, , 

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 

!lllP Jl)£ lJililD CiJ llDIJ] !, 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 

Mr. Joydeb Majumder Ool·~CD·tLlQ . 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, ~ . 

s~ .. " . in 

~U 

SW:d Vice-President 
STATE OF ILLINOIS 

ENVIRONMENTAL PROTECTION AGENCY 

DIVISION OF AIR POLLUTION CONTROL 

2200 CHURCHILL ROAD 

SPRINGFIELD, ILLI NOIS 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. ZIP 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 cORREsPoNDENC1 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 

DESIGNATION WILL BE REFERENCED IN CORRESPONDENCE FROM THIS AGENCY RELATIVE TO THIS APPLICATlON. YOUR DESIGNATION MUST NOT 

EXCEED TEN (10) CHARACTERS. 

J) THIS APPLICATlON MUST BE SIGNED IN 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 EOUIPMENT. 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 1 
9. 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 
CERTIFICA nON 

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: 

Tank 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 10000 0.216 0.946 

A-6 15000 0.324 1.419 

A-7 15000 0.324 1.419 

A-8 15000 0.324 1.419 

B-1 59000 1.274 5.582 

8-2 11500 0.248 1.088 

8-34 2500 0.054 0.237 

8-5 500 0.011 0.047 

8-6 2500 0.054 0.237 

8-7 30000 0.648 2.838 

Total 3.629 15.894 

Chrome Emissions (LB/HR) = Max Amps a 0.0000216 LBIHR"AMP 

Chrome Emissions PTE (TPY) = Emissions (LBIHR) a 8760 (HRfYR) 

Actual Chrome Emissions = Chrome Emissions a 0.025 

PAGES 

Actual Chrome Emissions (TPY) 

After Scrubber 

0.009 

0.011 

0.028 

0.043 

0.043 

0.043 

0.167 

0.033 

0.007 

0.001 

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 

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Df4bnAM 1II!11t1IM:m RJV AY nm 

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Exhaust EBOIL-1 

100 CFM 

130 F 

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Boiler 

BOIL-1 

Firing Rate 

1.674 Million BTU/HR 

PROllCI 

IOCAIKll 

1111( 

I i:MPIRE. 

Belli:· 'O!:. 

-~ SCIllIlI1 ( COIIIROI ~ lABS. INC. 

1I58SUl ,III ~OIDI AV[t1lJ[ 

C'IlCACO . Il 60621 

{-\AeO C1-1 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*--

of tfIia infonnallon II required undIr IftaS..:llDil. faiIIn to do .,...., 

~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::A TION 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: 

106 " 17. MAXIMUM FIRING RA~: 

1.674 x BTU/HR 1L 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 undIr1lwt Section. F .... IO do 10,.,., 

jlIfteftt UIIa form from being pra 11II ~ end could .... In V-

. eppIk:adan '-ing ..... ThIa form ilia t..'Iapprawd by.the FGan. 

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: 

A VERAGE 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. mciFICAU Y: 

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: 106 BTU/HR _1 ji.'Z~L.x. _1 a7 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. 0 D.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 

LOCAl 011 '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.utln yaur . I1IPicaIian IMing cMnied. T1ia form lID bllnlAl'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: 

DEC-FEB 50 % MAR-MAY ·1n :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: 

A VERAGE 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 TWa VE 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 SUPPL V: 

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 . :' -.~~.: .. ~ •.. ;;'II:'~'~~.~~ ~~~t-ff..r~C , .. ~.~~!~~;~ .. :~ '.~; ~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 PIUMARIL V 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: 1 9 •. 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.ICA TION): 

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 CALL V: 

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. cLB/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. cLI/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 OPERA nON 

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, !lPECIFICALL Y: 

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 SPEctFlCALL Y 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. ADSORBA TE(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 AL TERNA '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 OPERA nON 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. CATAL YST USED: 

0 NO 0 YES: DESCRIBE CATALYST 

10. HEA T EXCHANGER USED: 

, NO o YES: DESCRIBE HEAT EXCHANGER IAVERAGE 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 V ERAGE 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: 14

• 

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 I B. 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. FIL TERING 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: 

TEMPERA TURE 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 :.~~~::~ ::r , PACKED HEIGHT IN. . , 

. 

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:' "'lll 
EMISSION 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" ___ ) 

, 

Exhausted To 

Scrubber S3 

6000 CFM 

75 F 

-'''''';------------------1 

~._'O' __ ~~? I~ ~-_ R-D~-C- (Q~O~~~~------1 hili (' II'JC'fW;: ?L.Io.."nI t,... TtlC.., Ie S 

1<&1 'iWIIf( 

H5a ll

COlliN 

n "III --0\

•• 

'11101 

95. 'I: I --2£19. o;mjj . r l-"'--I-~ ________ "--I IQ..tfC " _ 

CU(Al.O. l to(,]) 
ISTATE C F ILLINOIS 

ENViRONMENTAL '''OlIOION AGENCY 

DiVIS ION OF AI~ POLLUTION CCNTRCl 

1200 CHURCHILL ROAD 

SPRiNGflUD, IUINOIS &2706 

"OATA AND INFORMATION 

/ROCESS EMISSICN SOURCE 

'THIS INFOIlMATiON FOilM IS ;0 SE COMf'l fl'fO FOR AN E.'.IISSION SOU~C[ O IHU THAN A ~UEl COM!USTION EMISS ION SOU ~CE O R .... N 

INC1NEitA TOl. A fUEL COM!USTION EMISSION SCURCE IS A FUINAct, 'aOIl.ER, OR SIMILAR ECU IPMENT USED PlI.l MARll Y FOR ~OOU NG 

HEAT OR I'OW~ ~y INOIUCT HEAr TRA NSFER. AN INCINERATOR IS AN .... P~.4RAfUS IN WHICH REFUSE IS BURNED. 

" 

N AME Of i'LA Ni O WNER: " NAME OF CORPORArf DIVISION CR p'~ANr (IF FFE ~NT FROM 

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,lINFOIMATION 

" NA ME ifF '~OCES , 6, NAME Of MISSi N SOURCl: f CU IPM[NT: 

Ha r Chromium Plating Chrome Plating Tank 

7, EMISS ION SOURCE eaU IPMENT MANUF ..... CTURER, s, MODEL NUhI.DU, I " HRlAl NU ~E!: 

- - - FLOW DIAGRAM OESIGNATlON(S) OF ( MISSION SOURCE, 

A-123 

n , IDENTITY!S) OF ANY SIMil AR SOURCE (S) AT THE PlA N T 01 PUMISES NOT eOVfKEO ~Y THE f ORM !If THE SOURCE IS CCVtREO BY ANOTHER 

Af'P\. ICArlON, IDENTIFY IHE API'lICATIONI: NA 

02, AVE~Gj OPERATING nl-'ff CF EMISSION SQU~Cf' OJ . . ..v..~1fW M CPERATlNGj' ME OF EMISSION S~CE' 

HRS!OA Y OA YS/WK WK.S/Yl! HRS/ OAY OAYS/WK WKSIYR 

u, i"ERCENT OJ' AN NU~iHROUGH : 25 25 25 oEc.;:n ~ MAil_MAY " JUN-..I.UG ,. SEPT-NOV " 

INStRUCTlCNS 

I . COMPlETE tHE .... 80VE IO{NTlFI(AfiON AND GENEAAl INFORMATION SECT ION. 

2. COMPLfTf!HE RAW MAIE~ , PRODUCT. WASTE MATUIAl. ANO FUEL USAGE SECTIONS fOR THE 'ARTICULAR SCURe:- ;::OUT'ME NT. 

COMPOSITIONS O F MA1BMLS MUST BE SUfFICIENTlY OETAILED TO )'lLOW OET ERMINAi"lON O f THE NAruRE AND QUANT ITY OF POTENTIAl 

EMISSIONS. IN PARTlCJl..PoR, THE COMPOSITI ON OF PA INTS, INKS. ETC •• AND ANY SOt 'IENTS MUSi ~~ fULLY DfTAILEO . 

l. EMISSION AN O EXHAUST .'011'11 INFORMAi lON MUST ~E COMPUTED. UNL ESS EMiSSION~ ARt. EXHAUSTED TH ROOGH AlII" PCLLUTION 

CON UOl EC UIPMENr. 

~. OPERATING TIME .1.1'10 ceUAIN THE~ IHMS UOUIR E eorH AVUACc "'NO MAXIMUM VALUES. 

s. FOI GENERAL INFORMATION REFER ro " '.:i;:NERAl I'I~ UC loN ) rOR PERMU APPLICATIONS.' APC- 20I . 

DEfiNITIONS 

AVERAGE · THE VALUE THAT SUMMARIZES 01 Of THE EMI SSION SOURCr. OR THE GENElJo,l HATE Of 

,II:OOUCIION OF IHE MI~SION I 

AVERAGE O PERAT ING TIME - ACTUAL TOTAL HOURS OF OPERA TION FOI WE PREC!:OING TWELVE MONTH I'fRIOO. 

AVERAGE RArE - ACTUAL 10TAl aUANTITY O F "MA TUIAl" FOR HIE PRECEDING TWELVE MONTH PEitlOO, DIVIDeD iJY THE AVERAGE 

OP~RAi1NG TIME. 

AVERAGe- CPEI'.ATION. OPERATION rYPIC).L O F THf i'.UCE 01NG TWelVE MONTH PERIOD. AS lIEPIIESENHD!Y AV!.RAGE O PERAT ING TI.v.f 

AND AVERAGf .U fES. 

MAXIMUM· THE G8EAl[U VALUE 

P~ODUCTION OF TIlE TC)UI~:-"\iit.i: ,;: 'll Tl':lE EMI SS ION SOURC:. OR THE PER IO D Of GilEATCST OR UTMOST 

MAXIMUM ; " ~HA"NC TJM( _ GlIEATESi EXPECTED TOTAL HOUtS OF OPERATIONS FOR ANY TWEl VE MON TH HRIOD. 

MAXIMUM RATE - <:; .. e.4I(H aUA NTlTY Of "MA TERIAL " €)(I"ECHO ~u ANY ONE HOUR Of O PUATI ON. 

MA XIMUM O PHATION " GaEAIEH eXPEClED OPfRA HOI'I. A~ EnEHNno SY !MXIMUM OPERA liNG TIME. AND M:t.XIMUM RA7ES . 

............ .., ...... 
'. 

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 INFORMA nON 

AVERAGE RATE MAXIMUM itA TE 

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 520. b. 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 

'ARTICULA TE 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. :lXIDlS Book, 1990 Ed., New York State Dept. of (VOl) LD/HR 

::>RGANIC 610. PPM b. c. Environmental ConselVation- Handbook, 1MT' . '. (VOL) LB/HR -

iULFU .. 620. PPM b. c. 

OIOXIOE 3600-3700, and Process Make-up Data. (VOL I LB/J{R 

'OTHER 63a. PPM b. 1:. 

iSPECIFy) (VOL I 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. Corpora t 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 Sourc e : __ --1'.i6c:'tcS5-SS_.JK,;:,ooss.tt..IUUe"rC-a""":se,,UlllJJ' p'-___ _ 

D. Name and Phone Number of 

Respondent: 

2. Electroolatina 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 ating 

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 each rec tifier: 

I. Hours o f operation: 

J. Hours per day 

electrodes are 

energized : 

K. Ampere-hours 

per day usage 

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 wks/yr 

p.veraoe 

____ 2222 ____ hr/day 

Averaae 

52 ,8 00 hr/ day 

Concentration 

3 0 oz/gal 

0.3 oz/gal 
M. 

N . 

o. 

Bath defoaming agents 

and concentrati ons : 

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 

ho 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 

Two -Sided 

b. packing size: 1 in. 

c. packed height :_---'4"'2'---__ in. 

ii. Spray 

a. numbe r of 

nozzles: 

b. nozzle 

pressure: - ____ --Pps ig 

__ ..1J......!~ ___ pH 

Average 

__ 4~4'- lb day 

B . Type of flow : 

(e.g., coeurrent, 

countercurrent, 

crossflow) 

NA - ~'lashed down 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, 

cl ean wa t e r , etc.) ____ -"c.:.'we..aa.Ilo'-'""'aa.tI:..ee"'r-___________ _ 

I. 

J. 

v. Is liquid 

recirculated in 

scrubber? 

Efficiency of control 

device : 

Identify all plating 

tanks controlled 

by this devi ce : 

4 . Exhaust Point Informacion: 

A. 

B. 

Exhaust exit height 

above ground level: 

Exit duct inside 

diameter : 

NO - 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. Dimensions 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 ft 
STATE OF ILLINO IS 

ENVIRONMEN TAL HOUCT rO N AC ENCY 

DIVISION OF AlA I'OLl UTI O N CONTROL 

2200 CHU~ CH L ROAO 

SPRINC FIElO, ILLI NO IS 61706 

°OA TA AN D INFORMATION 

,IlOCESS EMISSIO N SOURCE 

'IHls INFOlMAfiON FORM IS TO 9E COMPlETEO fOR AN EMISSION SOURCE o rHER THAN A ~UH COMaUSTiON EMI SSIO N SOURCE O~"' N 

IMCI Meu,TOK, A fUEL COMWSTlCN EMISSION SCUI!G IS A FU.NACE, 'aon..EI. O R SIMILAR EQUIPMEN T USEO i'RI M,ARIl Y FOIt n.ODUC ING 

HEAT OR i"OW~ lY INOIUCT HEAT TRANSFER, AN INCINERATOR IS AM .... ,.,.AlATUS IN WHICH REfUS E IS aURNEO. 

, . NAME OF i'lA N T OW Nfl: 1. NAME OF CORr OItATE DIVISION CR P\.ANT (IF OIFFERlN f ROM 

Empire Ha rd Chrome OWNO I: Empire H a rd Ch rome 

,. HUH ADDUS; OF EMISSION SOURCE: '. L , , , , 1615 S . Kastner Chicago 

GE NERAL INfOU.V. TIO N 

>. NAME OF P~OCESS , ,. NAME Of EMISSION SOURa !CUIPMENT, 

Hard Chromium Plating Chrome Plating T ank 

7. [MISS ION SOUICE ~aU PMENT M .... NUFACruREIt, •• MODEL NUMJlER, I •• HRlAl NUMU:~, 

- - -

flOW OIACitAM OESIGNATlON(S) O F EMISS ION SOURCE: 

A4 

". IDHHITYISIOf ANY SI MILAR SCURCE(s)AT THE Pl .... N T OR H EMlS£5 NO T COV{RED ny HiE fOR M (If THE SOURCE IS COVERED OY oloNOTHER 

Ai'i'lICATION, IDENTIfY THE APf>lIC,\TlON I: NA 

I'. oloVE~~ OPfIlAONC wg OF ~MISSIO N SCUg=j: 

". • ......,.~f'UM Cf'ERA TIN G flME OF EMISSLON ~~Cf.: 

HIiS/ OA Y OA YS/WK WKSI'YR HitS/DAY OAYStWK WKS/YR 

". ?ERC£N T OF ANN ~THItOUGHPUT' 25 25 25 DEC. F£II % MAR_MAY " JUN_we •• SEPT-NOV " 

IN SilUClIONS 

I . COMI'LEU THE .. eov£ 10ENTlflCMlO N ANO GENERAL INfORMArION SECTION. 

2, COMftEH THE RAW MAlEalAL, PROQUCT. WASH MA TE RIAL. "NO Fun uSAGE SECTIONS FOR THE PAUICULAIi SCURC; EOUIPMENT. 

COMPOS ITI ONS OF MA1HIALS MUST BE SU~ rCIEN n Y DHAllEO fO ALLOW DETERMINAtiON O F THE NAru~E AND CUANTITY OF POTENTIAL 

EMISSIONS. IN PARTICULAR, iHE COMPOSITION Of PAINTS, INICS, ETC., ,\NO ANY SOL VENTS MUS; liE FULLY D£1"AIUD. 

J , EMISSION AND EXHAUST POIN T INFORJ.v.ilON MUST ~E COMI\HtO, UNlESS EMISSIONS ARE f)(HA USTEO THROOGH AIR PCLLUTION 

CONTROL ECUIPMe,...r , 

~. O PERATING TIME ANa CERTAIN O THH ITEMS 

S, Fm GENEML INFORMATION REFER TO ~GE 

AND MAXIMUM VALues, 

PERMi t APPUCATIONS.· APC-ZOI , 

DE FINITION S 

AVEIlAGE - 'HE VAlue THAT SUMMAR IZES Cl REPRESEN TS THE GENE1I.AL COND ITION Of TIlE EMISSION SOURCE, OR THE C ENERAL STArE OF 

PRODUCTiON Of IHE t MIB ION SOURC E. ECI CALL Y: 

AVERAGE OPERATING TIME - .... CTUAL TO TAL HOURS OF OI'EItA HON FOR HIE PReC~OI C TWELVE MONTH PERIOD. 

AVERAGE RATE • ACTUAL TOTAL QUAN TI TY OF "MATUIAt· fOIt THE PRECEDING lWEl'lE MON TH PERIOD, OIVIOEO ay THE AVERAGE 

OPE~il NC liME. 

AVERAGf CPtRATION " OPUATION TYPIC).l OF THE i'.:teC:OING TWIl VE MONTH HRIOD. AS UPRESENH O 3Y AV£i'.AGE Oi'ElATlNG TIME 

AND AVERAGe UTES, 

MAX IMUM. iHE 011[,,1[51 VAlUE AH AINA!L: OR AnololNED FROM THE EMIS,ION SOURCE, Ot THE PERIO D Of CREATeST OR UTMOST 

PRODUCTIO N OF TltE N ~o cL 5PECIi'ICAlL Y: 

MAX IMU M QrfilATING TIME _ ~A ST EXPECTEO TOTAL HOURS OF O PERA TIONS FO~ ANY TWn v E MONT H PERIO~ . 

MAX IMUM RA TE - v~e ... TE.ST OUANTITY OF ·'MATERIAL· EXPECHD PEl ANY ONE HOUR OF OPERATION, 

MAX IMUM opeRATIOM " GaEATEH EXPEClEO OPE RATION. AS UP~HENH:O 3Y .'N\.XIMUM OHRA TIN G TIME AND M:t,XIMUM itAiES . 

PAGE 4S 
RAW MAR RIAL 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 J 
4!MISSION INFORIMTION 

51. HUMlEl Of IDENTICAL SOUICES (DESOU8£ AS UQUJREDh 

1 - AVOAGE OPERATION -~- ---- - - ---------- --- ---- - --------------------------- CONTAMINANT CONCENTRATION OR EMISSION ItA TE PER IDENTICAL MaHOD USED TO DETERMINE CONCENTRATION OR . SOURCE - EMISSION RATE 

I AlnCULATE 520. b. 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. 

JXIDES Book, 1990 Ed., New York State Dept. of (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 SOURCE EMISSION RA1'£ 

'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£RA lURE: 

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 Plan t Name; __ -,O"mlllf'pcl;.lr:<e,-HIia • ..tr:cdU C:::J:lbJ:r:COlllm"e'-_______ _ 

c. Addre s s 0 f Emi s sion Source : __ -1J..E6;':JL'53-SS_.lKuO:lSs.ttJ:0lfe"r=-A!Wu:eeu:puJ,.,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 material : 

(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 

each rectifier: 

H . Average daily setting 

of each rectifi er : 

I. Hours of operation: 

J . Hours per day 

electrodes are 

energized: 

K. Ampere-hours 

per day usage 

by tank/ metal : 

L. Bath parameters: 

Voltag 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 

Maximum 

96 000 hr!day 

Chemical 

Composition 

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 wks / 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 de foaming 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 elimi 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 Packing 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, 

countercu rrent, 

crossflow) 

-----------Pps ig 

NA - Washed down once per ' .... eek 

( 3 ) 
C. 

D. 

Manufacturer, make, 

and model of contr ol 

device : 

Typical inlet gas 

temperature: 

E. Inlet gas flow r ate: 

F. Exhaust gas flow rate : 

G . Gas pressure drop 

across cont rol 

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 

'15 Gti I. /t'IR 

Nil. gal/min 

D JJa)) 

Nat c .... 

clean wa t e r , et c . ) ____ ...Lc:.J'-'e".3.oc....-"wu.ur"ee.J:r'-___________ _ 

I. 

J. 

v. Is liquid 

recirculated in 

scrubber? 

Efficiency of control 

device: 

Identify all plati ng 

tanks cont rolled 

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. Gas flow rate through 

exhaust point: 6,000 CFM 

F. Exit distance from 

nearest plant 

boundary: 7< ft 

G. Dimensions of nearest 

building to the 

exhaust point 

(1 x w x h ) , 200 ft 200 f t 3 0 ft 

H. Distance o f nearest 

bu ilding to exhaust 

po int: 200 ft 

, 

PAGE 52 
STArE OF ILLINOIS 

ENVIRONMENTAL PROTECTION AGENCY 

DIVISION OF AIR POLLUTION CONTROL 

2200 CHURCHILL ROAD 

SPRINGFIELD, ILLI NOIS 62706 

'DATA AND INFORMATION 

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 eQUIPMENT OR CONTROL SYSTEM: 

SCRUBBER, S3 IVITH OlIP BED PACKING FILTER 

INSTRUCTIONS 

I, COMPlETE THE AaOVE IDENTIFICATION. 

2. COMPlETE THE APPROPRIATE SECTION FOR THE UNIT OF CONTROL EQUIPMENT. OR THE APPROPRIATE SECTIONS FOR THE CONTROL 

SYSTEM. SE CERTAIN THAT THE ARRANGEMENT OF VARIOUS UNITS IN A CONUOl SYSTEM IS oYoADE a.EAR IN THE PROCESS FLOW DIAGRAM. 

J . COMPlETE PAGE 6 OF THIS FORM, EMISSION INFORMATION AND EXHAUST PO INT INFORMATION. 

4.. EFFICIENCY VALUES SHOULD BE SUPPORTED WITH A DETAILED EXPLANATION OF THE METHOD OF CALCULATION. THE MANNER OF 

ESTIMATION, OR THE SCU~CE OF INFORMATiON. ~EFERENCE TO THIS FORM ANY ~ELEVANT INFORMATION O~ EXPLANATiON INO-UDED 

IN THIS PERMIT APPliCATION . 

5. EFFICIENCY VALUES AND 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 CONTROL eOUIPMENT WHEN THE SOU~ CE IS 

AT MAXIMUM OPERAT ION, AND "AVERAGE flOW RATE" IS THE FLOW RATE INTO THE CONTROL EQU IPMENT WHEN THE SOURCE IS AT 

AVERAGE OPERATION. 

6, FOR G~NERAL INFORMATION REFER TO "GENERAL INSTRUCTIONS FOR PERMIT APPliCATiONS", APC- 201. 

DEFINITIONS 

AVERAm - THE VALUE THAT SUMMAR IZES OR ~EPRESENTS THE GENERAL CONDiTION OF iHE EMISSION SOURC;: OR iHE GENERAL STATE OF 

PRODUCTION OF THE EM ISSION SOU~cE. SPEClF!CALL y, 

AVERAGE OPERATION - OPERATION TYPICAL OF THE PRECEDING TWELVE MONTH PERIOD, AS REPRESENTED BY AVERAGE OPERATING TIME AND 

AVERAGE RATES. 

'!MUM - THE OR ATTAINED FROM THE EMISSION SOURCE, OR THE PERIOD OF GREATEST OR UTMOST PROOUCI (I SPECIFICALLY: 

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: 

75 gal/wk GPM 110 gal/wk 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 54 
EMISSION 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 WE PER 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".A LCUr.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\JiPfl2-£ --- 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 ATINI- "'~ S' 

~h= --~ l-iJ~1'C 
STATE Of ILLIN OIS 

ENVIRONMENTAL P"-OTECTION AGENCY 

DIVISION OF All. I'OlLUTlON CCNTkCl 

1200 HU~CH lL kOAD 

S'~ NGFIElO, ILLI NOIS 62706 

'CATA AN D INFORMATION 

fROCESS EMISSION SOURCE 

' THIS INFOItMA IION FORM IS TO !IE COMI'UtED f OR AN EM ~SrON SCUItC[ O THER THAN A ~UH COMBUSTION EMI SSIO N SOUItCE OJ: AN 

INcrNERArOl, A FUEL COM!USTION EMISSION SOURC!: IS A fUINAa, '30lLE l , OR SIMILAII: ECU II'MENT USED i'RlMA RIL Y FOil i'I\COUCI NG 

HEAT CJ. ;>Cw~ y IN OIHCT HEAr rRA FER, AN INcrNfJ.ATO R IS AN I' ~A_A US IN WH ICH RE FUSE IS aURNE O, 

,. NAME OF nA-NT OWNER: 2. NAME OF cmrORATE ON ISI C N a ll PlANT (IF OlfFERENJ fROM 

Empire Hard Chrome OWNER]: EmpiTe H ard Chrome 

l. SUfEi AOORESS Of ~MIS 5ION SOURCE: '" ( W, o"""UH ""'""" 

1615 S. KostneT Chicago 

GENERAL INfORMAT ION 

,. NAME Of PROCeSS: •• NAME Of EMISS ION SOURQ !CUIPMENT: 

Hard C hromium Plating Chrome Plating Tank 

' . f MISS ION sou.c~ EOU IPMENT /,\ANUFACTU RER: •• MODEL NU,I.\lIU: I 9 • HRIAL NUMlU: 

- - -

fl OW DIAGilAM OES1GI'IATlOI'I(S) O F ( MISSIO I'I SOURCE, 

A-5 

II . IOENTITVISI Of ;"NY SIMil AR SCURC (S) AT THE PLANT OR i'lEMISES NOT COV!3t[O BY TIlE fOR M Uf THE SOURCE IS COVERED BY ANOTHER 

Arf'l. lCATlON , 10ENTlFY THE APP\.!C,\Tl ON1, NA 

12. '\VEAA~' OPERATING iI.V! CF EMISS ION SOUs

'1: IJ. MA~!rU M OPERATl NG ,p ME O F EMISS ION ''Stef: 

2 HIS/ DAY 6 DAYSjWK ~~/Y1I HRS / DAY DAYS /WK WKSI'"YR 

... ;>EIC ENT OF ANNU~THROUGHPU , 25 25 25 DEC.;[B '!I. MAl_MAY "- JUN ....... UC " SEI'T_NOV " 

INSTRUCTIONS 

I. COMPlElE THE ADOVE 10ENTlFICArION AND GE NERAL INFORMATIO N SEcrrON. 

!. COMPlEH THE R.AW J,U jE~ IA . PROOUCT. WASTE MATHIAL, AND fUEL US,t.,GE SECilO NS fOR i HE I'ARTICULAR SCU~ C: ::CUlPMENT. 

CO MPOSITIONS Of MATBIALS MUST BE SUfFICJENIl Y IlETAIU D ro ALLOW O::lERMINArrON O F iHE NAru~E AND QUA NTITy OF POTENtiAl 

:'MISSIONS. IN PAIlTIC'J!,.l.~, THE COMPOSITION O~ NiS, INKS. ETC •• AND ANY SOl VENTS MUS; aE fUll Y CETAll::O. 

J. EMISSION "'-N O EXHAUST ,OINT JNFOltMAitON MUST a e COMf'l..EHO, UN..E5S i:MISS 10M ARE EXHAUSiEO THROUGH AIR ?ClLUTlON 

CONflOt ECU1PME N T. 

~. o pe,.,. TI NG TIME ,\NO CERTA IN O THER IrEMS ~EOU IR E ~OT H AVEAAGe AND IMXIMUM VALUES. 

S. FO_ GE I'I~AAL INFORMATION REfeR TO -GE NERAL INSnUCTlONS tOR l'ERM lr APPLICATIONS, - AI'C-'OI. 

Df FINlT lONS 

TIlE !:MI SSIQN SCURCE, CI THE STAlE OF 

' RODUCTION I I 

AVERAGE OI'ERATlNG riME _ ACTUAL TO TAL HOURS OF OPERA TION FO~ HIE PRECEDING TWElve MONTH PERIOO. 

AveRAGE:tArt - ACTUAL lOTAl Q UANTITY Of "MATE1 IAL" FOR THE PRECEDING TWRVE MONTH PU IOO, DIVIDED ay THE AVERAGE 

OPElAilNG TIME . 

AVERAGE CPERATION - OPEAATION IYPICAL Of THE I'!IEC~OINC; TWHVE MONTH rERleo, ;..S ilEPRESENTED AVE RAG€. OPE~Tl NG TIME 

AND Ave~Gf .v. TU. 

MAXI MUM - rHE GREAHH VALUE ;..nAINA8t.: OR An AINEO fROM TH [ EMISSION mUle:, O R THE PER IOO O f GREATEST OR UTMOST 

OouCTION Cf THE f MIBION SOURCE. SrECIFICALL y , 

MAXIMUM Pf~ATING TIME· GlIEA TE ST EXPECi ED TO TAL HOURS OF O rUATIONS FOR ANY TWEl VE MONTll ~Rleo , 

MAX IMUM RATE - C~ eAl EST QUA NTITY Of "MATER IAL · EXPECl(O ~H ANY O NE HOUR OF PE~ATlON . 

MA XIMUM Ol'fRA flON - G~EAlES T EX P~CUD OPS:RATlON, AS UI'1HEN TEO 3Y .'M)(IMUM OPERA IING TIME AND 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 520. b. c:. 

MTTER GR/SCF U/HR Emission rates based on data from ''Ventilation 

:ARION !i3a. PPM 10. <:. 

w\ONOXloe & Air Pollution Control", Metal Finishing Guide (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. 

010", __ c. 3600-3700, and Process Make-up Data. (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 

__ -=.2 4::.-__ 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 

____ 2222 ____ hr/day 

Average 

179,000 hr/ day 

Concentration 

30 oz/gal 

0.3 oz/gal 
M. 

N. 

o. 

Bath de foaming 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<LL771'l'1llK'--- --- --------

I. 

J. 

Make-up rate: _ -""TI\'--___ gal / min 

Source: (e.g., 

rinse tank, 

clean water, etc. ) _ ___ -"c:.Jue .. aaIlo....l/W"aljtt:.eAJ:r '-_________ __ _ 

v. Is liquid 

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 64 
STATE OF ILLINOIS 

ENVIRONMENTAL PROTECTION AGENCY 

DIVISI ON OF AIR POLLUTION CONTROL 

2200 CHU~CHILL ROAD 

SPRINGFIELD, ILLINOIS 62706 

' OATA AND INFORMATION 

AIR PCLLUnON CONTROL EQUIPMENT 

T~" ••• ~ •• " . wl ........ I. , . ..... 

I ... . ~,.,_ " •• ~ .~ • • • ".~ ... ~ .. " •• 

so .. . .... 1119. c~ .... , II ••• 10 .... _ 

Ion. o ... , • • ~ ... , I" .. ,., ".~ 

......... . . ..... ,~ , .H"Oft, ... , ... 

•• •• •• "' .. ...... . I" .. I ..... It . ... 

• "'f . ........ ••• ..... ...... ." 

,h' " .""".' . ... . . . .... .. Th" 

I., .. ' " • ••• • •••• ••• • • IU ~. '''' ' 

.. . .. . ..... Ul c ..... 

'THIS INFORMATION FORM IS FOR AN INDIVIDUAL UN IT OF AIR POLLUTION CONUOL EOUIPMENT OR AN AIR I'CLLUTION CONTROL SYSTEM. 

I. 

J. 

NAME OF OWNER: 

FMPTRF H.Rn 

STR E~T ADDRESS OF CONiilCL EOUIPMENT: 

1 "1' , I 

2. 

'. 

NAME OF CORPORATE DIVISION OR PLANT (IF DIFFERfNT FROM 

OWNER): 

CITY OF CONTROL ::OUIPMENT: 

CHICAGO 

5. NAME OF CONTlOL :::OUIPMENT OR CONTROL SYSTEM, 

SCRUBBER , S2 (WITH MESH PAD FILTER) 

INSTRUC nONS 

I. COMPUTE THE Ai30VE IDENTIFICATION. 

2. COMPlETE THE APPROPRLATE SECTION FOR THE UNIT OF CONTRC1. EQUIPMENT. OR THE APPROPRIATE SEcn ONS FOR THE CONTRCL 

SYSTEM. aE CERTAIN THAT THE ARRANGEMENT OF VARIOUS UNITS IN A CONTROL SYSTEM IS MADe a.EAR IN THE PROC='SS FLOW OIAGitAM. 

J . COMPLETE PAGE 6 OF THIS FORM. EMISS ION INFORMATION AND fXHAUST PO INT INFORMATION. 

4. EFF ICIENCY VALUES SHOULD BE SU PPORTED WITH A DETA ILED EXPLANATION OF THE METHOD OF CALCULATION, THE MANNER OF 

ESTIMATION, OR THE SOURCS OF INFORMATI O N. REFERENCE TO TH IS FORM ANY EL ~VANT INFORMATION OR EXPLANATION INCLU DED 

IN THIS HIlMIT API'I..!CATION. 

5. EFF ICIENCY VALUES AND CERTA IN OTHER ITEMS OF INFORMATION AilE TO liE GIVEN FOR AVERAGE AND MAXIMUM OPERAT ION OF THE 

SOURCE EOUIPMENT. 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 RAH INTO THE CONTROL EQU IPMENT WHEN THE SOURCE IS AT 

AVERAGe OPERArJON. 

6. FOR GENERAL INFORMATION REFER TO GCNEilAL INS'iil.UCTIONS FOil PERMIT API'I..ICATlONS ", APC-201. 

DEFINITIONS 

AVERAGE - THE VALUE THAT SUMMARIZES OR REPRESENTS THE GENERAL CONDITION OF THE EMISSION SOURC~ OR THE GENERAL STAT!': OF 

PRODUCTION OF IHE EMISSION SOURCE . SPECIFltALL Y: 

AVERAGE OPERATION - OPERATION TYPICAL OF THE PRECEDING rwave MONTH PERIOD. AS REPRESENTED BY AVERAGE OPERATING TIME AND 

AVERAGE RATES. 

MAXIMUM - THE G~EAreST VALUE ATTA INABLE OR ATTAINED FROM THE EMISSION SOURC~ , OR THE PER IOD OF GREATEST OR UTMOST I'RODUC. 

TlON Of tHE EMISSION SOURQ . SPECIF iCAlLY: 

.AXIMUM OPERATION - THE GREATEST EXPECTED OPERATION, AS REPRESENTED 8Y MAXIMUM OPERATING TIME 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: 

0 COCURRENT 0 COUNTERQJRRENT • 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:/ 50 r..ru:.lliK GPM 5000 SCFM 75 GAL 1 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 6 
EMISSION IN FORMATION 

I. NUMIIER OF IDENTICAL CONTRCL UNITS OR CONTROL SYSTEMS (DESOJIIE AS I , 

- AVERAGE O PEItATlON OF SOURCE 

'CONT~~T r CONaNTiATI~~ ~ ~lssiON RATETeR IDENTICAL - METHOD USED To OeTERMINECONCENTlATJON -

OR EMISSION RATE 

20. o. .. MAm. Gii/SO' LlltHR CALCULATIONS BASED ON DATA FROM: 

CARBON I ' 0 . PPM .. I •. MONOXIDE (VOL) LII/Hit "VENTILATION & AIR POLLt1I'ION CONTROL" 

NITROGEN ... PPM •• ... OX METAL FINISHING GUIDEBOOK 1990 ED. NEVI IDES ,Vall LS/H' 

OilG~ NIC So. PPM I •. ' . MATERIAL (Val) LII/HR YORK STATE DEPT. OF ENVIRONMENTAL 

SULFUR I 

00. PPM I b. '. 

O

DIOXIDE 

THeP. 

(VaLl LII/HIt ~ ~ 

I ;0. 

~~C >PM •. 0.0043 .. MSDS PROCESS MAKE-UP DATA , POLLUTION 

(SPECIFYl (VC Ll lSIH' 

MAXIMUM OPERATION OF SOURC! 

---- - CONC~NTiATiO'N OR E .... assioN W: ?ER JDENTlCAl.- - - - METHOD USED TO DHERMlNECONCENTRAiJON - -

CO NT~M NANT CONTROL UNIT OR CONTROL SYSTEM OR EMISSION RATE 

' 0 , o . .. MAml GR/sCF LII/Hit nN n.",. ",,,~ . 

CAlBON 90, PPM •• .. MONOXIDe (VOL) LII/HR , & AIR . " 

100 . ?PM •• .. OXIDES (VOL) I lll/Hit 1990 ED. NEI'I -

ORe .Ie 110 , PPM •• .\o\AUltiAl (VOL) lll/HIt 

SULFUR 120 , PPM •• ~OF PROCESS 

DIOXIDE (VOL I t ll/HR 3600, 3700, MANUFACl'UR<R 

OTHER IJo. CHRQ/>UC ?PM •• •• M.SD5 

(Sl'fC1FYI MIST (VCL) 0.0054 LS/HI[ CONTROL EQUIPMENI' EFFICIENCIES 

. . . • OTHER CONT .. M INANT SHOULD BE USED FOR AN Alii CONTAMINANT NOT S?ECIFlCAlL Y NAMED ~DOVE. ?OSSleLE OTHER CONT~MIN~Nrs 

~RE ASIIESiOS, 3ERYUIUM. MERCURY. V INyt CHLORIDE. LEAD, ;;rc. 

:;:XHAUST POINT INFORMATI O N 

•• ,LOW DIAGi\AM OES IGNAilON(S ) OF :::X HAUST ?OINT, 

ES2 

2. OfSCitlPTION Of EXHAUST POINT (LOCATION IN RelATION TO BUILD INGS. DIREC710N , HOODING. TC J: 

STACK LOCA= 75 FI FROM NORTH WALL 

,. EXIT HEIGHT ;..SovE ~DE: • ~XIT OIAMETER: 

40 2 ' x 2 ' 

5. ~EAS EST HEIGHT Of NEARBY ilUILDINCS: •• EXIT OISTANC!; rROM NEAREST PlANT SCUNDARY: 

30 FT 75' ~T 

AVERAGE OPERATION OF SOURCE MAXIMUM OPERATION OF SOURC!; 

'. EXIT GAS TEMPERATURE: ,. EXIT GAS i EMI'ERATURE: 

70 OF 75 0. 

, --

~ .. ;~~ Flew RATE iHRQUGH EACH EXIT: 10. GAS FLOW RA rE THROUGH EACH EXIT: 

5000 ACFM "nnn ~C~M 

PAGE 67 
0'\ 

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' 'sciiuiiic-co-'IIROI'jAiiS."u=IC:-, --'-::::::'1_ --- _ Ol!_=-==-!!I:--'-~~V ~~:!: _ ~---""---~I~~-:=--_ ~_~Qf..!tJ-_ 

lisa SOUlIIY.OUI AV[UlJ[ 

CHICAGO, It 60621 
STATE OF ILLINOIS 

ENVIRONMEN TAL nOTEctloN AGENCY 

DIVISION OF AIR POll UTIO N CONTROL 

2200 CHURCHILL ROAD 

SPRINGFIELD, ILL INOIS 6Z706 

· OATA ANO INFOR MATION 

'ROCESS EM ISS IO N SOURCE 

· THIS INFORMATION fOItM IS ;0 BE COMI'LElED FOR AN EMISSION SOUR~E OTHEI THAN A Fun COMBUSTION EMISSION SOUltCE all: AN 

INCINE~TOR. A FUel COM!USTION EMISSION SOUltC: IS A FURNACE, BOILEl, OR SIMILAR EOUIPMfNT USED PRIMARILY f OR PRODUCING 

HEAT OR .POWER 8Y INO IRECT HEAT TRANSFER. AN INCINERATOR IS AN AI"ARATUS IN WHICH REFUSE IS BURN EO. 

I, NAME OF PLAN T OWN ER: 2, NAME OF CORPORATf OfYISION OR P' ... ANi (IF :lIF FERENT FROM 

Empire Hard Chrome OWNER), Empire Hard Chrome 

J, ST~~E{ A~01{S S OF EM ISSION SOURCE, " LI~ · .U~ ~ , ,~<C" 

5 . Qstner Chicago 

GENERAL INFORM" T ION 

" NAME ~F PROCES~: 

Har Chromium Plating 

6, NAME OF EMISS ION SOURe! ! QU IPMENT, 

Chrome Plating Tank 

7, EMISSI ON SOURCE EQUIPMENT MANUFACTURER: e, MODEL NUM6ER, I 9, HRtAL NUMIER, 

- - -

10, FLOW DIAGRAM DES IGNATlON(S) OF £MISS ION SOURCE, 

A-6 

" 

IDENTITV[SI Of ANY SIMILAR .sOURCHS) Ai THE PLANl OR PlEMISES NOT COVflI:£D BY THE fORM /IF THE SOURCE IS COVERED IIV ANOTH~R 

MPlICATlON, IDENTIFY THE MI'lICATl O N I: NA 

12, AVE~ OPERATiNG TI~ OF EMISSION SCU~'2': IJ, ~if'UM OPERATING j/ME OF EMISSION S~~CE: 

HRS/ DA Y 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 Aeove JOENTlfICArrON AND GENUAl INFORMATION SECTION. 

2. COMPl ETE THE RAW MA1E1UAL. PRODUCT, WASTE MA re.'Al , AND FUEl USAGE SECTIONS FOR THE PARTICULAR SOURCE EOUIPMENT. 

COMPOSITIONS OF MATH IALS MUST 8E ~FFICIENn v DETAILED TO ALLOW DETERMINATION OF THE NATURE AND QUANT ITY OF POTENTlo\l 

EMISS IONS. IN PARTICULAR, i HE COMPOSITION OF PAINTS, INKS , ETC., AND ANY SOL VENTS MUS . Bf fULLY DETAIlED. 

J. EMISSION AND EXHAUSi FaINT INFORMAiiON MUST eE COMPL(nO, UN.fSS EMISSION~ ARt. EXHAUSTED THROUGH AIR POLLUTION 

CONTlOl ECUIPMENT. 

. OPEkATiNG lJM~ AND <E~TAIN OTHEl ITEMS REOUIRE aOTH AVEMoGE AND MAXIMUM VALUES. 

S. FOR GEN EAAL INFORIAAT/ON REFER TO ~GENUAL INsnucrroNS fOR PERMit APPLI CATIONS, " APC- 20\ . 

DWNITIONS 

AVERAGE - THE VA.LUE 1i~::;~~~ '£!!iS~o;l"H;;~~~~l£~£:Co;;';-TTiHii Gi'ENNCE"' sSiT~A:tTEE(O;;F~-1 'ROOUC lJON ~ I 

AVEkAGE OPERATI NG TIME _ ACTUAL TOTAl HOURS OF- OI't"ItA TiON FOR THE PRECEDING TWElVE MONTH PEItIOO. 

AVERAGE 1tArt: - ACTUAL Tor AL a UAN Tl TY OF "MA.TEW\L" fOR THE PRECEDING TWElVE MONTH PERIOD, DIVIDED BY THE AVERAG( 

OPUATING TIME. 

AVERAGt CPtRATi O N - OPERATION TVPICAl Of THE PiUCEOING TWELVE MONTH fUIOO, AS REPRESENH O BY AVE.RAGE OHUTING TIME 

AND AVERAGf RATn. 

MtVCIMVM - THE GREATEST VALUE FROM THE EMISSION ~OU CE, OR THE PER IOD OF GREATEST OR UTMOST 

PJl:OCUCTlON CF Tm I I y, 

MAXIMUM orE RATING TIME - GREATEST EXPE CTEC TOT AL HOU S OF OPER"TlON~ f OR .... N V TWELVE MONTH PERIO~ . 

MAX IMUM RATE _ G REATen aU .... NTITY OF "MAH RIAL" EXPECHO PE_ ANV ON~ HOUR OF OPERATIO N . 

MAXIMUM OPERATION - GREATEST E:.cPEClEO OI'l:RATlON, AS REPIEUNHD!Y ,'M)(IMU M OPERATIN G TI ME "'NO MAXIMUM RAi ES, 

""C-220 (II.£VISED 1/27ml PAm I OF J 
RAW MATERIAL INFORMATION 

AVERAGE RATE MAXIMUM RATE 

NAMe OF RAW MA T£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 

'AAnCULATE 520. b. c. 

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 

'ARTICULA TE 

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. Corpora t e or Plan t Name : ___ E=m'!=pui..lr::Jp""-,,H.aacIro:d1..cCub.zr:colImWp""-_______ _ 

c . Add res S 0 f Em iss ion S ou r c e : __ --ll b6.: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 rOIDi !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 setting 

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. 

Voltage 

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 wks/yr 

Average 

___ hr/day 

Average 

261 ,000 hr/ day 

Concentration 

30 oz/gal 

0.30 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 

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 

a. packing Chip Bod Packing PiJter t¥pe: 

b . packing s~ze: NA in. 

in. 

B. 

c. packed height : __ -i6i(DL-__ 

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;nl.....l'<L'aatt .. 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 75 ft 20 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 76 
STATE OF ILLINOIS 

ENVIRONMENTAL PROTECTION AG~NCY 

OlVISION 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; .~ .. , 

'THIS 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 (IF OIFFEitENT FROM 

OWNER): 

J. STi:E!;T ADDRESS OF CONTiOL ECUIPMENT: 

1 "" " 

'. CITY OF CONTROL EQUIPMENi: 

CHICAGO 

5. NAME OF CONnCL EQUIPMENT OR CONTRCL SYST"..M: 

SCRUBBER, S4 WITH CHIP BED PACKING FILTER 

INSTRUCTIONS 

1. COMPLETE THE AaOVE IDENTIFICATION. 

2. COMPLETE THE APPROPRIATE SECTION FOR THE UNIT OF CONTROL eCUIPMENT. OR THE APPROPRIATE 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. EFFICI,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 IS FORM ANY RELEVANT INFORMATION OR EXPLANATION INCLUDED 

IN TH IS PERMIT APPliCATION, 

S. EFFICIENCY VALUES AND CERTA IN OTHER ITEMS OF INfORMATION ARE TO BE GIVEN FOR AVERAGE AND MAXIMUM OPERATION OF THE 

SOURo; ~aU PMENT, FOR EXAMPLE. "MAXIMUM EFFICIENCY" IS THE ,FFICIENCY OF THE CONTROL EOUIPMENT WHEN THE SOURCE IS 

AT MAXIMUM OPERATION. AND "AVERAGE FLOW RATE" IS THE FLOW RATE INTO THE CONTROL EOUIPMENT WHEN THE SOURCE IS AT 

AVERAGE OPERATION, 

6. roR GENERAL INFORMATiON REFER TO "GENERAL INSTRUCiIONS FOR PERMIT ,.l,PPUCATlONS ~, APC-201. 

DEF INITIONS 

AVERAGE - THE VALUE 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 REPRESENTED IIY AVERAGE OPERATING TIME ANO 

AVERAGE RATES. 

~ 'MUM. THE G~EATEST VALUE ATTAINABLE OR ATTAINED FROM THE EMISS ION SOURCE. OR THE PERIOD OF GREATEST OR UTMOST PRODUCTION Of iRE EMI~ ON SOURCE. SPEC1Flo..lLY: 

MAXIMUM OPERATION - THE Gi!.EATEST EXPECTED OPERATION, AS Rf?RESENTED 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 H2O 

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 ~ TJ 
EMISSION 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. 

OXIDES .:." Mm.'AL FINISHING "GUIDEBOOK 1990 ED. (VOL) . LS/HR NEW 

ORGANIC I Sa. 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 

;oARTICULA TE I aa. c. .:. 

MATTER GR/SCF LS/HR ['-AT flIT.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/Out 

5100 LB/HR ?(--

Work In/Out -~) 

1300 LB/HR ?(--

Exhausted To 

Scrubber S8 

6,000 CFM 

75 F 

Exhausted To 

Scrubber S1 

18,000 CFM 

75 F 

,Ii"' ... I ,I I " , , , , , , ~--------- ---- ----------~------------I ,.. I " I I 

, " , " , " , " 

R R RR Electr 

, 

, 

, 

, 

, 

, 

, ng : 

Chrome Plating Polish Tank, A-7 <=o_1 , 

, 

, 

, r------------------------------------· , 

Chrome Plating 

Tank, A-6 

R IACid I ~ Cle4ner 

C1 C2 

-rRuici;- --------------------------------------- tOC--t1 1)l1 

S<'!LI . .. sc_ml( COWP.tl IAIIS . u; 

JIS! sruUI r.0I.11 A\ltlL{ 

cuoco. t 60611 
STATE OF ILLINOIS 

ENVIRONM£NTAL PROnCTlON AGENCY 

DIVISION OF AIR POLLUTION CONTROL 

1200 CHURCHill ROAD 

SPRINGFI(lD, ItLlNOIS 62706 

"QATA. A.ND INFORMATION 

'Rocess EMISSION SOURCE 

' THIS INFOltMAl lON FOItM IS TO BE CQMI'lE'HD FOR AN EMIHION SOUR~ [ OTHER THAN A FUEt COMaUST10N EMISSION SOURCE at AN 

INCINERA TOR . A FUEL COMeUSTlON EMISSION SOUII:CE IS A FURNACE, SOltH. O~ SIMILAR EQU IPM!Nl USEO PWMRll Y FOR P1I:ODUCING 

HEAl eR PCWE~ 3Y INOIHCT HEAT rRANSFfR. AN INCINERATOR IS AN AP~A"AruS IN WHICH RHUH IS BURNED . 

" 

NAME OF nANT OWNER: " NAME OF CORPORATE DIVISION OR P'~ANT (IF DIFFER~NT fROM 

Empire Hard Chrome OWNER), Empire Hard Ch rome 

" SUEEr ADDRess OF ~MISSION SOURCE: co:., V' "~""VN >vv.co, 

1615 S. Kostner Chicago 

G(NEkAtINfORMA TION 

" 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 IGNATlON(S } OF {MISS ION 50UilCb 

A-S 

,,, IDENTITYISI OF ANY SIMILAR SQURCE (»AT THE PLANI OR HEMISB NOT COVOI(O BY THE fORM (IF THE SOURC~ IS COveRlO BY ~NOTHER 

"'~ICA TIO N, IDENTIfY TH~ APPLICATION 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 " 

INS aUCTIONS 

1. COMPUTE 'HE ABOVE IDENTIFICATION AND GENERAl INFORMATION SECTION . 

2. COMPLETE THE RAW MATERIAL, PRODUCT. WASH MAnR1AL. AND FUEl USAG! HCTIOM FOR THE PAR TICULAR SCU~C[ EOU ~M ENT. 

COMPOSITIONS OF MATHjAlS MUST S~ SUffICl£NTL Y tlHAILED TO ALLOW DElERMINAHON OF THE NATURE AI"O QUANTITY OF POTENliAL 

EMISS IONS. IN PARTICULAR, THE COMPOSITION Of PAINTS, INKS, ETC •• AND ANY SOL VENTS MUS; Bf FULLY DETAILED. 

3. EMISSION ANO EXHAUST ;OINI INfO,U..\.ATlON ,.,..uST BE COM .... UtO. Uf'.A.ESS EMISSIONS ARE EXHAUSTED THROUGH AIR POLLUTION 

CONUO\.. ECUIPMENT, 

.... OPERATING TIME AND CERTAIN OTHH JrEMS REOUIRE 80TH AVERAGE ANO MAXIMUM VALUES. 

S. FOI GENEW INFORMMION REFER TO ~GENtRAL INsHucnoN) 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 ION SOURCE, 01 ~ GENEML SlATE OF 

'ReOUCTlON 01 iHE tMIBION sow!:£. ~fECIFltAll Y: 

AVERAGE OPERATING TIME _ ACTUAL TOTAL HOURS OF O I'UAtlON FOR THE P~EC~01NG TWELVE MONTH PUIOD . 

AVERAGE RAr~ _ ACTUAL IOTA\.. OUANTITY OF "MATElIAl' fOt THE PRECED ING iWn.V~ MONTH PERIOD, DIVIDeD BY TH[ AVERAGE 

O,EIl.ATING TIME. 

AVfRAG~ CPEP.ATlON - OPERATION TYPICAl. OF THE l'itfCfDlNG TWELVE MONTH PER IOD. A~ RHRE5ENHO ,y AVHACE OPEkATiNG 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 TorAL HOUIS OF OPE lATIONS fOR ANY TWE\.VE MONTH PERIOD. 

MAX I.v.tJM P.ATE _ GIU .... IOT QUANTITY Of "MATH IAL" EXI'fClrO PEl .... NY ONE HOUR 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 . . - .-

OTHER GAS 0 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 T FURNACE. 

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: 

• AlTJCULA TE 520. Ia. 1;. 

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