# , , TESTING - CONSULTING 

## November 

## 16, 1995

Illinois Environmental Protection Agency Division of Air Pollution Control 2200 Churchill Road Springfield, IL 62794-9276 RE: Application for Air Pollution Control Permit Nathan Green Engineering Services 3158 South Kolin Avenue Chicago IL 60623-4889 Phone: 312·254·2406 FAX: 312·254-6661 

# OJ/be!) [UQ
.. RECENED



# r

JAN 0 5 1996 lEPA-DAPC-SPfLD.

Enclosed please find three (3) copies of a completed Application for Permit to Construct & 

## Operate prepared for our client: 

## Empire Hard Chrome 

## 1615 S. Kastner Chicago, IL 60623 The application covers the emission source(s)/control device(s) at 

## Empire Hard Chrome identified in the application as follows: Process AM-1, AM-2 A-123, A-4 A-5 A-6, A-7 A-8 8-1, 8-2 8-2 8-34, 8-5, 8-6 EP-1 S8-1, S8-2, S8-3 C1,C3, C5 C2,C4,C6 Emission Source Air Make-Up Units Chrome Plating Tanks Chrome Plating Tank Chrome Plating Tank Chrome Plating Tank Chrome Plating Tank Chrome Plating Tank Chrome Plating Tank Electropolishing Tank Sandblaster Units HCI Tanks Caustic Tanks Control Device NA Scrubber S3 Scrubber S2 Scrubber S1 Scrubber S4 Scrubber S5 Scrubber S6 Scrubber S7 Scrubber S8 Dust Collector DC1 Not Exhausted Not Exhausted

## Based on the PTE calculations, which are shown in Exhibit C, Empire Hard Chrome has the potential to emit more than 10 TPY of chromium particulates. However, based on the estimated efficiencies of the scrubbers, Empire Hard Chrome's actual emissions are 0.48 

## TPY. Therefore, Empire Hard Chrome would like to request a FESOP, with a self imposed restriction to use the scrubbers at all times while the rectifiers are in operation. If you have any questions, or if there is additional information which would help the Agency to complete their review of this application, please do not hesitate to call and we will assist in any manner possible.

NG:ng CN90997t cc: William G. Horne, Jr George Pearce

# 712tL~ Nathan Green Scientific Control Laboratories

### 03/05/1996 12:50 3127624710 EMPIRE HARD CHROME PAGE 01 

# !lllPJl)£ lJililD 

# CiJllDIJ]!, 

# JJ1C. Precision Platers of MOLDS • LARGE ROLLS • CYLINDERS • DRUMS • MACHINE PARTS PISTON RODS • DIES • WEIGHT 20 TON • GRINDING • BLASTING • POUSHING • UQUID HONING



### 1615 South Kostner Avenue Chicago, illinois 60623 Phone (312) 762-3156 FAX (312) 782-4710 

## March 5, 1996

# Ool·~CD·tLlQ Mr. Joydeb Majumder
. Illinois Environmental Protection**~gency** 

## Division of Air pollution Control 

## 2200 Churchill Road springfield, II. 62794 fax No. 217-524-5023 Dear Mr. Majumder: please withdraw our application request for a FESOP for our location at 1615 S. Kostner Ave., Chicago. We are requesting that our application be considered for an Illinois State Operating Permit. If you have any questions, please contact me. very:.**trU~lY** 

## yours,**~** 

# .

.. "
.**~U**

# s~ in 

## SW:d Vice-President

### STATE OF ILLI NO I S E NVIRONME NTAL PROTECTION AGENCY D I V I SION OF AIR POL LU T I ON CONTRO L 2200 CHURCHILL ROAD SPR I NGFIELD, I LLI NO IS 62794 -9276
APPLICATION FOR PERMIT(AI 

# r;J CONSTRUCT 

# G4J OPERATE LO. NO. PERMIT NO. NAME OF EOUIPMENT TO BE CONSTRUCTED OR OPERATED 

## Hard Chrome E:lecLLoplatillg PacilH:}' lSI DATE

la. NAME OF OWNER : 

### Empire Hard Chrome 2a
. NAME OF OPERATOR: 

### Empire Hard 

### Chrome I 

### Inc 

## Inc. lb STREET ADDRESS OF OWNER: 2b
. STREET ADDRESS OF OPERATOR; 

# "'''**~** 'UP 

## 1615 

# s . Kastner Ave. 1,. CITY OF**OWNE~~(** 20. <efiY OF OPERATOR : 

### Chica 0 

### J.cago Id
. STATE OF OWNER : 

# 1'· ZIP CODE: 2d. STATE OF OPERATOR: 20. 

### Z I P CODE: 

### Illinois 

## 60623 

## Illinois 60623

3a
. NAME OF CORPORATE**~~VISION** OR PLANT: 3b. STREET ADDRESS OF EMISSION SOURCE: "". g, Tnr 

## 1615 

# s. Kostner Ave. 3,. GIli' OF EMISSION SOURCE: 3d , LOCATED WITHIN CITY 30
. TOWNSHIP: 

# 131. COUNTY; 1 3g ZIP CODE : 

### rhicacro LIMITS: 

## CXl YES 

### DNa 

## Cook 60623

4
. ALL cORREsPoNDENC

# 1 TO: (nTLE ANDIOR**~A~** OF INDIVIDUAL) 

### f.1r Steve l 'ial in Vice Prsi en 5.**TE';~~Hr;~,; N~~~~R**  FOR AGENCY TO CALL: 6
. ADDRESS FOR CORRESPONDENCE: (CHECK ONLY ONE) 7. YOUR DESIGNATION FOR THIS APPlICATION :IC) 

# G=:J OWNER 

# 0 OPERATOR 

# o EMISSION SOURCE 

# .1.J1-=_L'Ll..
___

8. THE UNDERSIGNED HEREBY MAI<ES APPLICATION FOR A PERMIT AND CERTIFIES THAT THE STATEMENTS CONTA INED HEREIN ARE TRUE AND CORRECT, AND FURTHER ceRTIFIES THAT ALL PREVIOUSLY SUBMITTED INFORMATION

### REFERE~~I**~;HIS'~nON** REMAINS TRUE. CORRECT AND CURRENT. BY AFFIXING HIS SIGNATURE HERETO HE FURTHER ceRTIFIES THAT

### Il~is-A'tr1'AO~IZE6TO EXECUTE THISAPPliCATION. 

## BY===
__**~~~~""''I-!'>--** SIGNATURE 

## lEPA

- DAPC

- SPfLD
. DATE 

# iJ- S 

# -'Is' DATE 

# \j!\N 0 5 1990

TYPED OR PRINTED NAME OF SIGNER TITLE OF SIGNER (A) THIS FORM IS TO PROVIDE THE AGENCY WITH GENERAL INFORMATION ABOUT THE EOUIPMENTTO BE CONSTRUCTED OR OPERATED. THIS FORM MAY BE USED TO REOUEST A CONSTRUCTION PERMIT. AN OPERATING PERMIT, A CONSTRUCTION OR OPERATING PERMIT. (B) ENTER THE GENERIC NAME OF THE EOUIPMENT TO BE CONSTRUCTED OR OPERATED. THIS NAME WILL APPEAR ON THE PERMIT WHICH**t~AY** BE ISSUED PURSUANT TO THIS APPLICATION
. THIS FOAM MUST BE ACCOMPANIED BY OTHER APPUCABlE FORMS AND INFORMATION. C) PROVIDE A DESIGNATION IN ITEM 7 ABOVE \NHICH YOU WOULD UI<E THE AGENCY TO USE FDA IDENTIFICATION OF YOUR EOUIPMENT. YOUR DES I GNATION WILL BE REFERENCED IN CORRESPONDENCE FROM THIS AGENCY RELATIVE TO THIS APPLICATlON. YOUR DESIGNATION MUST NOT EXCEED TEN (10) CHARACTERS. J) TH I S APPLICATlON MUST BE SIGNED I N ACCORDANCE WITH 3S ILL. ADM. CODE 201.154 OR 201
. 159 \NHICH STATES: "ALL APPLICATIONS ANO SUPPLE, MENTS THERETO SHALL BE SIGNED BY THE OWNER AND OPERATOR OF THE EMISSION SOURCE OR AIR POlLUTION CONTROl EOU I PMENT. OR THEI AUTHORIZED AGENT, AND SHALL BE ACCOMPANIED BY EVIOENCE OF AUTHORrTYTO SIGN THE APPLICATION: IFTHE ONWEROR OPERATOR IS A CORPORATION. SUCH CORPORATION MUST HAVE ON FILE WITH THE AGENCY A CERTIFIED COPY OF A RESOlU· TlON OF THE CORPORATION'S BOARD OF DIRECTORS AUTHORIZING THE PERSONS SIGNING THIS APPLICATION TO CAUSE OR ALLOW THE CON· STRUCTION OR OPERATION OF THE EQUIPMENT TO BE COVERED BY THE PERMIT
. 

### PAGE 19. DOES THIS APPUCATION CONTAIN A PLOT PLAN/MAP:

## ~\,ES C]NO Ir A PLOT PLAN/MAP HAS PREVIOUSLY BEEN SUBMITTED, SPECIFY: AGENCY 1.0. NUMBER
_________ APPLICATION NUMBER
________ IS THE APPROXIMATE SIZE OF APPUCANrs PREMISES LESS THAN 1 ACRE?



# [i] YES 

# CJ NO: SPECIFY ACRES 10. DOES THIS APPUCATION CONTAIN A PROCESS FLOW DIAGRAM(S) THAT ACCURATELY AND CLEARLY REPRESENTS CURRENT PRACTICE. G]YES C]NO 11a. WAS ANY EQUIPMENT, COVERED THIS APPUCATION, OWNED OR CONTRACTED FOR, BY THE APPLICANT PRIOR TO APRIL 14, 1972: 11 b. HAS ANY EQUIPMENT, COVERED BV THIS APPLICA TlON, NOTPREVIOUSL V RECEIVED AN OPERATING WVES DNO IF ",(ES· ATTACH AN ADDITIONAL SHEET. EXHIBIT A, THAT: (a) LISTS OR DESCRIBES THE EQUIPMENT (b) STATES WHETHER THE EQUIPMENT WAS IN COMPLIANCE WITH THE RULES AND REGULATIONS GOVERNING THE CONTROL OF AIR POLLUTION PRIOR TO APRIL 4. 1972 PERMIT:WYES DNO IF ",(ES·, ATTACH AN ADDITIONAL SHEET, EXHIBIT B, THAT: (a) LISTS OR DESCRIBES THE EQUIPMENT (b) STATES WHETHER THE EQUIPMENT (I) IS ORIGINAL OR ADDITIONAL EQUIPMENT .(iI) REPLACES EXISTING EQUIPMENT, OR (III) MODIFIES EXISTING EQUIPMENT (e) PROVIDES THE ANTICIPATED OR ACTUAL DATES OF THE COMMENCEMENT OF CONSTRUCTION AND THE START·UP OF THE EQUIPMENT 12. IF THIS APPLICATION INCORPORATES BY REFERENCE A PREVIOUSLY GRANTED PERMIT(S), HAS FORM APC·210, "DATA AND INFORMATION-INCORPORATION BY REFERENCE" BEEN COMPLETED. 13. DOES THE STARTUP OF AN EMISSION SOURCE COVERED BY THIS APPLICATION PRODUCE AIR CONTAMINANT EMISSION IN EXCESS OF APPLICABLE STANDARDS: DVES WNO IF "YES: HAS FORM APC·203, ·OPERATION DURING STARTUP" BEEN COMPLETED FOR THIS SOURCE.

# ~ C]YES C]NO 

# e**~**

# ..................................................................................................................................................................................................................**~ ~**  14. DOES THIS APPUCATION REQUEST PERMISSION TO OPREATE 

### AN EMISSION SOURCE DURING MALFUNCTIONS OR 

# ffi BREAKDOWNS: 

### a.. CJ 

### z

# ~ w 

### a.. c:J VES 

# [i] NO IF ·VES: HAS FORM APC-204, "OPERATION DURING MALFUNCTION AND BREAKDOWN" BEEN COMPLETED FOR THIS SOURCE CJYES C]NO

## ~**~15-.**--I-S-A-N-E-M-IS-S-I-O-N-S-O-U-R-C-E-C-O-V-E-R-ED-BY-T-HI-S-A-P-P-LI-C-A-TI-O-N-S-U-BJ-E-C-T-r:-O-A-FU-T-U-R-E-C-O-M-P-U-A-N-C-E-D-A-TE-:

# -------1 12 z Q

### ~ <.> :;j 

### a.. a.. 

### < [=:JYES

## ~NO IF ·VES: HAS FORM APC-202, ·COMPLIANCE PROGRAM & PROJECT COMPLETION SCHEDULE: BEEN COMPLETED FOR THIS SOURCE: c:JYES C]NO 16. DOES THE FACILITY COVERED BY THIS APPLICATION REQUIRE AN EPISODE ACTION PLAN (REFER TO GUIDELINES FOR EPISODE ACTION PLANS): C]YES 4JNO 17. LIST AND IDENTIFY ALL FORMS, EXHIBITS, AND OTHER INFORMATION SUBMITIED AS PART OF THIS APPLICATION. INCLUDE THE PAGE NUMBERS OF EACH ITEM (ATTACH ADDITIONAL SHEETS IF NECESSARY):



## See table of contents
TOTAL NUMBER OF PAGES
__ _ IL**532~238** 

## PAGE 2 PAGE20F2 APC 200 Rev. 8/89

## Table of Contents Page APC 200 - Application To Construct/Operate 1 Table of Contents 

# 3 Certification Statement 5 Exhibit A 6 Exhibit B 7 Exhibit C 8 Exhibit D 

## 9 Plot/Plan Map 10 Facility Diagram 11 Process Emission Units Process Flow Diagram 12 APC 240 - Boiler 13 APC 240 - Stand-By Boiler 16 Process Flow Diagram 19 APC 240 - (2) Air Make-Up Units 20 Process Flow Diagram 23 APC 220 - Sandblast Unit 24

" ,., 

## APC 220 - (2) Sandblast Units 27 APC 260 - DustCollector (Cyclone with Filter Bag) 30 Chrome Plating Unes Process Flow Diagram 36 APC 220 - Chrome Tank A-123 37 IEPA Electroplating Information Request 40 APC 220 - Chrome Tank A-4 45 IEPA Electroplating Information Request 48 APC 260 - Scrubber S3 53 Process Flow Diagram 56 APC 220 - Chrome Tank A-5 57 IEPA Electroplating Information Request 60 APC 260 - Scrubber S2 65 Scrubber Diagram 68 APC 220 - Chrome Tank A-8 69 IEPA Electroplating Information Request 72 APC 260 - Scrubber S4 77

CAGE 3

## Process Flow Diagram APC 220 - Chrome Tank A-6 IEPA Electroplating Information Request APC 220 - Chrome Tank A-7 IEPA Electroplating Information Request APC 260 - Scrubber S1 Scrubber Diagram APC 220 - Electropolishing Tank EP-1 APC 108 APC 260 - Scrubber S8 Scrubber Diagram Process Flow Diagram APC 220 - Chrome Tank 8-1 IEPA Electroplating Information Request APC 220 - Chrome Tank 8-7 IEPA Electroplating Information Request APC 260 - Scrubber S5 Scrubber Diagram APC 220 - Chrome Plating Tank 8-2 IEPA Electroplating Information Request APC 260 - Scrubber S6 Process Flow Diagram APC 220 - Chrome Tank 8-34 IEPA Electroplating Information Request APe 220 - Chrome Tank 8-5 IEPA Electroplating Information Request APC 220 - Chrome Tank 8-6 IEPA Electroplating Information Request APC 260 - Scrubber S7 Scrubber Diagram



## PAGE 4 80 81 84 89 

# 92 97 100 101 104 105 108 109 110 113 118 121 126 

# 129 130 133 138 141 

# 142 145 150 153 158 

# 161 166 

# 169

## CERTIFICAnON

It 

# W,'lJ,'M1 

# G. t/Dtne., 

# Jt,
. do hereby certify that I am the Secretary of 

# E,hlp /I'e. 

# llad**CJ,I'()PI~** .Lc , an Illinois corporation; and am the keeper of the corporate records and seal of subject corporation; that the following is a true and correct copy of a certain resolution duly adopted by the Board of Directors of said corporation on 

## I:;' 

# -(-%5': and that the same has never been renounced and is still in full force and effect: RESOLVED. that

# W.·J1,~m 

# 6;

# flefD!) , 01, be and he is hereby authorized to sign and deliver all permit applications and to apprlve each and every provision of all compliance programs and project completion schedules in conformity with the laws and regulations of environmental control agencies of any state of the United States.

PAGE 5

### EXHIBIT A

EQUIPMENT 10 

### Status As Of 1972 Stand-By Boiler 

### 82 Compliant



### PAGE 6

### Empire Hard Chrome

EQUIPMENT ID CONTROL EQUIPMENT status
. Start-Ue, Date 

### Boilers B1 None Replacement 1982 Stand-By Boiler 82 None Original Pre 1972 Air Make-Up Units AM-1,AM-2 NA Original 1974 Chrome Plating Tank A-123, A-4 Scrubber, S3 Additional 1988
Chrome Plating Tank A-5 Scrubber, S2 Original 1985
Chrome Plating Tank A-6, A-7 Scrubber, S1 Additional 1986
Chrome Platina Tank A-8 Scrubber, S4 Additional 1986
Chrome Plating Tank B-1, B-7 Scrubber, 55 Original 1985
Chrome Plating Tank 

### B-2 Scrubber, 56 Additional 1988
Chrome Plating Tank B-34, B-5, B-6 Scrubber, 57 Original 1985 Eledropolishing Tank EP-1 Scrubber, 58 Original 1986 Sandblaster 5B1 Dust Collector, DC1 Original 1986 Scrubbers S1-S8 NA Original 1986 Cyclone/Filter Dust DC1 

# NA Original 1986 Colledor



### PAGE 7

### EXnlBITC
Emissions rrom Chrome Plating Tanks: 

## Tan k Max Amps 

### Emissions (CR6) Iblhr Chrome Emissions PTE (TPY) 

### A

-1 23 (eR6) 3000 0.065 0.284 A

-4 4000 0
.086 0.378 A

-5 1 0000 0.2 1 6 0.946 A

-6 1 5000 0.324 1.4 1 9 A-7 1 5000 0 .324 1.419 

### A-8 15000 0.324 1.4 1 9 B-1 59000 1
.274 5.582 8-2 11500 0.248 1.088 

### 8

-34 2500 0.054 0.237 8-5 500 0.0 1 1 0
.047 8-6 2500 0.054 0.237 8-7 30000 0
.648 2.838 Total 

### 3
.629 15 .894

Ch r ome Emissions (LB/HR) = 

### Max Amps a 

### 0 .0000216 LBIHR"AMP Chrome Emissions PTE (TPY) = 

### Em issions (LBIHR) a 

### 8760 (HRfYR) Actua l Chrome Emissions = 

### Chrome Emissions a 

### 0.025

PAGES Actual Chrome Emissi ons (TPY) After Scrubber 

### 0.009 0.0 1 1 0.028 0
.043 0.043 

### 0.043 0
. 167 0.033 0.007 0.00 1 0.007 0
.OB5 0.477

### Exhibit 

### 0

Non-Exhausted Tanks: Tank 

### 10 Composition Size (Gal) Emissions (LB/HR) C1 HCI 370 <0.1 C2 Caustic 340 < 0.1 C3 HCI 35 < 0.1 C4 Caustic 300 < 0.1 C5 HCI 360 < 0.1 C6 Caustic 2750 < 0.1

PAGE 9

# Business**~** 

### 0 0 

# -n -I 

# 1.5 M i les <1l 

# ::u Emp i re Hard c r rome 

# >=;;. CD (f) (f) 

# ( 0 

### D. 

## I CD 

# 125 FT OJ () 

### CD

# ~S- Q) 

# %,i. 2 &.,\'**~** 

## CJ 

# Nursing Home School

------**~OlC l** 

IOCAI ()Il 

# c: >A7 \"ji:.E \-\ OR () 

## C..;**~o ME:....** 



## - 1iI 1£ 

### Pu :..r'T 1' tAN 1) I A**<.>-R.~** CV\



### _SCill -I!!? 1!l!il!l.- 

### --'lL... 

# ::'k:

SC(Ulf ( COlllRi,X· iiDS. 

### n: 3.2."i:i:1: 0 }1 5! SOIIilI roll l AV{ 11lIl {l OCO. I f06?l

# w

# ~ a:: w 

# zIU) 

# o**~** 

# OFFICE 01 sal



# PROCESS 

# AREA

II , .' '



### o



## 1 gum:-I


# 17th STREET OFFICE



# -

rROMel IQCAlrJI 

## liiif 1 

# E"MPIRE FA'-tLiTy

---- 

### _1"**~_~S"** I It COIIIRIII lAOS. 11«:. .. SQL(-

SCUIlII/ )1511 

### sou CIIlCACO III 1(0181 AVUIU[

. II 60m 

# N 

# I

\-\A9-P**CH~oM€"**



## Df4bnAM 1II!11t1IM:m RJV AY 

## nm

Qoq',,," MCr lillfF

# Exhaust EBOIL-1 100 CFM 130 F /1',

I I I I I I I I I I I 

# Boiler BOIL-1

Firing Rate 1.674 Million BTU/HR

PROllCI IOCAIKll 1111( I 

# i:MPIRE. Belli:· 'O!:.

### ~**-~** SCIllIlI1 ( COIIIROI lABS. INC. ,III**~OIDI** AV[t1lJ[ 1I58SUl C'IlCACO. Il 60621 

# {-\AeO C 1-1 ef)NE..

IIJIAIJDr: In IIfV BY 

### nAIr**GOC\4\~** 

# "'I.-**loJ~r**, •••••• ,**'~**•• ! •••••• 

### ... ,- '._._,.' 

## -

# ....**~-.---.**
0 ••**~**


### STAre OF ILUNOIS ENVIRONMENTAL PROTECTION AGENCY DIVISION OF AIR POLLUTION CONTROL 2200 CHURCHILL ROAD SPRINGfIB.D. ILLINOIS 62706 Tl*AQIncy 118UCIDti.d 1D
.... dIIIlufllltNIIDi.

### i.nd.r ..... ReviMdStnIIII. 1979. 

### CJi8DW 1111/2, Sec:IIDii 1039.D*-- oftfIia infonnallon II required undIrIftaS..:llDil. faiIIn todo .,....,**~dIII** farm fnIm t.ing PI a ! IIId could 

### rilwtlft 'flU'



### -DATA AND INFORMATION FUEL COMBUSTION EMISSION SOURa application**t.ing~** Thia farm.,..
....**~br.1III** 

### ... "'l8QIiIMtitCenw.



### -THIS INFORMATION FORM IS TO BE COMl'lETED FOR A FURNACE. BOILER. OR SIMILAR EQUIPMENT USED FOR THE PRIMARY PURPOSE OF PRODUCING HEAT OR POWER BY INDIRECT HEAT TRANSFER. AN EMISSION SOURCE THAT DOES NOT FIr THIS DESCRIPTION, INO.UDING AN EMISSION SOURCE USING DIRECT HEATING, IS EITHER A PROCESS EMISSION SOURCE OR AN INCINERATOR.

I. 

### NAME OF OWNER: 2. NAME OF CORPORATE DIVISION OR PlANT (IF DIFFERENT FROM 

## EMPIRE HARD CHROME OWNER): 

### 3. STREET ADDRESS OF EMISSION SOURa: 4. CITY OF EMISSION SOURCE: 

### 1h1'i**~ ~l**  I..
...

·I·NI';I( ZHn:'I\1TJR 

## CHICAGO

GENERAL INFORMATION 

### S. FLOW DIAGRAM DESIGNATION(S) OF EMISSION SOURCE: 

## BOII.-1



## . MANUFAcnJRER: 

### 7. MODB. NUMBER: 

# l 8. SERIAL NUMBER: 

### SELLERS 15 SENIOR 

# --- 9. 

### AVERAGE OPERATING TIME Of EMISSION SOURa: 

### 1O. MAXI.w.JM OPERATING TIME Of EMISSION SOURCE:

### ~~ HRS/DAY 

# Z DAYS!WK 

# 52 WKS/YR

### ~4 HRS/DAY 

## 7 DAYS/WK 

## 52 WKS/VR 11. 

### PERaNT OF ANNUAL HEAT INPUT: OEC-F£B 

## 30 % 

### MAR-MAY 

## 25 % 

### JUN-AUG 

## 20 % 

### SEP-NOV 

## 25 %



### I NSllUCTlONS \. COWLEre THE ABOVE IDENTIFICATION AND GENERAL INFORMATION SECTION. 2. COMPLETE THE APPROPRIATE FUEL SECTION OJ SEcnONS. IF MORE THAN ONE FUEL IS FIRED OR IF THE CAPABILITY EXISTS TO FIRE MORE THAN ONE FUEL. THE ACTUAL USAGE OF FI!CLS AND THE RELATIONSHIP BETWEEN FUELS, SIMULTANEOUS FIRING, ALTERNATE FIRING, RESERVE FUEL, ETC., MUST BE MAOE a.EAR. 3. EMISSION AND EXHAUST POINi INFOP';MTION MUST BE COMPLETED, UNLESS EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONTROL EQUIPMENT. 4. FIRING RATES AND aRTAIN OTHER ITEMS REQUIRE BOTH AVERAGE AND MAXIMUM VALUES. 5. FOR GENERAL INFORMATION REFER TO "GENERAL INSllUCtIONS FOR PERMit APPliCATIONS," APC-201.

DEFINITIONS AVERAGE

- THE VALUE THAT SUMMARIZES OR REPRESENTS THE GENERAL CONDITION OF THE EMISSION SOURCE, OR THE GENERAL STAre OF HEAT PRODUCTION OF tHE EMISSION SOURCE. SPEciFICALLy: AVERAGE OPERATING TIME -AcnJAL TOTAL HOURS OF OPERATION FOR THE PRECEDING rwa.VE MONTH PERIOD. AVERAGE RATE

- ACTUAL TOTAL QUANTITY OF "MATERIAL" FOR THE PRECEDING TWB.ve MONTH PERIOD, DIVIDED BY THE AVERAGEOPERATING TIME. AVERAGE OPERATION

- OPERATION TYPICAL OF THE· PRECEDING TWB.VE MONTH PERIOD, AS REPRESENreD BY AVERAGE"OflOATlNG TIME AND AVERAGE RATES. l.tAXIMUM

- THE GREATEST VALUE ATTAINABLE OR ATTAINED FROM THE EMISSION SOURCE, OR THe PERIOD OF'GRFATEST OR UTMOST HEAT PRODUcTION OF THE EMISSION SOURCE. SPEciFICALLY: MAXIMUM OPERATING TIME

- GREATEST EXPECTED TOTAL**HOU~Qf!"-PEIYnION** 

### FOR ANY rwa.VE MONTH PERIOD. MAXIMUM RATE

- GREAresT QUANTITY OF "MAreRIAL" EXPECTaOnAN"9 'ONE HOUR OF OPERATION. MAXIMUM OPERATlON

- GREATEST EXPECTED OPERATION, AS REPRESENTED BY MAXIMUM OPERATING TIME AND MAXIMUM RATES.• .... < -< • -.- • ,_. ••**~** • • • • •• .:. _ ...... --- • 

# ----...**~--..............--.** clll,-**.~~"...**



### GAS FIRING "11. 

### ORIGIN OF GAS: 

# o DISTI1.LATE FUEL 

# 0 OTHER LIQUID FUEL 

# 0 SOLID FUEL 

# 0 BYPRODUCT: 

# 0 PIPELINE OIL GASIFICATION GASIFIc::ATION GASIFICATION SPECIFY SOURCE 12. ARE YOU ON AN INTERRUPTABt.E GAS SUPPLY: 

# Om '

### ~ NO IF ,"YES", SPECIFY ALTERNATE FUEL: 13. ANNUAl. CONSUMPTt0t: • 14. HEAT CONTENT: 

# r 15. SULFUR CONTENT: 

## 14.6 x 

## 10 

## so: 8TU/SCF %BVWT. 16. 

### AVERAGE FIRING RATE: 

## 10 6 " 

### 17. MAXIMUM FIRING**RA~:** 

## 1.674 x BTU/HR 

## 1 L 

## 674 x 

## 10 BnJ/HR "IF THE GAS FIRED IS NATURAL GAS, THESE ITEMS NEED NOT BE COMPLETED.

OIL FIRING 18. 

### TYPE OF OIL: GRADE NUMBER: 

# 01 

# o 2 

# o "' Os 0 & 

### OTHER: SPECIFY 

# 19. ANNUAL CONSUMPTION: 

### 20. HEAT CONTENT: 

# o BTUILB GALLONS 

# o BTU/GAL 

### 21. SULFUR CONTENT: 

### 22. ASH CONTENT: '?'o8VWT %8VWT 

### 23. DIRECTtON OF FIRING:



# 0 HORIZONTAL 

# 0 TANGENTIAL 

# 0 OTHER: SPECIFY 

### 24. AVERAGE FIRING RATE: 

### 25. MAXIMUM FIRING RATE: BTU/HR BTU/HR 

# -

SOLID FUEl. FIRING



### 26. TYPE OF SOLID FUEL:



# o SUB-3ITUMINOUS COAL 

# 0 illTUMINOUS COAL 

# o ANTHRACITE COAL 

# o OTHER: SPECIfY 

### 27. ANNUAL CONSUMPTION: TONS 

# I 28. HEAT CONTENT AS FIRED: BTU/LB 

### 29. MOISTURE CONTENT AS FIRED: %BVWT 

# I JO. ASH CONTENT AS FIRED: %BYWT 

# I J1. SULFUR CONTENT AS FIRED:**%8V~** 

### l2. TYPE OF FIRING:



# 0 CYCLONE 

# o PULVERIZED 

# {O WET BOTTOM O' 

# 0 DRY BOTTOM, 

# o HORIZONTALL

### v OPPOSED OR 

# 0 OTHER: SPECIFY 

# 0 SPREADER STOKER: % REINJECTION 

# o OTHER: SPECIFY 33. AVERAGE FIRING RATE: 

# I 34. 

### MAXIMUM FIRING RATE: BTU/HR BTU/HR SUBMIT COPIES OF THOSE PORTIONS OF COAL OR OTHER SOLID FUEL CONTRACTS WHICH SET FORTH THE SPECIFICATIONS OF THE FUEL AND THE DURATION OF THE CONTRACT. IF THE ACTUAL FUEl. FIRED IS A BLEND OF SOLIO FUELS, SUBMIT APPROPRIATE PORTIONS OF ALL FUEL CONTRACTS ANO SET FORTH THE MANNER IN WHICH THE FUELS ARE BLENDED AND ACTUALLY FIRED. REFtRENCE THIS INFORMATION TO THIS FORM.**".,..~** 

### ... _.- ....**~ISSION** INFORMATION

## ~:b. NUMBS OF IDENTICAl. SOURCES (DESCRIBE AS REQUIRED): 

### 1 AVERAGE OP£KATION

### ~---

# ~ CONaNTiATIoNOR EMISOO';;'tEPER

"iDENTiCAL

- r- - 

# MerHOD useD

# TO**mE~iCO~ncN** 

# OR -. CONTAMINANT SOURe! EMISSION RATE PARTICUlATE 36a. 

### b. 

### C 181106 BTU c. 

### MATTER GIVSCF 

### [] II/HR 

### EMISSION RATES BASED ON EMISSION CARlON 370. PPM 

### b. a 

### 181106 BTU c. MONOXIDE (VOL) 

### C 

### Ll/HR FACI'ORS FOR GAS-FIRED E)'JUIPMEm' NITROGEN 

### 380. PPM 

### b'. a LB/106 BTU c. OXIDES (VOL) 

### C LB/HR 

### AND NATURAL GAS USAGE FROM USEPA ORGANIC 39a. PPM 

### b. o LB/l06 BTU c. 

## AP-42 . MATEltIAL (VOL) a LB/HR 

# - SULFUR 400. PPM 

### b. a LB/la6 BTU c. DIOXIDE (VOL) a tB/HR MAXIMUM OPERATION 

## -----r- - - - --- - - - - - - -**~-** 

# ------------



# .. CONCENTRATION OR EMISSION RATE PER IDENTICAL METHOD USED TO DETUMINE CONCENTRATION OR

r-nNTAMINANT c;nIIRn: 

# - ." "
.....,...**IPA~** PARTICULATE 410. 

### b. a LB/l00 BTU 

# .. MATTER GR/SCF a LB/HR CARBON 42a. PPM 

### b. a LBlloO BTU c. MONOXIDE (VOL) a LB/HR NITROGEN 430. PPM 

### b. a LB/loO BTU c. OXIDES (VOL) a L8/HR 'NIC 40li0. PPM 

### b. a L8/I06 BTU c. h .c1UAL (VOL) aLB/Hit SULFUR 4Sa. PPM 

### b. CL8/I06 BTU c. DIOXIDE (VOL) CLB/HR "IF EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONTROL EQUIPMENT, OR IF NATURAL GAS IS THE FUa. FIRED, ITEMS 36 THROUGH 47 NEED NOT BE COMPlETED,

··EXHAUST POINT INFORIMTION 

### 46. flOW DIAGRAM DESIGNATlON(S) OF EXHAUST POINT: 

## EBOIL-l 

# - 1.7. DESCRIPTION OF EXHAUST POINT (LOCATION IN RB.ATION TO BUILDINGS, DIRECTION, HOODING, ETC.): 

### STACK LOCATED AIDNG NORTH EDGE OF BUILDING 48. EXIT HEIGHT ABOVE GRADE: SO. EXIT DIAMETER: 

## 34 

## ft 10" 49. GREATEST HEIGHT OF NEARBY BUILDINGS: 

### 51. EXIT DISTANCE FROM NEAREST PlANT BOUNDARY: 

## 30 FT 

## 20 FT AVERAGE OP£KATION MAXIMUM OPERATION 

### 52. EXIT GAS TEMPERATURE:**~.** EXIT GAS TEMPERATURE: 

## 130 OF 

## 130 OJ: 53. GAS FLOW RATE THROUGH EACt EXIT: 

### 55. GAS FLOW RATE THROUGH eACt EXIT: 

## 100 ACFM 

## 100 ACFM eMISSIONS ARE EXHAUSTED THROUGH AIR pOl.LlJnON CONTROL EQUIPMENT THIS SECTION SHOULD NOT BE COMPlETED. "_.f O .-,"

## . '. :: 

## .. STAT! OF ILLINOIS ENVIRONMENTAL PROTECTION AGENCY DIVISION Of: AIR POLLUTION CONTROL 2200 CHURCHILL ROAD SPRINGFIELD, IWNOIS 62706

eDATA AND INFORMATION ruEL COMBUSTION EMISSION SOURCE

### ".~ ..8IdIiarii.stltlWqlfttlailb'I.Ib"'undIr'" R
....StdIR 1979.a.w1111I2.,SecdDn103I.D
...... 

# 0' ttIia InfarmI1Ian II requinJd undIr1lwtSection. F
....IO do

# 10,.,., jlIfteftt UIIa form from being pra 11II**~** end could
....In V-

. eppIk:adan '-ing
.....ThIa form iliat..'Iapprawdby.theFGan. Maneg.memConw.
.

-THIS INFORMATION FORM IS TO BE COMPLETED FOR A FURNACE, BOILER, OR SIMILAR EQUIPMENT USED FOR THE PRIMARY PURPOSE OF PRODUCING HEAT OR POWER BY INDIRECT HEAT TRANSFeR. AN EMISSION SOURCE THAT DOES NOT FIT THIS DESCRlmON, INCLUDING AN EMISSION SOURCE USING DIRECT HEATING,IS EITHER A PROCESS EMISSION SOURCE OR AN INCINERATOR.

1. NAME OF OWNER: 2. NAME OF CORPORATE DIVISION OR PLANT (IF DIFFERENT FROM 

### EMPIRE HARD CHRG1E OWNEIt): 

### 3. STREET ADDRESS OF EMISSION SOURCE:**~.** CITY OF EMISSION SOURCE: 1 t:;;1 C; Q 

### CHICAGO

GENERAL INFORMATION 

### S. FLOW DIAGRAM DESIGNATION(S) OF EMISSION SOURCE: 

## BoIL-2 J. MANUFACTURER: 

### 7. MODB. NUMBER: 

# I 8. SERIAL NUMBER: 

## UNKNOWN ., 

# -- 

# --- 

# - 9. AVERAGE OPERATING TIME OF EMISSION SOURCE: 

### 10. MAXIt.tAJM OPERATING TIME OF EMISSION SOURCE:

### 2~ HRS/DAY 

## 2 OAYS/WK 

### 1 WKS/YR 

## J4 HRS/DAY 

# + DAYS/WK**~** WKSIYR 11. PERCENT OF ANNUAL HEAT INPUT: DEC-FfB 

## 30 % MAIt-MAY ?C; % JUN-AUG ?n % SEP-NOV ?r.:: %

INSTRUCTIONS 1. COMPLETE THE ABOVE IDENTIFICATION AND GENERAL INFORMATION SECTION. 2. COMPLETE THE APPROPRIATE FUEL SECTION Oil SECTIONS. IF MORE THAN ONE FUEL IS FIRED OR IF THE CAPABILITY EXISTS TO FIRE MORE THAN ONE FUEL. THE AcruAl USAGE OF FlleLS AND THE RELATIONSHIP BETWEEN FUELS, SIMULTANEOUS FIRING, ALTERNATE FIRING, RESEltVE FUEL. ETC •• MUST BE MACE a.EAR. 3. EMISSION AND EXHAUST ?OINi INFOP;MTlON MUST BE COMPLETED, UNLESS EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONTROL eCUIPMENT. 4. FIRING RATES AND CERTAIN OTHER ITEMS REQUIRE 30TH AVERAGE AND MAXIMUM VALUES. S. FOR GENERAL INFORMATION REFER TO "GENERAl I NSTRUCfloNS FOR 

### Pl!RMIf APPliCATIONS," APC-201.

DEFINITIONS AVERAGE

- THE VALUE THAT SUMMARIZES OR REPRESENTS THE GENERAL CCNDInON OF THE EMISSION SOURCE, OR THE. GENEItAL STATE Of HEAT PRODUCTION 

### OF THE**~MISSION** SOUACE. SPEciFICALlY: AVERAGE OPERATING TIME

- ACTUAL TOTAL HOURS OF OPERATION FOR THE PRECEDING 

### TWa VE MONTH P1!RIOD. AVERAGE RATE

- ACTUA1. TOTAL QUANTITY OF "MATERIAL" FOR THE PRECEDING TWB.VE MONTH PERIOD, DIVIDED BY THe AVERAGEOPERATING TIME. AVERAGE OPERATION

- OPERATION TYPICAL OF THE PRECEDING TWELVE MONTH PEltIOD, AS REPRESENTED BY AVERAGE OPERATING TIME AND AVERAGE RATES. n_ .'<IMUM" THE GREATeST 'IAlUE ATTAINABLE OR ATTAINED FROM THE EMISSION SOURCE, OR THE: PERIOD OF GREATEST OR UTMOST HEAT PROOUCTION OF THE EMISSION SOURCE. mciFICAUY: MAXIMUM OPERATING TIM!

- GREATEST EXPECTED TOTAL**HOU~ERbBON** FOR ANY rwa.VE MONTH PERIOD. MAXIMUM RATe

- GREATEST QUANTnV OF "MATeRIAL· EXPECTED PER ANY ONe HOUR OF OPERATION. MAXIMUM OPERATION

- GREATeST EXPECTED OPERATION, AS REPRESENTED BY MAXIMUM OPERATING TIME AND MAXIt.tAJM RAT!S.

# .. 

# --**t.:·::'·-··,~-· ~** 

### ..

GAS FIRING



# ...... 

# o DISTILLATE FUEL 

# 0 OTHER LIQUID FUel 

# 0 SOLID FUel 

# 0

'II. ORIGIN OF GAS: BYPRODUCT:



# 0 PIPeliNE OIL GASIFICATION GASIFICATION GASIFICATION SPECIFY SOURa 

### 12. ARE YOU ON AN INTERRUPTABlE GAS SUPPlY, 

### DYeS 

## []I NO IF ·YES", SPECIFY ALTERNATE FUel: 

### 13. ANNUAl. CONSUMPTION: 

### 5 

# I- 14. HEAT CONTENT: 

# r IS. SUlFUR CONTENT: 

## 2.8 X 

## 10 

## sa: BTU/SCF %BYWT. 

### 16. AVERAGE FIRING RATE: 

# I 17. MAXIMUM FIRING RATE: 

### 1 1i74 

### x: 10 

## 6 BTU/HR 

## _1

## ji.'Z~L.x. _1 

# a 7 STU/HR ,F THE GAS FIRED IS NATURAL GAS, THESE ITEMS NEED NOT BE COMPLETED.

OIL FIRING 

### 18. TYPE Of OIL: GRACE NUMBER: 

### 01 

# 0 2 

# 0 .1 

# C! : 

# 0**~** OTHER: SPECIFY 

### 19. ,l.NNUAL CONSUMPTION: 

### 20. HEAT CONTENT: 

# o BTUIlB GALLONS DaTU/GAL 

### 21. SULFUR CONTENT: 

### 22. ASH CONTENT: %Sywr %SYWT 23. OIRECiION OF FIRING:



# 0 HORIZONTAL 

# 0 TANGENTIAL 

# 0 OTHER: SPECIFY 

### 24. AVERAGE FIRING RATE: 

### 25. MAXIMUM FIRING RATE: BTU/HR STU/HR L-.

SOLID FUel FIRING 

# . 26. TYPE OF SOLID FUEL: 

# o SUS-aITUMINOUS COAL 

# 0 alTUMINOUS COAL 

# o ANTHRACITE COAL 

# o OTHER: SPECIFV 

# I 27. ,l.NNUAL CONSUMPTION: TONS 

# I 28. HEAT CONTENT AS FIRED: 

### I BTUIlS



### 29. MOISTURE CONTENT )'S FIRED: %BYWT 

# I 30. ASH CONTENT AS FIRED: 

# J 31. SULFUR CONTENT AS FIRED: %BYWT %BYWl 

### 32. TYPE OF FIRING:



# 0 evo.ONE 

# o PULVERIZED 

# {O WET ,onOM O. 

# 0D.vaonoM, 

# o HORIZONTALLY OPPOSED OR 

# 0 OTHER: SPECIFY 

# 0 SPREADER STOKER: % REINJECiION 

# o OTHER: SPECIFY 

### 33. ,l.VERAGE FIRING RATE: 

# I 34. MAXIMUM ;:IRING RATE: BTU/HR STU/HR SUBMIT COPIES OF THOSE PORTIONS OF COAL OR OTHER SOLID FUEL CONTRACTS WHICH SET FORTH THE SPECIFICATIONS OF THE FUEL AND THE DURATION OF THE CONTRACT. IF THE ACTUAL FUel FIRED IS A BLEND OF SOLID FUELS, SUBMIT APPROPRIATE PORTIONS OF AU FUEL CONTRACTS AND SET FORTH THE MANNER IN WHICH THE FUELS ARE BLENDED AND ACTUALLY FIRED. REFERENa THIS INFORMATION TO THIS FORM.



## PAGE 17 PAGE 2 OF l-EMISSION INFOIMATION

## ~. .**~UMlEI** OF IDENTICAL SOURCES (DESOIBE AS REQUIREDh 

### 1 AVERAGE OPERATION 

### ........ 

# ...... ".'

. 

## .. 

# .... 

# ..**~** 

# --**--~** 

# ---- ---.- - 

# - 

# --- 

# r------------------. CONCENTRATION 

# .2!. EMISSION RATE PER IDENTICAL METHOD USED TO DmRMINE CONOlNTRATION OR CONTAMINANT SOURCE EMISSION RATE PARTICULATE 360. 

### b. C ISIlo6 BTU c. MATTER GRlSa 

## a IIIHIt CARBON 370. PPM 

### b. a 

### 111106 BTU c. MONOXIDE (VOL) a LB/HR NITROGEN 

### 380. PPM 

### b'. a L8/100 BTU c. OXIDES (VOL) a L8/HR ORGANIC 390. PPM 

### b. a LB/l06 BTU c. MATERIAL (VCl.) a La/Hit 

# - SUlfUR 4Oa. PPM 

### b. C LBllo6 BTU c. DIOXIDE (VCl.) 

## o lBlHI MAXIMUM OPERATION • - - - -- - - - - - - - - - - - - - r-- 

# ------------ CONCENTRATION OR EMISSION RATE PER IDENTICAL METHOD USED TO DETERMINE CONCENTRATION OR ('nNTAMINANT**~nl'Rn:** 

# - I=M'
.... 'nN DAn: PARTICULATE 410. 

### b. o LBll06 BTU 

# .. MATTER GRlSCF C LBlHR CARBON 

### 420. PPM 

### b. o LBll06 BTU c. MONOXIDE (VOL) C LB/HR NITROGEN 430. PPM 

### b. aLB/l06 BTU c. OXIDES (VOL) C LB/HR 0"**~IC** 4Aa. PPM 

### b. a LB/l06 BTU c. M- AL (VOL) alB/HlI SU1.FUR 450. PPM 

### b. a LB/l06 BTU c. DIOXIDE (VOL) aLB/HR ·IF EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONTROL EQUIPMENT, OR IF NATURAL GAS IS THE FUB. FIRED, ITEMS 36 THROUGH 47 NEED NOT SE COMPlmD.

·-exHAUST POINT INFORMATION 

### 46. FLOW DIAGRAM DESIGNATION(S) OF EXHAUST POINT: 

## EBOIL-2 

# - .1.7. DESCRIPTION OF EXHAUST POINT (LOCATION IN RB.ATION TO BUILDINGS, DIRECTTON, HOODING, ETC.): 

### STACK LOCATED AIDNG NORl'H EOOE OF BUILDING 48. EXIT HEIGHT ABOVE GRADE: 

### 50. EXIT DIAMETER: 

## 34 10" 49. GREATEST HEIGHT OF NEARBY BUILDINGS: 

### Sl. EXIT DISTANCE FROM NEAREST PlANT BOUNDARY: 

## 30 FT 

## 28 FT AVERAGE OPERATION MAXIMUM OPERATION 

### 52. EXIT GAS TEMPERATURE: 

### 5". EXIT GAS TEMPERATURE: 

## 130 OF 130 

### "fI 53. GAS A.OW RATE THROUGH EACH EXIT: 

### 5S. GAS A.OW RATE THROUGH EACH EXIT: 

## 1nn AaM 

### 1nn ACFM •• IISSIONS ARE EXHAUSTED THROUGH Alit POt.LlJTlON CONTROL EQUIPMENT THIS SECTION SHOUlD NOT BE COMIU11!D.



## PAGE 18 PAGE 3 OF 3

# Exhausted Inside 55,000 CFM 70 F /1',

1 1 I 1 I 1 I 1 1 I 1 

# Air Make-Up Unit AM-1

Firing Rate 1.3 

# Million BTU/HR

fROJICI LOCAl011 

# 'tJVl ?1\2€**~\LWO** 

## CJ\WM£ 

## Mii A liZ. f'/'f\.cE - 

## uf Utvnr _SCaf
________ Ill!!DG dI SCIlIIIII C COIURIIl IAIIS_ IIC**~12!n:** 1158 SIlIJIII KI)lg1 AV[IM CtICACO_ It 60611 :



# . lIrV Itt 

### oAir WI..- LtL'l!J



# - . l.


### STATE OF ILUNOIS ENVIRONMENTAl. PROra:nON AGENCY DIVISION OF AIR POUunON CONTRC1. 2200 CHURCHILL ROAD SPRINGFIB.D, IUlNOIS 62706

-DATA AND INFORMATION FUEL COMBUSTION EMISSION SOURCE 

### .**.~**

### T1iaAg-.:yIs~ID"""ClllaiifGiI.IiDO"""" RNledS.,. 1979.c:a,..,w1 11 112.SectIan 1031.D
___ of CIlIa infGmaIIan Is**~** WldlrtflaSeclioft.FIiIIn ID do • ...,**~** tills form from IMing sa lind could r.utlnyaur

. I1IPicaIian IMing cMnied. T1ia form lIDbllnlAl'CMd
_ 

# tIM,...**~c.nw.** 

### .

-THIS INFORMATION FORM IS TO BE COMPleTED FOR A FURNACE, BOILER, OR SIMILAR EQUIPMENT UseD FOR THE PRIMARY PURPOSE OF PRODUCING HEAT OR POWER BY INDIRECT HEAT TRANSFER. AN EMISSION SOURCE THAT DOES NOT FIT THIS DESOIPTION, INa.uDING AN EMISSION SOURCE USING DIRECT HEATING, IS EITHER A PROasS EMISSION SOURCE OR AN INCINERATOR.

I. NAME OF OWNEIb 

### 2. NAME OF CORPORATE DIVISION OR PlANT (IF DIFFERENT FROM 

### untln OWNER): 

### 3. STREET ADDRESS OF EMISSION SOURCE: 4. CITY OF EMISSION SOURCE: 

### 1615 S. KOSTNER**A'v~u~** 

### ("J.J--nr.r

GENERAl. INFORMATION 

# s. flOW DIAGRAM DESIGNATION(S) OF EMISSION SOURCE, 

### AM-1, AM-2 6. MANUFACTURER: 7. MODa. NUMBER: 

# f 8. SERIAL NUMBER. 

## LENNOX LLBL240 5135 

## & 5136 Y. 

### AVERAGE OPERATING TIME OF EMISSION SOURCE: 10. MAXIMUM OP9ATING TIME OF EMISSION SOURCE, 

## 22 HIS/DAY 

## 2 DAYS/WK 

## 52 WKS/VR**~4** 

### HIS/DAY**~** 

### DAYS/WK 

### 3d WKS/VR 11. 

### PERCENT OF ANNUAL HEAT INPUT: 

### ·1n DEC-FEB 

### 50 % 

### MAR-MAY 

## :m 

# '*' JUN-AUG 

# '*' SEP-NOV 

### .,n 

# '*'

INSTRUCTIONS I. COMPLETE THE ABOVE IDENTIFICATION AND GENERAL INFORMATION SECTlON. 2. COMPLETE THE APPROPRIATE FUEL SECTION Oil SECTIONS. IF MORE THAN ONE FUEL IS FIRED OR IF THE CAPABILITY EXISTS TO FIRE MORE THAN ONE FUEL, THE ACTUAL USAGE OF FI!CLS AND THE RELATIONSHIP BETWEEN FUELS, SIMULTANEOUS FIRING, ALTERNATE FIRING, RESERVE FUEL, ETC., MUST BE MADE o.EAR. 3. EMISSION AND eXHAUST POINi INFOP':MTION MUST BE COMPLETED, UNLESS EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONTROL EQUIPMENT. 4. 

### FIRING RATES AND CERTAIN OTHER ITEMS REQUIRE BOTH AVERAGE AND MAXIMUM VALUES. S. FOR GENERAL INFORMATION REFER TO "GENERAL INSTRuctioNS FOR PERMit APPliCATIONS," APC-20t.

DEFlNmONS AVERAGE

- THE VALUE THAT SUMMARIZES OR REPRESENTS THE GENERAL CONDITION OF THE EMISSION SOURCE, OR THE GENERAL STATE Of HEAT PRODUCTION 

## Of TRE EMISSION 

# soCita. sPEdflCACtv: AVERAGE OPERATING TIME

- ACTUAL TOTAL HOURS OF OPERATION FOR THE PRECEDING TWaVE MONTH PERIOD. AVERAGE RATE

- ACTUAL TOTAL QUANTITY OF "MATERIAl· FOR THE PRECEDING TWaVE MONTH PERIOD, DIVIDED BY THE AVERAGE OP!JATING TIME. AVERAGE OPERATION

- OPERATION TYPICAL OF THE· PRECEDING TWaVE MONTH PERIOD, AS REPltESENTED BV AVERAGE OPERAnNG 

### nM£ AND AVERAGE RATES. "MUM

- THE GREATEST VALUE ATTAINABLE OR ATTAINED FROM THE EMISSION SOURCE, OR THE: PERIOD OP· GRfATEST OR UTMOST HEAT PRODUcTION OF THE EMISSION SOURCE. SPEciFICALLY: MAXIMUM OPERATING TIME

- GREATEST EXPECTED TOTAL**HOU~~ap~ION** 

### FOR ANY TWELVE MONTH PERIOD. MAXIMUM RATE

- GREATEST QUANTnY OF -MATERIAL- EXPECTtb",a ANY ONE HOUR OF OPERATION. MAXIMUM OPERATION

- GREATEST EXPECTED OP!JATION, AS REPRESENTED BY MAXIMUM OPeRATING TIME AND MAXINAJM RATES.


### PAGE 

### 20· 

## ..**~** 

### .. '" . 

### - 

## -

## ..**~** 

## . -- 

## - . 

### - .. 

### --"'-:'.**-~ ~-~--=..**  

### - ..-.' c:.". .**..;--~** ___

GAS FIRING ·11. ORIGIN OF GAS: 

# o DISTILLATE FUEL 

# 0 OTHER LIQUID FUB. 

# 0 SOLID FUEL 

# 0 BYPRODUCT:



# 0 PlPB.INE OIL GASIFICATION GASIFICATION GASIFICATION SPECIFY SOURCE 12. ARE YOU ON AN INTERRUPTABlE GAS SUPPLV: IF ·"VES", SPECIFV ALTERNATE FUB.: 

# DYeS IiI NO 13. ANNUAL CONSUrON: • 14. HEAT CONTENT: 

# ,e 15. SULFUR CONTENT: 

## 2.97 X 

## 10 SCF BTU/sa %BYWT. 16. AVERAGE FIRINGEfATE: 

# I 17. MAXIMUM FIRING RAn: 

## 1.30 

## x 10 BTU/HR 

## 2.595 

## x 1Jl 6 BTU/HR 

### ,F THE GAS FIRED IS NATURAL GAS, THESE ITEMS NEED NOT BE COMPLEnD.

OIL FIRING lB. TYPE OF OIL: GRADE NUMBER: 

# 01 

# o 2 

# 0 4 

# Os 

# 0 .s OTHER: SPECIFY 19. ANNUAL CONSUMPTION: 

### 20. HEAT CONTENT: 

# o BTUIlB GALLONS 

# o BTU/GAL 21. SULFUR CONTENT: 

### 22. ASH CONTENT: '!fo8YWT %BYWT 

### 23. OIRECTlON OF FIRING:



# 0 HORIZONTAL 

# 0 TANGENTIAL 

# 0 OTHER: SPECIFY 

### 24. AVERAGE FIRING RATE: 

### 25. MAXIMUM FIRING RAn: i..- BTU/HR BTU/HR

SOLID FUEL FIRING 26. TYPE OF SOL 10 FUEL:



# o SUB-aITUMINOUS COAL 

# 0 BITUMINOUS COAL 

# o ANTHRACITE COAL 

# o OTHER: SPECIFY 

### 27. ANNUAL CONSUMPTIONI 

# I 28. HEAT CONTENT AS FIRED: TONS BTU/LB 

### 29. MOISTURE CONTENT AS FIRED: 

# I 30. ASH CONTENT AS FIRED: 

# I 31. SULFUR CONTENT AS FIRED: %8YWT %BYWT %BYWl 

### 32. TYPE OF FIRING:



# 0 CYCLONE 

# o P\JL

### VERIZED 

# {O worr BOTTOM O' 

# 0 DRY BOTTOM, 

# o HORIZONTALLY OPPOSED OR 

# 0 OTHER: SPECIFY 

# 0 SPREADER STOKER: % REINJECTION 

# o OTHER: SPECIFY 33. AVERAGE FIRING RATE: 

# I 34. MAXIMUM FIRING RATE: BTU/HR BTUIHR SUBMIT COPIES OF THOSE PORTIONS OF COAL OR OTHER SOLID FUEL CONTRACTS WHICH SET FORTH THE SPECIFICAnONS OF THE FUEL AND THE DURATION OF THE CONTRACT. IF THE ACTUAL FUEL FIRED IS A BLEND OF SOLID FUELS, SUBMIT APPROPRIATE PORnoNS OF ALL FUEL CONTRACTS AND SET FORTH THE MANNER IN WHICH THE FUELS ARE BLENDEO AND ACTUALLY FIRED. REFERENCE THIS INFORMATION TO THIS FORM.

## .............. -.. 

### - _ 

## .... ' 

### . '.

. 

## •

-eMISSION INFORlAATlON**~** • tN. 

### NUMBER OF IDENTICAL SOURces (DESCRIBE AS REQUIRED): 

### 2 AVERAGE OP!RATION**~---.**

## ~-------~-----~------~------ CONCENTRATION 

# 2!EMISSION RATE PER IDENTICAL METHOD USED TO DmRMINE CONC!NTIATION Olt CONTAMINANT SOURCE EMISSION RATE PAlTICULATE 36a. 

### b. a II/To6 BTU e. 

### MATTEIt GalSCF a IB/HR 

### EMISSION RATES BASED ON EMISSION CAUON 

### 370. 

### PPM b. a IB/l06 BTU e. 

### MONOXIDE (VOL) a Ll/HR 

### FAcroRS FOR GAS-FIRED mOIPMENT NITROGEN 

### 380. PPM be. a L8/Tal' BTU e. 

### OXIDES (VOL) o L8/HIt 

### AND NATURAL GAS USAGE FROM USEPA ORGANIC 390. 

### PPM 

### b. a LB/Tal' BTU e. 

### MATERIAL (VOL) a La/HR 

## AP-42 0 

### SULfUR 400. 

### PPM 

### b. a LB/Tcf BTU e. 

### DIOXIDE (VOL) aLB/folK MAXIMUM OPERATION**~** 

# - - - 

# --- - - 

# - 

# - - - 

# - - - - - - 

# -**~** 

# - - - 

# - - 

# - - - ----- CONCENTRATION OR EMISSION RATE PER IDENTICAl. METHOD USED TO DETERMINE CONCENTRATION OR**~-** ,., II
.... A"lT**C;QIIR~** 

# -**~."""'''''** RAn: 

### PARTICULATE 410. b. 

### a LS/toG BTU .0 

### MATTEIt GR/SCf a lS/f.lIt 

### EMISSION RATES BASED ON t'dYI.**~~** JN 

### CARBON 42a. 

### PPM 

### b. a LS/t06 BTU e. 

### MONOXIDE (VOL) aU/Hit 

### FAcroRS FOR 

### GAS ,. .. KI';**mr·~pMF.N-l·** 

### NITROGEN 430. 

### PPM 

### b. a La/tal' BTU c. 

### OXIDES (VOL) a L8/HR 

### AND NATURAL GAS**n~Jl.r.R** FR()M**n~F.P.lI.** 

### O\NIC 4Aa. 

### PPM 

### b. oLl/I06 BTU c. 

### CRIAL (VOL) aU/tm 

## AP-42 SULfUR 450. 

### PPM 

### b. a Ll/t06 BTU e. 

### DIOXIDE (VOL) aU/HIt 'IF EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONTltOl EQUIPMENT, OR IF NATURAl GAS IS THE fUB. FIRED, ITEMS 36 THROUGH 47 NEED NOT BE COMPlETED.

'-EXHAUST POINT INFORMATION 

### 46. flOW DIAGRAM DESIGNATION(S) OF EXHAUST POINT: 

### EXHAUSTED 

# mro BUILDING 

# - 47. 

### DESCRIPTION OF EXHAUST POINT (LOCATION IN RB.ATlON TO BUILDINGS, DIRECTION, HOODING, ETC.): 

### NA All, 

### EXIT HEIGHT ABOVE GRADE: 

### NA 

### SO. EXIT DIAMETER: 

### NA 49. GREATEST HEIGHT OF NEARBY BUILDINGS: 

### 51, EXIT DISTANCE FROM**N~l.EST** 

### PLANT BOUNDARY: 

### NA FT FT AVERAGE OPERATION MAXIMUM OPERATION 

### 52. EXIT GAS TEMPERATURE: 

# 5"'. EXIT GAS TEMPERATURE: 

## 70 70 OF Of: 

### 53. GAS flOW RATE THROUGH EACH EXIT: 

### 55. GAS FLOW RATE THROUGH EAOf EXIT: 

### SS 000 ACFM 

## 55.000 ACFM 

# - :MISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONTROL EQUIPMENT THIS SECTION SHOULD NOT BE COMPLETED.



### n",...'[;1 ..,..,

# ." ./



### SandBlast UnitSB1 Exhausted Out Filter Bag, EDC-1 2400CFM 

## 70 F 

# 'l'

Dust I I I I I I I 

### Collector DC1 

## 99.9 % eft
. ./ 

### I"



### SandBlast UnitSB2 L 

### :"



### SandBlast UnitSB3



## PiiOiiCI**~**

lOCAUlIl 

# e <\'\

### t'{

# \2 £ 

# Hl\I2D**C~Ie.OIV\€** IIIl( 

### %tJv 

## "B**Lf\~T€t2** 

### S 

# .. , SQI[ o\It DRAWII«:IIIl R£Y II't .llAll SCI(IIiIfIC COIIIROl-lABS. IIC. QI"f'?Q 

### -r .N1r..**In/Q~** 1158 SOlllll r.OIBl AV(IIU[



# - 

# .. CIIICAGO. It 6061l.. ": ..•**.::.~ ~** **;.~:----:** .... :**~:"'<-** .......:. ..-: - '."
... _.- ..... - .....**-~.'** .. • J. .:.'**~** 

### .**~'.'** 

# . . '.".

,

### .. ,:- .:' '

## .. '

### STATE OF ILLINOIS'
. ·.;"i • . .. _

### .... - ..... ' ' 

### ......

_ •. ::..•.**~~.'.c'** •. : 

### . . 

### _." 

# ....... '7" ,.: ..• '



### . .'**,~'** 

### ENVIRONMENTAL PROTECTION AGENcY
. DMSION OF Alit 

### POLLUTION CONrROL
. 

# '':'' zzao 0fUICH1Lt. ROAD '
...:.:.:.-:..'
__ ., ::::.:.' '; •. ' :" • ... ... .-**~",** 

## ,.,.!...•

. - SPltNGFIaD IWNQIS 6Z1u.

### T~.:,.... 

## . . ... :: :;.......**:·~·;i~·(.-~~~<·:·** 

# .:..**::~**

# ...**··:'·r;':~\;.)~~:7..:~ji~~~~:~:~~,tf~~[~~t;~;;.;~:s;~iii~i ~~.~::.~~~~}1i~;:~;2;~~~''''';~'~'i** 

.

# ~. ". :"';'

# ~~'.'**.~** '.' '.,;:' ,Y
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# :~**'.~; ~1P~:'~~~~·~~~;~~?f.~** **~ ~:!** **~TA** 

### AND INFORMATION



## ..**.:...~** 

# ..':

. 

### PROCESS EMISSION SOURCE :":"..



### _

# ..

# -_

. 

### . 

## .

-THIS INFORMATION FORM IS TO BE COMPl.mD FOR AN EMISSION SOURCE OTHER THAN' A FUEL COMBUSTION EMISSION SOURCE OR AN

INCINERATOR. A FUEL 

### COMBUSTION EMISSION SOURCE IS A FURNACE, 'BOILER, OR SIMILAR EQUIPMENT USED PIUMARILV FOIt PltODUClNG HEAT OR POWER BY INDIItECT HEAT TRANSFER. AN INCINERATOIt IS AN APPARATUS IN WHICH REFUSE IS BURNED •


# .. 1. NAME OF PLANT OWNER: 

### 2. NAME OF CORPORATE DIVISION OR PLANT (IF DIFFERENT FROM 

### EMPIRE HARD CHROME 

# -- OWNER): 

# 3; STREET ADDRESS OF EMISSION SOURCE: 4. 

### CITY UI" 

### -souRcr:



### 1 615 S. KOSTNER AVENUE 

### CHI€AGO
. .' 

## .

GENERAL INFORMATION 

## s. NAME 

### OF PROCESS: 6. 

### NAME'OF EMISSION SOURCE EQUIPMENT; 

### SANDBLASTING SANDBLASTER UNIT 7. 

### EMISSION SOURe:! EQUIPMENT MANUfACTURER: 

### 8. MODEL NUMBER: 

# 19•. 

### SERIALNUMBER:



### _.**~7~R** 

### BLAST-LIQUID HONER " 

### flOW DIAGRAM DESIGNATlON(S) Of EMISSION SOURCE: 

## SB-1 11. 

### IDENTlTY(S) Of ANY SIMILAR SOURCE(S) AT THE PLANT OR PREMISES NOT COVERED BY THE FORM (IF THE SOURCE IS COVERED BY ANOTHER APPLICATION, IDENTIFY THE APPl.ICATION): 

### 12. AVERAGE OPERATING TIME Of EMISSION SOURCE: 13. 

### MAXIMUM OPERATING TIME OF EMISSION SOURce: 

### ] 

## 5 HItS/DAY 

### 6 DAYS/'NK 

## 52 WKS/VR 

## 2 HRS/DAY 

## 1 OAYS/'NK

### 5~ WKS/VR I". PERCENT OF ANNUAl THROUGHPUT: DEC-fEB 

## 25 

# " MAR-MAY 

## 25 

# " JUN-AUG 

## 25 '!!. 

### SEPT-NOV 

## 25 %



### INSTRUCTIONS I. COMPLm THE ABOVE IDENTIfiCATION AND GENERAL INFORMATION SECTION. 2. 

### COMPLETE THI! RAW MATERIAL, PRODUCT, WASTE MATERIAL, AND FUel 

### USAGE SECTIONS FOR THE PARTICULAR SOURCE EQUIPMENT. COMPOSITIONS OF MATERIALS MUST BE SUFFICIENTLY DETAILED TO ALLOW DETERMINATION OF THE NATURE AND QUANTITY Of POTENTIAl. EMISSIONS. IN PAItTlCULAR, THE COMPOSITION OF PAINTS, INKS, ETC., AND ANY SOLVENTS MUST BE FUlLY DETAILED. 3. 

### EMISSION AND EXHAUST POINT INFORMATION MUST BE COMPLETED, UNLESS EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONTROL EQUIPMENT. 4. 

### OPERATING TIME AND CERTAIN OTHER ITEMS REQUIRE BOTH AVERAGE AND MAXIMUM VAlUES. S. 

### FOR GENERAl INFORMATION REFER TO "GENERAL INSTRUCTIONS FOR PERMIT APpliCATIONS, "·APC-201.

DEfiNITIONS AVERAGE
.. THE VAlUE THAT SUMMARIZES OR REPRESENTS THE GENERAl CONDITION OF THE EMISSION SOURCE, Olt THE GENERAl STATE OF .1



### - '- _.. .. PRODUCTION-OF 

## THE EMlssioN.SQURd. SPECFlCAlly:.

- .... -.

__ ... ...... . __ u _____ --- •• -.- -_.-



### . AVERAGE OPERATING TIME
.. ACTUAL TOTAL HOURS OF- OPERATION FOIt TH! PRECEDING- TWELVS MONTH PERIOD.

AVERAGE RATE
.. ACTUAL TOTAL QUANTITY OF "MATERIAl" FOR THE PRECEDING TWELVE MONTH PERIOD, DIVIDED BV THE AVERAGE OPERATING TIME.
. AVERAGE OPERATION
.. OPERATION TYPICAL. OF THE PRECEDING TWELVE MONTH PERIOD, AS REPRESENTED BY AVERAGE OPERATING TIME AND AVERAGE RAm. MAXIMUM
.. THE GREATEST VALUE ATTAINABLE OR ATTAINED FROM THE EMISSION SOURCE, OR THE PERIOD OF GREATEST OR UTMOST PRODUCTION OF THE EMISSION SOURCE. SPEC IFI CALLV: MAXIMUM OPERATING TIME
.. GREATEST EXPECTED TOTAL HOUIIS OF OPERATIONS FOR ANY TWELVE MONTH PERIOD.
. MAXIMUM RATE
.. GREATEST QUANTITY OF "MATERIAL" EXPECTED PER ANY ONE HOUR OF OPERATION. MAXIMUM 

### OPFRATION
_**~IFATEST** 

### EXPECTED OPERATION. AS IlERR&&6NliD BY MAXIMUM OpeRATING TIME AND MAXIMUM RATES.

# ...**~** 

### ....

........



# -
, 201..



### , 2la.



### , 220. :

JOa.



### 31a. 32a. 

### 33a.

: :J.4,- '---

4OcI. 

### 41a. 42a.**~.** 44a.



### 500.



# -

- '.. '.; •••• - .. a •••• - •• ;: • ...; ••• : ••• ,.: .. - - •••

;. ,"



# . '10:' NAMEOPIAWMATERIAL



## ... :



## . 

# ......

NAME OF PRODUCT 

### MISe SANDBLASTED, PARTS

NAME OF WASTE MATERIAL

, , ," "**PA1r'""~JT.ATES** 

# ,- " 

# -

" , 

# - " ,.

FUel 

### USED NATURAL GAS 

## 0 b. OTHER GAS 

# . 0 'JIL 

## 0 ":OAL 

## 0 OTHER 

## 0 oiAVEAAGE FIRING RATE 

### PER IDENnCALSOURCE: 

# '. RAW Ml\TEJUAl. INFORMAnON 

## .

# ...

,**,~** 

### AV!lAGE RAm : " PSt 

### IDENTICAl. SOURCE ·-".MAXlMUMRAlE**,.~** 

### .- " ' : Pm 

### IDENTIcAL 

### SCUICE**~,**

### ...



### b.**;/t.~** 

# . , ,c:.. 

### 'UF/'HJ[**lr~** c;.- 

### IS/HIt 

### UtlHR II. c

### LB/HR 

### LI/liR

..


### PRODUCT INFORMAnON 

# ,- AVERAGE RATE 'MI\XIMUM RATE 

### PeR IDENTICAL SOURCE PER IDENnCAL SOURCE 

### b. c. 

## 250 LI/HR 

## 375 LB/HR 

### b. c

### LI/HR LS/HR b. c. 

### LI/liR LB/HR 

### b. c.



# - LI/HR LB!HR 

### b. c. 

### U/HR 

## - L8/HR

WASTE 

### Ml\TERIAL INFORMATION AVERAGE RATE 

### IAAXIMUM RATE 

### PER IDENnCAL SOURce PER 

### IDENTICAL SOURCE b., c. 

# o 5 U/HR 

# o 75 L8/HR b. c. 

### LB/HR LB/HR 

### b. c. 

# . U/HR L8/HR 

### b. c. 

### LI/HR L8/HR 

### b. c. 

### LI/HR LB/HR

-FUel 

### USAGE'INFORMATION
" .... 

### rtPE HEAT CONTENT 

### c. 1000 

### BTUISe:, 

# . BTUISe:' BTU/GAl ' BTUAB

BTUAB I.**~M** 

### FIRING 

### RATE PER IDENTICAL SOURCE:**BTU/h~** 

# ,

' 

# - BTU/Hir -Tl1IS SEcrtON IS TO BE COMPLETED FOR ANY FUel 

### UseD DIREcr1.Y IN THE PROCESS EMISSION SOURCE, E.G. 

### GAS IN A DRYER, OR COAL IN A MELT 

### FURNACE. 

# .. 

# .. :' :,-,1 

## .d 

## •

. !



### . -" .. 

## ,



## -

### -EMISSION INFORlMnON ' 

## . 

# . " 

### 51. NUMIEIt 

### OF IDlNTIa.L SCURaS (cesCllIBE AS REQUIII&O): 

# . 1 \ 

# - AveRAUE OP!RAnON 

# .

# --"-
---- 

# - -**~.-~~--------------** 

# --- 

# ---------------.-.-----**CC~AM 'C~~~1'RAnON**  

### OR EMISSION RAT'E'PEK IDeNnCAl.
. METHOD USED TO DEl'BMINeCONC!NTRAnOKOIt**~** _.• :;:0£._ 

### INANT**~n(** - 

### e.\ISSION RA**~** I.**~AmaJLAn;** 

# '24. b. c:. 

### SEE: 

## APe 260 

# . Ii' 

### MATT!R 

### GRlSa LB/HR CARlON**~.** 

### PPM 

### b. c ... 

### MONOXIDE (VOL) U/HR 

## . NlntOGEN S
.... 

### PPM 

### b. c:. 

### OXIDES (VOL) L81HR ORGANIC**~a.** 

### PPM 

### b•. v c. , 

### MATBIAL (VOL) LB/HR SULFUR 

### S6a. PPM 

### b. c. 

### DIOXIDE (VOL) LB{HR 

# . ··OTHER 570. 

### PPM 

### b. c. 

### (SPECIFY) /VOll LS/HR MAXIMUM OPEAATION 

# . 

# ----- -- 

# ---- ----------------- 

# .,..--- ---- -- ---- - 

# ------ ---- COl'laNTR.ATlON OR EMISSION RATE PER IDENnCAL METHOD USED TO DETERMINE CCNaNTR.ATION OR CONTAMINANT SOURCE

- EMISSION RATE PARnaJLATE 

### SBa. b. c. 

### SEE 

### APe 260 MATTER GR/sa LBlHR CARBON 

### S9a. PPM 

### b. c. 

### MONOXIDE (VOL) LBIHR 1'1 

### I

T1{OGI;N 600. 

### PPM b. c. 

### OXIDES (VOL) LB/HR ORG 

### C 010. 

### PPM 

### b. c. 

### MAT. 

# ., /vOll LB/HR SULfUR 

### a2a. PPM 

### b. c. 

### atOXIDE (VOll U/HR "OTHER 63a. 

### PPM 

### b. c. (SP£CtfY) 

### (VCL) LS/HR -ITEMS 52 THROUGH 03 NEED Nor BE COMPlETED IF EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONTIOL EQUIPMENT. -OTHER- 

### CONTAMINANT SHOULD BE USED FOR AN AIR CONTAMINANT I'IOT SPEOFICALl. Y NAMED ABOVE. POSSIBU OTHER CONTAMINANTS ARE ASWTOS, 9ERYLLIUM, MERCURY, VIN'tt. OiLORIDE, LEAD, ETC.**--~H.AUST** 

### POINT INFORMATION 64. 

### FLOW DIAGRAM OESIGNATlON(S) OF EXHAUST POINT: 

### EXHAUSTED 

### 'ID DUST f"I'1T.T. "lJ<l /")("_1 

### 65. OESClumON OF EXHAUST POINT (lOCATION IN RELATION TO BUILDINGS, DIRECTION, HOODING,**ETC:~** 66. 

### EXIT HEIGHT AaOVE GRADE: 

### 67. EXIT DIAMETeR: 

### 08. GREATeST HEIGHT OF NEARBY BUILDINGS: 

### 69. EXIT DISTANCE FROM NEAREST PlANT BOUNDARY: FT FT AVEAAGEOPaAnON MAXIMUM OPERAnON 

### 70. EXIT GAS TEMPERATURE: 

# n. EXIT GAS TEMPERATURE; OF" GIl 

# n. GAS flOW RATE THROUGH EAOt 

### EXIT: 

### 73. GAS flOW RAre THROUGH EACt EAOt EXIT: ACPM loaM 

# -

. 

# - SECT10N sHOuLD NOT BE COMPl.mD IF EMISSIONS ARE EXHAUSTED THROUGH AIR POlLUTION CONTROl.. EQUIPMeNT•STATE OF illINOIS ENVIRONMENTAL 1'l0TECTION AGENCY DIVISION OF AIR POLLUTION CONTROL 2200 CHURCHill ROAD SPRINGFIELD. IUINOIS 62706

°OATA AND INFORMATION 'ROCESS EMISSION SOURCE

"THIS INFORMATION FORM IS TO 8E COMPlETED FOR AN EMISSION SOURCE OTHER THAN A FU£L COMBUSTION EMISSION SOURCE Olt AN INCINERATOR, A FUEL COMBUSTION EMISSION SOURCE IS A FURNACE, 'BOILER, OR SIMILAR EQUIPMENT useD PRIMARILY FOR PRODUCING HEAT OR POWEll ay INOIRECT HEAT TRANSFER. AN INCINERATOR IS AN APPARArUS IN WHICH REFUSE IS BURNED.
I. NAME OF PLANT OWNER: 

### 2. NAME OF CORPORATE DIViSION OR PLANT (IF DIFFERENT FROM 

### EMPIRE HARD aIROME OWNER): l. STII£ET ADDRESS OF EMISSION SOURCE: 

# •• CITY Of t:MI))IUN )U\JKU:I 

## 1615 

# s. KOSTNER AVE CHICAGO

GENERAl INFOKMAoTlON 

### 5. NAME OF PRocess, 6. NAME OF EMISSION SOURCE eQUIPMENT: 

### SANDBLASTING SANDBLASTER UNIT 7. EMISSION SOURCE EQUIPMENT MANUFACTURER: 8. MODEL NUMBER: 

# I 9.**~ERIAL** NUMIfR: f-,-.:
. 

### TRINm rnR NF'T'**RT.A~** FLOW OIAGRAM DESIGNATlON(S) OF EMISSION SOURCEI 

## SB-2, SB-3 II. IDENTlTyeS) OF ANY SIMILAR SOURCE(S) AT THE I'\.ANT OR PREMISes NOT COVatED BY TliE FORM (IF THE SOURCE IS COVERED BY ANOTHER APPliCATION, IDENTIFY THE APPlICATIONI: 

# '2. AVERAGE OPERATING TIME OF EMISSION SOURCE: 13. MAXIMUM OPERATING TIME OF EMISSION SOURCE: 

## 1.5 HRS/DAY 

## f2 DAYS/WK 

## S2 WKS/Ylt 

## 2 HRS/DAY 

## 2 DAYS,lWK 

### S2 WKSIY1t 

# , ... PeRCENT OF ANNUAl THROUGHPUT: DEC-FEB 

## 25 

# "" MAR-MAY 

# 25 % JUN
.....UG 

## 25 'Yo SEPT-NOV 

## 25 %

INSTRUCTIONS I. COMPlETE THE ABOVE IDENTIFICATION AND GENERAL INFORMATION SECTION. 2. COMPlETE THE RAW MATERIAL, PRODUCT, WASTE MATERIAL, AND FUEL USA.GE SECTIONS FOR THE PARTICULAR SOURCE EQUIPMENT. COMPOSITIONS OF MATERIALS MUST BE SUFFICIENTLY DETAILED TO ALLOW DetERMINATION OF THE NATURE AND QUANTITY OF POTENTIAl. EMISSIONS. IN PARTICULAR, THE COMPOSITION OF PAINTS, INKS. ETC., AND ANY SOLVENTS MUST 9E FULLY DETAILED. l. EMISSION ANO EXHAUST POINT INFOltMA.T10N MUST BE COMPI.ErED. UNlESS EMISSIONS ARE E)(HAUSTED THROUGH AIR POLLUTION CONTROl EQUIPMENT. 4. OPERATING TIME AND CERTAIN OTHER ITEMS REQUIRE 80TH AVERAGE AND MAXIMUM VALUES, S. FOlt GENERAl. INFORMATION REFER TO "GENERAl INSTRUCTIONS 

### fOil PERMIT APPLICATIONS, • APC-20\.

DEFINITIONS AVERAGE

- THE VALUE THAT SUMMARIZES OR REPRESENTS THE GENERAl CONDITION OF THE EMISSION SOURCE, OR THE GENERAL STATE OF PRODUCTION OF tHE £MllisioN SOURCE. SPECIFICALLy: AVERAGE OPERATING TIMe

- ACTUAL TOTAL HOURS OF OPeRATION FOR THE PRECEDING TWElVE MONTH PERIOD. AVERAGE RATE
.. ACTUAL TOTAL QUANTITY OF "MATERIAL" FOil THE PRECEDING TWELVE MONTH PERIOD, DIVIDED BY THE AVERAGE OPERATING TIME. AVERAGE OPlAATION

- OPERATION TYPICAL OF THE I'IlECEDING TWELVE MONTH PERIOD, AS REP1tESENTED ISV A.VERAGE OPERATING TloW! AND AVERAGE RATES. MAXIMUM
.. THE Gi!EATtST VALUI: ATTAINA81E OR ATTAINED

### FRO~lsitem SOURCE, OR THE PERIOD OF GREATEST OR UTMOST PlODUCTION OF THE EMISSION SOURCE, !lPECIFICALLY: MAXIMUM OPERATING TIME

- GREATEST EJ(PECTED TOTAL HOURS OF OPERATIONS FOR ANY TWELVE MONTH PERIOD. MAXIMUM RATE

- GREATEST QUANTITY OF "MATERIAL" EXPECTED PEl ANY ONE HOUI OF OPERATION. MAXIMUM OPERATION

- GREATeST EXPECTED OPERATION, AS**REPRE~ENTED** BY MAXIMUM OPfRATlNG TIME AND MAXIMUM MTES.

### RAW MATERIAL INFORMATION AVERAGE RATE MAXIMUM'RATE NAME OF RAW MATERIAL PER IDENTICAL SOURce PER IDENTICAL SOURce 

### 20a. 

### b. c. 

### MIse PARTS 

## 140 LB/HR 

## 210 LB/HR 

### 21a. 

### b. c. 

### LB/HR LB/HR 

### 22a. 

### b. c. 

### LB/HR LB/HR 

### 23a. 

### b. c. 

# . LB/HR LB/HR 

### 24G. b. c. 

### LB/HR LB/HR

PRODUCT INFORMATION 

# . AVERAGE RATE MAXIMUM RATE NAME OF PRODUCT PER IDENTICAL SOURCE PER IDENTICAL SOURCE lOa. 

### b. c. 

### MIse SANDBLASTED PARTS 

## 140 LB/HR 

## 210 LB/HR 

### 31a. 

### b. c. 

### LB/HR LB/HR 

### 32a. 

### b. c. 

### LB/HR LB/HR 33a. 

### b. 

# . c. 

### LB/HR LB/HR 'I4a. 

# . b• c. 

### LB/HR LB/HR
"


### WASTE MATERIAL INFORMATION AVERAGE RATE MAXIMUM RATE NAME OF WASTE MATERIAL PER IDENTICAL SOURce PER IDENTICAL SOURce 4Oa. 

### b. c. 

## metal particulates 

# o 5 LB/HR 

# n,7" LB/HR 

### 41a. b. c. 

### LB/HR LB/HR 

### 42a. 

### b. c. 

### LB/HR LB/HR A3a. 

### b. c. 

### LB/HR LB/HR 44a. 

### b. c. 

### LB/HR LB/HR



## r -FUEL 

### USAGE INFORMATION FUEL USED TYPE 

### HEAT CONTENT SOa. 

### NATURAL GAS 

## 0 b. c. 

### 1000 8TU/SCF OTHER GAS 

## 0 BTU/SCF 

## on. 

# 0 BTU/GAL 

### COAL 

# 0 BTUAB OTHER 

# 0 BTU/U !d-AVERAGE FIRING RATE PER IDENTICAL SOURCE:**~ l~'**  

### MAXIMUM FIRING RATE PER IDENTICAL SOURCE: BTU/HR 8TU/HR -THIS SECTION IS TO BE COMPlmD FOR ANY FUEL USED DIREctly IN THE PROCESS EMISSION SOURCE, E.G, GAS IN A DRYER, OR COAL IN A MELT FURNACE. ",,,"'r.o "'0" " .", 

## .**~;** 

### .... *EMISSION INFORMAnON 

### !-

S\.

-- OF IIIENTIG'L 

### SO\JJCES 

### (DeS"'''' A$

# REQ\J1"D~ ...

# ~",,2 OPEIIAnON
. . _. '-'.'--·:'- •.

# ~.,,'04:-~.'.~-:~;:a'~.'-"'.'.,~,'of.l 

# !
..**~.~.~~.' ~**  

# ... - -- 

# -- 

# - - ------------- 

# ---- - -- 

# --------_ ....

# _-----------**CO~AMINANT: ~g~~NTlAnoN** **~EMISSION** RAT£PER IDENTICAl.

### ~.'**=~gNU:~TO** DETERMINeCONCENlRAnOMOIt PAIT1CUt.A TE ·MATTER S2a. b. • c:. 

### SEE APe- 260' ...'
_ .

# ..;:.~**~** CAaaON 

### MONOXIDE NITKOG£N OXIDES ORGANIC MAmrAL 

### SULflIR DIOXIDE ··OTHEIt (SPECIFY) S3a. S4a. "a. 

### 560. S7a. 

### GRlSCF PPM (VOL) PPM (VOL) PPM (VOL) PPM (VOL) PPM IVOL) LB/HR 

### b. c. 0 

### La/HR 

### b. c. 

### La/HR 

### b•.**~** c. 

### , LB/HR 

### b. c. 

### LB7HR , 

### b. c. 

### LB/HR MAXIMUM OPERATION 

# ------ ----- ----------------- ,------- 

# ------ 

# - ---------- CONTAMINANT PARTlOJl.Att MATTER 'CARBON MONOXIOe NITROGtN OXIDES

-OTHER (SPECIFY) CONCENTlIATlON OR EMISSION RATE PElt IDENTICAL METHOD USED TO DETERMINE CONCl:NTlIATlON OR SOURCE

- EMISSION RATE SBa. 

### b. c. 

### SEE 

### APe 260 GR/sa La/HR 

### 590. PPM 

### b. c. 

### (VOL) LaIHR 6Oa. 

### PPM 

### b. c. 

### (VOL) LB/HR 61a. 

### PPM 

### b. c. 

### IVOL) LB/HR 620. 

### PPM 

### b. c. 

### (VOL) LB/HR 63a. 

### PPM 

### b. c. 

### (VOL) La/HR ·ITEMS 52 THROUGH 63 NEED NOT BE COMPLETED IF EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONTROL EQUIPMENT. --OTHER" CONTAMINANT SHOUlD BE USEO FOR AN AIR CONTAMINANT NOT SPEctFlCALLY NAMED ABOVE. POSSIBLE OTHER CONTAMINANTS ARE ASBESTOS, BERYlLIUM, MERCURY, VINYl. OiLORIDE, LEAD, ETC. --EXHAUST POINT INFORMATION**~.** 

### FLOW DIAGRAM DESIGNATlON(S) OF EXHAUST POINT: 

### EXHAUSTED TO DUST mT.T. .JM 

### 1Y'-1 

### 65. DESOIPTION OF EXHAUST POINT (lOCATION IN RB.ATlON TO BUILDINGS, DIRECTION, HOODING,**ETC:~** 

### 66. EXIT HEIGHT ABOVE GRADE: 

### 67. EXIT DIAMETER: 

### 68. GREATEST HEIGHT OF NEARBY BUILDINGS: 

### 69. EXIT DISTANCE FROM NEAREST PlANT BOUNDARY: FT 

### AVERAGE OPERATION MAXIMUM OPERATION



### - . 

### 10. EXIT GAS ttMPERATURE: 

### 72. EXIT GAS TEMPERATURE: _. 

### .. 

## - - 

## .. 

## - ...... FT



### OF" 

## - ., 0 Of 

# n. GAS FLOW RATE THROUGH EAOI exiT: 

### r.J. GAS FLOW RATE THROUGH EAOI EAOi EXIT:



## - ACFM ACPM 

# ... 'S SECTION SHOULD NOT B€ 

### COMPUTED IF EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONTROL EQUIPMENT. 

## ':.,.:4

0· _ ....•.. <:."



### STATE OF ILLINOIS ENVIRONMENTAL PROTECTION AGE NCY DIVISION OF AIR POLLUTION CONTROL 2200 CHURCHILL ROAD SPRINGFIELD, ILLINOIS 62706

-DATA AND INFORMATION AIR POLLUnON CONTROL EQUIPMENT Ttl.. ., .... y .• • ••••' •••IIS •• " ••

### f"

.........,,. ........tle. 

# u....... lit •••, •• S.,••• " •.1". C" ••••, "'''. S.cue ... 1028. CU,.'O'.'. 

### a' 'illi. •....' ......011 I. ",,1111 ••_ vfl."r nu. , ........ 

## ,.n.,• •• 41 .... "' • ., .,....... ,,,.. r.,111 " ... 

## ".i... ,uoe,... d ..... • ••lel ,...... ia yo., ....U •••,•• b....., 

# eI...... T'''t fa,,. hi. tt ••" ...P,o".eI by U .. ,., ... ,

............... Cantl'



### -THIS INFORMATION FORM IS FOR AN INDIVIDUAL UNIT OF AIR POLLUTION CONTROL EQUIPMENT OR AN AIR POLLUTION CONTROL SYSTEM.

I. NAME OF OWNER: 

### 2. NAME OF CORPORATE DIVISION OR PLANT (IF DIFFERENT FROM**f.fa~T'I** 

### OWNER): 

### 3. STREET ADDRESS OF CONTROL EQUIPMENT: 4. 

### CITY OF CONTROL EQUIPMENT: 1 j:;1**~ ~**  f"f.fTf"':/H·
.. .,n 

### S. NAME OF CONTROL EQUIPMENT OR CONTROL SYSTEM: 

### DUST aJLLECroR (CYCLONE WITH FILTER)

I NSTRUC nONS 

### 1. COMPLETE THE ABOVE IOENTIFICATION. 2. COMPLETE THE APPROPRIATE SECTION FOR THE UNIT OF CONTROL EQUIPMENT, OR THE APPROPRIATE SECTIONS FOR THE CONTROL SYSTEM. BE CERTAIN THAT THE ARRANGEMENT OF VARIOUS UNITS IN A CONTROL SYSTEM IS MADE CLEAR IN THE PROCESS flOW DIAGRAM. 3. COMPLETE PAGE 6 OF THIS'FORM, EMISSION INFORMATION AND EXHAUST POINT INFORMATION. 4. EFFICIENCY VALUES SHOULD BE SUPPORTED WITH A DETAILED EXPLANATION OF THE METHOD OF CALCULATION, THE MANNER OF ESTIMATION, OR THE SOURCE OF INFORMATION. REFERENCE TO THIS FORM ANY RELEVANT INFORMATION OR EXPLANATION INo.UDED IN THIS PERMIT APPLICATION. 

### S. EFFICIENCY VALUES AND CERTAIN OTHER ITEMS OF INFORMATION ARE TO BE GIVEN FOR AVERAGE AND MAXIMUM OPERATION OF THE SOURCE EQUIPMENT. FOR EXAMPlE, "MAXIMUM EFFICIENCY" IS THE EFFICIENCY OF THE CONTROL EQUIPMENT WHEN THE SOURCE IS AT MAXIMUM OPERATION, AND "AVERAGE FLOW RATE" IS THE flOW RAn INTO THE CONTROL EQUIPMENT WHEN THE SOURCE IS AT AVERAGE OPERATION. 6. FOR GENERAL INFORMATION REFER TO "GENERAL INSTRUCTIONS FOR PERMIT APPliCATIONS", APC-201.

DEFINITIONS AVERAGE

- THE VALue THAT SUMMARIZES OR REPRESENTS THE GENERAL CONDITION OF THE EMISSION SOURe; OR THE GENERAL STATE OF PRODUCTION OF 

### THE EMissiON SOURd. SPECIFICACL

### Y: AVERAGE OPERATION

- OPERATION TYPICAL OF THE PRECEDING TWELVE MONTH PERIOD, AS REPRESENTED BY AVERAGE OPERATING TIME AND AVERAGE RATES. ·'MUM

- THE GREATEST VAlue ATTAINABLE OR ATTAINED FROM THE EMISSION SOURCE, OR THE PERIOD OF GREATEST OR UTMOST PRODUCTION 

### OF tAf EMISSION sOURd. SPECIFICALLY: MAXIMUM OPERATION

- THE GREATEST EXPECTED OPERATION, AS REPRESENTED BY MAXIMUM OPERATING TIME AND MAXIMUM RATES.

### .-- ADSORPTION UNIT 1. flOW DIAGRAM DESIGNATlON(S) OF ADSORPTION UNIT:



## - 2. MANUFACTURER: 3. MODEL NAME AND NUMBER: 4. ADSORBENT:



# 0 AcTivA'reD CHARCOAL: TYPE 

# o OTHER: SPECIFY 

### S. ADSORBATE(S 

### I:



# . 6. NUMBER OF BEDS PER UNIT: 

### 7. WEIGHT OF ADSORBENT PER BED: LB B. DIMENSIONS OF BED: 

## . THICKNESS IN, SURFACE AREA SQUARE IN 

### 9. INLET GAS TEMPERATURE: 10. PRESSURE DROP ACROSS UNIT: 

### OF INCH H20 GAUGE II. TYPE OF REGENERATION:



# o REPLACEMENT OS'reAM 

# o OTHER: SPECIFY 

### 12. METHOD OF REGENERATION:



# 0 ALTERNA're USE OF ENTIRE UNITS 

# 0 AL'reRNA're USE OF BEDS IN A SINGLE UNIT 

# 0 SOURCE SHUT DOWN 

# o OTHER: OESCIUBE AVERAGE OPERATION OF SOURCE MAXIMUM OPERAnON OF SOURCE 

### 13. TIME ON LINE BEFORE REGENERATION: 

### IS. TIME ON LINE BEFORE REGENERATION: I- MIN/BED MIN/BED I EFFICIENCY OF ADSORBER (SEE INSTRUCTION 4): 16. EFFICIENCY OF ADSORBER (SEE INSTRUCTION 4): % %

AFTERBURNER 

### 1. flOW DIAGRAM DESIGNATION(S) OF AFTERBURNER: 

### 2. MANUFACTURER: 

### 3. MODEL NAME AND NUMBER:**~.** COMBUSTION CHAMBER DIMENSIONS: LENGTH IN, CROSS-SECTIONAL AREA**SQ~ARE** IN. 

### S. INLE.T GAS TEMPERATURE: 

### 7. AJEL: 

### Df 

# 0 GAS 

# 0 OIL: SULFUR WT% 6. OPERATING TEMPERATURE OF COMBUSTION CHAMBER: 8. BURNERS PER AFTERBURNER: 

### OF @ BTU/HR EACH 9. CATALYST USED: 

# 0 NO 

# 0 YES: DESCRIBE CATALYST 10. HEAT EXCHANGER USED:



# , NO 

# o YES: DESCRIBE HEAT EXCHANGERIAVERAGE OPERATION OF SOURCE MAXIMUM OPERATION OF SOURCE II. GAS flOW RATE: 

### 13. GAS flOW RATE: SCFM SCFM 

### 12. EffiCIENCY OF AFTERBURNER(SEE INSTRUCTION 4): 

### 14. EFFICIENCY Of AFTERBURNER(SEE INSTRUCTION 4): '!Eo 

# . 'l;.CYClONE flOW DIAGRAM DESIGNATlON(S) OF CYClONE: 

### OC-l 2. MANUFACTURER: 3. MODEL: 

### D 4. 

### TYPE OF CYClONE: S. NUMBER OF CYClONES IN EACH MULTIPlE CYCLONE: 

# g SIMPlE 

# 0 MULTiPlE 6. DIMENSION THE APPROPRIATE SKETCH (IN INCHES) OR PROVIDE A DRAWING WITH EQUIVALENT**INFORMATION~** TANGENTIAL INLET CYCLONE
GAS OUT 

# +

4" 

## 22" 

# .-_'-_-1_ 6" 

# -1-----11

SECTION

PlAN 

# - AXIAL INLET CYCLONE (lNDIVIOUAL CYClONE OF MULTIPlE CYCLONE)

GAS OUT



# + t GAS IN GAS IN VANE ANGLE DEGREES



# I**~**

# ......-----------J-' 

# I

SECTION

NOT TO SCALE
A VERAGE OPERA nON OF SOURCE 7. GAS FLOW RATE: 

## 2400 8. EFFICIENCY OF CYClONE (SEE INSTRUCTION 41: 

## 95 SCFM MAXIMUM OPERATION OF SOURCE 9. GAS flOW RATE: 

## 2400 SCFM 10. EFFICIENCY OF CYClONE (SEE INSTRUCTION 41:**~.,** 

### .., 

## 95**~** CONDENSER I 1. .FlOW DIAGRAM DESIGNATlON(S) OF CONDENSER:


# .. ::: 

### 2. MANUFACTURER: 3. MODEL NAMf AND NUMBER: 

# 1 4 • HEAT EXCHANGE AREA: 

# n2



# - AVERAGE OPERATION Of SOURCE MAXIMUM OPERATION OF SOURCE S. COOlANT FLOW RATE PER CONDENSER: 

### 10. COOLANT FLOW RATE PER CONDENSER: WATER GPM AIR SCFM WATER GPM AIR SCFM OTHER: TYPE ,FLOW RATE OTHER: TYPE 

## , FLOW RATE 6. GAS FLOW RATE: 11. GAS FLOW RATE: saM saM 7. COOLANT TEMPERATURE: OF 

# IB. GAS TEMPERATURE: 

# . 12. COOLANT TEMPERATURE: 

# I 13 • GAS TEMPERATURE: INLET OF OUTlET INLET OF OUTLET OF INLET OF OUTLET OF INLET OF OUTlET OF 

# -- - 9. EFFICIENCY OF CONDENSER (SEE INSTRU<;TION 4): 14. EFFICIENCY OF CONDENSER (SEE INSTRUCTION 4): % %

"ELECTRICAL PRECIPITATOR I. FLOW DIAGRAM DESIGNATION OF ELECTRICAL PRECIPITATOR: 

### 2. MANUFACTURER: 

### J. MODEL NAME AND NUMBER: 4. COLLECTING ELECTRODE AREA PER CONTROL DEVICE: 

### FT2 AVERAGE OPERATION OF SOURCE MAXIMUM OPERATION Of SOURCE 0: GAS FLOW RATE: 

### 7. GAS FLOW RATE:

## ~. SCFM SCFM EFFICIENCY Of ELECTRICAL PRECIPITATOR(SEE INSTRUCTION 4): 

### 8. EFFICIENCY OF ELECTRICAL PRECIPITATOR (SEE INSTRUCTION 4): % SUDMIT THE MANUFACTURER'S SPECIFICATIONS FOR THE ELECTRICAL PRECIPITATOR. REFERENCE THE INFORMATION TO THIS FORM • • ELECTRICAL PRECIPITATORS VARY GREATlY IN THEIR DESIGN AND IN THEIR COMPLEXITY. THE ITEMS IN THIS SECTION PROVIDE A MINIMUM

AMOUNT OF INFORMATION. THE APPLICANT MUST, HOWEVER, SUBMIT WITH THIS APPLICATION THE MANUFACTURER'S SPECIFICATIONS, INCLUDING ANY DRAWINGS, TECHNICAL DOCUMENTS,ETC. IF THE INFORMATION PROVIDED BY THE MANUFACTURER'S SPECIFICATIONS IS INSUFFICIENT FOR FULL AND ACCURATE ANALYSIS, THE AGENCY Wn.L REQUEST SPECIFIC ADDITIONAL INFORMATION.
FILTER UNIT I. FLOW DIAGRAM DESIGNATlON(S) OF FILTER UNIT: 

### DC-1 2. MANUFACTURER: J. MODEL NAME AND NUMBER: DAY'roN SE820A 4. FILTERING MATERIAL: S. FILTERING AREA: 

### CLOl'H 20 

## ft 2 6. CLEANING METHOD: 

# o SHAKER 

# o REVERSE AIR 

# o PUlSE AIR 

# o PULSE JET 

# RJ OTHER: SPECIFY MANTJAT. 

### mfAKF. 7. GAS COOLING METHODNA 

# 0 DUCTWORK: LENGTH 

# o BLEED-IN AIR 

# 0 WATER SPRAY 

# 0 OTHER: SPECIFY FT., DIAM IN. AVERAGE OPERATION OF SOURCE MAXIMUM OPERATION OF SOURCE 

### R. GAS FLOW RATE (FROM SOURCE): 

### 12. GAS FLOW RATE (FROM SOURCE):



# ....... 2400 SCFM 2400 SCFM 9. GAS COOLING FLOW RATE: 

### na 13. GAS COOLING FLOW RATE: %

BLEED-IN AIR SCFM, WATER SPRAY GPM BLEED-IN AIR SCFM, WATER SPRAY GPM 10. INLET GAS CONDITION: 14. INLET GAS CONDITION: TEMPERATURE 

## 1Q Of OEWPOINT**N~** 

## or: TEMPERATURE 

## 2Q or: DEWPOINT**~ ~**  11. EFFICIENCY OF FILTER UNIT(SEE INSTRUCTION 4): IS. EFFICIENCY OF FILTER UNIT(SEE INSTRUCTI9N 4l: 

### 99.9>1.**~(f\** 

# , 

# .. 99.9>1- 

## Mm %

### SCRUBBER 1. 

### flOW DIAGRAM DESIGNATION(S) Of SCRUBBER: 2. MANUfAcnJW: 3. MODEL NAME AND NUMBER:**~** 4. 

### TYPE Of SCRUBBER: 

# 0 HIGH ENERGY: GAS STREAM PRESSURE DROP

. '. INCH H2O .• '-:-" .:so- • 

# 0 PACXED, PAClCING TYPE PACKING"Size

## :.~~~::~ , PACKED HEIGHT IN. ,. ::r


# . . , 

# 0 SPRAY: NUMBER OF NOZZLES , NOZZLE PRfSSURE PSIG 

# 0 OTHER: SPECIFY ATTACH DESCRIPTION AND SKETCH WITH DIMENSIONS S. 

### TYPE Of FLOW: 

# o COCURRENT 

# 0 COUNTERQJWNT" 

# 0 CROSSA.OW 6. 

### SCRUBBER GEOMmY: LENGTH IN DIRECTION Of GAS fl.OW IN., CROSS-SECTIONAL AREA SQUARE IN. 

### 7. CHEMICAl. COMPOSITION OF SaUBBANT:
AVERAGE OPERATION OF SOURCE MAXIMUM OPERATION Of SOURCE 

### 8. SCRUBBANT fl.OW RATE: 12. SCRUBBANT FLOW RATE: GPM GPM 

### 9. GAS FLOW RATE: 13. GAS flOW RATE: SCfM SCfM 10. INLET GAS TEMPERATURE: I". INLET GAS TEMPERATURE:**.~** 

### Of 

### H. EFFIClENCY OF SCRUBBER (SEE INSTRUCTION 4): 15. EFFICIENCY Of saUBBER(SEE INSTRUCTION 4):



# .... % 

### PARTICUL4.TE % GASEOUS % PARTICULATE _%GASEOUS

OTHER TYPE Of CONTROL EQUIPMENT I. FLOW DIAGRAM DESIGNATION(S) OF "OTHER TYPE" OF CONTROL EQUIPMENT: 

### 2. GENERIC NAME Of ·OTHER" EQUIPMENT: 

## J 3. MANUFACTURER: 

## J 4. MODEL NAME AND NUMBER:. 

### S. DESCRIPTION AND SICETCH, WITH DIMENSIONS AND FLOW RATES, Of "OTHEl" EQUIPMENT:



# . 1-, 

### AVERAGE OPERATION OF SOURCE MAXIMUM OPERATION OF SOURCE 

### 6. FLOW RATES: 

### 8. fl.OW RATES: GPM SCfM GPM SCFM 7. 

### EFFICIENCY OF ·OTHER" EQUIPMENT(SEE INSTRUCTION 4h 

### 9. EFFICIENCY OF "OTHER" EQUIPMENT(SEE INSTRUCTION 411 %**~** U. 'il2-0260 01\f"!1:' "'lllEMISSION INFORMATION NUMBER OF IDENTICAL CONTROL UNITS OR CONTROL SYSTEMS (DESCRIBE AS ReQUIRED): 

# , AVERAGE OPERATION OF SOURCE 

# I----r-------------

CONTAMINANT CONCENTRATION OR EMISSION RATE PER IDENTICAL - MeTHOD USEDro DETEiMiNECONcENTRAOON - CONTROl UNIT OR CONTROL SYSTEM OR EMISSION RATE PARTICULATE 

### 2a. b.**@alculat~ons** based on data from: MAmR GRlSCF 

## 0.0015 U/HR CARBON Ja. PPM 

### b. c:'venta.J.ataon 

### &**A~r Pollut~on**  MONOXIDE**(VOL~** LB/HR Control", Metal Finishing NITROGEN 

### 40. PPM 

### b.**c~U~QeJ:)QoJt J..~~U**  eel.; New YorK OXIDES (VOL) LB/HR state Dept. of Environmental ORGANIC 

### Sa. b.**c}ooun::ieL""VCl~.LUU** naD[ ::lOOK, J:lrocess PPM MATERIAL (VOL) LB/HR Source Handbook, Chapters 

## 3600 SULFUR 60. PPM 

### b. cf' ..) I VV , ,\.o"".I.C"" =0**.L~U~** =0, DIOXIDE (VOL) LB/HR process make-up data; 

### & 7a. 

### b. cyu ...... \.o
...""'U I.,;UUI..4U.L**c':lu..L1:"JU~UI..** OTHER PPM (SPECIfY) (VOL) LB/HR efficiencies. MAXIMUM OPERATION OF SOURCE

- - - - - CONCENTRATiON 

# OR**~siON** 

## RATE

# PeR IDENTiCAL - - - - METHOD useD 

# TO OeiERMiNECONaNTRAnoN - -



# -

fCONTAMINANT CONTROL UNIT OR CONTROL SYSTEM**~""** "**~.** OR
...**EMISSIO~** RATE**~** 

# -.

PARTICULATE 

### Bo. c. 

# c:---------··- ----- -.. ---- ----. MAmR GRlSCF 

## 0.0023 LB/HR 

# . CARBON 9a. PPM 

### b. c. VCU\.o
...... c;;a.I...LUll QC**~.LJ:;** .t"U.L.L ' MONOXIDE (VOL) LB/HR COx;ttrol", Metal Finishing NITROGEN lOa. PPM 

### b.**c~'** _ •• .L::1::1V CY.. I**.L'I~W ~UL-A**  ,)ES (VOL) LB/HR State

### Dep~. of Environmental ORGANIC l1a. PPM 

### b. c "'
...**"~'=**

## ... V c;;a. ........... , 

### na..lu
..."""UUI\" .t"L MATERIAL (VOL) LB/HR Source Handbook, Chapters 

## 3600 SULFUR 12a. PPM 

### b.**c~** ..) I UU ,**,~u.L""aL""** ::i J."l6:)UO:» ::i, DIOXIDE (VOL) LB/HR process make-up data; 

### &



# ..... 

# . 

# ... OTHER 130. PPM 

### b.**c~"""''''** ......... ,' "'
..... , ............ 

# ... -..- 

# , 

# ... (SPECIFY) (VOL) LB/HR efficiencies.
••.. OTHER· CONTAMINANT SHOULD BE USED FOR AN AIR CONTAMINANT NOT SPECIFICALLY NAMED ABOVE. POSSIBLE OTHER CONTAMINANTS ARE ASBESTOS, BERYLLIUM, MERCURV, VINYl CHLORIDE, LEAD, ETC.

EXHAUST POINT INFORMATION 1. FLOW DIAGRAM DESIGNATION(S) OF EXHAUST**POINT~** 

## EDC-1 2. DESCRIPTION OF EXHAUST POINT (LOCATION IN RELATION TO BUILDINGS, DIRECTION, HOODING, ETC.): 

## FINAL EXHAUST FRCM FILTER 

## BAG, LCX:ATED IN CENTER OF ROOF l. EXIT HEIGHT ABOVE GRADE:**~.** exiT DIAMETER:

### 3~ 

## ft 

## BAG DIAMm'ER - 5 ft S. GREASTEST HEIGHT OF NEARBV BUILDINGS: 

### 6. exiT DISTANCE**FRO~** NEAReST PLANT BOUNDARY: 

## 30 FT 

## 50 FT AVERAGE OPERATION OF SOURCE MAXIMUM OPERATION OF SOURCE i. EXIT GAS TEMPERATURE: 9. EXIT GAS TEMPERATURE: 

## 70 a F 

## 70 OF

, 

# . GAS FLOW RATE THROUGH EACH EXIT: 10. GAS FLOW RATE THROUGH EACH EXIT:**_~4QO_** ACFM 

### 2400 ACFM

# ,

, ) 

# " Work In/Out 

# ) 265 LB/HR 

# f-(-- R**~hrome** Chrome Plating 

# ----7) Work In/Out 

# 1A-4 Plating A - 123 

# ( 240 LB/HR



# , , , 

# , , , , , 

# ,


# : , I , 1 / , L

_______ __ :...L"
___ ) 

# , Ex hausted To Scrubber S3 6000 CFM 75 F

- ' ''''';--------------

---- 1

# ~._'O'__

# ~~?**I~ ~-_** **R-D~ -C-** **(Q ~O~** **~~ ~------** **1** h i li (' II 'JC'fW;: 

### ?L.Io.."nI t ,... TtlC.., 

### Ie 

## S 1<&1

-- 

# I o;

m

jj

# r l -"'--I -

"--I**"** 'iWIIf( COlliN ••95. 'I: 

### --2£19..**~** 

### IQ..tfC H5a**ll n**  " III 0\' 11101
_________ CU(Al.O. l to(,])

## ISTATE C F I LLINOIS ENViRONMENTAL '''OlIOION AGENCY DiVIS I ON OF**AI~** POLLUTION CCNTRCl

1200 CHURCHILL ROAD SPR i NGflUD , IUINO IS &2706

" OATA AND INFORMATION /ROCESS EM ISSICN SOURCE

'THIS INFO IlMATiON FOilM IS ;0 SE COMf'l fl' fO FOR AN E.'.IISSION**SOU~C[** O IHU THAN A**~U El**  COM!U STION EMISS IO N**SOU ~CE**  O R
.... N INC1NEitA TOl. A fUE L COM!U STION E MI SSION SCURCE IS A FU INA ct, 'aOIl.ER, OR SIMILAR ECU IPMENT U SED PlI.l MA R ll Y FOR**~OOU NG**  HEAT OR**I'OW~ ~y**  INOIUCT HEAr TRA NSFER
. A N INCINERAT O R IS AN
....**P~.4RAfUS** IN WHICH REFUSE I S BURNED. 

### " N A ME Of i'LA Ni O WNER : 

# " NAME OF COR P ORArf DIV ISION CR**p'~ANr** (IF**FFE ~NT**  F ROM Empire Hard Chrome OWNER!: Empire Hard Ch rome J, STU fT ADDUS; Of**~ISS ON**  SOURCE, <, co 0< > o**>UV '~,**  

### 1615 S
. Kostner Chicago

G [ NEV, lINF OIMATIO N 

# " NA ME 

# if F**'~OCES ,**  6, NA ME Of**MISSi N**  SO URCl: f CU IPM[NT: Ha r Chromium Plating Chrome Plating Tank 7 , EM ISS ION S OURCE eaU I PMENT MANUF
..... CTURER, 

### s, MODEL NUhI.DU, 

# I 

# " HRlAl**NU ~E!:**  

# - - - F L

OW DIAGRAM OESIGNATlO N(S ) OF ( MISSION SOU RCE , 

### A- 123 n , IDENTITY!S) OF ANY SI Mil AR SOURCE (S) AT T HE PlA N T 01 PUM ISES NOT eOVfKEO**~Y** THE f ORM !If THE SOURCE IS CCVtR EO BY ANOTHER Af'P\. ICArlON, IDENTIFY IHE API'lICA TIONI : 

### NA 02,**AVE~Gj** OPE RA TIN G 

# n l-' ff C F EM ISSION**SQU~Cf'** 

### OJ
. 

### .**..v..~1fW M**  CPERATlNGj ' ME 

### OF EMISSION**S~CE'** HRS!OAY O AYS /WK WK.S/Yl! H R

S/ OAY O AYS/WK WKSIYR u, i"ERCENT OJ'**AN NU~** **iHROUGH :**  

### 25 25 25 oE c. ;:n**~** MAil_MAY 

# " JUN-..I.UG 

# ,. SEPT-NOV 

# "

INStRUCTl CNS I
. COMPl E TE tHE
.... 80VE IO {NTlFI(AfiON AND GENEAAl I NFORMATION SECT ION. 2. COMPLfTf!H E R AW**MAIE~ ,**  PRODU CT
. WASTE MATU IAl. ANO FUEL USAGE SE CTIONS fO R THE 'A RTICUL AR SCURe:- ;::O UT'ME NT. COMPOSITIONS O F MA1BML S MUST BE SUfFICIE NTl Y OETAILED TO )'l LOW OET ERM INAi"lON O f THE NAruRE AND QUANT ITY OF POTENTIAl EMISS IONS. IN PARTlCJl..PoR, T HE COMPOSI TI ON OF PA INTS, INKS. ET C •• AND ANY SOt 'IENTS MUSi**~~** fU LL Y DfTAIL EO
. l. E M ISSION AN O EX HAUS T
. '01 1'11 INFORMA i lO N MUST**~E** COMPUTED. UNL ESS**EMiSSION~** ARt. EX HAUSTED TH ROOG H AlII" PCLLUTION CON UOl E C U IPMENr.**~.** OPE RATING T

IME .1.1'10 ceUAIN**THE~** IHMS UO UIR E eo rH AVUACc "'N O MAX I MUM VALUES. 

## s. FOI GENERAL INFORMATION REFER ro " '.:i;:NERAl**I'I~ UC** **loN )**  

### rOR P ERMU APP L ICATIONS .' APC

- 20I
.

DEfiNITIONS AVERAGE · THE VAL UE THAT SU MMAR IZES 01 Of THE E MI SSION SOURCr. OR T HE G ENElJo,l HATE Of ,II:OOUCIION OF IHE**MI~SION** I AVERAGE O PERAT ING TIME

- ACTUAL TOTAL HOURS OF O PE RA TI ON FOI WE PR EC!:OING TWELVE MONTH I'fRIOO. AVERAGE RArE

- ACTUAL 10TAl aUANTITY O F " MA T UIAl" FOR HIE PR ECE DING TWEL VE MONTH PEitlOO, DIVIDeD iJY THE AVERAGE**OP~RAi1NG** TIME. AVERAGe- CPEI'.A TIO N. OPERATION r YPIC).L O F THf i'
. UCE 01 NG T Wel VE MONTH PERIOD. AS lI E PIIE SENHD! Y AV!.RA GE O PERAT ING TI.v.f AND AVERAGf

. U fES. MAXIMUM· THE G8EA l[U VALUE**P~ODUCTION** OF TIlE**TC)UI~:-"\iit. i:** **,;: 'll** **Tl ':lE**  E MI SS ION SOU RC:. OR THE PER I O D Of GilEA TCST OR UTMOST 

## ; 

# " MAXIMUM**~HA"NC** TJM(
_ GlI EATESi EXPECTED T OTAL HOUtS O F OP ERA TIO NS FOR ANY TWEl VE MO N TH HRIOD. MAXIMUM RATE

- <:; ..e.4I (H aUA NTlT Y Of "MA TERIAL " €)(I"ECHO**~u** A NY ONE HOUR Of O PUATI ON. MA XIMUM O PHA TIO N " GaEAIEH eX PEClED OPfRA HOI'I.**A~ EnEHNno**  SY !MX IMUM OPERA liNG TIME. AND M:t.XIMUM RA 7 ES
.



## ............ .., 

# ......'. aAW MATERIAl. INFORMATION AVERAGE RATE MAXIMUM RATE**~** NAME OF RAW W.TERIAl PER IDENTICAL SOURCE PElt IDENTtCAL SOURCE

....vt.I. 

### Plated Metal Parts b. 

### 240 c. 

### 480 LJ/HI LB/HR 21a. 

### Chromic Acid b. 

### 0.111 c. 

### 0.222 U/HIt LB/HR 22a. 

### Sulfuric Acid b. 

### 0.003 c. 

### 0.006 LB/HR UVHR 230. 

### Water b. 

### 21 c. 

### 21 L&/HR LB/HR 

# 2...,. b. c. LB/HR LB/HR

PRODUCT INFORMAnON AVERAGE RATE MAXIMUM RATE NAME OF PRODUCT 

### PER IDENTICAL 

### SOURCE I'l:l IDENTICAL SOURCE JOG. 

### Chrome Plated Metal Parts b. 

### 240 c. 

### 480 Lil/HR LB/HR 3\a. 

### b. c. LB/HR LB/HR 32a. b. c. LP,/HR LP,/HR 

### 330. b. c. LB/HR LB/HR 

# J...,. b. c. LB/HIt I.B/HR 

# .

WASTE MATERIAL INFORMAnON AVERAGE RATE MAXIMUM itATE NAME OF WASTE MAmIlAL PER IDENTICAL SOURCE PER IDENTICAl SOURCE 4Oa. 

## NA b. c. 

### l8/HR LB/HR 410. b, c. LB/HR LB/HR 420. 

### b. c. l.8/HR La/HR 430. 

### b. c. L!!/HR LB/HR**~.** 

### b. c. LB/HR LB/HR

-FUEL USAGE INFORMATION FUEl USED TYPE HEAT CONTENT 

## sOa. NATURA,l:...::GA=S---.._

### !:D~

# __l-Jb!.:..
____ 

# =======- c. 1000 BTUISCL-
_____ '_.
_

__**..;;:O:.;.TH~EK::::...;G=A..::S~**___**--_O~:;-** 

## __. _____________________..• _____ ._. _____**u_u~£.._**

## I---O=R."------~OO~--t------------.-.------.---of----.-- 

# ..-'-
_______**I~** .

## .L~ COAL BTU/1.iI OTHER 

### [J---- 

### STUILB d,AVERAGE fiRING RATE PER IDENTICAL SOURCE; 

# I e. MAXIMUM FIRING RATE PElt IDENTICAL SOURCE: BTU/HR IITU/Hil 'THIS SECTlON IS TO BE COMPlETED FOR ANY FUEL USED DIRECT1.V IN THE PROCESS EMlSSION SOURCE. E.G. GAS IN A DRYER, OR COAl. IN A 

### MElT FURNACE.
PAGE 2 OF;]"EMISSION INFORMATION 5\. NUMBel Of IDENTICAL SOU.as (DfSCJUITE AS REQUIRED): 

### 1 

# - AVERAGE orOATION ... 

# -.- -- 

# -- - - 

# ------- 

# -- -**--~** 

# --- - 

# --- 

# ------- ------------------ CONTAMINANT CONCENTRATION OR EMISSION RATE PER IDENTICAl MfTHOD USED TO OETERMINE CONCENTRATION OR

. SOURCE 

# - EMISSION RAff 'AATICULATE 

### b. 520. c:. •• MTTER GRlSCF 18/HR 

### Emission rates based on data from "Ventilation :ARION s:Jo. PPM 

### b. c. 

### & 

### Air Pollution Control", Metal Finishing Guide oAONOXIDE (VOL) l.B/HR

... ITIOGEN 

### SAo. PPM b • 1:. JXI06 (VOl) LB/HR 

### Book, 1990 Ed., New York State Dept. of )RGANIC 550. PPM 

### b. 1:. AATERIAl. (VOL) ll/HR 

### Environmental Conservation- Handbook, iUlFUR 

### S6a. PPM b. c. )IOXIO£ (VOl) U;'HR 

### 3600-3700, and Process Make-up Data. 'OTHER 570. PPM 

### b. c. SPECFy} ('LOU 

### UL!lR MAXIMUM OPERATION 

# ----- 

# ----- ----------------- r-------- -- --------------- CONCENTRATION OR EMISSION RATE PEa IDENTICAl METHOD USED TO DETERMINE CONCENTRATION OR CONTAMINANT SOURCE EMISSION RATE 'ARTICULATE 

### SSo. b. c. 

### Emission rates based on data from''Ventilation 'AAmR GR/SCf LD/HR :ARiON 

### 590. 

### PPM 

### b. c. 

### & 

### Air Pollution Control", Metal Finishing Guide >,\ONOXIDE /VOl) lB/HR 'lITROGEN 600. P1'M b. c. 

### Book, 1990 Ed., New York State Dept. of :lXIDlS (VOl) LD/HR ::>RGANIC 610. PPM 

### b. c. 

### Environmental ConselVation- Handbook, 1MT'


### . 

## '. (VOL) LB/HR 

# - iULFU
.. 620. PPM 

### b. c. 

### 3600-3700, and Process Make-up Data. OIOXIOE (VOLI LB/J{R 'OTHER 63a. PPM 

### b. 1:. 

### iSPECIFy) (VOLI LI/HR 'ITEMS 52 THROUGH 63 NEED NOT BE COMflETED IF EMISSIONS ARe EXHAUSTED THROUGH AIR POLl.UTlON CONTROL EQUIPMENT. '-OYHER- CONTAMINANT SHOll.D IE USED FOR AN AIR CONTAMINANT NOT SPECIFICALLY NAMED ABOVE. POSSIBU OntER CONTAMINANTS

AlE ASR;STCS, ilERVlllUM,MEROJRY, VIN¥\' OilORIDE, LEAD, ETC.
'''EXHAUST POINT INFORMATION 64, 

### FLOW DIAGRAM DESIGNATlON(S) OF EXHAUST POINT: 

### Exhausted to Scrubber 53 65. DESCRIPTION OF EXHAUST POINT (\oOCATlON IN RELATION TO BUilDINGS, DIRECTION, HOODING, ETC.): 

### 66. EXIT HEIGHT A60VE GRADE: 

### 61. ex IT DIAMETER: 68. GREACEST HEIGHT OF NEARBV ilUllDINGS: 6'1. :.>cIT DISTANCE FROM NEAREST PLANT BOUNDAAY:



# . FT



# .. AVERAGE OPERATION MAXIMUM OPEMnON 

### 10. EXIT CAS TEMPERATURE: 

# n. EXIT GAS T£MPERA lURE I 

### FT

"F Of 

### 11. GAS flOW RATE THROUGH eACH eXITI 7:l. GAS FLOW RATE THROUGH EACH EACH EXIT: ACFM ACFM 

# ... THIS SECTION SHOUlD NOT DE COMPlETED IF EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUflON CONIROl EQUIPMENT.

## Illinois EPA Information Request Form for Electroplating Facilities 1. General Information: A. 

## Date: 101"'6 /0 5 

## , , 

## B. Corporat e or Plant Name:

_ __ F",m"'fP"i..Ir:.!Q,-H""a..Ir:.cd,--,Cc:nb..Ir:.cO)J:mrue '-

___ ____ _


# c. Addres s of Emi s 5 

## ion Source :__ --1'.i6c:'tcS5-SS_.JK,;:,ooss.tt..IUUe"r C-a""":se,,UlllJJ' 

## p'-
___ _


## D. Name and Phone Number of Respondent:

2. 

## Electro olatina information: F

•. 

## Electroplating metal:
B. Tank identification or designation:



## c. Type of operation: ( e.g., hard plating, decorative plating, dip plaitng (non-current), immersion (with current), anodizing) D. 

## Inside dimensions of Chicago, Illinois 60623



### St""ve Wallin

Chrnmi lim

A -1 2 3


### t.fa r d P l atin g



## tank ( 1 x 

## w x h ) : 

## __ --"

7

__Et 

# , ft E
. Actual volume of solution in tank: F. 

## Substrate material: ( e.g., steel, brass, plastic, etc.)

( 1) 3 20 

## gal 

## Steel 4 

## ft

### G. 

## Rated capacity of each rectifier:



## H
. Average daily setting of 

# eac h rec tifier:

I. 

## Hours o f operation:

J. 

## H ours per day electrode s are energized :



## K. Ampere-hours per day usag e by 

## tank/metal:



## L. Bath parameters: Voltaae l. ]? 

## v 2
. v 

## 3. v 4
. v 5
. v 

## Voltage l. <; 

## v 2. v 3. 

## v 4. 

## v 5
. v



## Maximum 24 

## hrs !day

____**-f days/wk**  

## 52 wks /yr



## Maximum



# __--=- 2

4 ::.-___ hr/ da

## y

Maximum 72 000 

## hr/day

Chemical 

## Comnosition Chromic Acid 

## Sulfuric Acid 

## (21

PA(;F, 4 1 

## AmDerage l. 

### 3000 

## amp 2
. 

## amp 3. 

## amp 4. 

## amp 5. 

## amp Amperage l. 

## ?400 

## amp 2
. 

## amp 3. 

## amp 4
. 

## amp 5
. 

## amp

Averaae 22 

## hrs/day 7 days/wk

52 wk s/yr



## p.veraoe

____ 2 22

2
____ 

## hr/day



## Averaae 5 2 

## ,8 00 

## hr/ day

Concentration

3 0 oz/gal 0.3 oz/gal

## M
.

N
. 

# o. Bath defoami n g agents and concentrat i o n s : Bath cover and thickness: Bath temperature and pH , 

## P
. Amount of electro

- 

# plating chemical used: (e.g., 

## chromic acid , e t c.) 

# Q
. Type o f ventilation h o od: ( e.g. t 

## one - sided , t, ....

## o - sided, 

## canopy I 

## etc . ) 

## 3. Emission Control Device: A. 

## Type of control device: (e.g
. , 

## mist eliminator, packed scrubber I 

## etc. ) 

## Packed: a. packing type: NB

NA


### 13 0



## Maximum

_4

.:..;

.",

8.::.

8



## _ --, lb/ da

## y
Tw o -Sided

b. packing size: 1 

## in. c. packed height 

## :_---'4"' 2

'---
__ in. ii. 

## Spray a. numbe r of 

## nozzles: b. nozzle pressure: -

____ --Pps ig 

## __**..1 J......!** **~**

## ___pH



## Average



## __**4~4 '-** **lb day** 



### B
. 

## Type of flow : 

## ( e.g., coeurrent, countercurrent, 

# crossflow) NA -**~'lashed** 

### do wn once per week

(3 )

DAr!R 4?

## C
.

D
. 

## Manufacturer, make, and model of c ontrol device:
Typical inlet gas temperature : 

## E. Inlet gas flow rate: F. 

## Exhaust gas flow rate: 

## G
. Gas pressure drop 

## across control device: 

## H. Scrubbing liquid: i. Chemic al 

## composition: ii. 

## Flow ra t e F


### 6 ,000 CFM 

## 6,000 rEM

'75 GAt.l1 !) K Dlla]]



### Water



### llJ.. Make-up rate : _-'NILIl"--

_ _ _ 

## gal/min lv
. Source : (e.g
. , 

## rinse t ank, clean wa t 

## e r , etc.)

____ -"

c .:.

'w

e ..aa.Il o'-' ""'aa.tI:..ee"' r-
___________ _

I. J. 

### v. Is liquid 

## recirculated in scrubber? 

## Efficiency of control 

# device : Identify all plating tanks controlled by 

## this dev i ce :



## 4
. Exhaust Point Informacion: A. 

## B. Exhaust exit height above ground level: 

## Exit duct inside diameter : 

## N O

- Spent water is put back in Chrome tank
.

A- J 2 3 , A-4

4 0 

### f t 2 ' x ? '


### (4)



## PAGE 43

## C. Dimensions of building 

## where duct is 

## located (1 

# x w 

# x hi, 1 75 ft 

## 200 ft 

## 30 ft 

## O. Exit Gas 

## Temperature 00 

## F E. Gas 

## flow 

## rate through exhaust point: 

## 6,000 CFi'o'l F. 

## Exit distance from nearest plant boundary: 7 5 

## ft G. 

## Dimensi o ns of 

## nearest building to the 

## exhaust 

## point 

## ( 1 

## x w 

## x hi , 700 

## ft 

## 200 ft 

## 30 ft 

## H. Distance of 

## nearest building to 

## exhaust point: 

## 200 ftSTATE OF I LLINO I S ENVI RO NME N TA L HOUCT r O N AC ENCY DIVISION OF AlA I'OL l UTI O N CONTROL 2200**CHU~ CH** **L** ROA O S P

R

INC FIElO , ILLI NO IS 61706

° OA T A AN D INFORMA TION ,IlOCESS E MIS SIO N SOURCE

'IHls INFOlMAfiON FORM IS TO 9E COMPlETEO fOR AN EMISSION SOURCE o rH ER THAN A**~UH** COMaUSTiON EMI SS IO N SOURCE**O~"' N**  IMCI Meu,TOK, A fUEL COMWSTlCN EM ISSION SCUI! G IS A FU.NACE, 

## 'aon..EI. O R SIMILAR EQUIPMEN T USEO i'RI M,ARIl

## YFOIt n.ODUC ING HEAT O R**i"OW~** lY INO IUCT HEAT TRANSFER, AN INCINERATOR IS AM
.... ,.,.AlATUS IN WH ICH REfUS E IS aURNEO.



# ,

# . NA ME O F i'lA N T OW Nfl: 1
. N AM E OF COR r OItATE DIVIS ION CR P\.AN T (IF OIF FE RlN f**RO M**  Empire Ha rd Chrome OW N O I : Emp ire H a rd Ch r ome 

# ,. HUH ADDUS; OF EM ISSION SOURCE: 

# '. L 

# , , , , 1615 S
. Kastner Ch icago

GE NERA L INfOU.V. TI O N 

### >. NAME O F**P~OCESS ,**  

# ,. NAME O f E MISS ION SOURa !CU IP MENT, Hard Chromium Plating Ch r ome Plating T ank 7. [MISS ION SOUICE**~aU PMENT**  M
.... NUFACruREIt, 

# •• MODEL NUMJlER, 

# I •• HRlAl**NUMU:~,** 

# - 

# - - flOW OI A CitAM OE S IGNATlON(S) O F E MI SS ION SOURCE: 

### A4 

# ". IDHHITYISIOf ANY SI MILAR SCURCE(s)AT THE Pl
.... N T OR H E MlS£5 NO T COV{RED ny HiE fOR M (If THE SOURCE IS COVERED OY oloNO T HER Ai'i'lICATION, IDENTIfY T HE APf>lIC,\TlO N I: 

### NA 

# I'.**oloVE~~** OPfIlAO NC 

# wg O F**~MISSIO N**  SCUg=j: 

# "
. •**......,.~f'UM** Cf'ERA TIN G flME OF EMISSLON**~~Cf.:** HIiS/ OA Y OA YS/WK WKSI'YR HitS/DAY O AYStWK WKS/YR 

# ". ?ERC£ N T OF**ANN ~THItOUGHPUT** **'** 

### 25 25 25 DEC
. F£II % MAR_MAY 

# " JUN_we 

# •• SEPT-N OV 

# "

I N SilUClIONS I
. COMI'LEU THE
..

### eov£ 10ENTlflCMlO N ANO GENERAL INfOR M ArIO N SECTION. 2, COMftEH THE RAW MAlEalA L, PROQUCT. WASH MA TE R I AL
. "NO Fun uSAGE SECTIONS FOR THE PAUICULAIi SCUR C; E OUIPMEN T
. CO MPOS ITI ONS OF MA1HIALS MUST BE**SU~ rCIEN** **n** Y DHAllEO fO AL LOW DETERMINAtiON O F THE**NAru~E** AND CUANTITY OF POTENTIAL E

MISSIONS. IN PARTICULAR, iHE CO MPOSITION Of P AINTS, INICS, ETC ., ,\NO ANY SOL VENTS MUS; liE FULL Y D£1"AIUD. J , E MISSION AND EXHAUST PO IN T INFORJ.v.ilON MUST**~E** COMI\HtO, UNlESS EMISSIONS ARE f)(HA USTEO THROOGH AIR PCLLUTION CO NTROL ECUIPMe,... r ,**~.** O PERATING TI ME ANa CERTA IN O T HH IT EMS S, Fm G EN E ML INFORMATIO N REFER TO**~GE** AN D MAXIMU M VAL ues, PERMi t APPUCATIONS.· AP C-ZOI ,

DE F INITIO N S AVEIlAGE

- 'HE VAlue T HAT SUMMAR IZES Cl REPRESEN T S T HE GENE1I.AL COND ITION Of TIl E E M I

SSION SOURCE, O R THE C EN ERAL STArE OF P R

ODUCTiON Of IHE t M IB ION SOURC E.**ECI CALL** 

### Y: AVERAGE OPERATING TIME

- .... CTUAL TO T AL HOURS OF OI'EItA H ON FOR HIE**PReC~OI C**  TWELVE MON TH PERIOD. AVERAGE RATE • ACTUAL TO T AL QUA N TI T Y O F "MATU IAt· fOIt THE PRECED ING lWEl'lE MON TH P ERIOD , OIVIOEO 

## ay THE AVERAGE**OPE~ il** **NC** liME. AVERAGf CPtRATION " OPUATION TYPIC).l OF THE i'
. :teC:OING TWIl VE MONTH HRIOD. AS UPRESEN H O 3Y AV£i'.AGE Oi'ElA Tl NG TIME AND AVERAGe UT ES, MAX IMUM. iHE 011[,,1[51 VAlUE AH AIN A!L: OR AnololNED FROM THE E MIS, ION SOURCE, Ot THE P E

R

IO D Of CREATeS T OR U T MOST PROD UCTIO N O F Tlt E**N ~o** **cL** 5PECIi'ICAl LY: MAX I MU M Qrf ilA TI NG TIME
_**~A ST**  EXPECT EO TOTA L HOURS OF O P ERA TI ONS**FO~** ANY TW n v E MONT H**PERIO~ .**  MAX IMU M RA T E

-**v~e** ... TE.ST OUANTITY OF ·'MATER IAL· EXPECHD PEl ANY ONE HOUR OF OPERATION, MAX IMUM opeRATIOM " GaEATEH EXPEClEO OPE RATION. AS**UP~HENH:O** 3Y .'N\.XIMUM OHRA T IN G TIME AND M:t,XI M UM itAiES
. 

### PAGE 4SRAW MARRIAL INFORMAnON AVERAGE RATE MAXIMUM RATE**~** NAME OF RAW MATERIAL PER IDENTlCAl SOUIlCE 

### PER IDENTICAL 

### SOUilCE



# . . Plated Metal Parts b• 

### 265 c. 

### 530 U/HR LB/HR 210. 

### Chromic Acid b. 

### 0.122 c. 

### 0.244 LB/HR La/HR 220. 

### Sulfuric Acid b. 

### 0.004 c. 

### 0.008 LB/HR LB/HR 23a. 

### Water b. 

## 24 c. 

## 24 LB/HR LI/HR 

### 240. b. c. LB/ttR LB/HR

PRODUCT INFORMAnON AVERAGE 

### RATE MAXIMUM RATE NAME OF PRODUCT 

### PER IDENTICAL SOURCE PI:It IDENTICAL SOURCE lOa. 

### Chrome Plated Metal Parts b. 

### 265 c. 

### 530 La/HR I.B/HR 

### 310. b. c. LB/HR I.B/ttR 320. b. c. U/HR LB/HR 

### 330. b. c. La/HR lB/HR J4a. b. c. 

# -' LB/HR I.B/HR

WASTE MATERIAL INfORMATION AVERAGE RATE MAXIMUM RATE NAME OF WASTE MATERIAL PER IOENTlo.l SOURCE PeR IDENnCAI. SOURa 400. 

### NA b. c. lB/HR I.B/HR 0110. b. c. LB/HR LU/HR 420. 

### b. c. LB/HR La/HR**~Q.** 

### b. <:. LB/HI 

### LB/HR**~.** 

### b. c. I.U/HI LI/HR

.,UEL USAGE INFORMATION FUEl. USED TYPE HEAT CONTENT

### S~.**NATU~~G~A~S~.**____

### ~~ ____

### ~-!b~.

## ______**~============~** 

# _.-...________**~~c~.~I~~~U~TU~~~C~F-----------·-** .• ---

_.

___ ....;;;O

... TH;.;;E;;;,;R;..;G;.;.A...;;s
_____ D:
____________________________ .. _____ . _____**n_u~~** OIL 

# 00 1--_·
________________. ________. ____ 

## +-______..._._.__**--:;;..s~** 

### .**.L~**

_ COAL ITUI1.B

_ OTHER 

## 0 ITUAU d.AVERAGE fIRING RATE PER IDENTICAL SOURCE: , •• MAXIMUM FIRING RATE PER IDENTICAL SOURCE:**~TUtl-lR** arU/HR

"THIS SECTION IS TO BE COMl'\.ETED FOR ANY FUEL USED DIRECTlY IN THE PROCESS EMISSION SOURCE. E.G. GAS IN" DRYER. OR COAL IN A 

### MfLT fURNACE.

I.PC-220 

### PAGE 46 PAGE 

### Z OF J4!MISSION INFORIMTION 51. HUMlEl Of IDENTICAL SOUICES (DESOU8£ AS UQUJREDh 

### 1 

# - AVOAGE OPERATION**-~-** 

# -- -- - 

# - 

# ----- ---- - -- - 

# --- - - 

# -- ------- ------------------ CONTAMINANT CONCENTRATION OR EMISSION ItATE PER IDENTICAL MaHOD USED TO DETERMINE CONCENTRATION OR

. SOURCE 

# - EMISSION RATE 

### b. I AlnCULATE 520. Clio. • M1TER GR/SCF 18/HA 

### EmiSSion rates based on data from ''Ventilation ::ARION $lG. PPM lo. c. 

### & 

### Air Pollution Control", Metal Finishing Guide .AONOXIDE (VOL) 18/HA -41T10GEN 

### 5<'0. PPM 

### b. c. 

### Book, 1990 Ed., New York State Dept. of JXIDES (VOL I U/H1t 'RGANIC SSG. PPM 

### b. c. AA1ERIAL (VOLI LI/H1t 

### Environmental Conservation- Handbook, iULfUlt S6a. PPM 

### b. c. )IOXIDE (VOLI LBi'l'A 

### 3600-3700, and Process Make-up Data. • OTHER 570. PPM b• c. :mcrFY} (VOL) U/HR MAXIMUM OPERATION 

# ----- 

# ----- ----------------- ------ 

# -- ---- 

# ------- ---- CONCENTRATION**~EMISSION** RATE**p~R** IOENTlCAL METHOD USED TO DETERMINE CONCENTRATION 

### 01 CONTAMINANT EMISSION RA1'£ SOURCE 'ARTICULATE 580. 

### b. c. 

### Emission rates based on data from ''Ventilation IMTTER GR/SCF 

### lB/HR :ARION 590. 

### PPM 

### b. c. 

### & 

### Air Pollution Control", Metal Finishing Guide "ONOXIDE (VOl) 1.8/HR**~ITROGEN** 600. PPM b. c. 

### Book. 1990 Ed., New York State Dept. of JXIDES (VOL) LD/HA ORGANIC 610. PPM 

### b. c. 

### Environmental ConselVation- Handbook, IMTr (VOL) 

### lBIHR


# - iULfUM 62G. PPM 

### b. c. 

### 3600-3700, and Process Make-up Data.**OfOXID~** (VOll 

### ll/HR 'OTHER 630. PPM 

### b. c. 

### ,. [SPECIFY) (VOL) 

### lB/HR "1TtMS 52 THllOUGH 63 NE£D NOT liE COMPlETED IF EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONnOL EQUIPMENT. '-O'IHER- CONTAMINANT SHOll.D BE USED fOR AN AIR CONTAMINANT NOT SPECIFICALLY NAMED ABOVE. POSSIBLE OntER CONTAMINANTS

ARE ASBESTOS,**~ERYLLIUM,** MERCURY, '1INYL CHLORIDE, LEAD, ETC•

••• eXHAUST POINT INFORMATION 64. FLOW DIAGRAM DESIGNAI10N(S) OF EXIiAUST POINT: 

### Exhausted to Scrubber S3 65. Dt:SCIIIPTION Of EXHAUST POINT (\.OCATION IN ReLATION TO BUILDINGS, DIRECTION, HOODING, ETC.!: 

### 66. EXIT HEIGHT ABOVE GRADE: 67. EX IT DIAMETeR: 68.**GII~AfEST** HEIGHT OF NEARBY BUILDINGS: 69. EXIT OISTANCE fROM NEAREST PLANT 80UNDARY: FT



# .. AVi:RAGE OPERATION MAXIMUM opERAnON 70. EXIT GAS TEMPERA TUllE: 

# n. EXIT GAS TEMP£RAlURE: FT



### or: Of 71. GAS flOW RATE THROUGH EACH eX1T1 i.l. GAS flOW RATE THROUGH EACH EACH EXIT: ACFM ACFM 

# ... THIS 5EcnON SHOULD NOT BE COMPlETED IF EMISSIONS AAE UHAUSTED THROUGH Alit POU.UJlON CONTROL EQUIPMENT.



### PAGE 47

## Illinois EPA Information Request Form for Electroplating Facilities 1. General Information:

2. 

## A. Date: 10176 / 05 

### , 

### , 

## B. Corpo ra te or Plant Name;
__ -,O"mlllf'pcl;.l r:<e

,-HIia • ..tr:cd U C:::J:lbJ:r:COlllm"e '-
_______ _


# c. Addre s s 0 

## f Emi s sion Source :__ -1J..E 6;':JL'5 3-SS_.lKuO:lSs.ttJ:0lfe"r=-A!Wu:eeu:pu J ,.,J

p'-

___ _



### D. 

## Name and Phone Number of Respondent:**E1e~troola!;,ing** 

## infQrmation: 

## A. Electroplating metal:
B. 

## Tank identification 

## or designation:



## c. Type 

## of operation : (e.g. , hard plaCing, decorative plating, dip plaitng (non - current) , immersion ( with current) , anodizing) 

## D. Inside dimensions 

## of tank 

## (1 

## x w 

## x h) , 

### E. 

## Actual vo lume 

## of solution 

## in tank: F. Substrate mat erial : (e. 

## g. , steel. brass, plastic, etc. )

(1) 

## Chi cago, I llinoi s 60523



## Steve Wallin

Chrt"\mi llm

A_4 

### Ha:r:d 

## E)ati ng

8 

## ft 3 

## ft 3

1:;00 

## gal Steel 

## ft

# G. Rated 

## capacity 

## of eac h rectifier:

H
. 

## Average 

## daily setting 

## of each 

## recti fi er :

I. Hours of operation:

J . 

## Hours per day ele ctrod es are energized:

K. Ampere-hours per day usage 

## by tank / metal :

L. Bath parameters: Volta g e l. ]? 

### v 

## 2. v 3
. v 4
. 

### v 

## 5. v


## Voltaae l. 

# " v 

## 2. v 3
. v 4. 

### v 

## 5. v



## Maximum

____**-2 ~4** 

### ___ 

## hrs ! day 7 days ! wk 52 wks / yr

Maximum



## __**24 ~** 

## ____hr ! day

M

a ximum 96 000 

## hr !day

Chemical 

## Co mposition Chromic Acid Sulfuric . l:\.cid ( 2 )



### PAGE 49 

## Amperaoe l. 

## acac amp 2. amp 3 . 

## amp 4. 

## amp 5
. 

## amp Arnoerage l. 'l. ? QO 

## amp 2
. amp 3. 

## amp 4
. 

## amp 5. 

## amp
Average 2? 

## hrs ! day 7 

## days / wk

1':; 2 

## wk s / yr

Averaae



## ____ 22:2'--

_ hr ! day

Averaae 7 0 , 400 

## hr/day

concentration



## 30 oz!gal 0 .3 o z ! gal

## M.

N. 

# o. Bath defoaming agents and concentrations : Bath cover and thickne s s ; Bath temperature and pH: 

## P. Amount of electroplating chemical used: (e
. g., 

## chromic acid, etc.)


## Q. Type of ventilation 

## hood: (e
. g . , anesided, two-sided , 

## canopy I 

## e t c . ) 

## 3. Emission Control Device: A. Type of control 

## device: (e
. g., 

## mist elim i nator, 

# packed scrubber, etc . ) i. Packed : 

## a. packing type: NA

1 ":1.0 

## OF

____**6**

## _______ :pH

Maximum Ave r age**.:.. .**  

### 4 ::.;

2 =-_--' lb/ da

## y


## ____**-2 ?~?** **J_lb day** 


## Two-Sided

S c r llbber , 53 

## Chi p Oed Pack in g Pi)tor 

## b
. packing size: 1 

## in.

B. c. packed height:
__**-s'~2**

## ____ _ 

## in. ii. 

## Spray 

## a . number of nozzles: 

## b
. nozzle 

# pressure: Type of flow: ( e.g., cocurrent, counterc u rrent, 

## crossflow) -----------Pps ig NA - Washed down once per '
.... eek

( 3 )

## C.



## D. Manufacturer, make, and model of cont r ol device :
Typical inlet gas temperature: E. Inlet gas flow r ate: F. 

## Exhaust gas flo w rate : G
. Gas pressure dro p across con t ro l device: H. 

## Scrubbing liquid: i. Chemical composition: ii. iii. lv. 

## Flow rate Make

- up rate: Source: (e.g., rinse tank, F 

## 6,000 CFM 6 , 000 

### ct<'M

' 1 5 Gti I. /t' IR Nil. 

## gal/min D JJ a))



## Nat c
....



## clean wa t e r , etc . )
____ 

## ...L

c:.J

' -'e"
. 3.o

c....-"wu.u r " ee.J: r '-

___________ _

I. 

## J. 

## v. 

## Is liquid recirculated in scrubber? Efficiency of control device: Identify all plat i ng tanks con t roll ed by this device :

4. 

## Exhaust Point Information: 

## A. B. Exhaust exit height above ground level: Exit duct inside diameter: No - 

## spent 'dater is put back in Chrome tank. 

# • ,
A_123 A_A 

## ,

40 

### f t 2 I x2'


### (4)

## C
. Dimensions 

## of building where duct 

# is located ( 1 

## x 

## w x h) , 175 

## ft 200 

## ft 30 

## ft 

## D. Exit 

## Gas Temperature 70 

## F E. 

## Ga s flow rate 

## through exhaust point: 

## 6,000 

## CFM F. 

## Exit distance from 

## nearest plant boundary: 7< 

## ft 

## G. 

## Dimensions of 

## nearest building 

## to the 

## e xhaust 

## point 

## ( 1 

## x w 

## x h ) , 200 

## ft 200 

## f t 3 0 

## ft 

## H. Distance 

## o f 

## nearest b u ilding 

## to 

## exhaust p o int: 

## 200 

## ft



# ,

PAGE 52STArE OF ILLINOIS ENVIRONMENTAL PROTECTION AGENCY DIVISION OF AIR PO LLUTION CONTROL 2200 CHURCHILL ROAD SPRINGFIELD, I LLI NOIS 62706

'DATA AND INFORMATI ON
AIR PCLLUTION CONTROL EQUIPMENT**~h"** .. ...... .**'~a** 

### ..... ,a ...**~** 

### .. .**,~,.** ,. , .. ... " ,•• , . d
. , ""
.... II ••, ,, . S''''' ' ' , '."
. Ch • • , .. "," , 

### s.." •• IgH
. 0
.. ".,
. .. . ' ,h" ,,, ,., .. . ,, •• 

## I, .... ; .. . . ..... ,h
. , ""'.".**~** 

## ..,.,.

, .... ..... ..**~** . .. .. , ,h
.. '
. .... "
.... • • i" , .... . .. . . •• • .."
... . . 11 ,. 

### ,n' ,• • h
.. h
.... . ,. , do
.. ,...**~** . .. '
..... '"
.... .. ....... h 'hI**~** .... ,

...u .. .. . .. , C u,,,

'THIS INFORMATlON FORM IS FOR AN INDIVIDUAL UNIT OF AIR POLLUTION CONuel**EaUI~MENT** OR AN AIR POLLUTION CONTROL SYSTEM.

1. NAME OF OWNeR: 

### 2
. NAME OF CORPORATE OIVISION OR PLANT (IF DIFfUENT FROM



## . H.Rn OWNER); l. STREEi ADDRESS OF CONTilCL EQUIPMENT: 

# '. CITY OF CONTROL £OUIPMENi, '"" <; 

### OHCAGO 

# , . NAME OF CONTllOL eQU IPMENT OR CONTROL SYSTEM: 

### SCRUBBER , 

## S3 IVITH OlIP BED PACKING FILTER

INSTRUCTIONS I, COMPlETE THE AaOVE IDENTIFICATION. 2. COMPlETE THE APPROPRIATE SECTION FOR THE UN I T OF CONTROL EQU I PMENT. OR THE APPROPRIATE SECTIONS FOR THE CONTROL SYSTE M. SE CERTAIN THAT THE ARRANGEMENT OF VARIOUS UNITS IN A CONUOl SYSTEM IS oYoADE a.EAR IN THE PROCESS FLOW D IAGRAM. J
. COMPl ETE PAGE 6 OF THIS FORM, EM ISSION INFORMATION AND EXHAUST PO INT INFORMATION. 4.. EFFICIENCY VALUES SHOU LD BE SUPPORTED WITH A DETAILED EXPLANATION OF THE METHOD OF CALCULATION. THE MANNER O F ESTIMATION, OR THE**SCU~CE** OF INFORMATiON.**~EFERENCE** TO THIS FORM ANY**~ELEVANT** INFORMATION**O~** EXPLANATiON INO-UDED IN TH IS PERMIT APPliCATION
. 5
. EFFICIENCY VALUES A ND CERTAIN OTHER ITEMS OF**INFO~TION A~E**  TO BE GIVEN FOR AVERAGE AND MAXIMUM OPERATION OF THE SOURC:: :aUIPMENT. FOR EXAMPlE. " MAXIMUM**EFFICIENCY~** IS THE EFFICIENCY OF THE CONTRO L eOUIPMENT WHEN THE**SOU~ CE**  IS AT MAXIMUM OPERAT ION, AND "AVERAGE flOW RATE" IS THE FLOW RATE INTO THE CONTROL EQU I PMENT WHEN THE SOURCE IS AT AVERAGE OPERATION. 6 , FOR**G~NERAL** INFORMATION REFER TO "GENERA L INSTRUCTIONS FOR PERMIT APPliCATiONS", APC - 201.

DEF IN ITIONS AVERAm - THE V ALUE THAT SUMMAR IZ ES OR**~EPRESENTS** THE GENERAL CONDiTION OF iHE EMISSION SOURC;: OR iHE GENERAL STATE OF PRODUCTION OF THE EM I SSION**SOU~cE.** SPEClF!CALL y, AVERAGE OPERATION - OPERATION TYP ICAL OF THE PR ECEDING TWELVE MONTH PERIOD, AS REPRESENTED BY AVERAGE OPERA TING TIME AND AVERAGE RATES.

' !MUM - THE OR ATTA INED FROM THE EMISS I ON SOURCE, OR THE PERIOD OF GREATEST OR UTMOST PROOUC I (I SPEC IFICALLY: MAXIMUM OPE.UTlON - THe GilEATEST EXPECTED OPERATION, AS UPRESENTED**~Y** MAXIMUM**OPE,~TiNG** TIME AND MAXIMUM RATES.

### saUBBER 

### 1. FlOW DIAGRAM DESIGNATlON(S) OF SCKlJSSER: 

### S3 2. MANUFActUW: 3. MODB. NAME AND NUMBER:



# - QUALL 

# ". fPE OF SauSBER: 

# '0 HIGH ENERGY: GAS STREAM PRESSURE DROP INCH H2O 

# '*' PACXED: PACXJNG TYPE 

## CHIP 

# BED, PACX:ING SIZE 

## 1" , PACx:ED HEIGHT 

## 42" IN. 

# 0 SPRAY: NUMBER OF NOZ!l.ES • NOZZLE PWSURE PSIG 

# 0 OTHER: SPECIFY ATTACH OESClUPTJON AND SKETCH WITH DIMENSIONS S. 

### TYPE OF FLOW: 

# o COCURR£NT 

# 0 COUNTEROJRRENT • 

# 0 aOSSFlOW 

### NA (DRY SCRUBBER) 6. SCRUBBER GEOMETRY: L£NGTH IN DIRECTION OF GAS flOW 

## 60 IN., c.'tOSS-SECTIONAI. AREA 

## 2,304 SQUARE· IN. 

### 7. CHEMICAL COMPOSITION OF SaUSBANT: 

## WATER, SCRUBBERS ARE WAHSED OOWN WEEKLY AVERAGE OPERATION OF SOURe: MAXIMUM OPERATION OF SOURe: 

### 8. SCKlJBBANT flOW RATE: 12. 

### SaUBBANT FlOW RATE: 

## 110 gal/wk 75 gal/wk GPM GPM 

### 9. GAS FlOW RATE: 

### 13. GAS flOW RATE: 

## 6000 6000 saM saM 10. 

### INLET GAS TEMPERATURE: 

# '''. INLfT GAS TEMPERATURE: 70 Of: 71:; .0,: 

### 11. EFFICIENCY OF SCRUBSER (SEE INSTRUCTION 4): 15. 

### EFFICIENCY OF SCRUBBER (SEE INSTRUcnON 4):

### 9~ % 

### PARTlCUL4TE % 

### GASEOUS 

## 97-98 % 

### PARTICULATE _%GASEOUS 

# -

OTHER TYPE OF CONTROL EQUIPMENT 1. 

### FlOW DIAGRAM DESIGNATION(S) OF ·OTHER TVPE- OF CONTROL EQUIPMENT: 

### 2. GENERIC NAME OF "OTHER" EQUIPMENT: 

# I J. 

### MANUFACTURER: 

# I 4. MODB. NAME AND NUMBER,- 

### S. OESCltlPTION AND Sx:ETCH. WITH DIMENSIONS AND flOW RATES, OF "OTHER" EQUIPMENT:



# .



# - AVERAGE OPERATION OF SOUle: MAXIMUM OPERATION OF**SOURC~** 6. 

### FlOW RATES: 8. 

### FlOW RATES: GPM saM GPM saM 7. 

### EFFICIENCY OF**~OTHER· ~QUIPMENT(SEE**  

### INSTRUCiION 4): 9. 

### EFFICIENCY OF "OTHER" EQUIPMENT(SEE INSTRUCTION .&1: % 

## cr.

PAGE 54EMISSION INFORM4TION I.
. 'UMBEl OF IDENTICAL CONTROL UNITS Olt CONTROL SYSTEMS (DESClUBE AS RfQUIRED): 

# I AVEJAGE OP£RATION OF SOURCE

## -~T~";':T

# r CONCENTRATiON

# OR eMissiON

# RAnTeR iDeNTiCAL" - MeTHOD UsEDro OfuiMiNiCoN"aNTiAl1oN

-

- CONTROL UNIT OR CONTROL SYSTEM Olt EMISSION RATE 'ARTICULATE 2a. b. <:. ,.\ATTEIt GRISe: L8/H1t 

## CALCULATIONS BASED ON DATA FROM: ::ARBON 

## Jo. PPM 

### b. c. ",ONOXIDE**(VOL~** La/Hit 

## "VENTILATION & 

## AIR POLLUTION CONTROL" "ITROGEN 

### Jo. PPM 

### b. c•. 

## MErAL FINISHING GUIDE8CXlK 1990 

## ED. NEW JXIOES (VOL) 

# . La/Hit JRGANIC 150. PPM 

# I b. c. MTERIAL (VOL) La/Hit 

## YORK STATE DEPT. OF ENVIRONMENTAL ;ULfUR 00. PPM 

### b. c.

## CONSERVATIO~O**~~l** PROCESS SOURCI llOXIDE (VOL) La/HR**Hiu>,lu~JlJl\** 

### 3 )0· 10 MANII,.'Af I'IIRI4'R JTHER 

### 1 70 • 

### OiROMIC PPM 

### b. c. 

## MSDS PROCESS MAKE-UP DATA: POLLUTION SPECIFY) 

### MIST (VOL) 

### 0.003 LS/HR IN', .'KU! ,.:. Jl 

# ..:,..,. r "1\1{ -I4'S MAXIMUM OPERATION OF SOURe:

- - - -, CONCENTRATiON 

# OR**E~siON** 

# WEPER IDENTiCAL

- 

# 1-

- METHOo useD

# TO ornRMtNECONCEN'TiAiiON

- - :ONTAMINANT CONTROL UNIT Olt CONTROL SVST!M OR EMISSION RATE 'ARTICULATE 

# I ao. 

# I Q. La/Hit 

# I c. MTTER GRISCF 

### C".ALCUr.A' ll>,l:-'**'Rn~m** ON nl1'T'ZI.**~nM·** :ARBON 

# I 90. PPM 

### b. La/HR 

# I c. .,\ONOXIDE (VOL) "V_l!J.V 

### CATION**&~** POLT IN 

# "**"ITRC'~F.N** lOa. i'PM b. c. JXIC 

# 'I (VOL) 

# I LB/HR 

# I MErAL FINISHING GUIDEBOOK 1990 

## ED. NEW JRGANIC 

# I 110. PPM b. 

# I c. ,.\ATERIAL (VOL) La/HR 

## YORK STATE DEPT. OF ENVmONMENTAL iULFUR 

# I 120. PPM 

### b. 

# I c. 

## CONSERVATION. HANDBCX)K, PROCESS SOURCi JIOXIOE I (VOL) LS/HR 

## HANDBOOK, 3600: 3700, 

## MANUFACI'URER JTHER 

## IIJo. amOMIC PPM 

# I b. 

# I c. 

## MSDS PROCESS 

## MAKE-UP DATA: POLLUTION SPECIFYl 

### MIST (VOL) 

### 0.004 LS/HR 

## CONTROL EQUIPMENT EFFICIENCIES ···OTHER· CONTAMINANT SHOULJ BE USED FOR AN AIR CONTAMINANT NOT SPECIFIc)"LL Y NAMED ABOVE. ?OSSIBLf OTHER CONTAMINANTS ARE ASBESTOS.**~ERyu'IUM,** MERaJRY, VINYl CHLORIDE, LEAD, ETC.

EXHAUST POINT INFORMATION i, rLOW OIAGaAM OESIGNATlON(S) OF ;XHAUST**POINT~** 

## ES3

, OESOIPTION Of ;XHAUST ?OINT (LOCATION IN RELATION iO BUILDINGS, OIRECTION, HOODING, ':TC.l: 

### STACK IOCATED 75 Fl' 

### FROM NORTH WALL**~.** EXIT HEIGHT ABOVE GilADE: 

# ". EXIT 0 IAMETER: 

### 40 

### 21 X 21 S, GitEASTEST HEIGHT OF NEARBY BUILDINGSI 6. EXIT OISTANa FROM NEAREST PLANT SOUNDARY: 

### 30 FT 

### 75 FT AVERAGE OPERATION OF SOURa MAXIMUM OPERATION OF SOURe:! 

### " EXIT GAS TEMPERA TURE: 9, EXIT GAS TEMPERATURE; 

### 70 OF 

### 70 0. I'
, , GAS 

### Flew RATE iHROUGH EACH EXIT: 10. GAS FLOW RATE iHROUGH EACH EXIT: 

### 6000 ACFM 

### 6000 AoC)=M



### PAGE 55

# Work In/Out - --7 ) 700 

# LB/HR 

# E-(

-- RR Exhausted to Scrubber S2 5 , 000 CFM 

# 75 F

Chrome Plating A-5 Exhausted to Scrubber S4 4000 CFM 

# 75 F / 1', 

# , , , , , , 

# , , , , I RR I RR I 

# i

, , , , 

# , ,**r---- --------** **----- --** **-- ----** **~** 

# , , Work In/Out - - Chrome Plating 1500 

# LB/HR E-- ( - - L

_ __ 

# A

_

-8

_ __ ----'

---- - - rRO.w 1000ItlIi 

## £i\JiP f l2-£



## ---

IIUf 

### Ct/ 2()1\
..

### C. 

## ,nil '>CUIII ( (OIlRII

- 1 illS : 'IC moil SWill nUl**vrrlJl** CrlOCO
_l E06?l

### ~~D 

### C

# t-\>Z 

## CiI1e 

# Pc A TINI-**"'~ S'** 

# ~h= 

# --**~**

# l-**iJ ~1'C** STATE Of I LL IN OIS ENVIRONME NTAL P"-OTECTION AGENCY DIVISION OF All. I'OlLUTlON CCNTkCl 1200**HU~CH lL**  kOA D**S'~ NGFIElO,**  I LLI NOIS 6 2706

'CATA A N D INFORMATION fROCES S EM ISSIO N SOURCE

' THIS INFOItMA II ON FORM IS TO !IE COMI'UtED f OR AN**EM ~SrON**  SCUItC[ O THER THAN A**~UH** COMBUSTION EMI SS IO N SO UItCE OJ: AN INcrNERArOl, A FUE L COM!USTION EM ISSION SOURC!: IS A fUINAa, '30lLE l , O R SIMILAII: ECU II'MEN T USE D i'RlMA RIL Y FOil i'I\COUCI NG HEAT CJ.**;>Cw~ y**  IN OIHCT HEAr**rRA FER,**  AN INcrNfJ. AT O R IS AN**I' ~A_A** **US** IN WH ICH RE FU SE IS aUR NE O , 

# ,. NAME OF nA- NT OW NER: 2. NAME O F cmrORATE ON ISI C N a ll PlANT (IF OlfFERENJ fROM Empir e Hard Chrome OWNER ]: EmpiTe H ard Chrome l. SUfE i AOORESS Of**~MIS 5ION**  S OURCE: 

# '" (W, o" "" U H ""'""" 1615 S. Kostne T Chicago

G E NERAL INfORMAT I ON 

# ,. NAME Of PROCeSS: 

# •• NAME O f EMISS ION SOURQ !CU I PMEN T : Ha r d C hromium Platin g Chrome Plating T ank


## '
. f MISS ION**sou.c~** EOU IPME NT /,\ANU FACTU RER: 

# •• MODEL NU,I.\lIU : 

# I 9 • HRIAL N U M lU :


# - 

# - - fl O W DIAGilA M OES1GI'IATlOI'I(S) O F ( MISSI O I'I SOUR CE, 

### A-5 II
. IOENTITVISI Of ;"NY SI Mil AR**SCURC (S)**  AT TH E PLA NT O R i'lEMI SES NOT C OV!3t[O B Y TI lE fOR M Uf T HE SOURCE I S COVERED BY ANOTHER Ar f'l. lCATl ON , 1 0ENTlF Y T HE APP\.!C,\ Tl ON1, 

### NA 12.**'\VEAA~'** OPERATING iI
. V! C F E MISS ION SOU

# s '1: IJ
.**MA~!rU M**  OPERATl NG , p ME O F EMISS I ON ''Stef: 

### 2 HIS/ DAY 

### 6 DAYSjW K**~~/Y1I** HRS / DAY DAYS /WK WK SI'"YR


# ... ;>EIC ENT OF**ANNU~THROUGHPU ,**  

### 25 25 25 DE C .;[ B '!I. MAl

_MA Y 

### "- JUN
....... UC 

# " SE I'T_NO V 

# "

INSTRU CTI ONS I. COMPlElE THE ADOVE 10ENTlFICArIO N AN D GE NERAL I NFORMATI O N SEcrrON. !. C OMPlEH THE R .AW**J,U jE~** **IA .**  PROOU CT
. WASTE MATH IA L, AN D fUEL US,t.,GE SECilO NS fO R i HE I'ARTICULAR**SCU~ C:**  ::CUlPMEN T
. CO MPOSITIONS Of MAT BIA L S MUST BE S UfFICJENIlY IlETA I U D ro AL L OW O::lERMINArrON O F iHE**NAru~E** AND QUA NTI Ty OF POTENtiAl :' MISSIONS. IN**PAIlTIC'J!,.l.~,** T HE C OMPOSITION**O~ NiS,**  INKS. ETC •• AND ANY SOl VENTS MUS; a E fUll Y CETAll::O. J. E MISSION "'- N O E XHAUST ,O INT JNFOltMAitO N MUST a e COMf'l..EHO, UN..E5 S i:MISS 1 0M AR E EXHAUSiEO THROUGH AIR ?ClL UTlON CONflOt E CU 1P ME N T.**~.** o pe,.,. TI NG TIME ,\NO CERTA IN O T HER IrEMS**~EOU IR** **E ~OT** **H** AVEAAGe AND IMXIMUM VALUES. S
. FO_**GE I'I~AAL**  INFORMATION REfeR TO -GE NERAL I NSnUCTlONS 

### tOR l'ERM lr APP LI CATIONS,

- AI'C-'OI.

Df FINlT lO NS TI l E !: MI SSIQ N S CURCE, C I THE STAlE OF ' RODU CTIO N I I AVE RAGE OI' E RA TlNG riME
_ ACTUAL TO TAL HOURS OF OPERA TI ON**FO~** HIE PR ECEDIN G TWElve MONT H PERIOO. AveRAGE:tArt

- ACTUA L lOTAl Q UANTITY O f " MAT E1 IAL" FOR THE PRECED IN G TWRVE MO NT H PU IOO, DIVIDED ay THE AVERAGE OP ElAilN G TIME
. AV ERAG E C PERA T ION

- OPEAATION IYPICAL Of THE**I'!IEC~OINC;** TWHVE MONTH rER le o, ;..S il EPRESENTED**AVE RAG€.** **OPE~ Tl** **NG** TIME AND**Ave~Gf** 

## .v. T U. MAXI MUM

- rHE GREAHH VALUE ;..n AIN A8t.: O R An AINEO fRO M TH [ EM ISS ION mUle:, O R T HE PER I OO O f GREA T E

ST OR UTMOST**OouCTION** Cf THE f MIBION SOURCE. SrECIFICA L L

y , MAXIMUM**Pf~ATING** TIME· GlIEA TE ST EXPEC i ED T O TAL HOURS O F O rUATIONS FO R ANY TWEl VE MON Tll**~Rleo ,**  MAX I MUM RATE

-**C~ eAl** **EST** QUA NTIT Y Of " MATER IAL · EXPECl(O**~H** ANY O NE HOUR OF**PE~ATlON .**  MA XIMUM Ol' fRA fl ON

-**G~EAlES T** **EX P~CUD**  OPS:RA TlON , AS UI'1HEN T EO 3Y
. ' M)( IM UM OPERA IIN G T IME AN D MAX IMUM**~iES.**'lAW MArERIAL INFORMATION AVERAGE RATE MAXIMUM RATE NAME OF RAW MATERIAL PEl IDENTICAl. SOURCE PER IDENTICAL SOURCE



# . Plated Metal Parts 

### h. 

### 700 10 • 

### 1400 U/HI LS/HR 210. 

### Chromic Acid 

### h. 

### 0.324 c. 

### 0.65 La/HR LS/HR 220. 

### Sulfuric Acid b. 

### 0.010 c. 

### 0.02 LS/Hl LS/HR 230. 

### Water b. 

### 44 c. 

### 44 U/HR L8/Hl 240. b. c. LB/HR LB/HR

PRODUCT INFORMATION AVERAGE RATE MAXIMUM RATE NAME OF PRODUCT PER IDENTICAL SOURce PtR IDENTICAL SOURCE lOa. 

### Chrome Plated Metal Parts b. 

### 700 c. 

### 1400 La/HI LB/HR 3\0. b. c. La/HI LB/HR 

### 320. b. 10. LBIHR U/HR 330. b. e. LB/HR LS/HR 3010. 

### b. c. LS/HR LD/HR 

# ..

WASTf: MATERIAL INFORMAnCN AVERAGE RATe MAXIMUM RATE NAME OF WASTE MATERIAL PER IDENTlo.l SOURCE PER IDENTICAL SOURa 400. 

### NA b. c. LB/HR LB/HR 

### .10. b. c. LB/HR L8/HR 42a. 

### b. c. L8/HR La/HR t)o. 

### b.**~.** U/HR l&/HR**~.** 

### b. 1:. L8/HR LB/HR

·FUEL USAGE INFORMATION FUEl. USED TYPE HEAT CONTENT 

### SOD. NATUAA,L GAS 

## Cl b. c. 1000 81U/SCF 

# . 

# .- 

# -- 0 !-. 

### alliER GAS 

## 0 

# .**ITU~EL-** 

# _. _."


# -- OIL 

## 0



# --- -- -----_......**a~.L~** COAL 

# a STUIlB


# -

_ OTHER 

## Cl STUIlS [d.-'VERAGE fiRING RATE PER IDENTICAL SOURCE: BTU/Hit \_. MAXIMUM FIRING RATE Pel IDENTICAL SOURCE: arU/HR

'THIS SECTION \S TO 8E COMPlETED FOR ANY FUEL USE 0 DIREC11.Y IN THE PROCESS EMISSION SOURCE. E. G. GAS IN A DRYER, OR COAL IN A MEl T FURNACE.
APC-220 

### PAGE 58 PAGE 2 OF J·EMISSION INFORMATIOH 51. NUMBER Of IDENTICAl. SOURCES (DESClUBE AS REQUIREDh 

## 1 AVERAGE OPUATJON


# - 

# - -- - - 

# -- - 

# - - - 

# - 

# -- 

# - -- - - 

# -- - - -- 

# -- -- 

# --- 

# ------------------ CONTAMINANT CONCENTRATION 01 EMISSION RATI! PER IDENTICAl. MUHOO USED TO DETERMINE CONCENTItATION Ot

. SOURCE 

# -**~MISSION** RAn 'AlnCULATE 

### b. 520. c:. 

### MTTER GR/SCF U/HR 

### Emission rates based on data from ''Ventilation :ARION !i3a. PPM 10. <:. 

### &Air Pollution Control", Metal Finishing Guide w\ONOXloe (VOL) I.8/HR -IITIOGEN 

## s.c.a. PPM 

### b. <:. 

### Book, 1990 Ed., New York State Dept. of 'XIOES (V0l1 LBI\-lR 'RGAN'C SSa. PPM 

### b. c:. MTUIAL (VOL} L&/HR 

### Environmental Conservation- Handbook, iULFUR 

### S6a. PPM 

### b. <:. 'IOXIDE (VOl) LB/liR 

### 3600-3700, and Process Make-up Data. 'OTHER S7a. 

### PPM 

### b. c. SPECFY) NOll LliHR MAXIMUM OPERATION 

# ----- ----- ----------------- r------- 

# -- ---- 

# ----------- CONCENTRATION 2!,EMISSION RAT!: PER IDENTICAL METHOD USED TO DETERMINE CONCENTRATION Olt CONTAMINANT SOURce EMISSION RATE 'ARTlctJLAn 

### sa." b. c. 

### Emission rates based on data from ''Ventilation 'MmR GR/SCF LDI\-lR :ARION 590. PPM 

### b. c. 

### &Air Pollution Control", Metal Finishing Guide**~ONOXIDE** (VOl) LB/lfR '1ITROGEN 600. P1"M b. <:. 

### Book, 1990 Ed., New York State Dept. of :JXIDfS (VOL) LD/HR ORGANIC 61.,. PPM 

### b. c. 

### Environmental Conservation- Handbook, 'MTERIAL (VOL) LDI\-lR 

# - iUlF 62D. PPM b. c. 

### 3600-3700, and Process Make-up Data. 010",
__ (VOL) lB/HR • OTHER 630. PPM 

### b. c. rSPECIFYl (VOL) L8/HA • IT!MS S2 THROUGH 6:J NEED NOT Ill! COMPlETED IF EMISSIONS ARE EXHAUSTED THROUGH AlII POLLUTION CONTROL EQUIPMENT. '-O'IHER" CONTAMINANT SHOUlD BE useD FOR AN AIR CONTAMINANT NOT SPECIFICALLY NAMED ABOVE. POSSIBU OntER CONTAMINANTS

AIlE ASBESTCS,**~ERYLLIUM.** MERCURY, VINYL CHLORloe, LEAD, ETC.
"-EXHAUST POINT INFORMATION 64. i=LOW DIAGRAM OESIGNATJON(S) OF EXHAUST POINT: 

### Exhausted to Scrubber S2 65. DeSCRIPTION OF EXHAUST POINT (\oOCATION IN RELAnON TO 8UILDINGS, DIRECTION, HOODING, ETC.h 

### 66. 

### Dur HE.IGHT ABOVE GRADE: 67. EXIT DIAMETeRl 68, GREATEST HEIGHT OF NEARBY BUILDINGS: 69. EXIT DISTANCE fROM NEAREST PLANT BOUNDARY: FT



# .. AVERAGE OPERATION MAXIMUM OPERAnON 70, :XIT GAS TEMPERA tURE: 

# n. EXIT GAS TEMPERA'NRe: FT

OF Of 71. Grr\S flOW RATE THROUGH EACH eXIT: 7:1, GAS FLOW RATE THROUGH EACH EACH EXIT: ACFM ACFM 

# .... ,HIS SECTION SHOULD NOT BE !=OMFtETED IF EMISSIONS AIl.E EJ<HAUSTED THROUGH AIR POLLUTION CONTROL EQUIPMENT.

APC-22Q 

### PAGE 59 PAGE lOf 3

## Illinois EPA Information Request Form for Electroplating Facilities 1. General Information:

2. 

## A. Date: 10/26/95 

## , . 

## B. Corporate or Plant Name: Empiro Hard Chrome

C. 

## Address of Emission Source: 161 t:; 

### S 

## Kastner /:\"'''D110

D. 

## Name and Phone Number of Respondent:
Electroglating information : A. 

## Electroplating metal:
B. 

## Tank identification or designation:

c. 

## Type of operation: (e.g
. , hard plating, decorative plating, dip plaitng (non-current) , immersion (with current) , anodizing) 

## D. Inside dimensions of tank (1 

## x w 

## x h) , 

## E. 

## Actual volume of solution in tank: F. 

## Substrate material: (e.g
. , steel, brass, plastic, etc . )
(1) 

## Chicago , Illjnois 

### 60623



## Stoue Wallin



## Cbromjnm

8

- 5 Hal:O 

## E] at j 

### Dg

11 

## ft 4 

## ft

2600 

## gal Steel



### PAGE 60 8 

## ft

## G. Rated capacity of each 

## rectifier:

H. 

## Average daily setting 

## of each rectifier:

I. 

## Hours of operation:

J. 

## Hours per day electrodes are energized:

K. Ampere-hours per day usage by tank / metal:



## L. Bath parameters: 1. 

## 2. 3. 

## 4. 5
.

l. 

## 2. 3. 

## 4. 5. 

## Voltage J 2 

## v J 

### 2 

## v v v v Voltage 5 

## v 5 

## v v v v



# Maximum 24 

## hrs / day 7 

## days / wk 52 

## wks/yr

Maximum

__ -=.24::.-
__ 

## hr/ da

## y

Maximum 

## 240 , 000 hr/ day

Chemical Composition Chromic Acid 

## Sulfuric Acid (2)



## PAGE 61 Amperaae l. 

### 5000 

## amp 2. 5000 

## amp 3. 

## amp 4. 

## amp 5. 

## amp Amperag e 1. 4000 

## amp 2. 4000 

## amp 3. 

## amp 4. 

## amp 5. 

## amp
Average 22 

## hrs / day 7 

## days/wk



## 52 wks/yr
Average



## ____ 2 22

2
____ hr/day

Average 

## 17 9,000 hr/ day
Concentration



## 30 oz/gal 0.3 oz/gal

## M.

N.


## o. 

## Bath defoaming agents and concentrations: Bath cover and thickness; Bath temperature 

## and pH: 

## P. Amount of electroplating chemical used: (e.g., 

## chromic acid, etc.)
Q
. 

## Type of ventilation h ood: (e.g., onesided, two
- sided, 

## canopy I 

## etc.) 3. Emission Control Device: A. Type of control device: (e
. 9
. , 

## mist eliminator, packed scrubber, etc. )

## Packed: 

## a. packing type: Nl\

NA

J 30 

# 0 "**~**

### __**OLJ6 ~** 

### ______ pH



## Maximum Average**14 ~.~** **25~**

## __**lb/day** 

## ____**-27~133_1b/day**


## Two-Sided

Scrubber 52 

## , Mesh Pad FiJ t pr 

## b
. packing size: NA 

## in
. in.

B. 

## c. packed height:
__**3~6** 

## ____ _ 1.1.
. 

## Spray 

## a. number of nozzles: 

## b. nozzle 

## pressure: Type of flaw: (e.g ., cocurrent, 

## countercurrent, crossflow) 

## ----- ---Pps ig NA

- Washed down once per week

(3 )



### PAGE 62

## C. Manufacturer, make, and model of control device:



## D. Typical inlet gas temperature: E. 

## Inlet gas flow rate: F. 

## Exhaust gas flow rate: G. Gas pressure drop across control device: H. 

## Scrubbing liquid: i. Chemical composition: 75 F 

## 18,000 CFM 1 8 00 0 

## cFM 

# , Cyclone

Wa t or 

## ii. iii. lv. Flow rate 11IOijl[1

## = = = ]I:::;A:I<LL7 71'

l'1llK'--- -- - -- ------

I. J. 

## Make-up rate:



## _ -""TI\'--
___ gal / min Source: (e.g., rinse tank, clean water, etc. )

_ ___ -"

c :.Jue ..

aaIlo....l/ W"aljt t:.eAJ: r '-

_________ __ _ 

## v. 

## Is li qu id recirculated in scrubber? Efficiency of control device: I dentify all plating tanks controlled by 

## this device: No - 

## Spent water 

# is put back in Chrome tank.

4. Exhaust Point Information: A
. 

## B. Exhaust e x it h e ight above ground level: Exit duct inside diameter: 40 f t 

### 1 5 x 

### 15ft
(4 )



## PAGE 63

## C. 

## Dimensions of building where 

## duct 

## is located 

## (1 

## x w 

## x hi, 175 

## ft 

## 200 ft 

## 30 ft D. 

## Exit Gas Temperature 70 

## F E. 

## Gas flow 

## rate through 

## exhaust point: 

## 5,000 CFM F. 

## Exit distance from nearest plant boundary: 7 5 

## ft 

## G. 

## Dimensions of 

## nearest building 

## to the 

## exhaust point 

## (1 

## x w 

## x h): 700 

## ft 

## 200 ft 

## 30 ft 

## H. 

## Distance of 

## nearest 

## building to 

## exhaust 

## point: 200 ft

PAGE 64STATE OF ILL INOIS ENVIRONMENTAL P ROTECTION AGENCY DI

V ISI ON OF AI R POLLUTION CONTROL 2200**CHU~CHILL** ROAD SPR INGFIELD, ILLINOIS 6 2 706

' OATA AND INFO RMATION
AI

R PCLLUnON CONTROL EQ UIPMENT**T~"** •••**~** •• "
. wl
........ I. , . ..... I
... .**~,.,_ "**  ••**~ .~**  • • •**".~** ...**~** .. " •• so .. . ... . 1119.**c~** .. .. , II ••• 10
.... _ I on. o ...,• •**~** ..., I"
..**,., ".~** 

........ . . . .....**,~ ,**  .H "Oft,
... , ... •• •• • • "'
.. .. ... . . I"
.. I
..... It
. ... 

### • "' f
. .... ... . •• • ..... . .. ... ." ,h ' " ." "" .'
. .. . . . . .. . . .. Th" I.,
.. ' " • •• • • ••• • ••• • • IU**~. ''''** **'**

.. . .. . ..... Ul c .... .

'THIS INFORMATION FORM IS FOR AN IND I VIDUAL UN I T OF AIR POLLUTION CONUOL EOUIPMENT OR AN AIR I'CL LUTION CONTR OL SYSTEM.

I. 

### J
. NAME OF OW NER: 

### FMPTRF H.Rn**STR E~T**  ADDRESS OF CONiilCL EOUIPMENT: 

### 1 "1' , 

# I 2.


# '
. NAME OF CORPORATE DI VISION OR PLANT (IF DI FFERfNT FROM OWNER) : CITY OF CONTROL :: OUIPMENT: 

### CHICAGO 5. NAME OF CONTlOL :::OUIPMENT OR CONTROL SYS TEM, 

### SCRUBBER , S2 

### (WITH MESH PAD FILTER)

INSTRUC nONS I. COMPUTE T HE Ai30VE IDENTIFICATION. 2
. COMPlETE THE APPROPRLATE SECTION FOR THE UNIT OF CONTRC1. EQUIPMENT
. OR THE APPROPR I ATE SEcn ONS FOR THE CONTRCL SYSTEM. aE CERTAIN THAT THE ARRANGEMEN T OF VARIOUS UNITS IN A CON T ROL SYSTEM IS MADe a.EAR IN THE PROC='S S FLOW OIAGitAM. J
. COMPLETE PAGE 6 OF THIS FORM. E MI SS ION INFORMATION AND fXHAUST PO INT INFORMATION. 4. EFF I CIENCY VA L UES SHOULD BE SU PPORTE D WITH A DETA ILED EXPLANATION OF THE METHOD OF CALCULATION, THE MANNER OF ESTIMATION, OR THE SOURCS OF IN FORMA TI O N. REFERENCE TO TH I S FORM ANY**EL ~VANT**  INFORMATION OR EXPLANATION INCLU DED IN THIS HIlM I T API'I..!CATION. 5
. EFF ICIENCY VALUES AND CERTA IN OTHER ITEMS OF INF ORMATION AilE TO liE GIVEN FOR AVERAGE AND MAXIMUM OPERAT I ON OF THE SOURCE E OUIPMENT. FOR EXAM PlE , "MAX IMUM EFFICIENCY'· IS THE EFFICIENCY OF THE CONTROL eQUIPMENT WHEN T HE SOURCE IS AT MAX IMUM OPERATION, AND**~AVERAGE** FLOW RATE" IS THE FLOW RAH INTO THE CONTROL EQU IPMENT WHEN THE SOURCE IS AT AVERAGe OPERArJON. 6
. FO R GENERAL I NFORMA TI ON REFER TO**GCNEilAL** INS'iil.UCTIONS FOil PERM I T API'I..ICATlONS ", APC-201.

DE FINI T ION S AVERAGE

- THE VALUE THAT SUMMARIZES OR REPRESEN T S THE GENERAL CONDITION OF THE EM ISSION**SOURC~** OR THE GENERAL STAT!': OF PRODUCT ION OF IHE EMI SSION SOURCE
. SPE CI FltALL Y: AVERAGE OPERATION

- OPERATION TYP ICAL OF THE PR ECED ING rwave MONTH P E RIOD. AS REPRESENTED BY AVERAGE OPERATING TIME A ND AVERAGE RATES. MAXIMUM

- TH E**G~EAreST** VAL UE ATTA I NABLE OR ATTAIN ED FROM THE EMISSION**SOUR C~** **,** OR THE PER IOD OF GREATEST OR UTMOST I'RODUC. TlON 

### Of tHE EM I SSION SOURQ
. SPECIF iCAlLY: .AXIMUM OPERA TION

- THE GREATEST EXPECTED OPERATION, AS REPRESENTED 8Y MAXIMUM OPERAT ING TIM E AND
. MAXIMUM RATES,



### PAGE 65

### SCRUBBER I. flOW DIAGRAM DESIGNATION(S) OF SCRUBBER: 2. MANUFACTURER; 3. MODEL NAME AND NUMBER: TYPE OF SCRUBBER: 

# .J HIGH ENERGY; GAS STREAM PRESSURE DROP INCH**~O** 

# 0 PACXED; PACKING TYPE • PACKING SIZE , PACKED HEIGHT IN. 

# 0 SPRAY: NUMBER OF NOZZLES • NOZZLE PRESSURE PSIG 

# 0 OTHER: SPECIFY ATTACH DESCRIPTION AND SKfTCH WITH DIMENSIONS 5. 

### TYPE OF FLOW: COUNTERQJRRENT • 

# 0 0 COCURRENT 

# 0 CROSSA-OW 

### 6. saUBBER GEOMETRY: LENGTH IN DIRECTION OF GAS FLOW IN., CROSS-SECTIONAl AREA**SQ~ARE** 

### IN. 

### 7. CHEMiCAl COMPOSITION OF SCRUBBANT:
AVERAGE OPERATION OF SOURCE MAXIMUM OPERATION OF SOURCE 

### 8. SCRUBBANT flOW RATE: 12. SCRUBBANT FLOW RATE: GPM GPM 

### 9. GAS flOW RATE: 13. GAS flOW RATE: SCFM SCFM 10. INLET GAS TEMPERATURE:**1~.** 

### INLET GAS TEMPERATURE:**.~** Of 11. 

### EfFICIENCY OF SCRUBBER (SEE INSTRUCTION 4): 15. 

### EFFICIENCY OF SCRUBBER (SEE INSTRUCTION A): % 

### PARTlCUL4TE % 

### GASEOUS % 

### PARTICULATE _%GASEOUS

r-- 

### OTHER TYPE OF CONTROL EQUIPMENT 

### 1. FLOW DIAGRAM DESIGNATlON(S) OF -OTHER TVPE- OF CONTROL EQUIPMENT: 

### S2 2. GENERIC 

### NAME OF -OTHER- EQUIPMENT: 

# I 3. MANUFACTURER: 

# I 4. MODel NAME AND NUMBER:. 

### DRY SCRUBBER CYCLONE 

# --- 5. DESCRIPTION AND SKETCH, WITH DIMENSIONS AND flOW RATES, OF -OTHER.- EQUIPMENT; 

### SEE SCRUBBER DIAGRAM



# .

. I- 

### AVERAGE OPERATION OF SOURCE MAXIMUM OPERATION OF SOURCE 

### 6. FLOW 

### RATES: 8. FLOW 

### RATES:/1 

## 50 

# r..ru:.lliK GPM 

## 5000 SCFM 

## 75 GAL WI< GPM 

## c;.nnn SCFM 

### 7. EFJ=ICIENCY OF ·OTHER- EQUIPMENT (SEE INSTRUCTION .e): 9. 

### efFICIENCY OF ·OTHER- EQUIPMENT(SEE INSTRUCTION A): 

## 97-98 % 

## 97-98 'Ie 

# PAGE 66 lL 532-0260 

### APe 260 PAGE 

### S OF 6EMISSION I N FORMATION I. NU M IIER OF ID EN TICAL CONTRCL UN I TS OR CON TROL SYSTEMS (D E SOJIIE AS I 

# ,



# - AVERAGE O PEItATl ON OF SOURCE

## 'CONT~~T r

## CONaN**TiA TI~~** **~ ~lss** **iON RATE** **Te R**  IDEN TI CAL 

# - METHOD USED 

## To OeTE RMI NECONCENTlATJO N - OR EMISSION RATE 20
. o. 

# .. MAm. Gii/SO' LlltHR 

### CALCULATIONS BASED ON DATA FROM:


# .. CARBON 

# I ' 0
. 

### PPM 

# I • . MONOXIDE (VO L) LII/Hit 

### "VENTILATION & 

### AIR POLLt1I'ION CONTROL "



# ... 

# ... NITROGEN 

### PP M 

# •• METAL FINISHING GUIDEBOOK 

## 1990 ED. NEVI OX I DES 

## ,Vall LS/H'**OilG~ NIC**  So. 

### PPM 

# I • . '
. MATERIAL (Val) LII/HR 

### YORK STATE DEPT
. OF ENVIRONMENTAL SULFUR 

# I 00. 

### PP M 

# I b
. 

## '.

# ~

# ~ D IOXIDE (Va L l LII/HIt O THeP. 

# I ;0.

# ~~C >PM 

## •. 0.0043 

# ..MSDS PROCESS 

## MAKE

- UP DATA , POLLUTION (SPECIFYl (VC Ll lSIH' MAXIMUM OPERATION OF SOUR C!



# ---

- -

### CONC~NTiATiO'N 

# OR E ....



# assioN W: ?ER JDENTlCAl. - - 

# - - METHOD US ED TO DHERMlNECONCENTRAiJON - -**CO NT~M** **NANT** CONTROL U NIT OR CONTROL SYSTEM OR EMISSION RATE

' 0 , o . 

# .. MAml GR/sCF LII/Hit 

### nN n.",.**",,,~ .**  CA lBON 9 0, 

### PPM 

# •• 

# .. MO NO X IDe (VOL ) LII/HR 

# , & 

### AIR 

# . " 100
. 

### ?PM 

# •• 

# .. OX ID ES (V OL ) 

# I lll/Hit 

## 1990 ED. NEI'I



# - O Re
. Ie 110 , 

### PPM 

# ••

. \o\AUltiAl (VO L ) lll/HIt SULF UR 120 , 

### PPM 

# ••

# ~OF PROCESS D IOXIDE (VOL I t ll/HR 

## 3600, 

## 3700, MANUFACl'UR<R OTHER IJ o. 

### CHRQ/>UC ?PM 

# •• • • M.SD5 ( Sl'fC 1FYI 

## MIST (VC L ) 

## 0.0054 LS/HI[ 

### CONTROL EQUIPMENI' EFFICIENCIES



# . 

# . . • OTHER C ONT..M I NANT SHOULD BE USED FOR AN Alii CONTAMINANT NOT S?ECIFlCAlL Y NAMED**~DOVE.** ?O SSleLE OTHER**CONT~MIN~Nrs ~RE**  ASIIESiOS, 3ERYUIUM. MERCURY . V I Nyt CH LORIDE. LEAD, ;;rc.

:;:XHAUST POINT I NFORMATI O N 

## •• ,LOW D IAGi\AM OES IGN AilON(S ) OF :::X HAUST ?O INT, 

### ES2 2. OfS CitlPTION Of EXHAUST P OINT (LOCATION IN RelATION T O BUILD IN GS. D I REC710N , HOOD I NG.**TC J:**  

### STACK 

# LOCA= 75 FI 

### FROM NORTH WALL 

# , . EXIT HEIGHT ;..SovE**~DE:** 

## •**~XIT** OIA METER: 

## 40 2 ' 

## x 2 ' 5
.**~EAS EST**  H EI GHT Of NEAR BY ilUILDINCS: 

# • • EXIT O ISTANC!; rROM NEAREST PlANT SCUNDARY : 

## 30 FT 

## 75'**~T** AVERAGE OPERATI ON OF SOURCE MAXI MUM OPERATION OF SOURC!; 

# '. EXIT GAS T EMPERATURE: 

# ,. EXIT GAS i EMI'ERATUR E: 

## 70 OF 

## 75 0. 

## , 

# --**~**

# ..**;~~** 

### Flew RATE iHRQUGH EACH EXIT: 10. GAS FLOW RA r E THROUGH EACH EXIT: 

## 5000 ACFM 

# " nnn**~C~M**



### PAGE 670'\ 

### co Vented From Tank A-S SOOOCFM ExhaustES2 SOOOCFM 

# f75 F**~-.** 

# I I**~** 

### Pofyster Filters 

# LJ On4Sides 10FT Above Roof



## ) L-- 

### Access Door**~** 

### ForWeeldy 

### 5' Washdown (50 GallWk) 

# Me-;hP;' iK

Filters 

## eo:

-----

## ~ 

# I**~** 

### Catch Basin For Washdown '---------' Dumped Back in Chrome Tank 

# Scrubber S2

PROJ£ci-' IOCAI(1I1 1111£ 

### 5C12c.H3e,ER PIA 

## 6- pAM 'SCAli' 

# --'-::::::'1_**Ol!_=-==-!!I:--'-~~V ~---""---~I~~-:=--_**  'sciiuiiic-co-'IIROI'jAiiS."u=IC:-, --- _**~~:!:** _**~_~Qf..!tJ-_**

lisa SOUlIIY.OUI AV[UlJ[ CHICAGO, It 60621STATE OF ILLI NOIS ENVIRON MEN TAL nOTEctlo N AGENCY DIVISION OF AIR POl l UTI O N CO NT ROL 2200 CHURCHIL L ROAD SPR INGF IELD, I LL INOIS 6Z706

· O

ATA A N O INFOR MATIO N 'ROCES S EM I SS I O N SOURCE

· THIS INFORMATION fOItM IS ;0 BE COMI'LElED FOR A N EM ISSION**SOUR~E** OTHEI THAN A Fun COMBUSTION EMISSIO N SOUltCE all: AN**INCINE~TOR.** A FUel CO M !US TI ON EMISSION SOUltC: IS A FURNACE, BO I LEl, OR S IM ILAR EOUI PMfNT USED PRIMARIL Y f OR PRODUCING HEAT OR .POWER 8Y INO I RECT HEAT TRANSFER. AN INCINERATOR IS AN AI"ARATUS IN WH ICH REFUSE IS BUR N EO. I, NA M E OF PLAN T OW N ER: 2, NAME OF CORPORATf OfYIS ION OR P'
... ANi (IF :l IF FERENT F ROM 

### E mpire H a rd Chrome OW NE R ) , 

### E mp i re Ha rd C hrome J,**ST~~E{ A~01{S** **S** OF EM I SSION SOURCE, 

# "**LI~ ·** **.U~ ~**  

# ,**,~<C"** 

### 5
. Qstner Chicago

GENERAL INFORM" T I ON 

# " NAM E**~F PROCES~:**  

### Har Chromium Plating 6, NAME O F EMISS ION SOURe! ! QU IPMENT, 

### Chrome P lating Tank 7 , EM IS SI ON SOURCE E QU IPMENT MANUFACTURER : 

### e, MODEL N UM6 ER, 

# I 9, HRtAL NU MIER,



# - - - 10, FLOW DIAGRAM DES IGNATlON(S ) OF £MI SS ION SOURCE, 

### A- 6

" IDE NTITV[SI Of ANY SIMILAR .sOURCHS) Ai THE PLAN l OR PlEM ISES NOT COVflI:£D BY TH E fORM /I F THE SOURCE IS COVERED IIV**ANOTH~R** MPlICATlON, IDENTIFY T HE MI'lICATl O N I: 

### N A 12,**AVE~** OPERATiNG**TI~** O F EMISSION**SCU~'2':** IJ,**~if'UM** OPERATING j/ME OF EMISSION**S~~CE:** HRS/ DAY 0,01. YSjWK WI(SIYR HRS/D
... Y OJ. 

### yS/wrc: WKSIYR 

# ", PUClNT OF**AN U~THROUGHPUT** **:** 

## 25 25 25 DEC_FEB % M
...._MA V 

# " JUN
....... UC 

# .. SEPT -NOV 

# ..

IN STRUCTlONS 1. COMPlETE THE Ae ove JOENTlfICArrON AND GENUAl INFORMATION SECTION. 2. COM Pl ETE THE RAW MA1E1UAL. PRODUCT, WASTE MA r e. ' Al , AND FUEl USAGE SECTIONS FOR THE PARTICULAR SOUR CE EOUIPMENT. COMPOSITIONS OF MATH IALS MUST 8E**~FFICIENn** 

### v DE T AILED TO AL LOW DE T ERMINATION OF THE NATURE AND QUA NT ITY OF POTENTlo\l EMISS IONS. IN PARTICULAR, i HE COMPOSITION OF PAINTS, INKS , ETC., AND ANY SOL VENTS MUS
. Bf fU LL Y DETA I lED. J. EMISSION AND EXHAUSi FaIN T INFORMAiiON MUST eE COMPL(nO, UN.fSS**EMISSION~** ARt. EXHAUSTED THROUGH AIR POLLUTION CONTlOl ECUIPMEN T
.**.** OPEkATiNG**lJM ~**  AND**<E~TAIN** OTHEl ITEMS R E OUIRE aOTH AVEMoGE AND MAXIMUM VALUES. 

### S. FOR GEN E AAL INFOR IAAT/ON REFER TO**~GENUAL** 

### INs nucrroNS fOR PERMit APPLI CATIONS, " APC

- 20\
.

DWNITIONS AVERAGE

- 

# THE VA.LUE

# 1i**~::;~~~ '£!** **!iS~ o;l** **"H;; ~~~~l£~£** **:Co;;' ;-** **TTiH ii** **Gi' EN** **NC E"'** **sSiT~A:tTEE(O;;F ~-1**  'ROOUC lJ ON

### ~ I AVEkAGE OPERA TI NG TIME
_ ACTUAL TO T Al HOURS OF- OI't"ItA Ti ON FOR THE PRECED ING TWElVE MONT H PEItIOO. AVERAGE 1tArt:

- ACTUAL Tor AL a UAN Tl T Y OF "MA.TEW\L" fOR THE PRECED ING TWElVE MONTH PERIOD, DIVIDED BY THE AVERAG( OPUA TI NG TIM E. AVERAGt CPtRATi O N

- OPERATION TVP ICAl Of THE PiUCEOING TWELVE MONT H fU IOO, AS REPRESEN H O BY AVE.RAGE OHUTING 

### TIME AND AVERAGf RATn. MtVCIMV M

- THE GREA TEST VALUE FROM THE EMISS ION**~OU CE,**  OR THE PER I OD OF GR E ATE ST OR U TMOST PJl:OC UCTlON CF Tm I I y, MAX IMUM or E RATING TI ME - G R EA T EST E XPE C T EC TOT A L**HOU S**  OF**OPER"TlON~** f OR
.... N V TWELVE MON TH**PERIO~ .**  MAX IMU M RATE
_ G R EA Ten aU
.... N TITY OF "MA H R I AL" EX P ECHO PE_ ANV**ON~** HO UR OF OPERATIO N
. MAXIMUM OP ERA TION

- GREATEST E:.cPEClEO OI'l:RATl ON, AS REPIEUNHD!Y ,'M)( IMU M OP E RA TIN G TI ME "'NO MAXIMUM RAi ES, ""C-220 (II.£V ISED 1/27ml PAm I OF JRAW MATERIAL INFORMATION AVERAGE RATE MAXIMUM RATE NAMe OF RAW MAT£RIAL PER. IDENTICAl SOURCE PER IDENTICAl. SOURCE

, 

### Plated Metal Parts b. 

## 1500 c. 

## 3000 La/HR LI/HR 21a. 

### Chromic Acid b, 

## 0.70 c. 

## 1.4 L8/HR LIIHR 

### 220. 

### Sulfuric Acid b, 

## 0.02 c. 

## 0.04 La/HR LB/HR. 

### 230. 

### Water b. 

### 66 c, 

### 66 La/HR LB/HR 2040. b. c, U/HR LB/HI

PRODUCT INFORMATION AVERAGE RATE MAXIMUM RATE NAME OF PRODUCT PER IDENT/CAL SOURCE PI:R IDENTICAL SOURCE 300. 

### Chrome Plated Metal Parts b. 

## 1500 c. 

## 3000 LB/HR LB/HR 3\a. 

### b. c. LB/HR LB/HR 

### 320. 

### b. c. L&/HR LII/HR 33a. b. c, LB/HR LB/HR 3'a. b. c. 

### LEI/HI LB/HR

WASTE MATERIAL INFORMATION AVERAGE RATE MAXIMUM RATE NAME OF WASTE MATE1IIAL PER IDENTICAL SOURCE PER IDENTICAL SOURCE <U)a. 

### NA b. c. La/HR I.B/HR 41a. b. c. l8/HR La/HR 420. 

### b. c. lB/HR LI/HR 430. 

### b.**~.** 

### LB/HR lB/HR**~.** 

### b. c. I.B/HR lBiHR

·FUEL USAGE INFORMATION FUEL USED TYPE HEAT CONTENT**~**

# ____**I~~**

# ______**~==========~** 

# __________**~~c~,-l~~~~Bru~J~~,C~F--.--------~·** . ___ , ________________ , ____.. ____•• _____ ._. _____**.......;.I.;..;TU~~** 

# =---1--,-----------.--,-------
..

# ---1---,----
...___...__. ___**""B~.L~** aruA.8 

### 500.**NATU~** GAS 

# -- 0 b. OTHER GAS 

# . 0 

# g- _. OIL COAL OTHER 

## 0**~** ERAGE FIRING RArE PER IDENTICAL SOURCE;

' e. MAXIMUM FIRING 

### RATE PER IDENTICAl. SOURCE; BTU/HR BTU/HR "THIS SECTION'S TO BE COMP\.mo FOR ANY FUEL USED DIRECT1.Y IN THE PROCESS EMISSION SOURCE. E. G. GAS IN A DRYER. OR COAL IN A MELT fURNACE,


### APC-220 

# PAGE 70 PAGE 2 OF J·EMISSION INFORMATION st. NUMBER OF IDENTICAL SOURCES (DESCRIBE AS R£QUIRED): 

### 1 AVERAGE OPERATION 

# - .. 

# _-- - 

# - -------------------,;..,; ------------------------- CONTAMINANT CONCENTRATION OR EMISSION RATE PER IDENTICAL MfTHOD USED TO DETERMINE CONCfNTRAJlON OR

, SOURCE - EMISSlnN RATF 

### 520. b. c. 'AAnCULATE 

### MTTn GR/SCF LB/HR 

### Emission rates based on data from "Ventilation :ARION ",ONOXIDE 'IITlOGEN :>XIDES )RGANIC AATERIAL jULFUIt )IOXIDE
• OTHER 

### :SPEClFy) 

### S3o.**~.** SSa. 

### 560. 570. PPM (VOL) PPM (VOL) PPM (VOL) PPM (VOL) 

### PPM (VOL) 

### b. c. 

### & 

### Air Pollution Control", Metal Finishing Guide I.B/Hit 

### b. c. U/liR 

### Book, 1990 Ed., New York State Dept. of b. c. UI/HR 

### Environmental Conservation- Handbook, b. c. U;'1iR 

### 3600-3700, and Process Make-up Data. b • c. la/HR



# ----- MAXIMUM OPERATION 

# ----- ----------------- i-'------ -- ---- ----------- CONTAMINANT 'ARTICULATE 

## w.mR ::ARBON I,\ONOXID£ '1ITROGEN :::lXID!;S ORGANIC 'MTERIAL CONCENTRATION OR EMISSION RATE PER IDENTICAL METHOD USED TO DETERMINE CONCENTRATION Olt SOURCE EMISSION RATE 580. b. c. 

### Emission rates based on data from 'Ventilation GR/SCF 

### lD/HR 

### 59o. PPM 

### b. c. 

### & Air Pollution Control", Metal Finishing Guide (VOl) 

### lBIHR 6Oa. 

### PPM b. c. 

### Book, 1990 Ed., New York State Dept. of (VOL) 

### LD/HR 610. PPM 

### b. c. 

### Environmental Conservation- Handbook, (VOL) LBIHR

,

## "----~~~----------~~~-----------~~~~-------------------------------------~ '. OTHER /SPeCIFY) 

### 620. 630. PPM (VOLl PPM (VOL 

### I b. c. 

### 3600-3700, and Process Make-up Data. l8/HR 

### b. c. 

### La/HR "ITEMS S2 THROUGH 6:J NEED NOT BE COMPlETED IF EMISSIONS ARe EXHAUSTEO THROUGH AIR POLLUTION CONTROl. EQUIPMENT. ·-orHER M CONTAMINANT SHOU.O BE USED FOR AN AIR CONTAMINANT NOT SPECIFICALLY NAMED A80VE. POSSI8LE OntER CONTAMINANTS

AlE ASBESTOS, 8ER"fl..LIUM, MERCURY, VINY1.. CHLORIDE, LEAD, ETC•

.... eXHAUST POINT INFORhV.T10N 

### 64. fLOW OIAGRAM DESIGNATlON(S) OF EXt-tAUST POINT; 

### Exhausted to Scrubber S4 65. D£SCRIPTION OF EXHAUST POINT (LOCATION IN RELATION 'TO BUILDINGS, OIRECTION, HOODING, ETC.): 

### 66. EXIT HE IGHT ABOVE GRADE; 67. EX 

### IT OIAMETU: 69. GREATEST HEIGHT OF NEARBY 8UILDINGS; 69. EXIT DISTANce FROM NEAREST PLANT BOUNDARY:



# . FT



# .. AVCRAGE OPERATION MAXIMUM OPERAnON i'Q. EXIT CAS TEMPERATURE: 

### 72. EXIT GAS TEMPERA lURE: FT

Of 

### OF 71. GAS FLOW 

### RATE THROUGH EACH EXIT: T.J. GAS FLOW RATE THROUGH EACH EACH EXIT, ACfM ACFM 

# ... THIS SECTION SHOUlD NOT 

### BE COMPtETED IF EMtsSIONS AIlE EXHAUSTED THROUGH AIR POllUTION CONTROL EQUIPMENT.



# PAGE 71 PAGE. J OF 

### l

## Illino i s EPA Information Request Form for Electroplating Facilities 1. General Informa t ion:

2. A. 

## Date: J Oh 6 / 0S 

## , , 

## B. Corporat e or Plant Name :

___E=m'!=pui..l r::Jp

""-,,H.aacIro:d1..cCub.zr:colImWp""-

_______ _


# c . Addres S 0 f 

## Em iss ion Sour c e : __ --l

l 

### b

6.:l1-, S ,--,S"---" KO:o,"s
..

t.n",,pcIr'--"!C1IL'PPIlIlcl;llL.eP '-
__ _



## D. Name and Phone Number of Respondent:
Electroolating information: A. Electroplating metal:
B
. 

## Tank identification
or 

## designation:

c . Typp 

## of operation: 

## (e. g. , hard 

## plating, decorative plating, dip plaitng (non-current) , immersion (with current) , anodizing) D
. 

## Inside dimensions 

## of tank ( 1 

## x w 

## x 

## hi, E
. 

## Actual volume 

## of solution 

## in tank: F. Substrate material: (e. g. , steel, brass, plastic, etc. )


## ( 11 Chicago , Illinois 60623

C h rO IDi !lID

fl.

_ R


### Ha..- d P)atjng

22 

## ft 3 

## ft
22 00 

## gal Stool



### PAGE 72 5 

## ft

# G. Rated capacity 

## of each 

## rectifier:



## H. Average daily sett ing 

## of 

## each rectifier:

I. 

## Hours 

## o f operation:

J. 

## Hours per day e l ectrodes are 

## energized:

K. Ampere - hours 

## per day usage by tank/metal,

L. Bath parameters; 1. 

## 2 . 3. 

## 4. 5
.

l. 

## 2. 3. 

## 4. 5. 

## Volta ge J 

### 2 

## v J? 

## v J 

### 2 

## v v v 

## Voltage 5 V 

### 5 

## v 5 

## v v v



## Maximum 24 

## hrs / day 

## 7 days / wk 52 wks / yr

Maximum
_--=- 2

## 4-=--
__ hr/ day



## Maximum

Chemical 

## Composition Chromic Acid Sulfuric Acid (2 )



## PAGE 73 Amoeraae 1. 5 

## , 000 

## amp 2. 5 

## , 000 

## amp 3 . 5 

### 000 

## amp , 

## 4 . amp 5. 

## amp Amperaoe l. 

### 4 

## , 000 

## amp 2. 4 

## , 000 

## amp 3. 4 

## , 000 

## amp 4. amp 5. 

## amp
Average 22 

## hrs / day 7 

## days / wk



## 52 w ks/yr

Average



## ___**hr/day**



## Average 

## 261 ,000 hr/ day

Concentration



## 30 oz/ga l 0.30 oz/ ga l

## M.

N
. 

## o. Bath defoaming agents and concentrations: 

## Bath cover and thickness; 

## Bath temperature and pH: 

## P. Amount of electroplating chemical 

## used : (e.g., 

## chromic acid, etc.)
Q. Type of ventilation hood: (e.g., onesided, two-sided, 

## canopy I 

## etc.) 

## 3. Emission Control Device: A. Type of control 

## device: (e
. g., mist eliminator, packed scrubber, 

## etc. ) i. 

## Packed: NZi

NIl

J 

### 30 

## ___ D"-"6
____ pH



## Maximum Average**~3~O**

## _______ lb / day ___**~'~''_lb day** 


## Two-Sided

Scrubber i 

### S4 

### Chip Bod Packing PiJter 

## a. packing t¥pe: 

## b
. packing**s~ze:** NA 

## in. in.

B. 

## c. packed height :__ -i6i( D L-
__ 

## ii. Spray 

## a. number of 

## nozzles: b. nozzle pressure: Type of flow: (e.g., cocurrent, countercurrent, crossflow) 

## ------ -Pps ig NA

- Washed down once per week

(3 )



### PAGE 74

### D. 

## Manufacturer, make, and model of control device:
Typical inlet gas temperature: 

## E. Inlet gas f l ow rate: 

## F. Exhaust gas flow rate : 

## G. Gas pressure drop across control device: 

## H
. Scrubbing liquid:**~.** 

## Chemical

ii
. iii. 

## Iv. composition: Flow rate Make-up rate: 

## Source: (e.g. I 

## rinse tank, 7 5 F 

## 4,000 CFM 4 , 000 

## CFM

50 GA:L/WK

Np, 

## gal/min Zin t e 1

Water



## clean water, etc. ),
____ -' C ::.

JLeeaao;n l.....l '<L'aat t ..

e"r '-
___________ _

I. 

### J. 

## v. Is liquid recirculated in scrubber? Efficiency of control device: Identify all plating tanks controlled by 

## this device :



## 4. Exhaust Point Information: A. B. 

## Exhaust exit height above ground level : Exit duct inside 

## diameter: No spent water is put back in Chrome tan k. 

## 97-98 

## A-8

40 

### ft 2 X 2 

### ft
(4)



### PAGE 75

## C. Dimensions of building where 

## duct 

## is located 

## (1 

## x w 

## x h) , 

## 1 7 5 ft 

## 2 0 0 ft 

## 30 ft 

## D. Exit Gas Temperature 70 

## F E. 

## Gas flow rate 

### through 

## exhaust point: 

## 4,000 CFM F. 

## Exit 

## distance from 

## nearest plant 

## boundary: 75 ft 

## G. Dimensions of 

## nearest building to the exhaust 

## point (1 

## x w 

## x h) , ?oo ft 

## 200 ft 

## 30 ft H. 

## Distance of 

## nearest building to 

## exhaust point: 

## 225 ft

I , .



## PAGE 76STATE OF ILLINOIS ENV I RONMENTAL PROTECTION**AG~NCY** OlV IS ION Of AIR POLLUTION CONTROL 2200 CHURCHILL ROAD SPRINGFIELD. IUINOIS 62706

· OATA AND INFORMATION
AIR POLLUTION CONTROL EQUIPMENT Th"
...**~** •• " u ..... .. .......... . 

# .... ,

# ........ .......... . , 

# ............... . . s . .. . ... . "". r; . . .... "'•• s • • " ••**cr~t.** 0 • • , •• , . .. . , • • " 1 •••, ... " •• 

# '. '

# ....... .... ... .. , "'''

# ...... . ... ,

# . .. ,

# ......... .. ., 

# . ..............

• • ,. , . , ... .... . .. .. On" •• • • " ,.

..... . ..... . "
.... . , .. , ". " '.**T~"** 

# ...... "" 

# . ..**~** 

# . .. . ....... " ,**~**

# .... .

.... ........ .**r; .~**  .. ,

'THI S INFORMATION FORM IS FOR AN INDIVIDUAL UN IT OF AIR POLLUTION CONTROL**~aUIPMENT** OR AN AIR POLLUTION CONTRCL SYSTEM.

I. NAME OF OWNER: 

### 2
. NAME OF CORPORATe DIVISION OR PLANT (I F OIFFEitENT FROM OWNER): J. S Ti:E!;T ADDRESS OF CONTiOL ECUIPMENT : 1 "" " 

# '. CITY OF CONTROL EQUIPMENi: 

### CHICAGO 5. NAME OF CONnCL EQU I PMENT OR CONTRCL SYST"..M: 

### SCRUBBER, S4 WITH CHIP BED PACKING FILTER

INSTRUCTIONS 1. COMPLETE T HE AaOVE IDEN TIFICATION. 2. COMPLETE THE APPROPRIATE SECT ION FOR THE UN IT OF CONTROL eCUIPMENT. OR THE APPROPR I ATE SECTIONS FOR THE CONTROL SYSTEM. BE CERTAIN THAT THE ARRANGEMENT OF VARIOUS UNITS IN A CONTROL SYSTEM IS MADE a.EAR IN TH: PROCESS FLOW DIAGitAM. J. COMPlETE PAG;; 6 Of THIS FORM, EMISSION INFORMATION AND fXHAUST PO INT INfORMATION. 4. E FFICI,NCY VALUES SHOULD BE SUPPORTED WITH A DETAILED EXPLANATION OF THE METHOD OF CALCULATION, THE MANNER OF ESTIMATION. OR THE SOURCE OF INFORMATION. REFERENCE TO TH I S FOR M ANY R EL EVANT INFORMATION OR EXPLANATION INCLUDED IN TH I S PERM I T APPliCATION, S. EFFICIENCY VA LUES AND CERTA I N OTHER ITEMS OF INfORMATION ARE TO BE GIVEN FOR AVERAGE AND MAXIMUM OPERATION OF THE SOUR o;**~aU PMENT,**  FOR EXAMPLE. "MAX IMUM EFFICIENCY" IS THE ,FFICIENCY OF THE CONTROL EOUIPMENT WHEN THE SOURCE IS AT MAXIMUM OPERATION. AND "AVERAGE FLOW RATE" I S THE FLOW RATE INTO THE CONTROL EOUIPMENT WHEN THE SOURCE IS AT AVERAGE O PERATION, 6. roR GENERAL INFORMATiON REFER TO "GENERAL INSTRUCiIONS FOR PERM I T**,.l,PPUCATlONS ~,**  APC-201.

DEF INITIONS AVERAGE

- THE V ALUE THAT SUMMARIZES OR**~EPRESENTS** THE GENERAL CONDITiON OF THE EMISSION SOURC: OR THE GENERAL STATE OF PRODUCTION OF thE EMISsION SOURcE. SPEC/FIClLL Y: AVERAGE OPERATION

- OPERATION TYPICAL OF THE ?RECEDING iW'E1.VE MONTH PERIOD. AS REPRESEN TED IIY AVERA GE OPERATING T I ME ANO AVERAGE RATES.**~** 'MUM. THE**G~EATEST** VALUE ATTAINABLE OR ATTAINED FROM THE EMISS ION SOUR CE. OR THE PERIOD OF GREATEST OR UTMOST PRODUCTION 

### Of iRE**EMI~ ON**  SOURCE. SPEC1Flo..lLY: MAXIMUM OPERATION

- THE Gi!.EATEST EXPECTED OPERAT ION, AS Rf?R ESENTED BY MAXIMUM QPEP..A!]NC TIME AND !'AAXIMUM RATES.



### PAGE 77

# . SCRUBBER 1. Ft.OW DIAGRAM OESIGNATION(S) OF ScruBBER: 

### S.!I 2. MANUFACTURER: 3. MODEL NAME AND NUMBER: 10- 

## ZINI'EI TYPE OF saUBBER: 

# L1 HIGH ENERGY: GAS STREAM PRESSURE DROP INCH H2 O 

# 0 PAaED: PACKING TYPE 

### CHIP BED , PACKING SIZE 

## 1" , PACKED HEIGHT 

## 54 IN. 

# 0 SPRAY: NUMBER OF NOZZLES , NOZZLE PRESSURE PSIG 

# 0 OTHER: SPECIFY ATTACH DESCRIPTION AND SKETCH WITH DIMENSIONS 5. TYPE OF FLOW: 

# o COCURRENT 

# 0 COUNTERaJRRENT • 

# 0 CROSSR.OW 

### NA DRY SCRUBBER 6. 

### SCRUBBER GEOMETRY: LENGTH IN DIRECTION OF GAS FLOW 

## 60 IN., CROSS-SECTIONAL AREA 

## 3600 SQUARE IN. 

### 7. CHEMICAl. COMPOSITION OF SCRUBBANT: 

## WATER, SCRUBBERS ARE WASHED OOWN WEEKLY AVERAGE OPERATION OF SOURCE MAXIMUM OPERATION OF SOURCE 8. 

### SCRUBBANT FLOW RATE: 12. SCRUB8ANT FLOW RATE: 

## 50 qal/wk GPM 

## 75 gal/wk GPM 9. 

### GAS FlOW RATE: 13. GAS FLOW RATE: 

## 4000 SCFM 

## 4000 SCFM 10. 

### INLET GAS TEMPERATURE: 

### 1-'. INLET GAS TEMPERATURE:**.~** 

## 70 OJ: 

## 75 11. EFFICJENCY OF SCRUBBER (SEE INSTRUCilON 4): 15. EFFICIENCY OF SCRUBBER(SEE INSTRUCTION 4): 

# 9Z-2a % 

### PARTlCUL4TE % 

### GASEOUS 

## 97 98 % 

### PARTICULATE _%GASEOUS

OTHER TYPE OF CONTROL EQUIPMENT 1. 

### R.OW D1AGRAM DESIGNATION(S) OF "OTHER TYPE" OF CONTROL EQUIPMENT: 

### 2. GENERIC NAME OF "OTHER" EQUIPMENT: 

# 1 J. 

### MANUFACTURER: 

# I 4. Mooa NAME AND NUMBER:. 

### S. DESCltlPTION AND SKETCH, WITH DIMENSIONS AND FLOW RATES, OF "OTHEl" EQUIPMENT:



# .**~** 

### AVERAGE OPERATION OF SOURCE MAXIMUM OPERATION OF SOURCE 

### 6. FLOW RATES: 

### S. Ft.OW·RATES: GPM SCFM GPM SCFM 7. 

### EFFICIENCY OF "OTHER" EQUIPMENT(SEE INSTRUCTION 4): 

### 9. EFFICIENCY OF "OTHER" EQUIPMENT(SEE INSiRUCTION 4): %**~** 

### IL 5J2-0260 

## PAG**~** 

## TJEMISSION INFORMATION I. NUMBER OF IDENTICAL CONTROL UNITS OR CONTROL SYSTEMS (DESCRIBe AS REQUIRED): 

# , . 

# - AVERAGE OPERATION OF SOURCE

### ·C;;T~~T**~** CONCE,,;W.TION 

# OR EMissiON RAnTeR iDeNnCAL - MeTHOD UsEDro DETEiMiNECONCENTRAOON

- CONTROL UNIT OR CONTROL SVS1CM OR EMISSION RATE PARTICULATE 

### 2Q. b. .:. MATTER GR/SCF LS/HR 

## CALCULATIONS BASED ON DATA FROM: CARBON Ja. PPM b. .:. MONOXIDE**(VOL~** La/HR 

## "VENTILATION & 

## AIR POLLUTION CONTROL" NITROGEN 40. PPM 

### b. 

## .:." Mm.'AL FINISHING 

## "GUIDEBOOK 1990 ED. OXIDES (VOL) 

# . LS/HR 

### NEW ORGANIC 

# ISa. PPM 

### b. .:. MATERIAL (VOL) La/HR 

## YORK STATE DEPT. OF ENVIRONMENTAL SULFUR 00. PPM 

# I a. .:.

## ~NSERVATI~OO**~F~!.!!QCESS** SOURa DIOXIDE (VOL) LS/Hit • MANI'to"A llloi":k' OTHER 

# I 70. 

## CHROMIC PPM 

### b. LS/HR 

# I .:. MSDS PROCESS MAKE-UP DATA: POLLUTION (SPECIFY) MTC:'1' (VOL) 

## 0.0065 JI\I"l"KUL to: II**~to"** -WN( 

# ..., MAXIMUM OPERATION OF SOURCE



# --------- --- ---------------- - - 

# --- I CONCENTRATION OR EIv;ISSION RATE PER IDENTICAL 

# I METHOD USED TO DETERMINE CONCENTRATION CONTAMINANT CONTROL UNIT OR CONTROL SYSTEM OR EMISSION RATE ;oARTICULATE 

# I aa. c. .:. MATTER GR/SCF LS/HR 

### ['-ATflIT.A IN:-i**'R1I.~m** ()N T'llI.'1'lI. l<'tIl"lM' CARBON 9a. PPM 

### b. 

# I .:. MONOXIDE (VOL) LB/HR liVEN", 

### .A':'""OP,)N & 

### AIR 'P()T ,T.I IN IN' 'k'{)1 " NITROGEN 

# ., lOa. PPM 

# I b. 

# I .:. OX'''':",\ (VOL) LB/HR 

## Mm.'AL FINISHING GUIDEBOOK 1 990 ED. NEW 

# - ORu"NIC 110. PPM 

### b. 

# I .::. MATERIAL (VOL) LB/HR 

## YORK STATE DEPT. OF ENVmONMENTAL SULFUR 12a. PPM 

### b. 

# I .::. 

## CONSERVATION. HANDBOOK, PROCESS SOURO DIOXIDE (VOL) LB/HR 

## HANDBOOK, 3600: 3700, MANUFACI'URER OTHER 130. 

## CHROMIC PPM b. 

## 0.0081 

# I .::. MSDS PROCESS MAKE-UP DATA: POLLUTION (SPECIFY) .MTS'J' (VOl.) LS/HR 

## CONTROL EQUIPMENT EFFICIENCIES ···OTHER- CONTAMINANT SHOULD BE USED FOR AN AIR CONTAMINANT NOT SPECIFICAl.L Y NAMED ABOVE. POSSIBLE OTHER CONTAMINANTS ARE ASBESTOS, aERYU.IUM, MERCURV, VINYL CHLORIDE, LEAD, ETC.

EXHAUST POINT INFORMATION I. i=LOW DIAGRAM DESIGNATlON(S) OF EXHAUST**POINT~** 

## ES4 ::!. DESCRIPTION OF EXHAUST POINT (LOCATION IN RElATION TO BUIl.DINGS, DIRECTION, HOODING, :rC.): 

## STACK LOCATED 75FT FROM NORTH WALL 3. EXIT HEIGHT ABOVE GRADE: 

# I 4. EXIT DIAMETER: 

## 40 

## 2' X 

## 2' S. GREASTEST HEIGHT OF NEARBY BUILDINGS: 

# I 6. EXIT DISTANCE FROM NEAREST PLANT BOUNDARY: '":In 

### FT 71:; 

### FT AVERAGE OPERATION OF SOURce MAXIMUM OPERATION OF SOURCE**~** I. EXIT GAS TEMPERATURE: 9. EXIT GAS TEMPERATURE: 

## 70 OF 

## 75 Op 

# ,. 

# --

.:-. GAS FLOW RATE THROUGH EACH EXIT: 10 • GAS FLOW RATE THROUGH EACH EXIT: 

### 4000 ACFM 

### A.nnn ACFM


# PAGE 79

# '" o 

# ) Work In/O ut 5100 L B/HR 

# ?(--

Work In/O ut

# -~) 1300 LB/HR 

# ?(-- E xhausted To Sc rubber S8 6,000 CFM 75 F Ex hausted To Scrubber S1 18,000 CFM 75 F 

# ,Ii"' ...

I ,I I " 

# , , , , , ,**~--------- ----** **----------~------------I** ,.. I " I I



# , " 

# , " 

# , " 

# , " 

## R R 

# RR Electr 

# , 

# , , 

# , , , , ng : Chrome Plating Po lish Tank, A-7 <=o_1 

# , , , , r------------------------------------ · 

# , Chrome Plating Tank, A-6 

# R IACid I

# ~ Cle4ner C1 C2



## - rRuici;

- ---------------------------------------

t OC

--t1 1)l1


### S<'!LI . . . sc _m l( C O W

P.tl IAIIS . u; JIS! sru UI r. 0I.1 1 A\lt lL{ 

### cuoco. t 60611STATE OF ILLINOIS ENVIRONM£ NTAL PROnCTlON AGENCY DIVISION OF AIR POLLUTION CONTROL 1200 CHURCHill ROAD SPR INGFI(lD, ItLlN O IS 62706

" QATA. A.ND INFORMATION 'Rocess EMISS ION SOURCE

' THIS INFOltMAl lON FOItM IS TO BE CQMI'lE'HD FOR AN EM IHION**SOUR~ [**  OTH E R THAN A FUEt COMaUST10N EMISS ION SOURCE 

### at A N INCINERA TOR
. A FUEL COMeUSTlON EMISSION SOUII:CE IS A FURNACE, SO ltH.**O~** SIMILAR EQU IPM!Nl USEO PWMR ll Y FOR P1I:ODUCING HEAl eR**PCWE~** 3 Y INOIHCT HEAT rRANSFfR. AN INCINERAT OR IS AN**AP~A"AruS** IN WHICH RHUH IS BURNED
. 

### " NAME OF nANT OWNER: 

# " NAME OF COR PORATE DIVI SION OR**P'~ANT** (IF**DIFFER~NT** fROM Em pire Hard Chrome OWNER), Empire Hard Ch r ome 

# " SUEEr ADDRess OF**~MISSION** SOURCE : 

# co:., V'**"~""VN** >vv.co, 

### 1615 S. Kostner Chicago

G(NEkAtINfO RMA TI ON 

# " NAME d'F PROCESS : 6, NAMf OF EMISSIO N saute! EQUIPMENT: Har Chromium Plati ng Chrome Plating Tank



## , 

# . EMISS ION SCUlC[ EOUIFMENT MANUFACTURER: 

# ., MOOEL NUMBER, 

# I 9, HRIAl**NU M~E** **:** 

# - 

# - - 

# "" FLOW O[ACAAM OlS I GNATlON(S } OF {M ISS ION 50UilCb 

### A- S 

# ,,, IDENTITYISI OF ANY SIMILAR SQURCE ( »AT THE PLANI O R HEM ISB NOT COVOI(O BY THE fORM (IF THE**SOURC~** IS COveRlO BY**~NOTHER "'~ICA** **TIO N,**  IDENTIfY**TH~** APPLICATI ON I : 

### NA 

# ".**~VE~~** OPERATING**T1~** OF EMISSION**SOU~:** 

### OJ.**MA~~UM** OPERATING flME Of [MISUON S'!H!CE : HRS/ DAY DAYSIWK 

### w"SM HtS/DAY DAYS/WIC Wt:S/YR 

### u, .:"ERCENT OF**ANNU~THROUGHPur :**  

## 25 25 25 DEC -fEB 'lIo MAR-MAY 

# " JUN-.l.UC 

# " SEPT_NOV 

# "

IN SaUCTIONS 1
. COMPUTE 'HE ABOVE IDENTIFICATION AND GEN ERAl INFORMATION SECTION
. 2. COMPLETE THE RAW MATERIAL, PRODUCT. WASH MAnR1AL. AND FUEl USAG! HCTIOM FOR THE PAR TI CULAR**SCU~C[ EOU** **~M ENT.**  COMPOSITIONS OF MATHjAlS MU ST**S~** SUffICl£N TL Y tlHAILED TO ALLOW DElERMINAHON OF THE NATURE AI"O QUANTITY OF POTENliAL E MI SS IONS. I N PARTICULAR, THE COMPOSITION Of PAINTS, INKS, ETC •• AND ANY SOL VENTS MUS; Bf FU LL Y DETAILED. 3. EMISSION ANO EXHAUST ;OIN I INfO,U..\.ATlON ,.,..uST BE COM
.... UtO. Uf'.A.ESS EMISSIONS ARE EXHA USTED THROUGH AIR POLLU TION CONUO\.. ECUIPMENT,

.... OPERATING TIME AND CERTAIN OTHH JrEMS REOUIRE 8 0TH AVERAGE ANO MAXIMUM VALUES. S. FOI GENEW INFOR M MION 

### R EFER TO**~GENtRAL** 

### INs HucnoN ) fOR PERMlr APPL ICATIONS. " APC- ZOI,

OEFINITIONS AVERAGE
_ ,HE VALUE THAT**SU MMA~lZH**  CI REPRESENTS HIE**mN~RAl** CONDIT ION OF THE [ MI SS IO N SOURCE, 01**~** GENEML SlATE OF 'ReOUCTlON 01 i HE tMIB ION 

### sow!:£.**~fECIFltAll** Y: AVERAGE OPERA TING TIME
_ ACTUAL TOTAL HOURS OF O I'UAtlON FOR THE**P~EC~01NG** TWELVE MONTH PUIOD
. AVERAGE**RAr~** _ ACTUAL IO T A\.. OUANTITY OF "MATEl IAl' fOt THE PRECED ING**iWn.V~** MONTH PERIOD, DIVIDeD BY TH[ AVERAGE O,EIl.ATING TIME.**AVfRAG~** CPEP.ATlON

- OPERATION TYPICAl. OF THE l'i tfCfDlNG T WEL VE MONTH PER IOD.**A~** RHRE5ENHO 

# ,y AVHACE OPEkA Ti NG 11 ,..'£ ANDAVERAGf tATES.. MAXIMUM

- THE lj!lfAHU VA.LUE !!,l OR**~ ~** **HO~ ~~E**  EMISSION**SOUIC~ ,**  O. THE P[R IOD OF GREATEST OK UTMOST PRODUCTION CF 'HIE I MAXI.v.uM O,e:u.TING 11M(
_ CiREATEST EXPECTED T orAL HO UIS OF OPE lA TIONS fOR ANY TWE\.VE MON TH PERIOD. MAX I.v.tJ M P.ATE
_ GIU
.... IOT QUANTITY Of "MATH IAL" EXI'fClrO PEl
.... NY ONE HOU R OF OPERATION. MAXIMUM OHRAIION

- GREATHT EXPEC1ED OPERATlOr>:, AS iiEPREHNHO 8Y
.."",XI MUM OPfRAtrNCi TI ME ANO MAXIMUM RA,ES, APc-no (REVISED 

### 1/17m) 

## PAGE 81 PAGE 1 OF J

# t 'lAW MARRIAL INFORMATION AVERAGE RATE MAXIMUM RATE NAoMI: OF RAW MATERiAl PElt IDENTICAl SOURCE PER IDENTICAL SOURCE



# . Plated Metal Parts b, 

### 1300 c, 

### 2600 U/HR LB/HR 21a. 

### Chromic Acid b, 

### 0.602 c, 

### 1.20 LB/HIl U/HR 22a. 

### Sulfuric Acid b, 

### 0.018 c, 

### 0.036 LB/HR LB/HR 23ca. 

### Water b. 

## 44 c. 

### 44 LB/HR LB/Hl 204G, b. c. LB/HR LB/HR

PRODUCT INFORNATION AVERAGE RATE MAXIMUM RATE NAME OF PRODUCT PER IDENTICAL SOURCE PtR IDENTICAL SOUKCE :lOa. 

### Chrome Plated Metal Parts b. 

### 1300 c, 

### 2600 LB/HR LB/HR 3la. b. c, LB/HR LB/HIt 

### 320. b, c. LB/HR LB/HR 33a. 

### b. c. LB/HR LB/HR 3010. b. c. LI/HR LB/HR

WASTE MATERIAL INFORMATION AVERAGE RATE MAXIMUM RATE NAME OF WASTE MATERIAL PER IDENTICb.L SOURCE PER IDENTICAL !>OURCE 400, 

### NA b, c. I.B/HR LB/HR 410. b. c. LB/HR L8/HR 420, b.· c. L8/HR L8/HR 430. 

### h. c. U/HR L8/HR 

### .4.40. 

### b. c, L8/HR LB/HR

·FUEL USAGE INFORMAtiON FUel USED TYPE HEAT CONTENT 

### 50a.**N"'TU~** GAS 

## D b, c, 1000 BTU/SCF 

# . - 

# .- 

# . 0 OTHER GAS**aTU~~** 

# 0 

# -. --- 

# ----- ----.- OIL


# --- --- -------_ ...**II!YL~** COAL 

# 0 BTU,.,.. OTHER 

# 0 IlTUAB IERAGE fiRING RATE PER IDENTICAL SOURa: 

# Ie. MAXIMUM FIRING RATE PElllDENTlCAL SOURCE: BTU!HR BTU/HR ·THIS SEatON IS TO BE COMPlETCO FOil ANV FUEL USED DIRECTLY IN THE PRO

## ass EMISSION SOURCE, E,G. GAS IN A DRYER, OR COAL IN A M£L

### TFURNACE.
APC-22D 

# PAGE 82 PAGE 2 OF J"EMISSION INFORMATION 51. NUMBEIOF IDENTICAL SOUlCES (DESCRIBr: AS REQUIKED): 

### 1 AVERAGE Of'fRATION



# . 

# '.---- - 

# --------------------- ------------------------- CONTAMINANT CONCENTAATION OR EMISSION RATE PER IDENTICAL METHOD USED TO DETERMINE CONCENTRATION OR

. SOURCE

- EMISSION RAn: 

### 520. Ia. 1;. •AlTJCULATE 

### MYTER GK/SCF LB/HR 

### Emission rates based on data from "Ventilation :ARSON ",ONOXIDE ""IOGEN 'XIDES 'ROANrc MIElIAI. iUlFUR >lOXIDE 'OTHER 'SPEOFy) S3a. 5040.**~.** 

### S6G. S7a. PPM ('lOLl PPM (VOLl PPM (VOL} PPM (VOLl 

### PPM NOL) e. 

### & Air Pollution Control", Metal Finishing Guide b. LB/HR e, 

### Book, 1990 Ed., New York State Dept. of b. LB/HR 

### b. 1;. L6/HR 

### Environmental Conservation- Handbook, b. c. U/'HR 

### 3600-3700, and Process Make-up Data. b. c. la/HR



## _ _ _ _ _ _ _____________**y~.!.M~~ ~~A!!O~**  ______________________ _ CONCENTRATION OR EMISSION RATE PER IDENTICAL METHOD USED TO DETERMINE CONCfNTRATION OR CONTAMINANT SOURCE EMISSION II"'TE 'ARTlCULATl: 'AAmR S8a. GR/SCF b. c. 

### Emission rates based on data from ''Ventilation LP/HR :ARION t,\ONOXIDE 

### 590. PPM IVO\.) 

### b. c. 

### &Air Pollution Control", Metal Finishing Guide**~ITROGEN :JXl~S**  ORGANIC 'MTERIAl

., OTHER ISPECIFY) 61a. 

### 620. 63a. 

### PPM (VOL) PPM (VOL) b. 

### b.
PPM b. rVOLl PPM b • IVOL) LB/HR c. 

### Book, 1990 Ed., New York State Dept. of tD/HR 

### LOIHR c. 

### Environmental Conservation- Handbook,
lB/HR c. 

### 3600-3700, and Process Make-up Data.
c. LB/HR • ITEMS 52 THROUGH 6:J NEED NOT 8E COMPlETED IF EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONTROL EQUIPMENT, ·-OTHER- CONTAMINANT SHOll.D 8E USED foa AN Alit CONTAMINANT NOT SPECIFICALLY NAMED ABOVE. POSSIBU OntER CONTAMINANTS

ARE ASBESTOS, !ER'tl.LlUM, MEROJRY, VINYl. CHLORIDE, LEAD, ETC.

••.. EXHAUST POINT INFORMATION 64, FLOW DIAGRAM DESIGNATlON(S) OF eXHAUST POINT: 

### Exhausted to Scrubber S1 65. DESCRIPTION OF EXHAUST POINT !LOCATION IN RelATION TO BUILDINGS, DIRfCTION. HOODING, ETC.): 

### 66. EXIT HEIGHT ABOVE GRADE: 

### 67. EX 

### IT DIAMETeR: 

### 68. GREATEST HEIGHT OF NEARBY aUILD1NGS: 69. EXIT DISTANCE FROM NEAREST PLANT BOUNDARY:

, FT FT



# - AVERAGE OPERATION MAXIMUM OPERATION 

### 70. EXIT GAS TEMPERATURE: 

### .72. EXIT GAS TEMPERATURE: Of Of 71. GAS FLOW RATE THROUGH eACH EXIT: 

### 73. GAS F\.OW RATE THROUGH EACH EACH [XlT: ACFM ACFM 

# .... THIS SECTION SHOULD NOT BE COMPlEUD IF EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION CONnOI. EQUIPMENT.



## PAGE 83 P"OE 3 OF 3