STAll OF ILLINOIS 

ENVIRONMENTAL PROTECTION AGENCY 

DIVISION OF AIR POLlUTION CONTROL 

2200 CHURCHILL ROAD 

SI'IUNGfItLD, ILLINOIS 62706 

DATA AND INFORMATION 

INCORPORATION /lY Illf£IllNa 

TIIII Agvncv I, ... Iho" .. d lei roq.ue tftia .. 1 ...... _ ....... wltlOit 

R._$"'~ IlIllI.ChI_'" I/Z.Sec:tIonl0390ia __ 

01_ entarmation. roquirod _IhIII Section. Fallin lei do ao may _llhiafannh_bclnG ___ ond ~ ruwllin_ 

IJIII!ation bcingdenild. Thia '-hit '*'" _~ br !he F_ 

~Cert*. 

JAN 29 lR9A 

THI~ fORM 15 TO BE USED TO INCORPORATE 011 TRANSFER INfORM4TION FROM ONE PERMIT APPLICATION TO... E • I . E 

TRANSFfR OF INFORMATION FROM A CONSTRUCTION PERMIT APPlIC4T10N INTO AN OPER4TtNG PERMIT APPliCATION. THIS FORM SHOULD 

ACCOMPANY THE APPlICA-TION INTO WHICH INFORMATION IS TO BE TUN~FERRED. 

I. NAME OF OWNER: • Economy Plating, Inc. I 2. NAME OF CORPORATE DIV. Oi PlANl' (IF DifFERENT fROM OWNER): 

3. STREET ADDRESS OF EMISSION SOURCf: 

2350 N. Elston 

CITY OF ~MISSION SOURCE: 15. IDENTIFICATlO~ NUMBER: 

ChlcaQO Q.:i..Liz.Si ~ C if IYI 

6. 

APP97040058£R: I 7. I] CONSTRUCTI~~1Ii 0 OI'ERATI~~nt OF ~ir II rinn"'eOllinm, 

B. SHOULD ALL I"'FORMATION IN THIS APPLICATION BE INCORPORATED BY REFERfNCf OR TRANSFfRRED? 

0 YES Oi NO 

IF "NO·, LIST IJEMS TO BE INCORPORATEDt 

9a. ITEM TO 8E INCORPORATED: b. PAGE: c. fLOW DIAGRAM DESIGNATION 

Cmo control SVSI~1 for tank~ 1 .4 ~ R 1 (IF APPLICABLE): 

.. " 

1D. DOfS THE DATA & INFORMATION DESCRIBING T~)EMS REMAIN TRUf. CORRECT. CURRfNT A"'D COMPlETfl 

is YES 0 NO . 

IF ·N~t SU&MIT THE AflLlCAalE FORMS AFIO CLEARLY STATE THE DATA AND INFORMATION WHICH IS NO lONGER TRUE, CORRECT. 

CURRE AND COMPlE • 

11. AP7303°1926KER: 112 • o CONSTRUCTION UI OPERATION 

OF 

13. SHOULD AlL INFORM-TION IN THIS APPliCATION BE INCORPC'RATED BY REFtRfNa OR TRANSFERRED? 

rx YES 0 NO 

If "NO", LIST ITEMS TO 8E INCORPORATED: 

1.40. ITEM TO B£ INCORPORATED. b. PAGE: c. FLOW DIAGRAM DESIGNATION 

(!F APPLICABLE): 

-

15. DOES THE DATA & INFORMATION DESCRIBING THESE lTE~ REMAIN TRUE. CORRECT. CURRENT ANO COMPlfTE? 

0 YES 0 NO 

IF "NO" SUBMIl THE tPlllCABlE FORMS AND CLEARLY STATE THE DATA AND INFORMATION WHICH IS NO LONGER TRUE. COWCT, CURRENt AND COMPL 1 • 

Il 53?-0?4S 

APe 210 Rev. 6/11/79 
Final Report of Emission Tests 

Emission tests for Economy Plating, Inc. were conducted by Victor Koerner 

and Scott Koerner on November 25,26,28 and December 11, 1997. All tests were 

performed while the equipment was running at normal operating and rate of 

plating levels. 

Calibration of the test equipment, the dry gas meter and the critical orifice, 

was performed by Measurement Controls, Inc. (See attachment Cert-I)in 

accordance with USEPA test method 306a. 

The schedule of tests was: 

Tuesday November 25, 1997 #5 & 6 system 

Wednesday November 26, 1997 # 1 system 

Friday November 28, 1997 #4 system 

Thursday December 11, 1997 #4 system 

8:00a.m. until 6:30p.m. 

8:00a.m. until 5:30 p.m. 

8:00a.m. until 2:00p.m. 

8:00a.m. until 6:30 p.m. 

On Friday, during test 4-1, the vacuum pump failed and necessitated a 

reschedule of system #4 tests to December 11, 1997. 

When the protocol was established it was noted that the records kept for the 

amperage was based on the 12 mQ3iii rolling average of non-reseUable amphour 

meters which were not calibra~a' to the amp meters on the rectifiers. In order to 

ensure adequate test setting, a 25% factor was added to the rectifier amperage 

setting (See attachment Roll-I) 

Five gallons of 0.1 NaOH was purchased from Accurate Labs, Inc. for use 

during all method 306a testing and a blank sample was submitted to Scientific 

Control Laboratories, Inc. for analysis. The results are: 

Blank 0.006mg/Liter (See attachment Lab-5) 

Test for #5 &6 CM P system. 

All pretest checks were performed according to the protocol (See attachment 

Prot-I). The traverses were checked with a manometer for angle and pressure 

differentiall according to method 306a (See attachment trav-5) and the calculations 

done on a computer. The raw data from the test are labeled Test 5-1, 5-2 and 5-3 

and the formula used to determine the chromium content is from method 306a. The 

stop watch malfunctioned during the first test and is the reason the test ran long. 

The results of the test are: 

test 1 0.013 mg/dscm test 2 0.005 mg/dscm test 3 0.007mg/dscm 

The analysis of the impinger liquid was done by Scientific Control Labs, Inc. 

in Chicago (See attachment Lab-5) 

Test for # 1 CMP with mist eliminator system. 

All pretest checks were performed according to the protocol (See 

attachment Prot-I). The traverses were checked with a manometer for angle and 

pressure differential according to method 306a (See attachment trav-I) and the 
,.,- calculations done on a COlllpu re7: The nlw d ata froillthe lesl :lre I:lbeled Test 1-1 , 1-

2 and 1-3 and Ihe formula used 10 delermin e Ihe chromiulIl conlelll is frOI11 met hod 

306n, 

T he r esults of the tests :II'C: 

t est I 0.010 mgldscm test 2 0.011 mgldsclll test 3 0.010 mg/dscm 

The ll nalysis ofl he impinger liquid W:IS dOlle by Scien tific Contr'ol Lllbs, Inc. in 

C hicligo (sec atllu:hlll ent Lllb-I), £collomy 1)lntillg, In c, would like to have # t 

eM P system with M ist Eliminator classified as :I sUluli exist ing soul'ce :l lId subj ec t to 

the 0.030 st'lIIdllrd based 011 lhe less t ha n 60 millioll II ll1pho urs used allhis facility 

(Sec :lttachmenl Roll-I), 

Test for # 4 eM I) with mist elimin:ltor system, 

All pretest checl{s were pel'formed ncco rding to the protocol 

(attachmellt PI'ot-I), The (!'llve rses were checked wit h a manometer for :lII gle 11llU 

JlI'essure difTerenlialliccording to method 306a (See :l tUlchment trav-4) :tnd the 

cH lcnl a tio ns dOll e 0 11 a com puter, T he rmv data from the test arc labeled Test 4-1, 4-

2 and 4-3 and the formu!:l used 10 determine the cllI'o miullI cont ent is from method 

306a, During the fi rst test but after the system leak test th e vacuulIl pump failed 

:llId t he test postponed to December II , 1997. The results of the test lire: 

test I 0,0 13 mgldscm test 2 0.012 IlIg/dscm lest 3 O,O l 6 111 g/dscm 

The :lna l)'sis of the impinge r liquid was done by Scientific Control Labs, Inc. in 

C hi cll go (See llttllchment Lllb-4). Eco llomy Plating. Inc. would like to hllVe # 4 

CMJ) system with !\llist Eliminator dnssifi ed as :l sma ll exisling source :lI1d subj ect (0 

th e 0.030 stlllldli rd based 0 11 the less tha n 60 million alllphours used III this facility 

(See lttt:lchmcnt Roll-I ), 

On FridllY November 28, 1997 C)rllthia Curtis, :Ill Ellvironment:11 Scientist 

from Ihe USE PA, conducted an inspection of the test procedur'es a nd reviewed 

prnio us h'st sites. It wtlS during IH :",...o se va tion of lest 4- 1 tha t the v,lt uum pUIlIP 

failed, She rl'CllleSfed 10 be 1I0 !lJ. d o f the retest date, 

O n TlIIII'Sd:IY Deccmber II , 1997 Cllesa r KrLY lllowski, C hi ef Inspector from 

the IEPA Field ollice in J\lbl)'wood Park, conducted:1II inspection of test procedures 

and reviewed IH'evious tests. I'l e viewed test 4-1 with pretest check Il nd verified a ll 

equ ipment settings, 

O n Thursday December 11 , 1997 Cynthia C Ul,tis returned with an associate 

1'1'0 111 the USE PA to view lest 4-2 llIId 4-3 :lIld inspect the Air pollution cOlltrol 

E,, ";pmcllt. 1M ~~ 

V;C!or J. rncr, Presidellt Economy Pl:lting, Inc, 
PROT-! 

Protocol 

Objective: Obtain representative sample of exhaust air for analysis for chromium 

Procedure: 

Prior to testing 

1. Detennine monthly and yearly average electrical usage 

2. Check temperature and hwnidity and Pbar 

3. Check plating solution temperature and chrome content. 

4. Check air capture device for leaks greater than allowed according to Method 

306A. 

5. Calibrate gas meter 

6. Check air flow for volume and speed 2000ft/min = 10,700 CFM 

7. Check cyclonic flow angle for each test point 

8. Take and record manometer reading for each test point and calculate test point times using flow 

angle. 

During the test. 

9. Energize plating tank(s) with the highest of monthly amp average + 25% 

10. Check pressure differential across control device. 

11. Collect air sample based on number of sample points in 306A and using flow angle. 

12. Rinse capture equipment according to generally accepted methods 

13. Check calibration of gas meter 

14. Record gas collected 

15. Verify electrical consumption during capture 

16. Check dry gas media 

17. Rinse impingers according to generally accepted methods 

18. Replace impinger jar and NAOH solution 

19. Mark and maintain sample 

20. Check air capture device for leaks greater than allowed according to Method 306A 

21. Energize tank(s) and record amp hour and gas meter readings 

22. Collect Sample #2 

Repeat items 9 through 20 

19. Collect Sample #3 

Repeat items 9 through 20 

20. Deliver marked Samples to Scientific Control Labs for analysis 
Repeal procedure for each air exhaust unit. 

The test will be performed by Victor Koerner CEF, President of Economy Plating, Inc, 

and Scott Koerner. 

The basis for the test procedure is the seminar sponsored by the AESF, NAMF, and the 

USEPA with Frank Clay. which was attended by Victor Koerner, We will be using the 

EXCEL worksheet supplied during the seminar on a laptop computer to do the 

calculations during the test. 

Scott Koerner has obtained a Bachelor of Science degree in Chemistry from the University 

of Illinois-Champaign in 1993 , He complete'd a course of study at National Louis 

University in 1994 and was certified by the American Society of Clinical Pathologists as a 

Medical Technologist and is currently employed at Northwestern Memorial Hospital in 

Chicago, lllinois. . 
Raw Test Data 

Test Date: 11-26-97 

Tank Number: 1 

Test Number: lof3 

Temperature of sampling stream: 56° F 

Gas Meter reading( start): 515.2 

Gas Meter reading (end): 580.6 

Total gas yolume captured: 65.4 fe 

Length of time of test: 127 min. 

Ampere setting on rectifier: 750 

Volt setting on rectifier: 5.5 

Non-resettable amphour meter reading(start): 646355 

Non-resettable amphour meter reading (end): 647873 

Hourly amphour rate: 717 amps per hour 

Rolling 12 month ampere average: 538 amps per hour 

Barometric Pressure: 29.65 in Hg 

Total Chrome captured: 0.062 mglL 

Total Liquid volume from imp~ers : 

Vacuum gage reading from impinger system: 

Calculations 

Sample # 1 

(0.068)-(0.006)= 0.062 mgIL 

(0.062mgll)(0.31O)= 0.0192mg 

310 ml 

27 

0.0192 mg 

( 19.2)(56 +460) ___ _ = 9907.2 =0.010 mgldscm 

(499.8)(1.0003)(65.4)(29.65) 969457.9 
Raw Test Data 

.,' if 

Test Date: 11-26-97 

Tank Number: 1 

Test Number: 20f3 

Temperature of sampling stream: 5611 F 

Gas Meter reading( start): 581.3 

Gas Meter reading (end): 648.9 

Total gas volume captured: 67.6 fe 

Length of time of test: 128 min. 

Ampere setting on rectifier: 750 

Volt setting on rectifier: 5.5 

Non-resettable amphour meter reading(start): 647894 

Non-resettable amphour meter reading (end): 649494 

Hourly amphour rate: 750 amps per hour 

Rolling 12 month ampere average: 538 amps per hour 

Barometric Pressure: 29.65 in Hg 

Total Chrome captured: 0.077 mglL 

Total Liquid volume from impingers : 

Vacuum gage reading from impinger system: 

Calculations 

Sample # 2 

(0.083)-(0.006)= 0.077 n;~L 

(0.077mgll)(0.290)= 0.0223mg 

290 ml 

27 

0.0223 mg 

( 22.3)(56 +460). ___ _ = 11506.8 =0.011 mg/dscm 

(499.8)(1.0003)(67.6)(29.65) 1002069.7 
Raw Test Data 

Test Date: 

Tank Number: 

Test Number: , ., 

""(1 

Temperature of sampling stre.m: 

Gas Meter reading( start): 

Gas Meter reading (end): 

Total gas volume captured: 

Length of time of test: 

Ampere setting on rectifier: 

Volt setting on rectifier: 

Non-resettable amphour meter reading(start): 

Non-resettable amphour meter reading (end): 

Hourly amphour rate: 

Rolling 12 month ampere average: 

Barometric Pressure: 

Total Chrome captured: 0.082 mgIL 

Total Liquid volume from impingers : 

Vacuum gage reading from impinger system: 

Calculations 

Sample # 3 

(0.088)-(0.006)= 0.082 mgIL 

(0.082mgll)(0.236L)= 0.0194mg 

( 19.4)(56 +460) ., 

(499.8)(1.0003)(65.2)(2~5) 

= 10010.4 

966493.2 

11-26-97 

1 

30f3 

56°F 

649.4 

714.6 

65.2 fe 

128 min. 

750 

5.5 

649520 

651274 

822 amps per hour 

538 amps per hour 

29.65 in Hg 

236 ml 

27 

0.0194 mg 

=0.010 mg/dscm 
7;e/lL/-/ 

Airtest1 

!~ VJf~! WORKSHEET Tank 1 I I --- TRAVERSE CYCLONIC aP SQUARE SROF aP SR OF aP Minute 

POINT FLOW FROM ROOT AVG.OF AVG SRt.P 1&1 

# ANGLE MANOMETER ~p ~p SQ.RT X3Min Seconds 

1 _. 0 0.2 0.447214 1 4.000 4 0 --2-- . 0 0.2 0.447214 1 4.000 4 0 

3 0 0.2 0.447214 1 4.000 4 0 -, 4 0 0.2 0.447214 1 4.000 4 0 

5 0 0.2 0.447214 1 4.000 4 0 - ... - 6 0 0.2 0.447214 1 4.000 4 0 

7 0 0.2 0.447214 1 4.000 4 0 

8 0 0.2 0.447214 1 4.000 4 0 -.- 9 0 0.2 0.447214 1 4.000 4 0 *-.--~- ----- ----,- ------. . 

10 0 0.2 0.447214 1 4.000 4 0 --.. 

11 0 0.2 0.447214 1 4.000 4 0 

12 0 0.2 0.447214 1 4.000 4 0 

13 0 0.2 0.447214 1 4.000 4 0 

14 . 0 0.2 0.447214 1 4.000 4 0 

15 0 0.2 0.447214 1 4.000 4 0 -, 

16 I 0 0.2 0.447214 1 4.000 4 0 

17 0 0.2 0.447214 1 4.000 4 0 

18 0 0.2 0.447214 1 4.000 4 0 

19 0 0.2 0.447214 1 4.000 4 0 

20 0 0.2 0.447214 1 4.000 4 0 

21 0 0.2 0.447214 1 4.000 4 0 

22 0 0.2 0.447214 1 4.000 4 0 

23 0 0.2 0.447214 1 4.000 4 0 

24 0 0.2 0.447214 1 4.000 4 0 

25 0 0.2 0.447214 1 4.000 4 0 ~---

4 0 1-_26 0 0.2 0.447214 1 4.000 

27 0 0.2 10.447214 1 4.000 I 4 0 -_ ..... ---~-. ..- 28 0 0.2 0.447214 1 4.000 4 0 

29 0 0.2 0.447214 1 4.000 4 0 

I- '-;,," 30 0 0.2 0.447214.: 1 4.000 4 0 1--. 

31 0 0.2 0.447214 1 4.000 4 0 

32 0 0.2 0.447214 1 4.000 4 0 . -_. __ ._- - ------

0.2000 0.4472136 128.0 

AVG.OFap .. VG. OF SQ. TOTAL MIN:SEC '. "f"-'" '----'-'" ROC)! ~'P'S MINuTE$"*' 

=--~== --=-.':=-'~'~--- '---=r STACK TEMP AT END OF TRAVERSE: I DEG.F 

I 

MINIMUM OF 120 MINUTES IS REQUIRED. 

-.. _-- '---'-

j I '- - , 

I-- . 

-.... -. 1 --. -L 

I I 

.......j-~-c------ -----j~---r--. ... -." .......... =1=1---- -------_ . 

--.... - I f·----- ._----- -'-.-- I I ---·---1-----' 
Raw Test Data 

Test Date: 

Tank Number: 

Test Number: 

Temperature of sampling stream: 

Gas Meter reading( start): 

Gas Meter reading (end): 

Total gas volume captured: 

Length of time of test: 

Ampere setting on rectifier: 

Volt setting on rectifier: 

Non-resettable amphour meter reading(start): 

Non-resettable amphour meter reading (end): 

Hourly amphour rate: 

Rolling 12 month ampere averag~:-' 

Barometric Pressure: f 

Total Chrome captured: 0.103 mgIL 

Total Liquid volume from impingers : 

Vacuum gage reading from impinger system: 

Calculations 

Sample # 1 

(0.109)-(0.006)= 0.103 mgIL 

(0.103mgll)(0.268L)= 0.0276mg 

12-11-97 

4 

10f3 

540 F 

731.7 

805.2 

73.5 fe 

135 min. 

1300 

5 

816838 

820240 

1512 amps per hour 

1007 amps per hour 

29.94 in Ug 

268 ml 

27 

0.0276 mg 

( 27.6)(54 +460) ___ _ = 14186.4 =0.0129 mgldscm 

(499.8)(1.0003)(73.5)(29.94) 1100552.3 
Test Date: 

Tank Number: 

Raw Test Data 

12-11-97 

4 

Test Number: 2 of 3 

Temperature of sampling stream: 54° F 

Gas Meter reading( start): 806.45 

Gas Meter reading (end): 879.45 

Total gas volume captured: 73.0 fe 

Length of time of test: 128 min. 

Ampere setting on rectifier: 1300 

Volt setting on rectifier: 5 

Non-resettable amphour meter reading(start): 821400 

Non-resettable amphour meter reading (end): 824930 

Hourly amphour rate: 1655 amps per hour 

Rolling 12 month ampere average: 1007 amps per hour 

Barometric Pressure: 29.95 in Hg 

Total Chrome captured: 0.074 mglL 

Total Liquid volume from impingers : 

Vacuum gage reading from impinger system: 

Calculations 

Sample # 2 

(0.080)-(0.006)= 0.074 mglL 

(O.074mgll)(0.350L)= 0.02~~'1I~ .,~ 

'dlf 

350 ml 

27 

0.0259 mg 

( 25.9)(54 +460) ___ _ = 13312.6 =0.0122 mgldscm 

(499.8)(1.0003)(73.0)(29.95) 1093065.6 
Raw Test Data 

Test Date: 12-11-97 

Tank Number: 4 

Test Number: 3 of 3 

Temperature of sampling stream: 56° F 

Gas Meter reading( start): 898.2 

Gas Meter reading (end): 976.48 

Total gas volume captured: 78.3 fe 

Length of time of test: 135 min. 

Ampere setting on rectifier: 1300 

Volt setting on rectifier: 5 

Non-resettable amp hour meter reading(start): 828100 

Non-resettable amphour meter reading (end): 832197 

Hourly amphour rate: 1821 amps per hour 

Rolling 12 month ampere average: 1007 amps per hour 

Barometric Pressure: 30.00 in Hg 

Total Chrome captured: 0.111 mgIL 

Total Liquid volume from impingers : 325 ml 

Vacuum gage reading from imP.tf~er system: 27 

"(f" 

Calculations 

Sample # 3 

(0.117)-(0.006)= 0.111 mglL 

(0.111mgll)(0.325L)= 0.0360mg 

0.0360 mg 

(36.0)(56 +460), ___ _ = 18576.0 =0.0158 mgldscm 

(499.8)(1.0003)(78.3)(30.00) 1174382.4 
AIRTEST4-1 

TRA VERSE WORKSHEET Tank 4 1 1 

TRAVERSE CYCLONIC AP SQUARE SROF AP SR OF AP Minute 

POINT FLOW FROM ROOT AVG.OF AVGSRAP 1·&1 

# ANGLE MANOMETER AP AP SQ.RT X 3.2 Min Seconds 

1 0 0.5 0.707107 1 3.200 3 12 

2 0 0.5 0.707107 1 3.200 3 12 

3 0 0.5 0.707107 1 3.200 3 12 

4 0 0.5 0.707107 1 3.200 3 12 

5 0 0.5 0.707107 1 3.200 3 12 - 6 0 0.5 0.707107 1 3.200 3 12 

7 0 0.5 0.707107 1 3.200 3 12 

__ ·4 8 0 0.5 0.707107 1 3.200 3 12 ----'--

0.707101"- .. _--

9 0 0.5 1 3.200 3 12 

10 0 0.5 0.7071m 1 3.200 3 12 

11 0 0.5 0.707107 1 3.200 3 12 

---:;2 0 0.5 0.707107 1 3.200 3 12 ----- -- ----t----- 13 0 0.5 0.707107 1 3.200 3 12 

14 ~ 0 0.5 0.707107 1 3.200 3 12 

15 0 0.5 0.707107 1 3.200 3 12 

16 0 0.5 0.707107 1 3.200 3 12 

17 0 0.5 0.707107 1 3.200 3 12 

18 0 0.5 0.707107 1 3.200 3 12 

19 0 0.5 0.707107 1 3.200 3 12 

20 0 0.5 0.707107 1 3.200 3 12 

21 0 0.5 0.707107 1 3.200 3 12 

22 0 0.5 0.707107 1 3.200 3 12 

23 0 0.5 0.707107 1 3.200 3 12 

24 0 0.5 0.707107 1 3.200 3 12 

~5 0 0.5 0.707107 1 3.200 3 12 -- 26 0 0.5 0.707107 1 3.200 3 12 

27 0 0.5 0.707107 1 3.200 3 12 

28 0 0.5 0.707107 1 3.200 3 12 

29 0 0.5 0.707107 1 3.200 3 12 -

30 0 0.5 0.707107 1 3.200 3 12 --- 31 I 0 I 0.5 0.707107 1 3.200 3 12 

32 0 0.5 0.707107 1 3.200 3 12 

33 0 0.5 0.707107 1 3.200 3 12 - 34 0 0.5 0.707107 1 3.200 3 12 -- 35 0 0.5 0.707107 1 3.200 3 12 ---- ----- 36 0 0.5 0.707107 1 3.200 3 12 --- 37 0 0.5 0.707107 1 3.200 3 12 -- I 38 0 0.5 0.707107 1 3.200 3 12 ------ ---- -----,- - ------+ -_. 

39 0 0.5 0.707107 1 3.200 3 12 

40 0 0.5 0.707107 1 3.200 3 12 

0.5000 10.7071068 128.0 

AVG.OFAP ~VG. OF SQ. TOTAL MJN:SEC 

IROOTAP'S , MINUTES· 

1--- ., 

rucK TEMP AT END OF TRAVERSE: 

-1~ 

DEG.F 1------- I 

VlINIMUM OF 120 MINUTES IS REQUIRED. 

=-=~-~ I I ------ ---~, - --- ~-- I i I 
.. -

Raw Test Data 

Test Date: 

Tank Number: 

Test Number: 

Temperature of sampling stream: .,' 

Gas Meter reading( start): .,,-rt 

Gas Meter reading (end): 

Total gas volume captured: 

Length of time of test: 

Ampere setting on rectifier: 

11-25·97 

5&6 

lof3 

630 F 

326.38 

388.395 

62.0 fe 

160 min. 

5- 1750 6- 2000 

Volt setting on rectifier: 5- 7.5 6- 7.0 

Non-resettable amphour meter reading(start): 5- 615007 6- 774831 

Non-resettable amphour meter reading (end): 5- 621315 6- 780104 

Hourly amphour rate: 5- 1977 6- 2366 amps/hour 

Rolling 12 month ampere average: 5- 1356 6· 1541 amps/ hour 

Bnrometric Pressure: 

Total Chrome captured: 0.077 mgIL 

Total Liquid volume from impingers : 

Vacuum gage reading from impinger system: 

Calculations 

Sample # 1 

(0.083)-(0.006)= 0.077 mglL 

(0.077mgll)(0.300L)= 0.0231 mg 

( 23.1)(63 +460) 

(499.8)(1.0003)(62.0)(29.85) 

= 12081.3 

925257.4 

29.85 in Hg 

300 ml 

27 

0.0231 mg 

=0.013 mgldscm 
Raw Test Data 

Test Date: 11-25-97 

Tank Number: 5&6 

Test Number: 20f3 

Temperature of sampling stream: 66u F 

Gas Meter reading( start): 388.50 

Gas Meter reading (end): 450.8 

Total gas volume captured: 62.3 re 

Length of time of test: 144 min. 

Ampere setting on rectifier: 5-1600 

Volt setting on rectifier: 5-7.0 

Non-resettable amphour meter reading(start): 5- 621315 

Non-resettable amphour meter reading (end): 5- 627135 

Hourly amphour rate: 5- 2425 

Rolling 12 month ampere average: 5- 1356 

6- 2000 

6-7.0 

6- 780104 

6-785224 

6- 2133 amps/hour 

6- 1541 amps/ hour 

Barometric Pressure: 29.85 in Hg 

Total Chrome captured: 0.034 mglL 

Total Liquid volume from impingers : 

Vacuum gage reading from impinger system: 

Calculations 

Sample # 2 

(0.040)-(0.006)= 0.034 mgIL ., (0.034mgll)(0.250L)= 0.~85mg 

250 ml 

27 

0.0085 mg 

(8.5)(66 +460) ___ _ = 4471.0 =0.005 mgldscm 

(499.8)(1.0003)(62.3)(29.85) 929734.4 
, . 

Raw Test Data 

Test Date: 

Tank Number: 

Test Number: 

Temperature of sampling stream: 

Gas Meter reading( start): 

Gas Meter reading (end): 

Total gas volume captured: 

Length of time of test: 

Ampere setting on rectifier: 

11-25-97 

5&6 

30f3 

60°F 

451.10 

513.6 

62.5 fe 

144 min. 

5- 1600 6- 2000 

Volt setting on rectifier:., 5- 7.0 6- 7.0 

#- Non-resettable amphour meter'reading(start): 5- 627135 6- 785224 

Non-resettable amphour meter reading (end): 5- 632625 6- 790474 

Hourly amphour rate: 5- 2288 6- 2187 amps/hour 

Rolling 12 month ampere average: 5- 1356 6- 1541 amps/ hour 

Barometric Pressure: 

Total Chrome captured: 0.042 mg/L 

Total Liquid volume from impingers : 

Vacuum gage reading from impinger system: 

Calculations 

Sample # 3 

(0.048)-(0.006)= 0.042 mglL 

(0.042mgll)(0.310L)= 0.0130mg 

29.85 in Hg 

310 ml 

27 

0.0130 mg 

(13.0)(60 +460) ___ _ = 6760.0 =0.007 mgldscm 

(499.8)(1.0003)(62.5)(29.85) 932719.1 
AIRTEST5&6 -1 

TRAVERSE WORKSHEET Tank 5 & 6 1 1 

TRAVERSE CYCLONIC 6P SQUARE S"i<. OF 6P SR OF 6P Minute 

POINT FLOW FROM ROOlit' AVG.OF AVGSMP 1&1 

# ANGLE MANOMETER 6P ilP SQ.RT X3 Min Seconds 

1 0 0.2 0.447214 1 3.000 3 0 --------'-----

2 0 0.2 0.447214 1 3.000 3 0 

3 0 0.2 0.447214 1 3.000 3 0 

4 0 0.2 0.447214 1 3.000 3 0 '---_. -- -- S 0 0.2 0.447214 1 3.000 3 0 --, 6 0 0.2 0.447214 1 3.000 3 0 

7 0 0.2 0.447214 1 3.000 3 -.~ 0 - --- -++--- .---- -_ .. -- . ---- -+- - _ .. -- -- -- ---- .-~- - .~ .- -- -- '--'--3 . ------ 8 0 0.2 0.447214 1 3.000 0 

9 0 0.2 0.447214 1 3.000 3 0 

10 0 0.2 0.447214 1 3.000 3 0 

11 0 0.2 0.447214 1 3.000 3 0 

12 0 0.2 0.447214 1 3.000 3 0 - 13 0 0.2 0.447214 1 3.000 3 0 --1-4----..- 0 0.2 0.447214 1 3.000 3 0 

15 0 0.2 0.447214 1 3.000 3 0 

16 0 0.2 0.447214 1 3.000 3 0 

17 0 0.2 0.447214 1 3.000 3 0 

18 0 0.2 0.447214 1 3.000 3 0 

19 0 0.2 0.447214 1 3.000 3 0 

20 0 0.2 0.447214 1 3.000 3 0 

21 0 0.2 0.447214 1 3.000 3 0 

22 0 0.2 0.447214 1 3.000 3 0 

23 0 0.2 0.447214 1 3.000 3 0 

:--.. 24 0 0.2 0.447214 1 3.000 3 0 

25 0 0.2 0.447214 1 3.000 3 0 -'"-------- 26 0 I 0.2 0.447214 1 3.000 3 0 

27 0 0.2 0.447214 1 3.000 3 0 

28 0 0.2 0.447214 1 3.000 3 0 

29 0 0.2 0.447214 1 3.000 3 0 - 30 0 0.2 0.447214 1 3.000 3 0 1----

31 0 0.2 0.447214 1 3.000 3 0 

32 I 0 0.2 0.447214 1 3.000 3 0 

33 0 0.2 0.447214 1 3.000 3 0 .. _._.-. ---t--- -.. 34 0 0.2 0.44721:4 ~ ... ' 1 3.000 3 0 

35 0 0.2 0.447211411 1 3.000 3 0 

36 0 0.2 0.447214 1 3.000 3 0 

37 0 0.2 0.447214 1 3.000 3 0 -- ---38 0 0.2 0.447214 1 3.000 3 0 

39 0 0.2 0.447214 1 3.000 3 0 

40 0 0.2 0.447214 1 3.000 3 0 

41 0 0.2 0.447214 1 3.000 3 0 

42 0 0.2 0.447214 1 3.000 3 0 

43 0 0.2 0.447214 1 3.000 3 0 

44 0 0.2 0.447214 1 3.000 3 0 

45 0 0.2 0.447214 1 3.000 3 0 

46 0 0.2 0.447214 1 3.000 3 0 

47 0 0.2 0.447214 1 3.000 3 0 

--_._-. 

48 0 0.2 0.447214 1 3.000 3 0 --.. 

--- -- --.... --_. _. 0.2000 0.4472136 144.0 -,_ •• + 

~O(!U UlG...OF SQ. TOTAL MIN:SEC 

ROOT 6P'S MINUTES· , 
Report To: 

TESTING - CONSULTING 

Mr. Victor Koerner 

Economy Plating, Inc. 

2350 North Elston Avenue 

Chicago IL 60614 

Timothv E. Denhof 

Laboratorv Manager 

3158 S. Kolin Ave. 

Chicago IL 60623·4889 

Phone: 773·254·2406 

Ex tension 301 8 

FAX: 773·254·6661 

LAt- I 

P. O. Number: 02183 

Project Type: Stack Testing 

Project Number: 

Project Inception: 

Report Date: 

1997-120257 

12-12-97 

12-22-97 

IDENTifiCATION OF MATERIAL: 

Three (3) samples, identified below. 

PROCEDURE: 

All analyses were performed in accordance with the EPAIIEPA approved test 

procedures as specified in 40 CFR, Part 60, Method 306A. 

Scientific Control Labs, Inc., is a certified laboratory for analysis of potable water 

(IEPA Cert. #100183), and a certified laboratory for wastewater analysis (State of 

Washington Cert. #C165, State of Wisconsin DNR #998091930). This means we 

have a quality control program in effect and that this quality control program is 

monitored and reviewed annually by the certifying agencies. 

RESULTS: 

Sample 10: 

SAMPLE #1 TANK 4 

SAMPLE #2 TANK 4 

SAMPLE #3 TANK 4 

QUALITY CONTROL DATA: 

Concentration in ppm (mg/U 

TOTAL CHROMIUM VOLUME (mil 

--. 0.109 268 

0.080 350 

0.117 325 

The samples were analyzed by Graphite Furnace Atomic Absorption for detection of 

Total Chromium. 

TED:amo 

CERTIFICATION: 

Sample: 

Duplicate: 

Spike: 

LEB: 

LRB: 

21.86 ppb 

20.89 ppb = 

32.87 ppb = 

10.10 ppb = 

1.08 ppb = 

relative:: percent difference 

110.1 % spike recovery 

101.0% recovery 

< minimum detection limit 

= 4.54% 

The above statements and report were subscribed d sworn to before me this 

TWENTY-SECOND day of DECEMBER, 1997. 

adh~~~ ~- Notar~Y"PUblT~-r·:-I~,·'l (.:r~/\ . ~ . l. .. r' . v_ 

:\ ArJi·;idJi··Ji-: O~JlA' IN 

~ t,,· 'J'I'" ""1'01111"0;5 .,' ". to.!,' I I,.~ .c, ..... thU fl I 

," . . , < :."',1 C !I'.: .', "'d .• :;;In:$ 11/1 3/99:~ 

NlHt:. II I~ our polley 10 kt:cp '()Plt:~ uf re:purlS for SIX momhs. Tht: dala IS kepI on file: for up III Ihree·years:· Samples-(jf ilpjlllclibletn'n!.te"r'for 

Ihrc:c: weeks, Samples that arc: hazanluus will bt: returned 10 the clienl. If this policy poses a difficulty, please cunract us to l1Iake other 

arrangelllcnts. If re:prudu.:c:d, our rc:pon, I1IUSI be: rt:producc:d complelely. Any unauthoflzed altt:ratioll of thiS rcpon invalidales Ihe cOIllt:nt. 
~ /jf\

I ... 

Report To: 

TESTING CONSULTING 

Mr. Victor Koerner 

Economy Plating, Inc. 

2350 North Elston Avenue 

Chicago IL 60614 

Swnuel Wright 

Labolelory Manegor 

3168 S. Kolin Avo. 

Chicago IL 60623·4889 

Phono: 773·264-2408 

Exton.ion 3041 

FAX: 773·264-8881 

P. O. Number: 02183 Project Number: 1997-120025 

Project Inception: 12-01 -97 

Project Type: Stack Testing Report Date: 12-10-97 

IDENTIFICATION OF MATERIAL: 

Three (3) samples, identified below. 

PROCEDURE: 

,All analyses were performed in accordance with the EPA/IEPA approved test 

'procedures as specified in 40 CFR, Part 60, Method 306A . . - Scientific Control Labs, Inc., i~"'~ertified laboratory for analysis of potable water 

(lEPA Cert. #100183), and a certified laboratory for wastewater analysis (State of 

Washington Cert. #C165, State of Wisconsin DNR #998091930). This means we 

have a quality control program in effect and that this quality control program is 

monitored and reviewed annually by the certifying agencies. 

RESULTS: Concentration in ppm (mg/U 

Sample ,p; TOTAL CHROMIUM VOLUME (rol) 

SAMPLE #1 TANK 1 

SAMPLE #2 TANK 1 

SAMPLE #3 TANK 1 

QUALITY CONTROL PATA: 

0.068 310 

0.083 290 

0.088 236 

The samples were analyzed by Graphite Furnace Atomic Absorption for detection 

of Total Chromium. 

TED:clm 

CERTIFICATION: 

Sample: 10.09 ppb 

Duplicate: 10.99 ppb = relative percent difference = 8.54% 

Spike: 20.46 ppb = 103.7% spike recovery 

LFB: 10.53 ppb = 105.3% recovery 

LRB: 1.74 ppb = < minimum detection limit 

Respectfully sub 'tted, 

SCIENTIFI~ T ABORATORIES, IN~ 

By __ ~~~~~~~~~~ ____ ___ 

The above statements and report were subscribed 

TENTH day of DECEMBER, 1997. 

, . 

Note: II il our policy 10 keep !:epic. ofrepor1l (or lix molllh •. 1bc lei (if applieablc) arc kepi (~.J'97 three weeu. Sample.lhat arc bazardoul will be rctumed I,":~iii~ clieBl. If !hi. policy pOK' • difficullY, pleaac &loolact UI 10 make other 

arranjlcQlCRIJ. If reproduced, our report, mull be ?ed compJeltl)'. An)' unaulborized aIltratioD or \hie report invalidalC.thc conteBl. 
~;'ent;lic CONTROLlJILABORATORIES. INC. 

Samuol Wright 

laboratory Manager 

3158 S, Kolin AVe, 

Chicago IL 60623-4889 

Phono: 773·254-2408 

Extenlllon 3041 

FAX: 773·264-6681 

Report To: 

TESTING - CONSULTING 

Mr. Victor Koerner 

Economy Plating, Inc. 

2350 North Elston Avenue 

Chicago IL 60614 

Project Number: 1997-110395 

P. O. Number: 02110 

Project Type: Stack Testing 

Project Inception: 11-26-97 

Report Date: 12-10-97 

IDENTIFICATION OF MATERIAL: 

Four (4) samples, identified below. 

PROCEDURE: 

• All analyses were performed in accordance with the EPA/I EPA approved test 

'procedures as specified in 40 CFR, Part 60, Method 306A. 

Scientific Control Labs, Inc., is a certified laboratory for analysis of potable water 

(lEPA Cert. #100183)' and a certified laboratory for wastewater analysis (State of 

Washington Cert. #C165, State of Wisconsin DNR #998091930). This means we 

have a quality control program in effect and that this quality control program is 

monitored and reviewed annually by the certifying agencies. 

RESULTS: 

Sample 10: 

SAMPLE #1 BLANK 

SAMPLE #2 TANK 5-6 

SAMPLE #3 TANK 5-6 

SAMPLE #4 TANK 5-6 

QUALITY CONTROL DATA: 

Concentration In ppm {mglU 

TOTAL CHROMIUM VOLUME (rol) 

0.006 325 

0.083 300 .. -- 0.040 250 if"' 0.048 310 

The samples were analyzed by Graphite Furnace Atomic Absorption for detection 

of Total Chromium. 

Sample: 

Duplicate: 

Spike: 

LFB: 

LRB: 

10.09 ppb 

10.99 ppb - 20.46 ppb = 

10.53 ppb = 

1.74 ppb = 

relative percent difference 

103.7% spike recovery 

105.3% recovery 

< minimum detection limit 

Respectfully sub 'tted, 

SCIENTIFIC AD 

= 8.54% 

TED:clm 

CERTIFICATION; 

By' __ ~~~~~~~~==~~ __ 

The above statements and report were subscribed 

TENTH day of DECEMBER, 1997. 
DATE 7-2-96 CUSTOMER Economy Plating 

WO # 2668 METHOD 306-A-CALlBRAIlON 

ROCKWELL 175-5 SERIAL # ___ 3_0_62_0 ___ _ 

TEMP. = 69 F. 

: y= Vs x Ys (460 + T . \ Pb 

Vt (J1H.. + Pb )( 460+ T) 

13.6 

Pb= 29.85 

FLOW RATE == 75 CFM OVERALLAVERAGE-Y 1.0003 

CALIBRATION PERFORMED ON AMERICAN BELL PROVER # 2989, 

CERTIFICATION DATED 10-23-95, CERTIFIED TO 0 00% ERROR, AND 

TRACEABLE TO THE N.I.S.T.. 

CALIBRATION OF ORJFICE -

PIVI = 

TI 

P2 V2 

T2 

PI'" Current B-arometric Pressure 

V)= Volume of Dry Gas Meter x (Ym) 

TI .... Temp. of Meler +460 

P2= 29.92" Hg 

V - To Find 

T2= 68 F. + 460 "- 528 

VOLUME FOR 10 MIN.= 

7.3955 seE 

By Measurement Controls, Inc 
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System Description: 

1 ea 10,000 dm ventilation and 4-stagp chromic acid IIIIc;t spparator system: 

Stage #U: UP FRONT hood deillist p8d 

Stage #1: 

Stage #2: 

12 -layer Kimre B·G( IN composite IlIPc;h demist pad 

12 - layer Kimre B-GON coalesce p"d 

Stage #3: 6- layer Kimre B-Gone reintrainment c;ppmalor pad 

including CrHS 10000 !=\epa rat or, steel fFIII. slflck. dall1p0f~. Ir~circulation pump, ,. UP FRONT hoods.~~d control system. tI~· 

Motor star1er. disconnect and plulllbin~1 "I)fll~ lIpS In fl p~11 wnlpr and drains by 

othels 

Quofe#: 

Customer PO#: 

Q1188R1 

Verbal 

.. - .,' -'. ~'," 

Op.eratill9.-CornJ)on.ents~ 

Equipment. _____ ..MQue! # .. Serial # 

UP FRONT hoods downdraft'IFIlpi ;:11 2 per tHill' 

Scrubbpr CrHS 10000 7)25 flIc)7 Date oCMfg. 

Fan 

Pump 

032·30-BCP:-i 9 i048Hr:llll! 

100001'1111 @ 85" 

20 hp 230/460/(i(}/.1 

Arranqp.IIIGllt #9, Clac;!=: II. 

Sleel willi standard C(lrll"l~1 

VibratloJl isolators: RVU-2-fl 

Belts ()), 5VX840 

EH 1 1/2-2S(: II~) () I.X '·;('>,-11 :11165 

20 gpm @ 6:' fl, Vilon 0 '111 II! 

1585 rpm 

256T frame 

Controls Magnellelic gl-lIl!-l8 # 2010 ar.:III!'S slPlges #1, #2 & #3 

". - Magnehelic gml!-le II 2005 across slClge #2 

i'l./ Indicator lamp pump 011 

Chicflgo Plastic Systems Inc. 

Opemlrng and Mailltenance MClnual I'::ql~ 1 

10/20/97 

7n5SPEC.wP~ 
. 

. 

.... .. 

~" 

Stage #2 

,. 

Stage #3 

... if~·· 

" .. --. 

.' .-

AlI~jliary . .compon~nts.;. 

Irttake duct manifold 

Pac:killq 

TypE' 

Size 

r- ace 1\, PH 

Velllnly 

SprClY Nozzles: 

NumlJ('" 

Flow r,gl(' 

Valve 

Paci<"lq 

Type. 

Size 

FAce 1\, (·';1 

Velocrly 

S pr <ly f\Jn7ZIf~5 

Nurlll'PI 

Flow lAir:. 

Valvp 

Vi'''If~ 

1:' n/q(l 

• c;, 'ppn, t frame 

I~ I 1I~)";ow: 53 112" + 3/4% 

"'''I 'P' lit frame; 

".'~" v h:~" OD 

11'," x !i!j" 10 (open) 

') 1"""('(, 

I ; c:;, I " 

r'::l1 IP'Il 

n· 'I(~ 11-1 fF8FC 

IJ 

I1II yprnlsf (5 gpm total) 

H. nkert :340-C-3/4-B-BR-

:1/1 ?'1/00-08-V-H-OOO 

wI lillie,. 3-way 

1':"'111=' 

(i \lftl7 

(; \ 1/')" x 53 1/2" + 3/4% 

~'rl sq n ~Ill) fPlIl 

B~>Ir~ ~IB fF14FC 

,1 

I I I 9lHn/sf (20 gpm total) 

H, II KPII 340-C-3/4-S-BR-

:"t1 ?t1/50-08-V-H-OOO 

w/lill'Pl, 3-way 

rreestanding stack With vplrll'lly r.r:lp and ':::111l1'1i1l!., ports 

UP FRONT hoods for 96" 11111'1 t811ks 

ChiCCtgo Plastic Systems Inc. 

Opel ating and Maintenance Manu~1 

10/17/: T 

7n'iSPEC.~;· s 
...,~.-- . 

Installation Rew.uirements 

Elec tri:a I: ran: 208-230/460/3/60 ~)II IIp ~"I.' 1 ( lperating amps 

rump: 208-230/460/3/60 ) 'III r. 11 FilII Load Amps 

System: 230 vac 

Spray controls: 24 VFW 

Level controls: 120 vnc 

. Plumbing: Stage #1 : pump: 20 gplrl 

2" suction, 1 I U" discharge 

Drain back to recirculation Inllk: 2" 

Fresh water inlet: 1/2" PV<; wi solenoid 

Waste: Existing recirculation tank 

Other: Hecommend 01 water 

Chemical Reagent Feed: StagA II) & #3: frpsh waler 

Recir clIl;ltion tank' fr p!;h w~ler 

.. ~-. '-

O.th~r. System In~ation: 

System capacity specified by ECorl()IOY Plating. rl::lll to add third tank with 

hoods in the future. 

Chicago Plastic Systems Inc. 

Operc:lting and Maintenance Manual Page 4 

10/17/97 

7225SPECWPS 
Flow meter- r~Yrln 11p-ICO #~)fun-lt;l, 

!,IllysuI fOlle/PVC, 65 gpm full scale 

Level control r II lwlll Ie AP t 3 -/ 12U switch wI compact 

'Pl;)y. U<30 SE'c-llwls lime delay, 120 vae 

Sensor: 

Valve: 

nF capacitallce, PF A material 

nlHkerl 2BO-A-ll? F- RR-1/2-120/S0-08-

I II 1)00, /'-WflY 

Spray timers () r. Illilll/les 

Serubb!=!rISeparator: WH 10000 

Rice: ·Face: 

,,7'uverall: 

~;:\ 1/2" x 53 1/)" 

'):1 1/2"W x 63 J I;'>". I x 84"L box 

~-ll~ 112" W x 69 10" J-I x 146 1/2" L o/a 

Maximum Operating T emppl'~llIre 

Slage #U 

Stage #1 

UP FR( H-J I hood 

Pack;IIq 

Type: 

Size' 

PAcklll!J 

Type 

Size: 

Face AI f~t1 

Velocity 

Spray N07Zles 

Numb(~r 

Flow mit) 

Chicago Plastic Systems Inc. 

Opemting and Main~;'/~imee Manual 

1 )11" r 

Killlre 

t1 :\ 11~)'" 

t -;\ 11~r7 

()" y ~In" 

1(11 HIP. 

:~ : \ 1/~/f 

'I I r.mr; 

1\ 111C)(i 

1 . \ 119/f 

G:1 II/." x 53 1/2" + 3/4% 

20 <;'1 ft 

501l fpm 

n(~I~ 3/(1 I F20FC 

4 

;.> qpll1/sf (40 ypm total) 

10/17/97 

7225SPECWPS 
. ..., 

. 

. 

Stage #2 

Stage #3 

.•. --- ~. 

Au~iliary . .cOInpone.nts; 

Intake duct manifold 

Pac:kirHI 

Type 

Size 

Face 1\11'8 

Velocilv 

SprflY Nozzles: 

Numbpi 

Flow rAI(~ 

Valve 

Packillq 

Type. 

Size' 

F neA 1\1 ('~rl 

VeloCity 

Spmy NIl7ZIf~s 

Nurllhpi 

Flow mt(·~ 

Valvf" 

l'.illllP 

I;,' l\/tll, 

I "'Ippnl t frame 

I~\ IIr x 53 1/2" + 3/4% 

t;11f'pnr I frame; 

r,T' v n:~" 00 

11 (," x 1;5" 10 (open) 

') I'IPI'P 

, .. <;11 " 

r,::n f 1'111 

npln 1/-1 fFBFC 

t1 

1/1

\ gprn/sf (5 gpm total) 

Rllrkerl :340-C-3/4-8-BR-

:1/'1 ?-1mO-08-V-J-I-000 

w/lilllE'I, 3-way 

VIIIHP 

(\\if()7 

r,:\ II')" x 53 1/2" + 3/4% 

~'f) !;q rt 

~()I) fplll 

B~*~ 1m fF14FC 

,I 

I II 9PITl/sf (20 gpm total) 

n'll kpi I :340-C-3/4-8-BR-

:\/-1 ?1\/60-08-V-H-OOO 

w/lilllPI, 3-way 

Freestanding stack with vp.IIl,·ily CHP and ":lllll'lin~~ ports 

UP FRONT hoods for 96" IOIlC! tallKs 

Chicago Plastic Systems Inc. 

Opel ating and Maintenance Manuc:ll 

10/17/:.1 

7?2'iSPEC.Vv.- S 
..,r .. -. Installation Rev.uirements 

Electrical: Fan: 208-230/460/3/60 ~)O hI' rl-1l)1 Uperating amps 

Pump: 208-230/460/3/60 ) "') r-; 11 F, III Load Amps 

System: 230 vac 

Spray controls: 24 v;;w 

Level controls: 120 V:1C 

. Plumbing: Stage #1: pump: 20 gp' n 

2" suction, 1 II)" discharge 

Drain back to recirculation I;mk: 2" 

Fresh water inlet: 1/2" PVC wi solenoid 

Waste: Existing recirculation tank 

Oth~r: Hecommend 01 water 

Chemical Reagent Feed: Stag~~ it) & #3. hpsh water 

RecirclIt;'ltion tank: fl p~h wr:tter . ,i'~ 

.~-

ill: Other. System Inf~rmation: 

System capacity specified by Economy Plating rlr:m to add third tank with 

hoods in the future . 

~, .. ~' 

..,-.. -

Chicago Plastic Systems Inc. 

Operating and Maintenance Manual Page 4 

10/17/97 

7225SPECWPS 
Chicago. Plastic Systems, Inc. 

. ~. 

I 

z '--- Air Flow --

Stage #1 

.- -- ' .. 

- - - - - \ - - . \- - -

Staoe #2 

'" 

, -

i ~ 

. , 

B 

/ 

/ - _ <ft...:-_ 

• - - - ..... 

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-l 

-u \

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D~a::1s -- ---::-

Irrigation 

Stage #1: 

Stage #2: 

(;L_

g_ .J,J,",. 

vld' t:::; ++.:J. 

l 

---'-'-"-- -----.-.---.-.. ---.----. 

Continuous vw'ith dilute ch'rome rinse 

Short duration rinse every 2-4 hours with fresh water 

Short duration rinse every 12-24 hour~ \· .. ith fresh water 

CrHS Chrome Separator 

C"j 

~ 

,~ 

0-... 

~ 

.-=><.,. ~ 

~ 
Buss gars 

------- 18" dia tjUC! 

16112" 

.- _ .. t--~ 

• • • .. ·~:'I 

tc-f-' --ol-.f--r-l . . . . n-... rl· .. -n --r 

I!, _ -i _ , 

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1 

.- ..... -

. E~d View 

.. r[J'~-'" - . .. -..... - '. ! . 

- .. ! . , --:''' 

.. --.-.-. - .-

-_.- UP FRONT hoed 

C:~:c::go Plastic SY,~:ms Inc. 

J7225b ~/16:",( 

Economy P!aur.g 
01':''' ~ -

.------~ • 

" 

-

Chicago Plastic Systems Inc. 

J7225 7/21197 

Economy Plating 

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Chrome Plating Tank 

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Chicago Plastic Systems Inc . 

Q1188R1 11/25/96 

Economy Plating 

End View 
.' 

..,' .. -

Moisture Extractor . Moisture Exlractor is effective on entrained water and other 

relatively heavy. aIrborne particles. Moisture removal is accomplished centrifugally as the aIr passes,.tMough a set of stationary 

blades. At design air flow a O.75~ s;ic pressure drop is required. 

Moisture Extractor is constructed of PVC and is complete 

with a drain coupling and spray system for periodic wash down. 

This unit is designed for installation in a vertical run of duct. 

DIMENSIONS IN INCHES 

A I 10 12 14 " 18 20 22 24 26 2a 30 32 34 

B 14 U 20 22 24 1(21,> 3D 32 34 3' 31 41 46 4. 

F 29 

..... 34 40 

• 

36 la 4& 42 44 46 4a 54 6G' 

S2 54 57 60 63 66 69 7' 16 

46 52 56 
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Cover 

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End View 

1811 

UP FRONT Hood 

Chicago Plastic Systems Inc. 

Q1188R1 11/25/96 

Economy Plating 
.. 

Moisture Extractor . Moisture Extractor is effective on entrained water and other 

relatively heavy. airborne particles. Moisture removal is accom· 

pllshed centrifugally as the air passes .• tI'tJough a set of stationary 

blades. At design air flow a 0.75" s;;'c pressure drop is required. 

. Moisture Extractor is co",structed of PVC and is complete 

with a drain coupling and spray system for periodic wash down. 

This unit Is designed for installation in 8 vertical run of duct. 

OIM~N810N8 IN INCHES 

A • 10 12 14 U 11 20 22 24 26 28 30 32 34 

B 14 U 20 22 24 i(il) 30 32 34 36 31 41 46 41 

F 29 

.,..; 

34 40 

• 

36 38 40 42 44 46 48 54 60' 

52 54 57 60 63 " 69 16 16 

46 52 S6 
Tank # 1 

Chrome 

plati ng 

Tank # oJ. 

Chrome plating 

Tank # 5 

Ch rome plating 

Tank # 6 

Chrome plating 

¢ 

¢ 

Composite 

Mesh Pad 

Composite 

Mesh Pad 

Up f ront 

Composite 

mesh pad 

Up Front 

Composite 

mesh pad 

Mist 

Eliminator 

Mist 

Eliminator 

3 stage 

composite 

mesh pad 

¢ 

Exhaust 

Blower 

Exhaust 

Blower 

Exhaust 

Blower 

Exhaust 

Stack 

Exhaust 

Stack 

Exhaust 

Stack 

Air Flow Diagram 

(Process) 
Chicago Plastic Systmes 

11/6/96 . MACT Chrome Separation 

Concept Diagram 

UP FRONT hood 

Duct from hoods to 

chrome separator 

Minimum ducme 

oCt\lmulatttln . 

hoods and ducts I 

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Pre-filter with - --, 

Kimre B·GON - UP FRONT 

Mist Eliminator hood(S) , -- on 

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. ---ft------.-

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f 

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\ 

-----~---: 

Composite Mesh Pad 

returns chrome mist 

to plating tank 

ChlQmC 

Plal,r.g 

Tan" 

3-Stage Chrome Separator 

enr"", .. R".. 

Tanl( 

-- Fan 

--._ ... ----- 1'--7 

\ 

,.- - --- --- Fresh water through programmable 

timer valves irrigates stages #2 & #3 

Chrome separator 

irrigation system uses 

chrome rinse for 1st stage 
/>-J6 

Exhaust Opening Locations Plot 

;i4l~~~=J~+----__ =-roof top location of # 1 exhaust. 

roof top location 

of # 4 exhaust 

23.50 

hldc 

omce 

B 

Economy Plating, Inc. 

2350 N. Elston 

Cbicago, IL 60614 

125 ft. 

roof top location 

of # 5 & 6 exhaust 

and 3 stage CMP 

system. 
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I<Inn B-GON \. 

Mist Eliminator 

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.~- Composite Mash Pad 

retums chrome mist 

10 plating tank 

Centrifical 

Mist 

Eliminator 

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1

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Fan 
I ~ alle~ ~I 75ft _ 

.El parking CD lot 

2350 

bldg 

office 

B 

Economy Plating, Inc. 

2350 N. Elston 

Chicago, IL 60614 

125 ft. 
,/<'Ol-L-/ 

Sheet I 

'.~ Roiling 11 monlh DlllpCl"agC UIC38c 

JAN FEB MAR. APR MAY lUL AUG SEP OCT NOV DEC TOTAL AVERAGE AVERAGE Plus 

PER MONTI! PERIIOUR 25°& 

TANK I 62797 86100 38667 41275 302315 287035 432610 2-13411 306972 291144 47308 37622 2189956 336916 m 673 

TANK 4 264708 31lS00 295067 427700 327800 279300 343900 483111 2SS04S 509500 283600 314900 -1098131 630482 1007 1259 

TANKS 515498 81S236 645850 407568 452815 373408 362499 2S6403 281908 865620 610119 S06943 e 849011 1156 1695 

/ 

TANK 6 678901 445517 483981 511342 519199 540629 530919 4476S7 263880 619386 614778 -I9J7:!7 6269982 964613 1541 19:!6 

TANIO 

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