKS/YR) GAL/YR 375 .00 GAL/YR FROM NOI

HOURS OF OPERATION
HOURS PER DAy .......•...••. 8 HOURS/DAY FROM NOI DAYS PER WEEK .••••••••••.•• 5**DAYS/~EEK** FROM NOI WEEKS PER YEAR •••••.••.•••
. 52**~EEKS/YEAR** FROM NOI HOURS PER YEAR •••.•.....••
. 2080 HOURS/YEAR**(HOURS/DAY)~(DAYS/WEEK)~(WEEKS/YEAR)**



### 4.2.4-80510LLED AND UNCONTROLLED EMISSiON ESTIMATES FOR: FILE: 220 DATE: FEB-14-90 TIME: 9:00 AM

SOURCE: YATER REDUCIBLE PRIMER COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 220

CONTROLLED UNCONTROLLED
HOURLY ANNUAL POLLUTANT LBS/HR GRAMS/SEC TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 2.15 0.27 2.24 0.06 0.00 2.15 2.24**AP-~2** FQC:':7r. E:;:7:0:; SE?T. 1ge5 V::;:"UHE SECTION 4 EVAPORATION LOSS SOURCES 4.2 SURFACE COATING TABLE 4.2.2.1-1 VOC EMISSIONS FOR UNCONTROLLED SURFACE COATING PAINT TYPE: CONVENTIONAL**~g~/GAL** OF VOC : VOC CONTENTS OF COATING COMMENTS
VOC non METHANE •.•••••••••• 2.80 LBS/GAL FROM NOI

V(%) •••••••••••••••••• % COATING DENSITy ••••••• 8.90**LSS/G':'~**

GAL/HR 

## o.n GAL/HR (GAL/YR)/(HOURS/DAY)/(DAYS/YEEK)/(YEEKS/YR) GAL/YR 1600.00 GAL/YR FROM NOI

HOURS OF OPERATION
HOURS PER DAy

. 8 HOURS/DAY FROM NO! DAYS PER YEEK ...••..•....•• 5 DAYS/YEEK FROM NOI YEEKS PER YEAR .•••••••••••. 52 YEEKS/YEAR FROM NOI HOURS PER YEAR

. 2080 HOURS/YEAR (HOURS/DAY)*(DAYS/YEEK)*(YEEKS/YEAR)



### 4.2.4-806**.~** ILLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: 220 DATE: FEB- 14·90 TIME: 9:00 AM

SOURCE: NITROCELLULOSE LACQUER COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

. BUILDING 220

CONTROLLED UNCONTROLLED
HOURLY ANNUAL POLLUTANT LBS/HR GRAMS/SEC TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 1.44 0.18 1.50 0.04 0.00 1.44 1.50

Ap·'2**FOURT~ EDITIO~**  SEDT.**'o~5** VOLUM! 1 SECTION 4 EVAPORATION LOSS SOURCES 4.2 SURFACE COATING TABLE 4.2.2.'-' 

### voe EMISSIONS FOR UNCONTROLLED SURFACE COATING PAINT TYPE: CONVENTIONAL

,GAL OF VOC VOC CONTENTS OF COATING COMMENTS
VOC non METHANE .•..•••.••.• 4.80 LBS/GAL FRctI NOI VC%) ••..••••••.•••.•.. %**:OhiI~~ D~~~ITY**  .•.•••• O.CO**LBS/(j,,~** ;:ROM NOI

GAL/HR 0.30 GAl/HR**CGAL/YR)/(HOURS/DAY)/CDAYS/~EEK)/(~EEKS/YR)** GAl/YR 625.00 GAl/YR fROI'I NOI

HOURS OF OPERATION
HOURS PER DAy .•.•.•.•...... 8 HOURS/DAY FROM NO! DAYS PER IJEEK ••.•••..•••..• 5 DAYS/IJEEK FROI'I NOI**~EEKS** PER YEAR •••.•••.•..•• 52 IJEEKS/YEAR FRctI NOI HOURS PER YEAR ..•....• ••..• 2080 HOURS/YEAR (HOURS/DAY)-CDAYS/IJEEK)-CIJEEKS/YEAR)



### 4.2.4-807:OLLED AND UNCONTROLLED EMISSION ESTIMATES FOR: FILE: 220 DATE: FEB-14-90 TIME: 9:00 AM

SOURCE: MISCELLANEOUS COMPANY NAME: DEPT. OF THE AIR FORCE LOCATION: HILL AFB

- BUILDING 220

CONTROLLED UNCONTROLLED
HOORLY ANNUAL POLLUTANT LBS/HR GRAMS/SEC TONS/YR GRAMS/SEC % CNTRL LBS/HR TONS/YR
VOC non METHANE 1.88 0.24 1.95 G.06 0.00 1.88 1.95

AP-l.2 FOURTH EDITION SEPT. 1985**VO:"U~~::** 1 SECTION 4 EVAPORATION LOSS SOORCES 4.2 SURFACE COATING TABLE 4.2.2.'-1 VOC EMISSIONS FOR UNCONTROLLED SURFACE COATING PAINT TYPE: CONVENTIONAL**~u~/GAL** OF VOC 

## = VOC CONTENTS OF COATING COMMENTS
VOC non METHANE ..•..•.••... 6.00 LBS/GAL FROM NOI

V( %) •••••••••••••••••• %**CGAT[~G** DENSITy ..••... 9.00 LilS/GAL ,ROM tWI

GAL/HR 0.31 GAL/HR**(GAL/YR)/(HOURS/DAY)/(DAYS/~EEK)/(~EEKS/YR)** GAL/YR 650.00 GAL/YR FROM NOI

HOURS OF OPERATION
HOURS PER DAY .•••.•....•. •. 8 HOURS/DAY FROM NOI DAYS PER**~EEK** ...•.•.... ..•. 5**DAYS/~EEK** FROM NOI**~EEKS** PER YEAR .••••••..•••• 52**~EKS/YEAR** FROM NOI HOURS PER YEAR .••.•.••••••• 2080 HOORS/YEAR**(HOURS/DAY)*(DAYS/~EEK)*(~EEKS/YEAR)**



### 4.2.4-808**P.ECEiV~D** 

### : -,**~~/..J** 

### UNITED STATES ENVIRONMENTAL PROTECTION AGENCY 

## J**lJ)~** 

# 20 1990 

# .- REGION VIII 999 18th STREET

- SUITE 500 DENVER, COLORADO 80202-2405



### Ref: 8AT-AP Mr. David Kopta Engineering Unit Manager Bureau of Air Quality Utah Department of Health P.O. Box 16690 Salt Lake City, Utah 84116-0690 Dear Dave: Upon review of the May 22, 1990, Notice of Intent to approve five projects at Hill Air Force Base (Installation of Steam Boilers, Vapor Seals for JP-4 STorage Tanks, Waste Hydraulic Fluid Reclamation Units, a Paint Spray Booth, Lab Hoods, and a Paint Spray Hanger), EPA has the following comments: 1. The proposed approval order Condition 4.G, for the paint spray hanger at building 220, should include the usage of 375 gallons/year of epoxy polyamide primer. 2. Although the proposed approval order Condition 5, for the hydraulic fluid waste reclamation unit, states that the condenser must be 95% effective, there is no requirement to demonstrate this efficiency, such as through performance testing. The efficiency of the condenser may be determined by monitoring solvent input to the condenser, and solvent recovery. Condition 5 only requires monitoring the amount of hydraulic fluid processed, and the amount of solvent recovered from the condenser. In addition to these parameters, HAFB should be required to pericdically ffieaSUre and record the solvent content of the hydraulic fluid being processed. The State should add this requirement to Condition 5, and also require the calculation of solvent emissions to the air, on a 12-month rolling monthly basis. 3. The requirements for solvent degreasing, in Condition 11, should be updated to reflect the revised UACR 4.9.4.A. 

### Please contact Mindy Mohr at (303) 294-7539 

### with any questions regarding our comments. Sincerely,

# ~- 

# -**-B-~**



# u /. /-c Marius J. Gedgaudas, Chief Compliance Section 4.2.4-809IU 

# o UNTEO STATES ENVIRONMENTAL PROTECTION AGENCY



# ft R'EGION VIII 999 18th STREET

- SUITe 500 DENVER, 

## COLORADO 80202-2405 

# JUN 

# 2 2**!tJ~)** 

## Ref: SAT-AP Mr. Oavid 

## Kopt.!. Enqineering Unit Manager 

## Bureau of Air Quality Utah Department 

## of Health**~.O. ~ox** **i~~90** 

## Salt Lake 

## City, 

## Utah 84116-0690 

## Dear Dave: Upon 

## review of the 

# May 22, 1990, Notice of Intent to approve five projects at Hill Air Force Base 

## (Installation of Steam 

## Boilers, V.!.por Seals for**JP-~** 

## STora98 Tanks, Waste Hydraulic FlUid 

## Reclamation Units, a Paint Spray Booth, Lab 

## Hoods, ana 

## a Paint Spray 

## HanCjer), EPA has the follo'Wing 

## comments:
1 • 

# The proposed approval 

## order Condition 

# 4.G, for the 

## paint 

# ­**spr~f han~er**  

# at**bUildin~** 

# 22Q r**9hQ~~d .nQ~~gi**  

# thl**~5aij6** 

# of 375**~allon6/year** 

## of epoxy polyamide 

## primer. 2. "Although the proposed 

## approv.!.l ord.r 

# Condition 5, for 

## the 

# hydraulic tluld**w~6te** 

## reclamation unit, 

# stat., that the**~ond8n~.r mu.~**  

## b. 95' effective, there 

## is no requirement to demonstrate this etf1ciency, 

## such as through 

## performance testing.**~he** 

## efficiency of**~he** 

## condenser may be determined 

## by monitoring 

## solvent**inpu~** 

## to the 

## condenser, and solvent recovery. Condition 

## 5 only requires monitoring the amount 

## of**hyd=a~lic** 

## fluid processed, and the 

## amount 

## ot solvent recovered from 

## the condenser. In addition to these 

## parameters,**HA~E** 

## Ihould be required 

## to periodically 

## measure and record the solvent content of the hydraulic fluid beinq**processed~** 

## The State should add this 

## requirement to Condition 

# =, and also r.qui:. 

## the caloulation of solvent emi6sioil5 to 

### the**ai~,** 

### on 

### a 

## 12-month =ollin9 monthly babib.**~.** 

## The**~,qu~rem.nts** 

## for solvent ca9reabing, in 

## Conditior. 1i, 

## should be updated to 

## reflect the 

## revised UACR**4.~.~.A.** 

### Please**co~~a=t** 

## Mindy Mohr**a~** 

### (303) 294-7539**w~th** 

## any 

## questions regarding our =ornments. 

## Sincerely, 

# T£)-uY!.-­ £riu6 J.

# Gedgauda~: I

# ~f 4.2.4-810 Compliance 

## SectionDEPARTMENT OF THE AIR FORCE HEADQUARTERS OGDEN AIR LOGISTICS CENTER IAFLCi HILL AIR FORC E BASE. UTAH 84056-5990
AIR Q[JAi lTV



### Mr 

### F. Burnell Cordner, Executive Secretary 

# 22 NOV 

# 1989 Utah Air Conservation Committee Bureau of Air Quality 288 North 1460 West 

### P.O. Box 16690 Salt Lake City, UT 84116-0690
RE: Notice of Intent to Construct, Paint Spray Hangar Modification, Bldg 220
Dear 

## Mr. Cordner
In compliance with Section 3.1 of the State Air Conservation Regulations, we submit the attached Notice of Intent to Construct.
If this office can provide additional information, please feel free to contact Jay Gupta at 777-7651. Sincerely

1 Atch**JAM~S** 

## R. VAN ORMAN Notice of Intent to Construct



### Director Envr'iltl MDt 

## Dir

4.2.4-811

### Notice of Intent to Construct Modification of Aircraft Paint Hangar, Bldg 220 Hill Air Force Base, Utah

1. PROJECT DESCRIPTION:
We propose to modify our existing aircraft paint hangar in building 220. The existing paint hangar is a grand-fathered source that was built in the 50's and therefore, we currently do not have an air quality permit for this source. Please refer to your Approval Order dated Dec 28, 1987 for corrosion control bUilding 220, where three new paint booths were permitted. Those paint booths were as a result of conversion of aircraft chemical stripping areas into paint booths. Existing paint hangar waterfall troughs and piping is corroded out. These troughs and piping will be replaced by Devilbiss**~.~~dular** 

### tUI'boclean chambers**cc~.,;.lct.t:** 

### ::: ttl 

### pumps, nozzles, associated piping, controls and sludge disposal. A manufacturer's bulletin on these turboclean chamber units is attached (Atch 1). There will be a total of 9 units including 2 exhaust fans per unit. Based on a volumetric flow rate of 18,500 cubic feet per minute (CFM) per tan, total exhaust volume will be approximately 333,000 CFM. The points of discharge will be approximately 52 feet above ground. A face velocity of at least 100 feet per minute (FPM)**shal~** 

### be maintained across the crossectional area of each unit. The paint hangar can accomodate up to three aircrafts for painting at one time and hangar can be spl1 t into three painting areas using movable parti**~~c.** 

### •• ",. 

### 2. AIR EMISSIONS:
Air emissions from painting operations include hydrocarbons and particulates. 80-90% of painting in the hangar involves painting exterior of aircraft and related components. Only a limited number of miscellaneous items will be painted. According to Utah. Air Conservation Regulation 4.9.6.g. (1) 

### (g) painting exterior of airplanes is ·exempt· from VOC regulation under miscellaneous metal parts and**p~oducts** 

### VCC emissions. Also, as stated above, these emissions have existed over the years since these sources were grand-fathered. We are not adding any new emissions as a result 

### ot this modification. In fact, the overall emissions will be reduced due to (a) substitution of solvent base primer with water reducible primer and (b) using high volume low pressure 

## (HVLP) paint guns to increase the transfer efficiency of paint guns. Particulate emissions are controlled using waterfalls, reduction in hydrocarbon emissions is estimated as follows: Approximate Paint Usage: Polyurethane 4600 gals/yeaI' Epoxy Polyamide Primer 375 gals/year Water Reducible Primer 1600 gals/year Nitrocellulose Lacquer 625 

### gals/yeaI'**Mis~~llaneous** 

### 650**gals/y~ar** 

### Average 

# voe content of paints
VOC (lbs/gall Density (lbs/gals) Polyurethane 4.7 9,2**Epc~j** 

### Polyamide Primer 5.8 10.5 

### 4.2.4-812**Wate~** 

### Reducible**P~ime~** 

### 2.8 8.9**Nit~ocellulose Lacque~**  

### 4.8 8.0 

### Miscellaneous 6.0 9.0**Hydroca~bon** 

### emission**befo~e** 

### modification: 4600x4.7 + 

### 1600x5.8 + 

### 375x5.8 + 

### 625x4.8 + 

### 650x6/2000 

# = 20**tons/yea~ Hydroca~bon**  

### emissions**afte~** 

### modification:
4600x4.7 + 

### l600x2.8 + 

### 375x5.8 + 

### 625x4.8 + 

### 650x6/2000 = 

### 17.6**tonB/yea~ Hyd~oca~bon** **~eduction** 

### due to this modification:
20-17.6 

# = 2.4**tons/yea~** 

### Reduction in**hyd~oca~bon** 

### emissions due to**inc~ease** 

### in**t~ansfe~** 

### efficiency is not shown above. It is estimated that the**t~ansfe~** 

### efficiency of HVLP system could be 60-701 

### as compared with**30-40~ fo~**  

### the conventional type**sp~ay** 

### gun. This increase in**t~ansfer** 

### efficiency will**~educe ove~all**  

### paint consumption**the~eby ~educing**  

### emissions to the**atmosphe~e.** 

### A**manu!acture~'s** 

### bulletin on HVLP system is attached (Atch 2).**Manufactu~e~** 

### claims**t~ansfe~** 

### efficiency as high as 90t on certain**wo~kpieces.** 

### 3. AIR CLEANING DEVICES:
Paint**pa~ticulate** 

### emissions will be**cont~olled** 

### by waterfalls.**Hyd~oca~bon** 

### emissions**a~e cont~olled**  

### by substituting solvent base**p~ime~** 

### by water**~educible p~imer**  

### and by using HVLP system spray gun. No**othe~ cont~ol**  

### devices**a~e p~oposed**  

### due to high cost of**cont~olling** 

### diluted**hydroca~bon ai~** **st~eam f~om**  

### the paint**hanga~.** 

### This is illustrated by the cost analysis**fo~ ca~bon** **adso~ption** 

### units as follows:
Total volume of gas flow to be treated = 

### 330,000 

### CFM. According to EPA**a~ticle ·Recove~y**  

### of Volatile Organics**fo~** 

### Industrial**Sou~ces·** 

### by James 

## T. Spivey, Typical capital costs**fo~** 

### conventional**steam-gene~ated** 

### systems are '15-20/CFM.**Fo~** 

### large volumes, use 'lO/CFM. Capital cost of**ca~bon** 

### adsorption units 

## = '3,300,000. Annualized cost assuming 20**yea~s** 

### life at 8X**~ate:** 

### :: '3,300,000 x Capitol Recovery Factor 

# = '3,300,000 x 0.1019 

# =. 336,270 Annual**ope~ating** 

### costs including labor, utilities, and**ca~bon ~egene~ation:**  

### Assume at 151 

## = • 495,000 Assuming 90% efficiency, pollutant reduction :: 17.6x.9 

## = 15.84 tons/year Cost '/ton pollutant = $ 

### 831,270 15.84

= 

### 52,480 '£/ton pollutant 4. EMISSION POINTS: There will be eighteen exhaust stacks**discha~ging app~oximately**  

### 330,000 CFM into the**atmosphe~e.** 

### Point of discharge will be about 52 feet above**g~ade.** 

### 4.2.4-813

## 5. SAMPLE POINTS:
No sampling points are provided. 

## 6. OPERATING SCHEDULE:
This facility will normally be operated three 8-hour shifts a day, 5 days a week, 52 weeks a year.



# -

4.2.4-814

## ! 

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### ,,:::}**Lo~** 

### .. r 

### Type TURBO CLEAN Cham!;ers Both typS3 

### c**~e** 2v2.i'2.:::; in 

### 24".36" and 

### 48" a:r v:2.silers. The**ch2.~::: :.;~s**  proVlO:; t:-:e fo:lowing**su~f:cient** w2s::iilg**capacit~·:** 24"**ch~~~~,:2;-L'p** to 1000 dm per foot of v"idth 23 GPkL 

### 36"**ch::~-,::er-":U;J** 

### to; 400 cf;n per foot 

### 0;**v.~dth** 22 GPM. 

### 48" 

### d'i.:,':;:':·8r-Uptc 2eaO cf:n 

### perfeot**ofwidU~** 

### 55 GPM. 

### Elevafc::f 

### Type _I:**Elev2.~sj** chcT.j·::;rs 

### cie [Jre!erred**wheneve~ ~"**  .. 

### <::::er1t**ceilin~ ::s:g~t**  is**a'.'2.::~b:e** (minimum of 14 t).
E It is**d:~'** 

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### ..

horiz::. -,:':: ';'**2~.\:.o:** 

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## 0:**~he** rebour": j f::,;n Co**fi2.~** 

### ::c:dsheet.

Ill; Air is v:::.s,.."ss t·

... :.:s -uc:ssing through a f1ooc':' :cct of



### water**2.~C \:.C:~** **s::~c.:** 

### :::sj and t!gitated in 

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• Three 

# c.:r velocities: 

### 100. 125 and 150 fpm.

. _ Entire volume of 

### water on wash down sheet.

II 

### Very tow resista:lC8 to 

### a;i flow.

I: Conven:s;ot inspe-::ticn 2.nd clean-out doors. 

### LowTJ-pe II 

### LoWlype chambers are employed where building ceiling

heigh:s restrict the use of elevated type-minimum of 10 

### fl. E in. ceiling height required.
II: Airiswashed lwice-passing through the curtain 

### 0; water

from wash down sheet-scrubbed and agitated in dense, overlapping spray from nozzles.**IlThreeairvelocities-~C8.** 125and 150fpm.

Q**Wa!~flo'** .. : 0:1 'Nash dm';n sheet traps paint. ke:s::s

sul1ace clean and provides first stage washing.

E Convenient inspe:::tion and clean,out doors.

Low Chamber 

# ATCH-J. 4.2.4-815 

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### trc..-

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### :cc
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.. ..:**~.:** ... :>J;-;"j \\'hCiC**l~l~'/ ".;~,"Ti.**  .3 ti,:::;**CC~:.::':;.** i: :i'-c.:'CS 2. V:2sis "c.1rpet" 0:1th8**bc~:­** 

### ,c:.;;;-;**r0,);ese:,~;,;; ;:'i~'I**  

## 'A 

# tn 10 

### Ito th of the**origi;,2~,~'~** of L'lG paint spizyed intc the**bo~th.** 

### i;,e T:JF=i5C ::;i..EAN**"c:~:~':::'** is 

### :nade up e:-,tir€:l:, of**~he** solid non-VC:':I!e part 0: 1;:8 p2.int. 

### It is a r,oi1flammable, Ob-ncxious**Cdc;~** 

### t.roL:r.c Sooth-lmprov),,:::**nC:1·sjj::~y** ',', ,:s!e-z Q'C:': e;o' ·::.:::-:;nental improve;nent ir**Vl(;,~j::g Ccnclti:.·~s.**  

### ti1e**bOG:~** 2-,,-:':2. 

### as cor::**:::.:~C: ':';::~**  

### ,,'1e sticky, hazardous, 

### TrH3 cc-::;r;;.;ous ?c:,cUon:r.**t!~e** 

### TURBOCLEAN 

### b: diIE:;;.!:!**~.:** ::!san p3.,;-,t**\·,:'I~;;** &';:::;u;nu!ates 

### i., most water tair.s ahigh 

### lave: ct disso;ved 0xygen In the wate:.**i:~:s** tar,ks. 

### Tr.2 3.CUC;I of the 

### TUR50CLEAN cone mi;.;es air 

### in eliminC::!l3s stagr.:::"icn and p:events the gro

...... 1h cf cjc:­ water, t':us mz:ntc:ninQ 2. high level of oxygen. This flow 

# 0:**s.at.:~ng** anz,cro:: ,c :;ac:eria.**oxyger.:3,~:::j** 

### ',va:(;,**aro~;l:'~** the; ta:-,k 

### z:.t alileve!s reduces**Fu~p ~!1d** **No;.:::~e. C!oQ~::-,g.**  

### . "'- s:<lgroGb:,; E;.;-,d 

### ,,8:pS piS','C:!, 

### ,lie growth of ana''::'cbic 7:-l(;**,C:''::t::l~cj** \/;';."1:1.1;1 cone**::~** :ocated adjacci,: to:: " ' b:::'ClCri.:::**:~:s :i~;s** **~&C:C:-** :::::: c:z,L,;sc:s the tyr;.;ca 

### :oui cdc, :;;;<:;,..:::; -:,.d fXO'lijcs prote:::;.Jn forme pumps en':; :::.:.. , __**[;.$s.:;~z.:.::i ~'**  ..**;::~** c:c**::~.** ,C

..**:~~.~.:** .. ,·,',J.stl bocths,**2.g2:.i,'~: ;:,:ogg:~,g.**  This gicaLiy reduces booth do\\';-,:,::';'

-­ NG: :.::-,: 5 C2.;/**~c** ;T";2"':2 :.:. ;sink, Sorrlc of**~bei"'rl** ;1C:Z,i. on a:)c**fTi:::.~e** bocl.-, "uptime" r:>eans more**produCli\';~:':::** -.,**v\'at~r** .. -;:;**;~:J~2.t8 ai1~**  h2.i:-::;C= these**~2iLjcles.** a c:**n~roUea Co~~c~nd**  

### USZ4ge

..**1;C:Z.~:~"· J:--;~;**  

### ;s p;CV:C0:.-;**::~** the !3.:lk, trapping 0 .y par· l:s uj'::c;ue \',3:er was:ling act:c:l causes a**mo;~** COl':"**~~'.** , ::c,:;s**:~-** •. '::on'1**S;j~** Elf ..•**C::·':·li:::::~ ~heir**  re:nov, \',:-18n**;;r~2!'::;,::;"/"** 0; p3in: pc:.rtici8S. 5y**d€Cre2sjn~** the**i,:;:~** ::.:', :l22(;;S":.:**.~:.** T;-::Js,**~he T~/,-·:~?:",CL5;'./\'**  

### booth**g;'"e.:~;y chi:.i~L::::S:**  cS:T.pound**brea:~::own,** tot2: becth opc;z;:;C**l~-~;:;C'..'~:'~ t~~** **:re3.ti7~e:l~** c'- 

### Q::**:':1~·es** of paints inci .,c.:i;lg c.,:':£:S**2~G :e~uced.** **pri;'l:::~s** 

### '.::.:)**,':C2.~$.** en2.;Y.(';:S.**·~;::JAY3. ureUI2.nC~** 

::**\:..:~~ 2·~**  ;3(;::;**t~2** l.seC for f;"(

..**c~er:t** ski:THTI::IQ.**Reg'_.~·** '--::':::::;..:;:i -:;:**~:~.8** ::ce-:r: can C:'; c;\'12

. 

### ,dcc**::~** v/ceks 0:- r..**rr:.:;:~;"';~:** ..**~dd** 

### to el:S red\J:::c.:d**',·;·2.s~e** disposal a;-:d**y~** .**.'~:':' ;~::)"**  

### .. : c 

### iiJ,ciBOCLE;',N sp:a'! bQottl can pay (or ilsc:r ;;; "

· ..**"~~ry.' ;~.~Q""** **ti:"i:e.·~**



### 4.2.4-816DeVILBISS 

# H\-LP 

# Svstell1 89'\;

'­

.,,_. 

# Complete systems for industrial High. Volume. 

# Low Pressure applications.

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## -\ir conversion units. turbine air" 

## generators, handguns and more

. 

# (

... 

### 4.2.4-817 

# A,CH-Z­

# \Vhat"s 

# the best 

# HVLP systen1 for you: 

# Here are son1e 2uidelines for C1100sing 

# an HLVP 

# svsteIll.

High·production. continuous-duty. For hlgtholume InCiustnai use.**~ou** 

### neec lile 5\Slem lhat"s procluclI\e hour after Ilour ancl lia\· after**aa~.** 

### lOU need a

.......

; 

### l)e\ i1l1iss \\ali·moumea**~,Ii** 

### Com erSion Lnll Wilh pressure**lan~** 

### or piston DumD iluld supply. These s\srems can handle one or [\\0**~uns** 

### per air SilJiCe**con[Jr.uousl~** 

### prO\lding up to 

### 10 pSI. Tiley can he xaered \\ llh heJ\**\'CiUl~** 

### air neaters (-\ic**_.~ '-~**  

### Comerslon LnilS \\"lhoUl Ileal can be 

## .-., mounted inside lhe spray ooorh.) -\:

"

.. .J 

### maXlmur.l pressul'e. they nandle hlgner**'-~** ;-**.~** 

### solids levelS than oltler 

### j-j\LP systems. -\na no turbine Urill IS 

### requlrecl. \Iedium·low production. portability.**~,u:** 

### Turbine Lnlls need no compressed all' .""1 

### supply. They neea no air healer because lhe wrbme healS [he air. They simply

.. plug Into slJnaard 110 

### \olt power

supplies. \Vhen used With cup·fed guns or wllh a l\\o-gallon oressure lank. the:: go anywhere: :ust plug them Ir. ann you·re ready [r) 

### go When properiy JnSlallecl. used. and maimalned. JII Del, liblSS H\'LP systems are dt'S!gnea to 

### meel or P..\ceecl inSUrJnct' maUSl,':**safel~** 

### standards.

:" :.::**:~sU:J(C'(J** '.. ,eli; \ ; 

# I "1- "'e 0"" ,.".,,,- 'n

/J ,l:'>l,.**~'.** ,iJ f\,\.

.... , .. II 

### e I r I !)t'r,ll or S :13!1n u,mron.JDle 

## i II hen sprallnJ:! II·Hn hlJ:!h I •. ­ 

# .-1**[en~De~ature** air



### 4.2.4-818"**:~~;~** .. lre:)**(or~e(!** :ill l'llnSlrUClIlJJ1 to 1\ \ IJ1Dustrial use, '.:',\CCiil"::l JtOlrllZJliUil**,~** ';It't'l !lUlL! liP <lll(]**~Jltern** IS iilll!lllt':\ ill**~eC1** neecllr t'.\ler.d (lCi!UstJOle**f~()rn** 

### (u::**~z;r:** to rouna 

# JGHV: _-\ DeVilbiss S[)l'ClY 

# £uo ciesi£ned 

# spedfically for 

# HVLP 

# atoolizatiotl.**.:,~** 

### io\\**rxessure:~** 

### s :'2r mori:' C1ifficullLO

### bi'eaK-~I;**Da!-j~: ~t0**  smail panicles. \lost ::3;)I'a\ guns \\QUid Cl0 

### 2 marginai 100 

### Tile 

### JG H\ :5**~r:e ::,\ce~lIon.**  

### De\ilo:ss :s**~o:** 

### sl:npi\ a hard\\are ::3uooiier' ',\("'-:' :,:::nous**fo~** 

### 2tOmlZ2tJon. \\e 

### Kno\\ no\\ 

# ,0 c:es!gn all**,~aos,** 

### and \\e KnO\\ 

### ho\\ to**c::JI;i~** 

### DJir,t ':'t ]**~,_** 

### :0 ::S:, 

### the JCi1\ pro\ldes ,:onslsten: :::i:WE 8rea,

.. 

### :-U0 !: generales a :SO:l**~\~~"I ;~'C:~~::~~** **~hC1t** 

### produces a "niforr:: :)JII(1**~!~e** 

### JCf-1\' 

### has proouced iirgh**c~a'::\** :'il'SI':::'S**\\IC~** 

### SOlids le\'e!s as**::!~!1** 

### cb 

# =5**~"~ :~~~**  

### s :'ci:'**r;!~~e:-- ~n3n** **~OSl** i\\ 

### pressure ::3\ S:::;[1S can nanale,

-\nd 

### ye:. ::k'**JC~\** 

### ccesnt compromise**()OerJwr~-o:T:(~)r'~** 

### :lS forqed aiUffimcm JO(JY anu I,au;:; ,:,ns;meerec: plastic gnp r,,2Ke 

### I: (,I:';[Or,J:;;:: JnG lighL \\ lth good**balance,:~c'** 

### the r;:(iustry,standard jG.-\, 

### Because you CJ" cnoose from a \\ide 

### \anelY of tlDS 2,10 

### rlUld caps, you can be sure there S <Jne tnats laeal for you.**~CH\** 

### 112n(lirS s,)i\er+i"i)ased and \\JterjcJ:':l::'**sa~e:')3:S** !: 

### CJIl De ordered \\Ith a ]'2011Ior: Glessure lam: or \\'Itn 

### a**Te!lon-J,!n~~; C:"::~'.**  

### Top ngnr 

### On!! g:,.'J i;anciles SOI\enl or :ioleriJOI'nr: ,'!)o,f'rtals 

### Ii 

### can Ix: 

### used \i '/[i7 

### :::[hl:'r preSSLJff:**:~~** 0:" 

### SU[{Jon 

### (eed \i'leh
\ /iejo!e**r'~n** -i;,:**~.r;;r:proauces** 

### higi7 qualJ{'. :";,:"'::'::;nt>:: ::, :':,'7 e.I:)"**//:,!~** 2S :: 

### pSI. ,,[ i (J ,'JSi'**~anr;-,s** '::EOlUr:;-;;1£rJ 

### solids !30[[On:';;l:;!**~)c[2,'!!e(!** 

### :ir::,\iiJ/e 

### balli.'"1Y::' Sii;\;o1 :'0:;:7:-:'[::;" :XU\ 

### !C'es comoleee i)7ane:/i ef2:)I'::', "," 9.,::,!!:::g !nco ugiJ[ :'i:-fas

The JGH\ can use a Del**;IC:IS~** 

### 4.2.4-819 Tef1on'iJnea cu D ur u oressure lJnK as SI1O'.\ n f,t,e

# \Vith more air source options than any other 

# .­ sUQplier. 

# D.eVIlbiss }1as 

# an 

# ans\ver for 

# every HVLP need.

\Jor.e than any QLner pa:LOf-your**H~LP** 

### system. the air source will limIt your options and determine ho\\' you can use the equipment.. De'/ilblss offers t\\D basic systems and lots of options. The first configuration IS 

### the .-\ir Comerslon L'nit. This \rall·mounted unit accepts high pressure air from any normal compressed air source and proauces low pressure air for HHP application. It's designed for contlnuous·duty industrial applications where the utmost comroi IS 

### neeaed. Pressure!s adjustabie from 2 to 

### 10 pSI. To improve Oash and taCK time. It can be supplied WIth either a fixed· or adiustable-temperature heavyauty air heater that offers fast warm-up and consistent air temperature. !t can be used with one or t\\·o guns The most portable' unit 1I1lhe DeJilbisS line is the .Air Turbine l'nit 

### (.ATLJ This system uses a heavy-duty three-stage turbine-alr generator whlcn requIres no compressed air source. only a 110 

### volt -\C po\ver supply Turbine units are placed outSide me spray booth. spray room or designated hazaraous iocatlons.
Top ierr The moael**~Ci..··500** 

### offers aa/usrable OUUJU[ 

### ,'Jressure. Top right 

### '1'1 o4CL moaeis Inciude l7earers.**rt7e~G550** 

### fsnOlln; and [he 4C['·560 l>t[n 

### adius£2Die near Rigl1L The po([aole 

# J.n models are complere/v self-':omamed. Plug [hem !nCO 

### a standard 170 lAC paller 

### source and you fe 

### read.l· {O 

### oam; 

# /

4.2.4-820

# Hi£ll \olurne Lo\\ Pressure: 

# Higll**'.~~(){** ,.\**;J~:~Lt"r:'** 

# transfer efficiency. ane! a lot 1110!'C. I**·J~·SP:·2\. ~l()**  ().'11 r.1!i 

### (-:r:21:: \1.**():'~o!e(l;"'~** SliCtl h!2!' 

### [,'ur>'f"**,:,rfCI::.':W·~::l;·U\i'S :lc:ll1lln~**  !)c',',I}["'iiCir:ct> J:) leSS**ina~t'riJI** i;:; 

# !m**---.--..,;~ -~,:'J** 
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### ..... '_ .... 

# ­ <1**'-"~~iL~,**

"!!H \::''';'.\L.:Y' 'I l;l·.\**,)O~r2.Ul)n "':i~'.** **~C::** :i--: ·)['cerec \\;[h ',\ irnoL;t 21r**:,~~lers** \\cb[c'U 

### Tilt' 8(1)lh 

### :ic'ecls It:)S



### s\**~~ems ?~.~**  DIO\ IUeG \\**'~h :,:~n~r**  J;:;\)['Hineu 

### rn.:uer:2'**::~I~~~** 

### -.;; ;1,:**~;>~.)c:z:;;'. ~~:~!.2!r.et~·CC** **~'.'- ~>~:i~** **'(1l;~(1(~ '.;~~~:'**  Oc\**;jl)!~S j·f~;:rt:,r':tc;:!\.('** 



### 4.2.4-821

### S PECIFI C..;TI 0:\ S: 

# I -\IR CO\\'ERSIO\ L\rTS 

### I -\IR L\rT I :)PR\l GL \ DimenSIon,; Input i I)utoul i \\ei2hl 

# I \lodel (inchesl \-ollaee PSI i-PSI (F\i 

### -r Discnar!!e Te:no. ; (Pounds! \lode! \Cl·SOO·16FT JGH\·303·16Fr:' ')35 II -1mml 

### I**-\(l·SOO·l~fY** 6 \ 3 \ :> n!a 100 10 30 .-\mblent 3.S JGH\ ·303· 1-1 FI : 039 L9Rmmi I -\(lj·500·16DE .JGH\ ·SOJ·lfiDE !rJ70 (Ulmml 

### I -\CL·S50·16FF JG\H·SOJ·16FF i 

### 055 (l-1mmlI**-\CL·550·I~FY** 36 \ 

### 9 \ -T i 10\ \ 15,\ 

# I lOO 10 30 180 e F 50 JGH\-S03·I-1FY 1039 r.9Rmmll -\([·550·16DE .JGH\·5OJ-IGDE 1.070 (1.8mml 

### I 

## I -\Cl·560-16FF 

# -I JGH\·503·HiFF lOSS tfTmmll _.­

J,CL'·560·14F!· 36 \ 9 '\--1 

## 110\**~- I~.-\**  - 100 10 30 to 210 c F 

# I 50 JGH\-303'I-IFl 

### I .ilJ9 (YHmml -\Cl·560·16DE JGH\-503-lfiDE 1070 (l.8mml \ole: .-\11 .-\CL models allow the opllonal use 

### at Tenon·linea Dainl CUDS (\Iooel TLC3031 ane 2'/, gallon oalf)[ lan;;.s (\locel PT·3}!)1 \\1 ,;\';lemS InclUde a 30' air hose assemhl\ 

# I-\IR TCRBI:'\ES

.-\IR U:\IT : SPR\l 

### CD

, DimenSIOns Inout 

## o UlQUl :**\\ej~hl** 

# I I '.Iodel I , \lodel , Tip :Size i1nchesl 

# I \ollaee 

### I PSI , PSI 

### I Cell , Discharee TemD. 

### I (Pounds)

. I 

### I -\TL'·520·16FF I .JGH\'-503·1GFF 1055 {l-lmml 

### I 

# i 20 \ 14 \ 12 110V '( 15r\ nla -1 .:J - 16 

## ! 180 0 F 

# I -15**JG\H-:i03·1~r:·** 

### i 0391.9Rmmii -\TL·520· J-IF! 

# I I 

# I !

I i I JG\H-503·) 6FF [ 055 (l4mml 

## I I 

### I 32 

### x 1<l \ 12 

# I 110V \ 15.-\ 

# I n!a 

# I -15 

### I 16 ) ISO c F 

# I 55

-\TL'·530·t6 F'F 

## I JGIH·j03·I-IFY i ;119 iYHmml! \Ole: Each .-\TL·320 system Includes Tenon'llned pali1t::.m (\hlde: TLCSo:'l\ anc oaln! tanKS are oplional Eacn \TL ·;)3()**~\:itcm** :i1CiUOe:; J 1':, gallon**palOllan~** (\Iooel PT5301 ana Dalm CUDS are OOlIonat.l,11 S\Slems Inciuoe 

### a 30' air hose assemblY 

### CAPS, TIPS AND \EEDLES: H\LP I\FOR.\I.-\TIO\: I -\Tl-530·1-1 FY



# - DeVilbiss has made a major commitment [0

_ 11\7P Tip Size Fluid TiD .-\Ir Cap 

### '1 \eedle 

### H\lP**~echnoi()gy** 

### inCluding**~eseat'C~.** appilGlliO(1 _L8(.70mm) JGHV·6,: • ,; JGHV·16·12 JGHV·404·G 

## I .034 (.85mml

. JGHV·60Hj\ JGHv·16·12 JGHH04-GX

.039 (.98mmf JGHV·60 j·FY JGH\·16·14 JGHV-40Hi' 055 (1.4mml JGHV·60HF JGH\··16·14 JGH\-404·FF .070 (1.801011 JGHV·60 L·DE JGHV·16·16 JGHV-404-DE 

# .... 

# ­ e:12meering. nationwIde soare parts ano**~em('e.** 

# :::.­ 

# -........ ­ ",-s-a-resuil De\'i1blss 

### H\LP systems renect-­ our 100·year reputation 

### as spray 

### finishing and atomization experts. 

## =­ 

## =­ Our free pamphlet (Form no. F·81 

### II clesCrJht's 

# '--­
=.- , When ordering. specify air sUDply mOdel. JGH\ gun model ana paint 

### thiS 

### ne-.\ tectmology

..**-\s~** 

### your De\llblss cup. supply lank ane «lP/liP oplions :iistrirlU[Or 

### for a 

### cnP\ Or' 

### ((111 I-ROO-Dt:\·.l-pn.
U.S. Regional Offices 520 

### \Vharton Circie 

### P.O. 

## Box 43226

. .l..t1ama. 

### G.A 30336 404 

### 696-4988 8205 S. Cass SUite 

### 102 

### Darien. IL 60559· 3 12 

### 969{)440 i 

### 2878 Florence .",-venue 

### Sama Fe Sprmgs. 

# c.; 90670 213 944-1111 

### 300 Phillips

. .l..ve:1ue 

### P.O.30x913 TOIF-do. 

### Ohio 

### 43692 70-2169 

### National Automotive Sales Group 

### 2455 S. [ndustriaL SUite C .';nn :\rOOr. \1l48104 

### 31399+8800

Customer sen'ice 

### & Order Entry 1·800·0EV-4448 (L.:.S. Onl\')

Distributed 

### by: Canadian Offices 

### Vancouver. British Columbia 604 

### 294-3787 Toronto.Ontano .l 

### 16789· 1866 

### \ !ontreal. Quebec 

### 5 i-! 

### 326·96';0 Bame. OntarIO 

### 705 

### 728-.5501

Sales 

### and sef\lce available in 

### rmncirJal cities**[hrOu~hol![ ~"!e**  

### world.



### 1 

# DeVILBISS

# Cs~-= 4.2.4-822 The DeVilbiss 

### Company Toledo. Ohio 43692 \lodels and**Soectfi(atl{Jn~** SUOt('(';. to**cnan£:'~** ',\ Itnout notIce**~: ~B**  'S) 1989 The De\ ilblss**ComD3,~,\ ~?a~'.e~il~ts-':':0t~':~o~:n~,u~-----_·-_·----** **--'.~::n"'.,".::._c** -,":i...:-:\

_