Clean Air EngineeringCAE Project No: 5815-1 SUMMARY INTRODUCTION Clean Air Engineering was...
Transcript of Clean Air EngineeringCAE Project No: 5815-1 SUMMARY INTRODUCTION Clean Air Engineering was...
Clean Air Engineering
REPORT ONVOLATILE ORGANICS TESTING
Performed for:VERTAC SITE CONTRACTORS
Conducted at:VERTAC CHEMICAL CORPORATION
SUPERFUND SITEJACKSONVILLE, ARKANSAS
CAE Project No: 5815-1December 1 1 , 1 9 9 1
VOLUME I
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
CONTENTS
VOLUME I
1. SUMMARYINTRODUCTIONSUMMARY OF TEST RESULTS
2. DESCRIPTION OF INSTALLATION
3. SUMMARY OF PROCEDURESSAMPLING PROCEDURESANALYTICAL PROCEDURESQUALITY CONTROL PROCEDURES
4. COMMENTS
5. APPENDIXNOMENCLATURESAMPLE CALCULATIONSPARAMETERSCALIBRATION DATAFIELD DATACHAIN OF CUSTODY
VOLUME II
5. APPENDIXLABORATORY DATA
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
SUMMARY
INTRODUCTION
Clean Air Engineering was contracted by Vertac Site Contractors to determinethe levels of volatile organics emissions at the Vertac Chemical CorporationSuperfund site located in Jacksonville, Arkansas in support of their trial bum.
The testing took place at the Stack on October 10, 1991. Coordinating the fieldtesting were;
R. Apa - Vertac Site ContractorsP. Schwindt - US EPAM. McCorkle • State of Arkansas Department of Pollution
Control and EcologyC. Young - Independent Quality Assurance AdvisorJ. Chapman - Clean Air Engineering
SUMMARY OF TEST RESULTS
The test conditions and results of analysis are presented in Tables 1 A through1 C on pages 1 -2 through 1 -4.
To the best of our knowledge, the data presented in this report are accurateand complete.
Respectfully submitted,
CLEAN AIR ENGINEERING
- ' " ' . "h,'-^^ .A/;;-^•''/ ' •• /7 • / /Kimberiy Kempt L'Manager, Technical Communications
John ChapmanVice PresidentResearch and Development
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
SW-846 Method 00Volatile OrganlcsStack
Run No.1
Date (1991)Start Time (approx.)Stop Time (approx.)
Gas Conditions2
Temperature (°F)Moisture (volume %)Oz (dry voluma %)COz (dry volume %)
Volumetric Flow Rate2acfmdscim
Volatile Organic*
Chloromethane ^o ^ug/dscmppbIb/hr
Bromomethane iug/dscmppbIb/hr
Methylene Chloride '''•,.--:ug/dscmppbIb/hr -^.•.
Acetone 1 '•'•ug/dscmppbIb/hr
1,1-Dichloroethene 7 "ug/dscmppbIb/hr \ . . • > • - -
Chloroform " •ug/dscmppbIb/hr
"* Run 3 samples were2 The gas conditions a
sampling train.ND indicates that the o
the average.
lary of Test Re
1
October 102:19 PM2:29 PM
20143.01 1 . 17.9
28,10011 ,940
^1065.0
5074.76E-02
(<0,205) ND(<0)
(<8.16E-07)..••
1717.5486
1.32E-06
310.2129
2.00E-03^'A
21.75
2.52E-05
386.978
3.14E-05
not analyzed, seend volumetric flow
ompound was not
suits
2
October 10 C2:48 PM3:08 PM
20143.01 1 . 17.9
26,10011,940
218.9104
9.79E-03
5.61
4.63E-06
288.482
6.10E-06
9.44
1.02E-05
2.31
8.00E-08
78.516
6.64E-07
Comments, page 41.rate data was obtained f
detected. Non-detected
4
>ctober 103:56 PM4:16 PM
20143.01 1 . 17.9
26,10011,940
254.1121
1.14E-02
7.22
6.81 E-06
238.968
6.41 E-06
12.85
1.15E-05
3.61
1.72E-07
106.521
1.43E-06
rom the concurrent
values were not inc
Average
20143.01 1 . 17.9
26.10011,940
512.7244
2.29E-02
6.42
5.72E-06
748.3212
4.61 E-06
110 .846
6.72E-04
9.22
8.48E-06
190.638
1.12E-05
MM5
;luded in
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
SW-846 Method 0030Volatile OrganlcsStackRun No.1
Date (1991)Start Time (approx.)Stop Time (approx.)
pas Condltions2Temperature ("F)Moisture (volume %)Oz (dry volume %)COz (dry volume %)
Volumetric Flow Rate2
actmdscfm
Volatile Organic*Trichlorofluoromethane '
ug/dscmppbIb/hr
2-Butanona "- ' , .>• .pg/dscmppbIb/hr
1.1,1-Trlchloroethane v^;ug/dscmppbIb/hr
Carbon Tetrachloride ''^r'ug/dscmppbIb/hr
Bromdichloromethaneug/dscmppbIb/hr
Trichloroethene / r ' - . t / v^ug/dscm v
ppbIb/hr
1 Run 3 samples were no2 The gas conditions and
y of Test Re
i
October 102:19 PM2:29 PM
20143.01 1 . 17.9
26,10011,940
J" .' l'*-
47.98
6.94E-05
64.11 0
1.15E-05•'\
105.419
2.53 E-05i
67.21 1
2.65E-05
256.938
6.47E-05
3.8 E1
3.64E-06
t analyzed, seevolumetric flow
suits
2
October 102:48 PM3:08 PM
20143.01 1 . 17.9
26,10011,940
14.22
4.17E-06
(<0.154) ND(<0)
(<8.18E-09)
44.58
2.57E-08
52.18
8.68E-06
79.212 •
1.55E-05
4.01
1.19E-06
Comments, page 41.rate data was obtaine
4
October 103:56 PM4:16 PM
20143.01 1 . 17.9
26,10011,940
5.51
2.19E-06
(<0.570) ND(<0)
(<1.17E-08)
29.25
6.24 E-08
1 1 1 . 817
1.22E-05
115.217
4.82E-05
4.61
1.97E-06
d from the concurrc
Average
20143.01 1 . 17.9
26,10011,940
22.54
2.52E-05
64.110
1.15E-05
59.71 1
8.47E-06
77.012
1.58E-05
150.422
4.28E-05
4.11
2.27 E-06
Bnt MM5
1-3
r-0'.—r i00
sampling train.NO indicates that the compound was not detected. Non-detected values were not included in
the average.
•
3
1
October 102:19 PM2:29 PM
20143.01 1 . 17.9
26,10011,940
39.85
5.64E-07
5.12
7.62E-07
(<0.205) ND(<0)
(<3.92E-09)
2.7 E0
2.04E-09
13.74
1.37E-07
(<0.102) ND(<0)
(<5.25E-09)
! analyzed, see. volumetric flow
suits
2
October 102:48 PM3:08 PM
20143.01 1 . 17.9
26,10011,940
103.512
1.55E-06
3.01
1.17E-06
129.112
1.46E-06
5.11
2.46E-06
1.8 E0
3.52E-08
3.11
2.13E-08
Comments, page 41.rate data was obtaine
4
Octobsr 103:56 PM4:16 PM
20143.01 1 . 17.9
26,10011,940
161 .219
2.75E-06
3.91
2.38E-06
192.018
2.83E-06
5.41
3.92E-06
2.2 E1
4.44E-08
2.81
2.28E-08
d from the concurrent
Average
20143.01 1 . 1
7.9
26,10011.940
101.512
1.62E-06
4.01
1.44E-06
160.51 5
2.15E-06
4.41
2.13E-06
5.92
7.21 E-08
2.91
2.21 E-08
MM5
1-4
000
m00
pound was not detected. Non-detected values were not included in
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
DESCRIPTION OF INSTALLATION 2-1
Vertac Site Contractors operates a transportable rotary kiln thermaldestruction unit (TDU) which is used to destroy hazardous wastes. The TDUis custom built specifically to process and destroy 2,4-Dichloropnenoxyaceticacid (2,4-D) still bottom and pesticide waste material located at the VertacChemical Corporation superfund site. The primary components include arotary kiln (primary combustion chamber), a hot cyclone, an after burner(secondary combustion chamber), a spray dryer/quench tower, fourbaghouses, a venturi/baffle plate absorber, an induced draft fan and a stack.
The testing reported in this document was performed at the Stack.
A schematic of the process is shown below.
STACKSWL1HBPCHISi
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
SUMMARY OF PROCEDURES
SAMPLING PROCEDURES
The sampling followed procedures as detailed in U.S. Environmental ProtectionAgency (EPA) Solid Waste Method 0030. This method can be referenced inSW-846 "Test Methods for Evaluating Solid Waste, Volume 1A: Field Manualfor Physical/Chemical Methods." This methods is titled:
• SW-846 0030 — "Volatile Organics Sampling Train."
The sampling apparatus is shown in Fig 1 on page 3-2. The samplingequipment was designed and manufactured by Nutech Inc. and Clean AirEngineering to meet U.S. EPA standards. All equipment was calibrated at theClean Air Engineering laboratory prior to shipment to the job site.
Sampling Locations
The Stack has two ports. For volatile organics sampling a single point near thecenter of the stack was sampled for 20 minutes.
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
Figure 1
The SW-846 Method 0030 sampling apparatus is shown.
CONDENSER
PARTICULATEFILTER THERAOCOUPLE EXHAUST
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
SUMMARY OF PROCEDURES (Continued)
ANALYTICAL PROCEDURES
Volatile OrganicsThe VOST tubes were analyzed according to the guidelines of SW-846Methods 8240 and 5040. The contents of the sorbent cartridges were spikedwith internal and surrogate standards and thermally desorbed with a purge gasprior to analysis. The volatile organics were separated by temperature-programmed gas chromatography and detected by mass spectrometry, whichwas used to provide both qualitative and quantitative information.
QUALITY CONTROL PROCEDURES
Quality control procedures for all aspects of field sampling; samplepreservation and holding time; reagent quality; analytical method; analysttraining and safety; and instrument cleaning, calibration and safety werefollowed. These procedures are generally consistent with EPA guidelinesdocumented in "Quality Assurance Manuals for Air Pollution MeasurementSystems," Vol 3, "Stationary Source Specific Methods" (EPA-600/4-77-027b).
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
COMMENTS
The Run 3 samples were not analyzed as the data was lost during analysisdue to an electrical storm.
No deviations from standard U.S. EPA testing procedures were noted.
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
APPENDIX
NOMENCLATURESAMPLE CALCULATIONSPARAMETERSCALIBRATION DATAFIELD DATACHAIN OF CUSTODY
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
NOMENCLATURE
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
SAMPLE CALCULATIONS
VERTAC SITE CONTRACTORSCAE Project No : 5815-1
SAMPLE CALCULATIONS - RUN 1, STACK(Note: results are taken from computer analysis)
14. Chloromethane
casern .J^f35^fq(V^)l m3 J
=(10dlD (35.31)(0.35)
=1065.0HQ
ppb ——SL—f^ss^^YioooP^I(V. ) [453,590^) I MW A PpmJ
^1) fssil Y^oo^(0.35) [453,590^) I 50.49 A PPm
=507
Ib/hr fioooiis.1F-a^——- (dscfm) (60)
(V.,.,) [453,590^)10.411
fl 000^1= ———\—!aJ——^1 • 940)(60)
(0.35)[453,590^J=4.76x10-2
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
PARAMETERS
VERTAC SITE CONTRACTORSCAE Project No: 5518
VOLATILE ORGANICS
LOCATION STACK
RUN NO.Date (1991)
FIELD BLANKOct10
ChloromethaneM
BromomethaneM
Methylene ChlorideW
AcetoneM
1,1-DichloroetheneM
ChloroformM
TrichlorofluoromethaneM
2-ButanoneM
1,1,1-TrichloroethaneM
Carbon Tetrachloride48
BromdichloromethaneM
TrichloroetheneM
DibromochloromethaneM
Benzene49
BromoformW
TetrachloroetheneM
TolueneM
ChlorobenzeneM
0.053
(<0.001) ND
0.034 E
0.065
(<0.001) ND
0.005 E
(<0.001) ND
0.089
(<0.001) ND
(<0.001) ND
(<0.001) ND
(<0,001) ND
(<0.001) ND
(<0.001) ND
(<0.001) ND
(<0.001) ND
0.01 O E
(<0.001) ND
ND - not detectedE - estimated
VERTAG SITE CONTRACTORSCAE Project No: 5518
VOLATILE ORGANICS
LOCATION STACK
RUN NO.*Date (1991)Start Time (approx.)Stop Time (approx.)
Pb (in. Hg)Vm (LITERS)Vm (ft3)DHYdTm
CALCULATED RESULTS
Vmstddscfm**
ChloromethaneMVUQ/dscmppbIb/hr
BromomethaneMug/dscmppbIb/hr
Methylene ChlorideMug/dscmPPbIb/hr
AcetoneUSug/dscmppbIb/hr
1,1-DichloroetheneMug/dscmppbIb/hr
ChloroformU9ug/dscmppbIb/hr
1Oct10
2:19 PM2:29 PM
30.0010.000.351.50
0.999983
0.3511,940
10.4111065.0
5074.76E-02
(<0.002) ND(<0)(<0)
(<8.16E-07)
16.7891717.5
4861.32E-06
3.032310.2
1292.00E-03
0.21221.7
52.52E-05
3.782386.9
783.14E-05
2Oct10
2:48 PM3:08 PM
30.0019.990.711.50
0.999985
0.6911,940
4.264218.9
1049.79E-03
0.1105.6
14.63E-06
5.618288.4
826.10E-06
0.1849.4
41.02E-05
0.044 E2.3
18.00E-08
1.52978.5
166.64E-07
4Oct10
3:56 PM4:16 PM
30.0020.01
0.711.75
0999991
0.6811,940
4.900254.1
1211.14E-02
0.1387.2
26.81 E-06
4.608238.9
686.41 E-06
0.24712.8
51.15E-05
0.0693.6
11.72E-07
2.054106.5
211.43E-06
AVERAGE
MW= 50.496.525512.7
2442.29E-02
MW= 94.940.124
6.42
5.72E-06MW= 84.94
9.005748.3
2124.61 E-06
MW= 58.051.154110.8
466.72E-04
MW= 96.940.108
9.22
8.48E-06MW = 119.38
2.455190.6
381.12E-05
* Run No. 3 was not analyzed. The samples were tost due to an electrical storm."The flow rate was taken from the corresponding MM5 run.ND - not detectedE - estimatedNon-detected values were not included in the average.
VERTAC SITE CONTRACTORSCAE Project No: 5518
VOLATILE ORGANICS
LOCATION STACK
RUN NO." 1 2 4 AVERAGEDate (1991) Oct10 Oct10 Oct10Start Time (approx.) 2:19 PM 2:48 PM 3:56 PMStop Time (approx.) 2:29 PM 3:08 PM 4:16 PM
Pb (in. Hg)Vm (LITERS)Vm (ft3)DHYdTm
30.0010.000.351.50
0.999983
30.0019.99
0.711.50
0999985
30.0020.01
0.711.75
0.999991
CALCULATED RESULTS
Vmstd 0.35dscfrn" 11,940
0.6911,940
0.6811,940
TrichlorofluoromelhaneMug/dscmppbIb/hr
2-ButanoneMug/dscmppbIb/hr
1,1,1-TrichloroethaneMtig/dscmppbIb/hr
Carbon TetrachlorideMug/dscmppbIb/hr
BromdichloromethaneMug/dscmppbIb/hr
TrichloroetheneMug/dscmppbIb/hr
MW = 137.400.468 0.276 0.106 0.28347.9 14.2 5.5 22.5
8 2 1 46.94E-05 4.17E-06 2.19E-06 2.52E-05
MW= 148,210.627 (<0.003)ND (<0.011)ND 0.627
64.1 (<0) (<1) 64.110 (<0) (<0) 10
1.15E-05 (<8.18E-09) (<1.17E-08) 1.15E-05MW a 133.41
1.030 0.886 0.563 0.826105.4 45.5 29.2 60.0
19 8 5 1 12.53E-05 2.62E-08 6.24E-08 8.47E-06
MW = 153.820.657 1.015 2.156 1.27667.2 52.1 111 .8 77.0
1 1 8 17 122.65E-05 8.88E-06 1.22E-05 1.59E-05
MW= 163.832.511 1.543 2.221 2.092256.9 79.2 115.2 150.4
38 12 17 226.47E-05 1.55E-05 4.82E-05 4.28E-05
MW= 131.390.037 E 0.078 0.088 0.068
3.8 4.0 4.6 4.11 1 1 1
3.64E-06 1.19E-06 1.97E-06 2.27E-06
* Run No. 3 was not analyzed. The samples were tost due to an electrical storm."The flow rate was taken from the corresponding MM5 run.ND - not detectedE - estimatedNon-detected values were not included in the average.
VERTAC SITE CONTRACTORSCAE Project No: 5518
VOLATILE ORGANICS
LOCATION STACK
RUN NO.*Date (1991)Start Time (approx.)Stop Time (approx.)
Pb (in. Hg)Vm (LITERS)Vm (ft3)DHYdTm
CALCULATED RESULTS
Vmstddscfrn"
DibromochloromethaneMug/dscmppbIb/hr
BenzeneWug/dscmppbIb/hr
Bromoformuglig/dscmppbIb/hr
TetrachloroetheneMug/dscmppbIb/hr
TolueneWug/dscmppbIb/hr
ChlorobenzeneMug/dscmppbIb/hr
1Oct10
2:19 PM2:29 PM
30.0010.000.351.50
0.999983
0.3511,940
0.38939.8
55.64E-07
0.0505.1
27.62E-07
(<0.002) ND(<0)(<0)
(<3,92E-09)
0.026 E2.7
02.04E-09
0.13413.7
41.37E-07
(<0.001) ND(<0)(<0)
(<5.25E-09)
2Oct10
2:48 PM3:08 PM
30.0019.99
0.711.50
0.999985
0.6911,940
2.016103.5
121.55E-06
0.0593.0
11.17E-06
2.514129.1
121.46E-06
0.0995.1
12.46E-06
0.036 E1.8
03.52E-08
0.0603.1
12.13E-08
4Oct10
3:56 PM4:16 PM
30.0020.01
0.711.75
0.999991
0.6811,940
3.108161.2
192.75E-06
0.0763.9
12.38E-06
3.703192.0
182.83E-06
0.1055.4
13.92E-06
0.042 E2.2
14.44E-08
0.0542.8
12.28E-08
* Run No. 3 was not analyzed. The samples were lost due to an electrical storm."The flow rate was taken from the corresponding MM5 run.ND-not detectedE - estimatedNon-detected values were not included in the average.
AVERAGE
MW = 208.291.838101.5
121.62E-06
MW=78.120.062
4.01
1.44E-06MW = 252.75
3.109160.5
152.15E-06
MW= 165.830.077
4.41
2.13E-06MW=92.13
0.0715.9
27.21 E-08
MW a 112.560.057
2.91
2.21 E-08
VERTAC SITE CONTRACTORSCAE Project No; 5518
VOLATILE ORGANICS
LOCATION
RUN NO.Date (1991)Start Time (approx.)Stop Time (approx.)
AUDIT CYCLINDER 470
470-1Oct10
5:08 PM5:18 PM
470-2Oct10
5:29 PM5:49 PM
470-3Oct10
5:52 PM6:02 PM
AVERAGE
Pb (in. Hg)Vm (LITERS)Vm (ft3)DHYdTm
30.0010.020.351.75
0.999986
30.0010.020.351.75
0.999986
30.0010.040.351,75
0.999986
CALCULATED RESULTS
Vmstd 0.34 0,34 0,35
ChloromethaneWpg/dscmppb
Vinyl ChlorideMpg/dscmppb
Methylene ChlorideWpg/dscmppb
AcetoneWpg/dscmppb
ChloroformWpg/dscmppb
TrichlorofluoromethaneWpg/dscmppb
1,1,1-Trichloroethanempg/dscmppb
Carbon Tetrachloridepgpg/dscmppb
BenzeneVQpg/dscmppb
TetrachloroetheneWpg/dscmppb
(<0.001) ND(<0.1)
(<0)
0.44645.7
18
6.709687.9
195
0.13613.9
6
1.706174.9
35
0.32533.3
6
1.178120.8
22
0.66868.5
11
0.80882.8
26
1.074110.1
16
1.308134.1
64
0.36537.4
14
6.346650.7
184
0.12012.3
5
1.656169.8
34
0.23824.4
4
0.95197.5
18
0.67268.9
11
0.81583.6
26
1.049107.6
16
1.396142.9
68
0.30331.0
12
6.338648.6
184
0.10110.3
4
1.534157.0
32
0.22523.0
4
0.57558.8
11
0.60161.5
10
0.72674.3
23
0.96598.8
14
MW= 50.490.902
9244
MW= 62.500.371
3815
MW a 84.946.464
662188
MW» 58.050.119
125MW= 119,38
1.63216734
MWs 137.400.263
275MWs 133.41
0.9019217
MW> 153.820.647
6610
MW» 78.120.783
8025
MWs 165.831.029
10515
ND - not detectedNon-detected values were not included in the average.
VERTAC SITE CONTRACTORSCAE Project No: 5518
VOLATILE ORGANICS
LOCATION AUDIT CYCLINDER 471
RUN NO. 471-1 471-2 471-3 AVERAGEDate (1991) Oct10 Oct10 Oct10Start Time (approx.) 6:13 PM 6:33 PM 6:50 PMStop Time (approx,) 6:23 PM 6:43 PM 7:00 PM
Pb (in. Hg)Vm (LITERS)Vm (ft3)DHYdTm
30.0010.020.351.75
0.999984
30.0010.000.351.75
0.999984
30.0010.010.351.75
0.999984
CALCULATED RESULTS
Vmstd 0.35 0.34 0.35
Chloromethane49 1.038ug/dscm 106.1ppb 51
Methylene ChlorideHg 6.532ug/dscm 667.6ppb 189
Acetoneug 0.324ug/dscm 33.1ppb 14
1,1-Dichloroetheneug 0.484Ug/dscm 49.5ppb 12
Trichlocofluoromethaneug 0.209ug/dscm 21.4ppb 4
2-Butanonepg 0.080ug/dscm 8.2ppb 1
1.1,1-TrichtoroethaneM 0.469ug/dscm 47.9ppb 9
Toluenepg 0.440ug/dscm 45.0ppb 12
ChlorobenzeneM 0.502ug/dscm 51.3ppb 11
1.643168.2
80
8.184838.1
237
0.31632.4
13
0.54455.7
14
0.22923.5
4
0.0545.5I
0.34735.5
6
0.42343.3II
0.48950.1
1 1
2.117216.6
103
6.758691.4
196
0.23323.8
10
0.45146.1
1 1
0.12713.0
2
0.0687.0I
0.31131.8
6
0.40541.4II
0.51352.5
11
MW = 50.491.599
16478
MW= 84.947.158
732207
MW = 58.050.291
3012
MW = 96.940.493
5013
MW = 137.400.188
193MW = 148.21
0.0808IMW = 133.41
0.376387MW s92.13
0.42343II
MW= 112.560.501
5111
VERTAC SITE CONTRACTORSCAE Project No: 5815-1
CALIBRATION DATA
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Proof RecordWV^H COHP.
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VERTAC SITE CONTRACTORSCAE Project No: 5815-1
CHAIN OF CUSTODY
6 ^ i ^ O O
3500CHAIN OF CUSTODY RECORD
PROJ.NO.
^f- »
PROJECT NAME
\J t (i T F\ C.
SAMPLERS:MPLERS: IponlunO
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SAMPLENO.
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NO.OF
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REMARKS
T>J NOT ».^Ac- ( -7 fc fi.^t4^-
d.^fi 2.
(2.JN 3
flunrr ^ ^ 0 - 1
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nelinqutehod by: (Slynatun) Oaf/Tim*
RMiriMd by: (S(9M«k« ReUnqulihad by: (SJgnffumJ
RellnquWtMt by: fitoiMlUKtf
>tf MARKS:
Dale/Tim*
-< ^^/ '•-/-L^ iL.^1^ \ JM^ (^ ( t ^ N i > ^ . - ^ A,^^A- ^.zfr-^f) Clean Air Engln—ring
500 W. Wood StrestPalatine. IL 60067708/991-3300
/•USTOMER COPV