United States
Environmental Protection
Agency
Office of Air Quality
Planning and Standards
Research Triangle Park, NC 27711
EPA-454/R-99-002c
February 1999
AIR
   ©EPA

   Final Report - Volume III of III

   Emissions Testing of Combustion
   Stack and Pushing Operations at
   Coke Battery No.  5/6 at ABC Coke
   in Birmingham, Alabama
            VEdTf*

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                    FINAL REPORT
   EMISSIONS TESTING OF COMBUSTION STACK AND
COKE PUSHING OPERATIONS AT COKE BATTERY NO. 5/6
                    AT ABC COKE
              IN BIRMINGHAM, ALABAMA

                       Volume III
                 Appendices E through H
               EPA Contract No. 68-D-98-004
                Work Assignment No. 2-02
                      Prepared for:

                John C.Bosch, Jr. (MD-19)
                Work Assignment Manager
               SCGA, EMC, EMAD, OAQPS
            U.S. Environmental Protection Agency
             Research Triangle Park, NC 27711

                     February 1999
                     p:\s512.000\finrpt.wpd
                      Submitted by:

        PACIFIC ENVIRONMENTAL SERVICES, INC.
               5001 S. Miami Blvd., Suite 300
                  Post Office Box 12077
           Research Triangle Park, NC 27709-2077
            (919)941-0333  FAX (919) 941-0234

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                                  DISCLAIMER

      This document was prepared by Pacific Environmental Services, Inc. (PES) under EPA
Contract No. 68D98004, Work Assignment No. 2-02. This document has been reviewed
following PES' internal quality assurance procedures and has been approved for distribution.
The contents of this document do not necessarily reflect the views and policies of the U.S. EPA.
Mention of trade names does not constitute endorsement by the EPA or PES.
                                         n

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                        TABLE OF CONTENTS

                                                            Page

1.0   INTRODUCTION	1-1

2.0   SUMMARY OF RESULTS  	2-1

     2.1   EMISSIONS TEST LOG	2-1
     2.2   FILTERABLE PARTICULATE MATTER, METHYLENE CHLORIDE
          EXTRACTABLE MATTER (MCEM), AND METALS	2-1
     2.3   POLYCYCLIC AROMATIC HYDROCARBONS (PAHs)	2-27
     2.4   NON-PUSHING AND NON-CHARGING COKE OVEN BATTERY
          OPERATION - UNDERFIRE STACK	2-32

3.0   PROCESS AND CONTROL EQUIPMENT OPERATION	3-1

     3.1   INTRODUCTION	3-1
     3.2   PROCESS DESCRIPTION	3-1
     3.3   PROCESS AND CONTROL DEVICE MONITORING 	3-3

4.0   SAMPLING LOCATIONS	4-1

     4.1   COKE OVEN BATTERYNO. 5/6	4-1

5.0   SAMPLING AND ANALYTICAL PROCEDURES 	5-1

     5.1   LOCATION OF MEASUREMENT SITES AND
          SAMPLE/VELOCITY TRAVERSE POINTS  	5-1
     5.2   DETERMINATION OF STACK GAS VOLUMETRIC FLOW RATE  	5-3
     5.3   DETERMINATION OF STACK GAS EMISSION RATE CORRECTION
          FACTORS, DRY MOLECULAR WEIGHT, AND EXCESS AIR 	5-3
     5.4   DETERMINATION OF STACK GAS MOISTURE CONTENT 	5-3
     5.5   DETERMINATION OF PARTICULATE MATTER/METHYLENE
          CHLORIDE EXTRACTABLE MATTER/METALS	5-4
     5.6   POLYCYCLIC AROMATIC HYDROCARBONS 	5-6

6.0   QUALITY ASSURANCE/QUALITY CONTROL PROCEDURES AND RESULTS 6-1

     6.1   CALIBRATION OF APPARATUS 	6-1
                               111

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                   TABLE OF CONTENTS (Concluded)
     6.2   ON-SITE MEASUREMENTS 	6-5
     6.3   LABORATORY ANALYSES 	6-9

APPENDIX A  PROCESS DATA
APPENDIX B  RAW FIELD DATA
APPENDIX C  ANALYTICAL DATA (Except CARB 429)
APPENDIX D  ANALYTICAL DATA (CARB 429)
APPENDIX E  CALCULATIONS
APPENDIX F  QA/QC DATA
APPENDIX G  PARTICIPANTS
APPENDIX H  SAMPLING AND ANALYTICAL PROCEDURES
                               IV

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                                 LIST OF TABLES
                                                                              Page
Table 2.1     Emissions Test Log, ABC Coke, Birmingham, Alabama	2-2
Table 2.2     Particulate Matter/MCEM/Metals Emissions Sampling and Flue Gas
             Parameters - Baghouse Inlet, ABC Coke, Birmingham, Alabama  	2-4
Table 2.3     Filterable Particulate Matter Concentrations and Emission Rates -
             Baghouse Inlet, ABC Coke, Birmingham, Alabama	2-6
Table 2.4     Methylene Chloride Extractable Matter Concentrations and Emission
             Rates - Baghouse Inlet, ABC Coke, Birmingham, Alabama	2-7
Table 2.5     Multiple Metals Concentrations and Emission Rates - Baghouse Inlet,
             ABC Coke, Birmingham, Alabama	2-8
Table 2.6     Particulate Matter/MCEM/Metals Emission Sampling and Flue Gas
             Parameters - Baghouse Outlet, ABC Coke, Birmingham, Alabama	2-11
Table 2.7     Filterable Particulate Matter Concentrations and Emission Rates -
             Baghouse Outlet, ABC Coke, Birmingham, Alabama  	2-12
Table 2.8     Methylene Chloride Extractable Matter Concentrations and Emission
             Rates - Baghouse Outlet, ABC  Coke, Birmingham, Alabama 	2-13
Table 2.9     Multiple Metals Concentrations and Emission Rates - Baghouse Outlet,
             ABC Coke, Birmingham, Alabama	2-14
Table 2.10    Baghouse Dust Multiple Metals Concentrations, ABC Coke,
             Birmingham, Alabama	2-18
Table 2.11    Filterable Particulate Matter and Methylene Chloride Extractable
             Matter Removal Efficiencies, Coke Oven Battery No. 5/6 Baghouse,
             ABC Coke, Birmingham, Alabama	2-19
Table 2.12    Particulate Matter/MCEM/Metals Emissions Sampling and Flue Gas
             Parameters - Underfire Stack, ABC Coke, Birmingham, Alabama	2-20
Table 2.13    Filterable Particulate Matter Concentrations and Emission Rates -
             Underfire Stack, ABC Coke, Birmingham, Alabama	2-21
Table 2.14    Methylene Chloride Extractable Matter Concentrations and Emission
             Rates - Underfire Stack, ABC Coke, Birmingham, Alabama	2-23
Table 2.15    Multiple Metals Concentrations and Emission Rates - Underfire Stack
             ABC Coke, Birmingham, Alabama	2-24
Table 2.16    PAH Emissions Sampling and Flue Gas Parameters - Baghouse Inlet
             ABC Coke, Birmingham, Alabama	2-28
Table 2.17    PAH Concentrations and Emission Rates, Baghouse Inlet,
             ABC Coke, Birmingham, Alabama	2-29

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                            LIST OF TABLES (Continued)

                                                                              Page
 Table 2.18    PAH Emissions Sampling and Flue Gas Parameters - Baghouse Outlet
             ABC Coke, Birmingham, Alabama	2-33
 Table 2.19    PAH Concentrations and Emission Rates, Baghouse Outlet,
             ABC Coke, Birmingham, Alabama	2-34
 Table 2.20    PAH Emissions Sampling and Flue Gas Parameters - Underfire Stack
             ABC Coke, Birmingham, Alabama	2-37
 Table 2.21    PAH Concentrations and Emission Rates Underfire Stack
             ABC Coke, Birmingham, Alabama	2-38
 Table 2.22    Particulate Matter/MCEM/Metals and PAH Emissions Sampling
             and Flue Gas parameters - Underfire Stack Non-pushing and Non-charging
             Operation, ABC Coke, Birmingham, Alabama	2-42
 Table 2.23    Particulate Matter/MCEM Concentrations and Emission Rates -
             Underfire Stack Non-pushing and Non-charging Operation, ABC Coke,
             Birmingham, Alabama	2-43
 Table 2.24    Multiple Metals Concentrations and Emission Rates -
             Underfire Stack Non-pushing and Non-charging Operation, ABC Coke,
             Birmingham, Alabama	2-44
 Table 2.25    PAH Concentrations and Emission Rates - Underfire Stack Non-pushing and
             Non-charging Operation, ABC Coke, Birmingham, Alabama 	2-45

 Table 3.1 A   Pushing Control Device Parameters: Test Run No. 1, 9/21/98	3-4
 Table 3.IB    Pushing Control Device Parameters: Test Run No. 2, 9/22/98	3-5
 Table 3.1C    Pushing Control Device Parameters: Test Run No. 3, 9/23/98	3-6
 Table 3.2A    Combustion Stack Parameters: Test Run No. 1,9/24/98	3-8
 Table 3.2B    Combustion Stack Parameters: Test Run No. 2,9/24/98	3-8
 Table 3.2C    Combustion Stack Parameters: Test Run No. 3,9/25/98	3-9
 Table 3.2D    Combustion Stack Parameters: Test Run No. 4,9/25/98	3-9
 Table 3.3     Combustion Stack Opacity Readings	3-10

 Table 5.1     Summary of Sampling Locations, Test Parameters, Sampling Methods,
             and Number and Duration of Tests, ABC Coke, Birmingham, Alabama	5-2

 Table 6.1     Summary of Temperature Sensor Calibration Data	6-2
 Table 6.2     Summary of Pitot Tube Dimensional Data 	6-4
 Table 6.3     Summary of Dry Gas Meter and Orifice Calibration Data  	6-6
 Table 6.4     Summary of EPA Method 315 and CARB Method 429 Field Sampling
             QA/QC Data	6-8
 Table 6.5     Summary of EPA Method 315 Analytical QC Data Lab Blank Analysis	6-10
Table 6.6     Summary of EPA Method 315 Analytical QC Data Field Blank Analysis ... 6-11
Table 6.7     Summaryof EPA Method 29 Analytical QC Data Lab Control Sample
             (LCS) Recovery and Duplicate Analysis	6-13
Table 6.8     Summary of CARB Method 429 Analytical QC Data Field Blank
             Results  	6-14
                                        VI

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                          LIST OF TABLES (Concluded)

                                                                          Page
Table 6.9     Summary of CARB Method 429 Analytical QC Data Lab Control
            Sample (LCS)	6-15
Table 6.10    Summary of CARB Method 429 Analytical QC Data Surrogate
            Standard Recoveries	6-17
                                      VII

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                                LIST OF FIGURES

                                                                             Page

Figure 1.1     Key Personnel and Responsibility for Testing at ABC Coke,  Birmingham,
             Alabama	1-2

Figure 4.1     Baghouse Inlet Sample Location, ABC Coke, Birmingham, Alabama	4-2
Figure 4.2     Method 1 Calculation Sheet, Baghouse Inlet, Method 315, ABC Coke,
             Birmingham, Alabama	4-3
Figure 4.3     Method 1 Calculation Sheet, Baghouse Inlet, Method CARB  429,
             ABC Coke, Birmingham, Alabama	4-4
Figure 4.4     Baghouse Outlet, Sampling Location, ABC Coke,
             Birmingham, Alabama	4-5
Figure 4.5     Method 1 Calculation Sheet, Baghouse Outlet, ABC Coke,
             Birmingham, Alabama	4-6
Figure 4.6     Combustion (Underfire) Stack Sampling Location, ABC Coke,
             Birmingham, Alabama	4-8
Figure 4.7     Method 1 Calculation Sheet, Combustion Stack, ABC Coke,
             Birmingham, Alabama	4-9

Figure 5.1     Sampling Train Schematic for EPA Method 315  	5-5
Figure 5.2     Sampling Train Schematic for CARB Method 429	5-7
Figure 5.3     CARB Method 429 Sample Recovery Schematic	5-8
Figure 5.4     CARB Method 429 Analytical Schematic	5-9
                                       vin

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 APPENDIX E




CALCULATIONS

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                    Nomenclature and Dimensions

An   =      Cross-sectional area of sampling nozzle, ft2

As    =      Cross-sectional area of stack, ft2

Bws  =      Proportion by volume of water vapor in the gas stream, dimensionless

Cp   =      Pitot rube coefficient, dimensionless

Cs    =      Concentration of pollutant matter in stack gas-dry basis, grains per dry
             standard cubic foot (gr/dscf)

%CO =      Percent of carbon monoxide by volume, dry basis

%CO2=      Percent of carbon dioxide by volume, dry basis
o.
AH   —      Average pressure drop across the sampling meter flow orifice, inches
             of water (in. H2O)

GCV =      Gross calorific value, Btu/lb

I     =      Percent of isokinetic sampling

La    =      Maximum acceptable leakage rate for either a pretest leak check or for
             a leak check following a component change/ equal to 0.020 cubic foot
             per minute or 4% of the average sampling rate, whichever is less

Md   =      Dry molecular weight, Ib/lb-mole

Mn   =      Total amount of pollutant matter collected, milligrams (mg)

Ms    =      Molecular weight of stack gas (wet basis), Ib/lb-mole

%N2  =      Percent of nitrogen by volume, dry basis

%O2  =      Percent of oxygen by volume, dry basis

Ap    =      Velocity head of stack gas, inches of water (in. H2O)

Pbar  =      Barometric pressure, inches of mercury (in. Hg)

Ps    =      Absolute stack gas pressure, inches of mercury (in. Hg)

Pstd  =      Gas pressure at standard conditions, inches of mercury (29.92 in. Hg)

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pmr  =      Pollutant matter emission rate, pounds per hour (Ib/hr)

Qs    =      Volumetric flow rate - wet basis at stack conditions, actual cubic feet
             per minute (acfin)

Qsstd =      Volumetric flow rate - dry basis at stack conditions, actual cubic feet
             per minute (dscfm)

Tm   =      Average temperature of dry gas meter, °R

Ts    =      Average temperature of stack gas, °R

Tstd  =      Temperature at standard conditions, 528°R

Vic   =      Total volume of liquid collected in impingers, ml

Vsg  =      Volume of moisture collected in silica gel, grams

Vm   =      Volume of dry gas sampled at meter conditions, ft3

Vmstd=      Volume of dry gas sampled at standard conditions, ft3

Vs    =      Average stack gas velocity at stack conditions, ft/s

Vwstd =      Volume of water vapor at standard conditions, scf

Y     =      Dry gas meter calibration factor, dimensionless

6     =      Total sampling time, minutes

NOTE: Standard conditions = 68°F and 29.92 in. Hg

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          Example Calculations for Pollutant Emissions


1.    Volume of dry gas sampled corrected to standard conditions, ft3.
      Note: Vm must be corrected for leakage if any leakage rates exceed La.
                                                DA
                                                Poor
                     Vmstd = 17.647  *  Vm * v  *  - —
                                                  Tm,  °R
2. Volume of water vapor at standard conditions, ft3.


                         Vmstd = 0.04707 * Vic + 0.04715 * Vsg


3. Moisture content in stack gas, dimension less.



                                         Vwstd
                              Bws  =
                                     Vwstd + Vmstd
4. Dry molecular weight of stack gas, Ib/lb -mole.


                  Md = 0.44 * %CO2 + 0.32 * %O2 + 0.28 * (%N3 + %CO)


5. Molecular weight of stack gas, Ib/lb-mole.


                            Ms = Md (l-B\vs) + 18 * BWS


6. Stack velocity at stack conditions, f/s.
                      Vs = 85.49 * Cp * —- /A D -    Ts' °R
                                                 'y Ps * Ms




7.  Stack gas volumetric flow rate at stack conditions, cfm.


                                 Qs = 60*Vs *As


8.  Dry stack gas volumetric flow rate at standard conditions, cfm.



                      Osstd = 17.647 * Os *   Ps   * (l-Bws)
                                     *    Ts,°R

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9.  Concentration in gr/dscf.

                                Cs = 0.01543  *
                                                Vmstd



10. Concentration in Ib/dscf.


                                 Cs, Ib/dscf =
                                               7000



11. Pollutant mass emission rate, Ib/hr.


                             Pmr, Ib/hr = Ib/dscf* Qsstd * 60


12. Pollutant mass emission rate, Ib/MMBtu.


                             pmr, Ib/MMBtu = <^i
                                              MMBtu/hr



13. F-factor, Fd.



            106*(3.64*%#) + (1.53*%Q + (0.57 *%S) * (0.14*%A/)  - (0.46*%O>)
      Fd = 	;	•
                                       GCV (Btullb)




14. F-factor, pollutant mass emission rate, Ib/MMBtu.

                                = Ib/dscf * F * 20.9

                                     (20.9 - %02)




15. Heat imput, MMBtu/hr fuel.

                          =  GVC (Btullb) *  Feed Rate (Ib/hr)

                                          106



16. Heat input, MMBtu/hr, F-factor.



                     Qsstd
                      Fd
                           * ((20.9  - %O2) + 20.9)  *  60

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Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 • EOM/Particulate Matter/Metals
Baghouse Inlet
Page 1 of 2


Pstatic
y
Pbar
vm
Dp1/2
DH
Tm
T.
V,c
C02
02
N2
CP

As
Q
Dn
Push



An
Vm(std)
Vm(std)
Qm
PS
Bw,
Bws(sat)
Vwsw
1-Bw,
Md
M.
v,
A
Qa
Q,
Q.
I
RUN NUMBER
RUN DATE
RUN TIME
MEASURED DATA
Stack Static Pressure, inches H20
Meter Box Correction Factor
Barometric Pressure, inches Hg
Sample Volume, ft3
Average Square Root Dp, (in. H20)1/2
Avg Meter Orifice Pressure, in. H20
Average Meter Temperature, "F
Average Stack Temperature, °F
Condensate Collected, ml
Carbon Dioxide content, % by volume
Oxygen content, % by volume
Nitrogen content, % by volume
Pilot Tube Coefficient
Circular Stack? 1=Y,0=N:
Diameter or Dimensions, inches:
Sample Run Duration, minutes
Nozzle Diameter, inches
Tons of Coke pushed
Total Test Time, hours
Tons of Coke per Hour
CALCULATED DATA
Nozzle Area, ft2
Standard Meter Volume, ft3
Standard Meter Volume, m3
Average Sampling Rate, dscfm
Stack Pressure, inches Hg
Moisture, % by volume
Moisture (at saturation), % by volume
Standard Water Vapor Volume, ft3
Dry Mole Fraction
Molecular Weight (d.b.), lb/lb«mole
Molecular Weight (w.b.), Ib/lb-mole
Stack Gas Velocity, ft/s
Stack Area, ft2
Stack Gas Volumetric flow, acfm
Stack Gas Volumetric flow, dscfm
Stack Gas Volumetric flow, dscmm
Isokinetic Sampling Ratio, %
A-l-315-1
9/21/98
1128-1911

-5.90
1.004
29.70
192.272
0.6287
0.7221
111
138
115.5
0.2
20.2
79.6
0.84
0
4680
458
0.192
257.46
7.72
33.3
A-l-315-2
9/22/98
1018-1816

-4.50
1.004
29.74
103.570
0.3760
0.3016
113
154
44.9
0.2
20.3
79.5
0.84
0
4680
421.4
0.192
281.98
7.97
35.4
A-l-315-3
9/23/98
1016-1800

-5.50
1.004
29.80
152.489
0.5372
0.7612
109
137
57.7
0.2
20.3
79.5
0.84
0
4680
435
0.192
269.72
7.73
34.9
Average

-5.30
1.004
29.75
149.444
0.5140
0.5950
111
143
72.7
0.2
20.3
79.5
0.84

4680
438
0.192
269.72
7.81
34.5
All Calculations are on Tim* Weighted Average Basis
0.000201
177.437
5.024
0.387
29.27
3.0
19.0
5.437
0.970
28.84
28.52
38.2
32.5
74,526
62,426
1,768
100.3
0.000201
95.274
2.698
0.226
29.41
2.2
28.3
2.113
0.978
28.84
28.61
23.1
32.5
44.982
37.181
1,053
98.3
0.000201
141.706
4.013
0.326
29.40
1.9
18.5
2.716
0.981
28.84
28.64
32.5
32.5
63,350
53,989
1,529
97.6
0.000201
138.139
3.912
0.313
29.36
2.3
21.9
3.422
0.977
28.84
28.59
31.3
32.50
60,952
51,199
1.450
98.7

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                                    Method 315 Analytical Results (g) and Blank Corrections
                                              ABC Coke - Birmingham, Alabama
                                                       Baghouse Inlet

                                                All Weights are listed in grams
  Run No.
Filters
                                                                                               Corrected Total
 A-l-315-1
                                                                                             0.0112
0.8754      0.0009       0.0794       0.0008      0.0005      0.0084      0.0008       0.9545
 A-l-315-2      0.8613       0.0003      0.1277      0.0003       0.0001       0.0059      0.0003      0.9887
  A-l-315-3     1.0267      0.0002       0.0925       0.0002      0.0007      0.0029       0.0002       1.1189
Blank Values    0.0001
      0.0000      0.0002
                                                              0.0001       0.0001

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Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - EOM/Particulate Matter
Baghouse Inlet
Page 2 of 2

RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA
EMISSIONS DATA
Particulate Matter
PM Total Catch, g
CPM @ 7% O2 Concentration, gr/dscf @ 7% O2
CPM @ 7% O2 Concentration, g/dscm @ 7% O2
CPM Concentration, ug/dscm
EPM Emission Rate, ug/hr
CPM
CPM
EPM
Push

EOM
CEOM @ 7%
CEOM @ 7%
CEOM
EEOM
CEOM
CEOM
EEOM
Push
Concentration, gr/dscf
Concentration, Ib/dscf
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Extractable Organic Matter
Total Catch, g
Oz Concentration, gr/dscf @ 7% O2
O2 Concentration, g/dscm @ 7% 02
Concentration, ug/dscm
Emission Rate, ug/hr
Concentration, gr/dscf
Concentration, Ib/dscf
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
A-l-315-1
9/21/98
1128-1911
0.9545
1.6484
3.77E+06
1.90E+05
2.01E-HO
0.083
1.19E-05
44.4
1.33E+00

0.0112
0.0193
4.43E+04
2.23E+03
2.36E+08
9.74E-04
1.39E-07
0.521
1.56E-02
A-l-315-2
9/22/98
1018-1816
0.9887
3.7100
8.49E+06
3.66E+05
2.32E+10
0.160
2.29E-05
51.0
1.44E+00

0.0067
0.0251
5.75E+04
2.48E+03
1.57E+08
1.09E-03
1.55E-07
0.346
9.78E-03
A-l-315-3
9/23/98
1016-1800
1.1189
2.8229
6.46E+06
2.79E+05
2.56E+10
0.122
1.74E-05
56.4
1.62E+00

0.0040
0.0101
2.31 E-KM
9.97E+02
9.14E+07
4.36E-04
6.22E-08
0.202
5.78E-03
Average
1.0207
2.7271
6.24E+06
2.78E+05
2.30E+10
0.122
1.74E-05
50.6
1.46E+00

0.0073
0.0182
4.16E+04
1.90E-»-03
1.62E-I-08
8.32E-04
1.19E-07
0.356
1.04E-02

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Method 315 Analytical Results (ug) and Blank Corrections
          ABC Coke - Birmingham, Alabama
                   Baghouse Inlet
Target Catch, tig/sample

Metal
Antimony
Arsenic
Barium
Beryllium
Cadmium
Chromium
Colbalt
Copper
Lead
Manganese
Mercury
Nickel
Phosphorus
Selenium
Silver
Thallium
Zinc
A-I-315-1

0.5
16.8
36.2
0.35
0.38
12.9
2.5
16.1
20.6
36.3
0.0
19.6
59.0
4.4
0.3
1.1
70.0
A-I-315-1
Corrected
0.5
16.8
36.2
0.35
0.38
12.9
2.5
16.1
20.6
33.6
0.0
19.6
59.0
4.4
0.3
1.1
65.0
A-I-315-2

0.0
11.5
41.8
0.47
0.36
11.8
2.0
11.4
17.6
18.7
0.0
14.0
56.0
3.6
0.1
1.1
47.0
A-I-315-2
Corrected
0.0
11.5
41.8
0.47
0.36
11.8
2.0
11.4
17.6
16.0
0.0
14.0
56.0
3.6
0.1
1.1
42.0
A-I-315-3

0.0
9.7
35.6
0.48
10.2
9.8
1.6
25.7
17.1
20.9
0.0
24.3
70.0
4.3
0.0
1.2
54.0
A-I-315-3
Corrected
0.0
9.7
35.6
0.48
10.2
9.8
1.6
25.7
17.1
18.2
0.0
24.3
70.0
4.3
0.0
1.2
49.0
Filter Blank
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
2.7
0.0
0.0
0.0
0.0
0.0
0.0
5.0

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Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 -Metals
Baghouse Inlet
Page 1 of 6




Sb
CSb
Csb @ 7% O2
vm
ESb
Push

As
CAS
Csb @ 7% O2
EAS
EAS
Push

Ba
CBa
CBa @ 7% O2
EBa
EBa
Push
RUN NUMBER
RUN DATE
RUN TIME
Antimony
Target Catch, ug
Concentration, pg/dscm
Concentration, pg/dscm @ 7% 02
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Arsenic
Target Catch, pg
Concentration, pg/dscm
Concentration, pg/dscm @ 7% 02
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Barium
Target Catch, pg
Concentration, pg/dscm
Concentration, pg/dscm @ 7% 02
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
A-l-315-1
9/21/98
1128-1911

0.5
0.10
2.0
10,555
2.32E-05
6.96E-07

16.8
3.3
66
354,633
7.80E-04
2.34E-05

36.2
7.20
143
764,149
1.68E-03
5.04E-05
A-l-315-2
9/22/98
1018-1816

0.0
0.00
0.0
0
O.OOE+00
O.OOE+00

11.5
4.3
99
269,272
5.92E-04
1.67E-05

41.8
15.49
359
978,745
2.15E-03
6.09E-05
A-l-315-3
9/23/98
1016-1800

0.0
0.00
0.0
0
O.OOE+00
O.OOE+00

9.7
2.4
56
221,739
4.88E-04
1.40E-05

35.6
8.87
206
813,805
1.79E-03
5.13E-05
Average



0.2
0.03
0.7
3,518
7.74E-06
2.32E-07

12.67
3.3
74
281,881
6.20E-04
1.80E-05

37.87
10.52
236
852,233
1.87E-03
5.42E-05

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 -Metals
Baghouse Inlet
Page 2 of 6





Be
CBe
CBe @ 7% O2
EBe
EBe
Push

Cd
CCd
CCd @ 7% O2
ECd
ECd
Push

Cr
Ccr
CCr @ 7% O2
Ecr
Ecr
Push
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA - Continued
Beryllium
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% 02
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Cadmium
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% O2
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Chromium
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% 02
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
A-l-315-1
36059
1128-1911


0.4
0.070
1.38E+00
7,388
1.63E-05
4.87E-07

0.4
0.076
1.50E+00
8,021
1.76E-05
5.29E-07

12.9
2.57
5.10E+01
272,307
5.99E-04
1.80E-05
A-l-315-2
36060
1018-1816


0.5
0.174
4.04E+00
11,005
2.42E-05
6.84E-07

0.4
0.133
3.09E+00
8,429
1.85E-05
5.24E-07

11.8
4.37
1.01E+02
276,296
6.08E-04
1.72E-05
A-l-315-3
36061
1016-1800


0.5
0.120
2.77E+00
10,973
2.41 E-05
6.92E-07

10.2
2.542
5.89E+01
233,169
5.13E-04
1.47E-05

9.8
2.44
5.66E+01
224,025
4.93E-04
1.41 E-05
Average




0.43
0.121
2.73E+00
9,789
2.15E-05
6.21 E-07

3.6
0.917
2.12E+01
83,207
1.83E-04
5.25E-06

11.50
3.13
6.96E+01
257,543
5.67E-04
1.64E-05

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 -Metals
Baghouse Inlet
Page 3 of 6





Co
CCo
CCo @ 7% O2
ECO
ECO
Push

Cu
Ccu
CCu @ 7% O2
ECU
ECU
Push

Pb
Cpb
CPb @ 7% O2
EPb
EPb
Push
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA - Continued
Colbalt
Target Catch, |jg
Concentration, pg/dscm
Concentration, pg/dscm @ 7% O2
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Copper
Target Catch, pg
Concentration, pg/dscm
Concentration, pg/dscm @ 7% O2
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Lead
Target Catch, pg
Concentration, pg/dscm
Concentration, pg/dscm @ 7% 02
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
A-l-315-1
36059
1128-1911


2.5
0.498
9.88E+00
52,773
1.16E-04
3.48E-06

16.1
3.20
6.36E+01
339,856
7.48E-04
2.24E-05

20.6
4.1
8.14E+01
434,847
9.57E-04
2.87E-05
A-l-315-2
36060
1018-1816


2.0
0.741
1.72E+01
46,830
1.03E-04
2.91 E-06

11.4
4.23
9.79E+01
266,930
5.87E-04
1.66E-05

17.6
6.5
1.51E+02
412,103
9.07E-04
2.56E-05
A-l-315-3
36061
1016-1800


1.6
0.399
9.24E+00
36,576
8.05E-05
2.31 E-06

25.7
6.40
1.48E+02
587,494
1.29E-03
3.70E-05

17.1
4.3
9.87E+01
390,901
8.60E-04
2.46E-05
Average




2.03
0.546
1.21E+01
45,393
9.99E-05
2.90E-06

17.73
4.61
1.03E+02
398,094
8.76E-04
2.54E-05

18.4
5.0
1.10E+02
412,617
9.08E-04
2.63E-05

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 -Metals
Baghouse Inlet
Page 4 of 6
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA - Continued
Manganese
Mn Target Catch, ug
Cn/in Concentration, Mg/dscm
CMH @ 7% O2 Concentration, ug/dscm @ 7% O2
EMH Emission Rate, ug/hr
EMH Emission Rate, Ib/hr
Push Pounds per Ton of Coke Pushed
Mercury
Hg Target Catch, ug
CHQ Concentration, pg/dscm
CHQ @ 7% O2 Concentration, ug/dscm @ 7% O2
EHQ Emission Rate, ug/hr
Ehg Emission Rate, Ib/hr
Push Pounds per Ton of Coke Pushed
Nickel
Ni Target Catch, ug
CNS Concentration, ug/dscm
CNJ @ 7% O2 Concentration, ug/dscm @ 7% O2
ENJ Emission Rate, ug/hr
ENS Emission Rate, Ib/hr
Push Pounds per Ton of Coke Pushed
A-l-315-1
36059
1128-1911


33.6
6.7
1.33E+02
709,265
1.56E-03
4.68E-05

0.0
0.00
O.OOE+00
0
O.OOE+00
O.OOE+00

19.6
3.9
7.75E+01
413,738
9.10E-04
2.73E-05
A-l-315-2
36060
1018-1816


16.0
5.9
1.37E+02
374,639
8.24E-04
2.33E-05

0.0
0.00
O.OOE+00
0
O.OOE+00
O.OOE+00

14.0
5.2
1.20E+02
327,809
7.21 E-04
2.04E-05
A-l-315-3
36061
1016-1800


18.2
4.5
1.05E+02
416,046
9.15E-04
2.62E-05

0.0
0.00
O.OOE+00
0
O.OOE+00
O.OOE+00

24.3
6.1
1.40E+02
555,491
1.22E-03
3.50E-05
Average




22.60
5.7
1.25E+02
499,984
1.10E-03
3.21 E-05

0.00
0.00
O.OOE+00
0
O.OOE+00
O.OOE+00

19.30
5.0
1.13E+02
432,346
9.51 E-04
2.76E-05

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 -Metals
Baghouse Inlet
Page 5 of 6





P
CP
Cp @ 7% O2
EP
EP
Push

Se
Cse
CSe @ 7% O2
Ese
Ese
Push

Ag
Gag
CAg @ 7% O2
EAg
EAg
Push
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA - Continued
Phosphorus
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% O2
Emission Rate, [jg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Selenium
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% 02
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Silver
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% 02
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
A-l-315-1
36059
1128-1911


59.0
11.7
2.33E+02
1,245,436
2.74E-03
8.22E-05

4.4
0.88
1.74E+01
92,880
2.04E-04
6.13E-06

0.3
0.0597
1.19E+00
6,333
1.39E-05
4.18E-07
A-l'315-2
36060
1018-1816


56.0
20.8
4.81 E+02
1,311,237
2.88E-03
8.15E-05

3.6
1.33
3.09E+01
84,294
1.85E-04
5.24E-06

0.1
0.0371
8.59E-01
2,341
5.15E-06
1.46E-07
A-l-315-3
36061
1016-1800


70.0
17.4
4.04E+02
1,600,179
3.52E-03
1.01E-04

4.3
1.07
2.48E+01
98,297
2.16E-04
6.20E-06

0.0
0.0000
O.OOE+00
0
O.OOE+00
O.OOE+00
Average




61.67
16.6
3.73E+02
1,385,617
3.05E-03
8.82E-05

4.10
1.09
2.44E+01
91,823
2.02E-04
5.86E-06

0.13
0.0323
6.81 E-01
2,891
6.36E-06
1.88E-07

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 -Metals
Baghouse Inlet
Page 6 of 6





Tl
CTI
On @ 7% O2
ET,
ETI
Push

Zn
Czn
CZn @ 7% O2
Ezn
Ezn
Push
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA - Continued
Thallium
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% O2
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Zinc
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% 02
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
A-l-315-1
36059
1128-1911


1.1
0.22
4.35E+00
23,220
5.11E-05
1.53E-06

65.0
12.9
2.57E+02
1,372,090
3.02E-03
9.05E-05
A-l-315-2
36060
1018-1816


1.1
0.41
9.45E+00
25,756
5.67E-05
1.60E-06

42.0 .
15.6
3.61 E+02
983,428
2.16E-03
6.12E-05
A-l-315-3
36061
1016-1800


1.2
0.30
6.93E+00
27,432
6.03E-05
1.73E-06

49.0
12.2
2.83E+02
1,120,125
2.46E-03
7.06E-05
Average




1.13
0.31
6.91 E+00
25,469
5.60E-05
1.62E-06

52.00
13.6
3.00E+02
1,158,548
2.55E-03
7.41 E-05

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 • EOM/Particulate Matter/Metals
Baghouse Outlet
Page 1 of 2


Pstatic
y
Pbar
vm
Dp1/2
DH
Tm
Ts
Vlc
C02
02
N2
CP

As
Q
Dn
Push



An
Vm(std)
Vm(std)
Qm
PS
BWS
Bws(sat)
vwsld
1-BWS
Md
Ms
vs
A
Qa
Q,
Q»
I
RUN NUMBER
RUN DATE
RUN TIME
MEASURED DATA
Stack Static Pressure, inches H20
Meter Box Correction Factor
Barometric Pressure, inches Hg
Sample Volume, ft3
Average Square Root Dp, (in. H20)1/
Avg Meter Orifice Pressure, in. H20
Average Meter Temperature, °F
Average Stack Temperature, "F
Condensate Collected, ml
Carbon Dioxide content, % by volum
Oxygen content, % by volume
Nitrogen content, % by volume
Pitot Tube Coefficient
Circular Stack? 1=Y,0=N:
Diameter or Dimensions, inches:
Sample Run Duration, minutes
Nozzle Diameter, inches
Tons of Coke Pushed
Total Test Time, hours
Tons of Coke per Hour
CALCULATED DATA
Nozzle Area, ft2
Standard Meter Volume, ft3
Standard Meter Volume, m3
Average Sampling Rate, dscfm
Stack Pressure, inches Hg
Moisture, % by volume
Moisture (at saturation), % by volum
Standard Water Vapor Volume, ft3
Dry Mole Fraction
Molecular Weight (d.b.), Ib/lb-mole
Molecular Weight (w.b.), Ib/lb-mole
Stack Gas Velocity, ft/s
Stack Area, ft2
Stack Gas Volumetric flow, acfm
Stack Gas Volumetric flow, dscfm
Stack Gas Volumetric flow, dscmm
Isokinetic Sampling Ratio, %
A-O-315-1 A-O-315-2 A-0-315-3
9/21/98 9/22/98 9/23/98
1126-1911 1028-1819 1020-1806

0.15
1.005
29.70
176.377
0.5154
0.9621
92
118
103.9
0.20
20.40
79.4
0.84
1
85.75
412
0.216
257.46
7.75
33.2

0.15
1.005
29.74
109.102
0.3265
0.4801
94
133
62.0
0.2
20.4
79.4
0.84
1
85.75
404
0.216
281.98
7.85
35.9

0.15
1.005
29.80
140.811
0.4731
0.8511
88
120
55.6
0.1
20.4
79.5
0.84
1
85.75
420
0.216
269.72
7.77
34.7
Average

0.15
1.005
29.75
142.097
0.4383
0.76
91
124
73.8
0.2
20.4
79.4
0.84

85.75
412
0.216
269.72
7.79
34.6
All Calculations are on Time Weighted Average Basis
0.000254
168.639
4.775
0.409
29.71
2.8
11.0
4.891
0.972
28.85
28.54
30.6
40.1
73,527
64,792
1,835
99.6
0.000254
103.955
2.944
0.257
29.75
2.7
16.4
2.918
0.973
28.85
28.55
19.6
40.1
47,139
40,579
1,149
100.0
0.000254
136.034
3.852
0.324
29.81
1.9
11.5
2.617
0.981
28.83
28.63
28.0
40.1
67,395
59,951
1,698
85.2
0.000254
136.209
3.857
0.330
29.76
2.5
13.0
3.475
0.975
28.84
28.57
26.1
40.10
62,687
55,108
1,560
94.9

-------
                                     Method 315 Analytical Results (g) and Blank Corrections
                                               ABC Coke - Birmingham, Alabama
                                                       Baghouse Outlet

                                                 All Weights are listed in grams
                                                                                                               Corrected Total
                            0.0000      0.0043      0.0011
  A-O-315-2      0.0039       0.0000      0.0048      0.0005      0.0003      0.0038      0.0003      0.0086
  A-O-315-3    0.0111       0.0000       0.0044      0.0005      0.0000      0.0021      0.0003      0.0154
 Blank values
* Blank Value for the MeCI2 - BHR were erroneous, so the lab blank value was used.

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - EOM/Particulate Matter
Baghouse Outlet
Page 2 of 2





PM
CpM @ 7% 0
CpM @ 7% 0
CPM
EPM
CPM
CPM
EPM
Push

EOM
EOM @ 7% 0
EOM @ 7% 0
CEOM
EEOM
CEOM
CEOM
EEOM
Push
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA
EMISSIONS DATA
Participate Matter
Total Catch, g
Concentration, gr/dscf @ 7% O2
Concentration, g/dscm @ 7% O2
Concentration, ug/dscm
Emission Rate, |jg/hr
Concentration, gr/dscf
Concentration, Ib/dscf
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Extractable Organic Matter
Total Catch, g
Concentration, gr/dscf @ 7% O2
Concentration, g/dscm @ 7% O2
Concentration, ug/dscm
Emission Rate, pg/hr
Concentration, gr/dscf
Concentration, Ib/dscf
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
A-O-315-1
9/21/98
1126-1911



0.0062
0.0158
3.61 E+04
1.30E+03
1.43E+08
5.67E-04
8.11E-08
0.315
9.48E-03

0.0156
0.0397
9.08E+04
3.27E+03
3.60E+08
1.43E-03
2.04E-07
0.793
2.39E-02
A-O-315-2
9/22/98
1028-1819



0.0086
0.0355
8.12E+04
2.92E+03
2.01 E+08
1.28E-03
1.82E-07
0.444
1.24E-02

0.0034
0.0140
3.21 E+04
1.16E+03
7.96E+07
5.05E-04
7.21 E-08
0.176
4.89E-03
A-O-315-3
9/23/98
1020-1806



0.0154
0.0486
1.11E+05
4.00E+03
4.07E+08
1.75E-03
2.50E-07
0.898
2.59E-02

0.0014
0.0044
1.01 E+04
3.63E+02
3.70E+07
1.59E-04
2.27E-08
0.082
2.35E-03

Average



0.0101
0.0333
7.62E+04
2.74E+03
2.51 E+08
1.20E-03
1.71E-07
0.552
1.59E-02

0.0068
0.0194
4.43E+04
1.60E+03
1.59E+08
6.97E-04
9.96E-08
0.350
1.04E-02

-------
Method 315 Analytical Results (ug) and Blank Corrections
          ABC Coke - Birmingham, Alabama
                  Baghouse Outlet
Target Catch, ug/sample

Metal
Antimony
Arsenic
Barium
Beryllium
Cadmium
Chromium
Colbalt
Copper
Lead
Manganese
Mercury
Nickel
Phosphorus
Selenium
Silver
Thallium
Zinc
A-O-315-1

0.0
0.3
4.9
0.0
0.09
1.9
0.0
2.8
1.2
5.2
0.0
0.0
16.0
0.0
0.0
0.0
16.0
A-O-315-1
Corrected
0.0
0.3
4.9
0.0
0.09
1.9
0.0
2.8
1.2
2.5
0,0
0.0
16.0
0.0
0.0
0.0
11.0
A-O-315-2

0.0
0.4
6.9
0.03
0.12
3.0
0.0
3.6
2.5
7.2
0.0
1.8
15.0
0.6
0.0
0.0
18.0
A-O-315-2
Corrected
0.0
0.4
6.9
0.03
0.12
3.0
0.0
3.6
2.5
4.5
0.0
1.8
15.0
0.6
0.0
0.0
13.0
A-0-315-3

0.0
0.5
7.8
0.04
0.07
3.5
0.0
4.4
1.6
8.1
0.0
1.2
20.0
0.0
0.0
0.0
20.0
A-O-315-3
Corrected
0.0
0.5
7.8
0.04
0.07
3.5
0.0
4.4
1.6
5.4
0.0
1.2
20.0
0.0
0.0
0.0
15.0
Filter Blank
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
2.7
0.0
0.0
0.0
0.0
0.0
0.0
5.0

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - Metals
Baghouse Outlet
Page 1 of 6



Sb
Csb
Csb @ 7% O2
Esb
Esb
Push

As
CAS
CSb @ 7% O2
EAS
EAS
Push

Ba
CBa
CBa @ 7% O2
EBa .
EBa
Push
RUN NUMBER
RUN DATE
RUN TIME
Antimony
Target Catch, ug
Concentration, ug/dscm @ 7% 02
Concentration, ug/dscm
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Arsenic
Target Catch, ug
Concentration, ug/dscm @ 7% 02
Concentration, ug/dscm
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Barium
Target Catch, ug
Concentration, ug/dscm @ 7% 02
Concentration, pg/dscm
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
A-O-315-1
9/21/98
1126-1911

0.0
0.0000
O.OOE+00
0.000
O.OOE+00
O.OOE+00

0.3
1.75
0.0628
6,916
1.52E-05
4.58E-07

4.9
28.5
1.03
112,956
2.49E-04
7.48E-06
A-0-315-2
9/22/98
1028-1819

0.0
0.0000
O.OOE+00
0.000
O.OOE+00
O.OOE+00

0.4
3.78
0.1359
9,369
2.06E-05
5.74E-07

6.9
65.2
2.34
161,608
3.56E-04
9.90E-06
A-O-315-3
9/23/98
1020-1806

0.0
0.0000
O.OOE+00
0.000
O.OOE+00
O.OOE+00

0.5
3.61
0.1298
13,221
2.91 E-05
8.38E-07

7.8
56.3
2.02
206,252
4.54E-04
1.31 E-05
Average


0.0
0.0000
O.OOE+00
0.000
O.OOE+00
O.OOE+00

0.4
3.04
0.1095
9,835
2.16E-05
6.23E-07

6.53
50.0
1.80
160,272
3.53E-04
1.01 E-05

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - Metals
Baghouse Outlet
Page 2 of 6
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA - Continued
Beryllium
Be Target Catch, |jg
Cae Concentration, ug/dscm @ 7% O2
CBS @ 7% O2 Concentration, ug/dscm
EBe Emission Rate, ug/hr
EBe Emission Rate, Ib/hr
Push Pounds per Ton of Coke Pushed
Cadmium
Cd Target Catch, pg
CCd Concentration, ug/dscm @ 7% 02
Ccd @ 7% O2 Concentration, pg/dscm
ECd Emission Rate, ug/hr
Ecd Emission Rate, Ib/hr
Push Pounds per Ton of Coke Pushed
Chromium
Cr Target Catch, jjg
CCr Concentration, pg/dscm @ 7% 02
CCr @ 7% O2 Concentration, ug/dscm
ECr Emission Rate, pg/hr
Ecr Emission Rate, Ib/hr
Push Pounds per Ton of Coke Pushed
A-O-315-1
09/21/98
1126-1911


0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

0.1
5.24E-01
1.88E-02
2,075
4.56E-06
1.37E-07

1.9
11.1
0.398
43,799
9.64E-05
2.90E-06
A-O-315-2
09/22/98
1028-1819


0.0
2.83E-01
1.02E-02
703
1.55E-06
4.30E-08

0.1
1.13E+00
4.08E-02
2,811
6.18E-06
1.72E-07

3.0
28.3
1.019
70,264
1.55E-04
4.30E-06
A-O-315-3
09/23/98
1020-1806


0.0
2.89E-01
1.04E-02
1,058
2.33E-06
6.70E-08

0.1
5.05E-01
1.82E-02
1,851
4.07E-06
1.17E-07

3.5
25.3
0.909
92,549
2.04E-04
5.87E-06
Average




0.02
1.91E-01
6.86E-03
587
1.29E-06
3.67E-08

0.1
7.21 E-01
2.59E-Q2
2,245
4.94E-06
1.42E-07

2.80
21.6
0.775
68,871
1.52E-04
4.36E-06

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - Metals
Baghouse Outlet
Page 3 of 6



Co
Ceo
CCo @ 7% O2
ECO
ECO
Push

Cu
Ccu
CCu @ 7% O2
ECU
ECU
Push

Pb
CPb
CPb @ 7% O2
EPb
EPb
Push
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA - Continued
Colbalt
Target Catch, MS
Concentration, ug/dscm @ 7% 02
Concentration, ug/dscm
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Copper
Target Catch, pg
Concentration, ug/dscm @ 7% 02
Concentration, ug/dscm
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Lead
Target Catch, ug
Concentration, ug/dscm @ 7% 02
Concentration, ug/dscm
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
A-O-315-1 A-O-315-2 A-O-315-3
09/21/98 09/22/98 09/23/98
1126-1911 1028-1819 1020-1806


0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

2.8
16.300
0.586
64,546
1.42E-04
4.27E-06

1.2
6.99E+00
0.251
27,663
6.09E-05
1.83E-06


0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

3.6
33.998
1.223
84,317
1.85E-04
5.16E-06

2.5
2.36E+01
0.849
58,554
1.29E-04
3.59E-06


0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

4.4
31.754
1.142
116,347
2.56E-04
7.37E-06

1.6
1.15E+01
0.415
42,308
9.31 E-05
2.68E-06
Average


0.00
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

3.60
27.351
0.984
88,404
1.94E-04
5.60E-06

1.8
1.40E+01
0.505
42,841
9.43E-05
2.70E-06

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - Metals
Baghouse Outlet
Page 4 of 6
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA - Continued
Manganese
Mn Target Catch, pg
CMn Concentration, pg/dscm @ 7% O2
CMP @ 7% O2 Concentration, pg/dscm
EMn Emission Rate, pg/hr
EMn Emission Rate, Ib/hr
Push Pounds per Ton of Coke Pushed
Mercury
Hg Target Catch, pg
CHg Concentration, pg/dscm @ 7% O2
CHQ @ 7% O2 Concentration, pg/dscm
EHg Emission Rate, pg/hr
EHg Emission Rate, Ib/hr
Push Pounds per Ton of Coke Pushed
Nickel
Ni Target Catch, pg
CNi Concentration, pg/dscm @ 7% O2
CNi @ 7% O2 Concentration, pg/dscm
ENi Emission Rate, pg/hr
ENj Emission Rate, Ib/hr
Push Pounds per Ton of Coke Pushed
A-O-315-1
09/21/98
1126-1911


2.5
1.46E+01
0.524
57,631
1.27E-04
3.82E-06

0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

0.0
0.00
0.000
0
O.OOE+00
O.OOE+00
A-0-315-2
09/22/98
1028-1819


4.5
4.25E+01
1.529
105,397
2.32E-04
6.46E-06

0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

1.8
17.00
0.611
42,159
9.27E-05
2.58E-06
A-O-315-3
09/23/98
1020-1806


5.4
3.90E+01
1.402
142,790
3.14E-04
9.05E-06

0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

1.2
8.66
0.312
31,731
6.98E-05
2.01E-06
Average




4.13
3.20E+01
1.151
101,939
2.24E-04
6.44E-06

0.00
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

1.00
8.55
0.308
24,630
5.42E-05
1.53E-06

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - Metals
Baghouse Outlet
Page 5 of 6



P
Cp
CP @ 7% O2
EP
EP
Push

Se
CSe
CSe @ 7% O2
Ese
ESe
Push

Ag
cag
CAg @ 7% 02
EAg
EAg
Push
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA - Continued
Phosphorus
Target Catch, ug
Concentration, pg/dscm @ 7% 02
Concentration, |jg/dscm
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Selenium
Target Catch, ug
Concentration, ug/dscm @ 7% 02
Concentration, ug/dscm
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Silver
Target Catch, ug
Concentration, ug/dscm @ 7% 02
Concentration, pg/dscm
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
A-O-315-1 A-O-315-2 A-O-315-3
09/21/98 09/22/98 09/23/98
1126-1911 1028-1819 1020-1806


16.0
93.1
3.35
368,836
8.11E-04
2.44E-05

0.0
0.0000
0.0000
0
O.OOE+00
O.OOE+00

0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00


15.0
141.7
5.10
351,322
7.73E-04
2.15E-05

0.6
5.67
0.2038
14,053
3.09E-05
8.61 E-07

0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00


20.0
144.3
5.19
528,850
1.16E-03
3.35E-05

0.0
0.00
0.0000
0
O.OOE+00
O.OOE+00

0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00
Average


17.00
126.4
4.55
416,336
9.16E-04
2.65E-05

0.20
1.89
0.0679
4,684
1.03E-05
2.87E-07

0.00
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 31 5 - Metals
Baghouse Outlet
Page 6 of 6





Tl
CT,
C-n @ 7% O2
En
En
Push

Zn
Czn
CZn @ 7% O2
Ezn
Ezn
Push
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA - Continued
Thallium
Target Catch, ug
Concentration, ug/dscm @ 7% 02
Concentration, ug/dscm
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
Zinc
Target Catch, ug
Concentration, ug/dscm @ 7% 02
Concentration, ug/dscm
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coke Pushed
A-0-315-1
09/21/98
1126-1911


0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

11.0
64.0
2.30
253,575
5.58E-04
1.68E-05
A-O-315-2
09/22/98
1028-1819


0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

13.0
122.8
4.42
304,479
6.70E-04
1.86E-05
A-O-315-3
09/23/98
1020-1806


0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

15.0
108.3
3.89
396,638
8.73E-04
2.51 E-05
Average




0.00
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

13.00
98.4
3.54
318,231
7.00E-04
2.02E-05

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - EOM/Particulate Matter
Underflre Stack
Page 1 of 2



Pstatic
y
Pbar
vm
Dp1/2
DH
Tm
T,
Vte
C02
02
N2
cp

As
Q
Dn
Charge



An

Vm(std)
Qm
P,
BWS
Bws(sat)
vwstd
1-Bw.
Md
M,
V.
A
Q.
Q,
Qs
I
RUN NUMBER
RUN DATE
RUN TIME
MEASURED DATA
Stack Static Pressure, inches H2O
Meter Box Correction Factor
Barometric Pressure, inches Hg
Sample Volume, ft3
Average Square Root Dp, (in. H20)1/2
Avg Meter Orifice Pressure, in. H20
Average Meter Temperature, °F
Average Stack Temperature, °F
Condensate Collected, ml
Carbon Dioxide content, % by volume
Oxygen content, % by volume
Nitrogen content, % by volume
Pitot Tube Coefficient
Circular Stack? 1=Y,0=N:
Diameter or Dimensions, inches:
Sample Run Duration, minutes
Nozzle Diameter, inches
Tons of Coal Charged
Total Test Time, hours
Tons of Coal per Hour
CALCULATED DATA
Nozzle Area, ft2
Standard Meter Volume, ft3
Standard Meter Volume, m3
Average Sampling Rate, dscfm
Stack Pressure, inches Hg
Moisture, % by volume
Moisture (at saturation), % by volume
Standard Water Vapor Volume, ft3
Dry Mole Fraction
Molecular Weight (d.b.), Ib/lb-mole
Molecular Weight (w.b.). Ib/lb-mole
Stack Gas Velocity, ft/s
Stack Area, ft2
Stack Gas Volumetric flow, acfm
Stack Gas Volumetric flow, dscfm
Stack Gas Volumetric flow, dscmm
' Isokinetic Sampling Ratio, %
A-U-315-1
9/24/98
1025-1344

-1.00
0.981
29.85
123.816
0.0898
1.42
99
449
394.6
2.70
14.70
82.6
0.84
1
187
180
0.740
168.63
3.32
50.8

0.002987
114.814
3.251
0.638
29.78
13.9
2976.1
18.574
0.861
29.02
27.49
6.8
190.7
77,773
38,682
1,095
105.3
A-U-315-2
9/24/98
1443-1806

-1.00
0.981
29.85
123.200
0.0954
1.44
102
437
426.4
3.0
15.00
82.0
0.84
1
187
180
0.740
183.96
3.38
54.4

0.002987
113.638
3.218
0.631
29.78
15.0
2626.5
20.071
0.850
29.08
27.42
7.2
190.7
82,178
40,898
1,158
98.6
A-U-315-3
9/25/98
0738-1029

-1.00
0.981
29.85
116.290
0.0996
1.46
88
480
393.0
2.7
13.20
84.1
0.84
1
187
171.4
0.740
0.00
2.85
0.0

0.002987
110.010
3.115
0.642
29.78
14.4
4044.8
18.499
0.856
28.96
27.38
7.7
190.7
87,884
42,039
1,190
97.5
A-U-315-4
9/25/98
1110-1428

-1.00
0.981
29.85
119.763
0.0951
1.36
101
476
360.5
2.8
13.50
83.7
0.84
1
187
180
0.740
122.64
3.30
37.2

0.002987
110.643
3.133
0.615
29.78
13.3
3892.6
16.969
0.867
28.99
27.53
7.3
190.7
83,514
40.634
1.151
96.6
Average*


-1.00
0.981
29.85
122.260
0.0934
1.41
101
454
393.8
2.8
14.4
82.8
0.84
1.0000
187.00
180
0.740
158.41
3.33
47.5

0.002987
113.032
3.201
0.628
29.78
14.1
3165.1
18.538
0.859
29.03
27.48
7.1
190.73
81.155
40,071
1.135
100.2
*Run A-U-315-3 is not included in averages.  This Test was conducted under non-push conditions.

-------
                                   Method 315 Analytical Results (g) and Blank Corrections
                                             ABC Coke - Birmingham, Alabama
                                                     Underfire Stack

                                              All Weights are listed in grams
  Run No.
      Filters
                                                                 Corrected Total
                PM
            MCEM
PM
MCEM
MCEM
MCEM
MCEM
PM
MCEM
 A-U-315-1
0.0674      0.0000       0.0481      0.0033      0.0003      0.0018       0.0003     0.1153
 A-U-315-3     0.0751       0.0001      0.0680      0.0028      0.0001       0.0044      0.0004     0.1429
Blank Values    0.0000       0.0000      0.0002      0.0000      0.0001       0.0003       0.0002     0.0002
                                                                                              0.0006

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - EOM/Particulate Matter
Underfire Stack
Page 2 of 2



PM
CpM @ 7% 02
CpM @ 7% 02
CPM
EPM
CPM
CPM
EpM
Charge

EOM
CEOM @ 7% 02
CEOM @ 7% O2
CEOM
EEOM
CEOM
CEOM
EEOM
Charge
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA
EMISSIONS DATA
Participate Matter
Total Catch, g
Concentration, gr/dscf @ 7% O2
Concentration, g/dscm @ 7% O2
Concentration, pg/dscm
Emission Rate, pg/hr
Concentration, gr/dscf
Concentration, Ib/dscf
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
Extractable Organic Matter
Total Catch, g
Concentration, gr/dscf @ 7% O2
Concentration, g/dscm @ 7% O2
Concentration, ug/dscm
Emission Rate, pg/hr
Concentration, gr/dscf
Concentration, Ib/dscf
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
A-U-315-1 A-U-315-2 A-U-315-3 A-U-315-4
9/24/98 9/24/98 9/25/98 9/25/98
1025-1344 1443-1806 0738-1029 1110-1428


0.1153
0.0347
7.95E+04
3.55E+04
2.33E+09
1.55E-02
2.21E-06
5.14E+00
1.01E-01

0.0051
0.0015
3.52E+03
1.57E+03
1.03E+08
6.85E-04
9.79E-08
2.27E-01
4.47E-03


0.1409
0.0451
1.03E+05
4.38E+04
3.04E+09
1.91E-02
2.73E-06
6.71 E+00
1.23E-01

0.0042
0.0013
3.07E+03
1.31E+03
9.07E+07
5.70E-04
8.15E-08
2.00E-01
3.67E-03


0.1429
0.0362
8.28E+04
4.59E+04
3.28E+09
2.00E-02
2.86E-06
7.22E+00
O.OOE+00

0.0072
0.0018
4.17E+03
2.31 E+03
1.65E+08
1.01E-03
1.44E-07
3.64E-01
O.OOE+00


0.1694
0.0444
1.02E+05
5.41 E+04
3.73E+09
2.36E-02
3.38E-06
8.23E+00
2.21 E-01

0.0018
0.0005
1.08E+03
5.75E+02
3.97E+07
2.51 E-04
3.59E-08
8.74E-02
2.35E-03
Average


0.1419
0.0414
9.47E+04
4.44E+04
3.04E+09
1.94E-02
2.77E-06
6.69E-»-00
1.49E-01

0.0037
0.0011
2.56E+03
1.15E+03
7.78E+07
5.02E-04
7.18E-08
1.72E-01
3.50E-03
*Run A-U-315-3 is not included in averages.  This Test was conducted under non-push conditions.

-------
Method 315 Analytical Results (ug) and Blank Corrections
          ABC Coke - Birmingham, Alabama
                  Underfire Stack
Target Catch, ug/sample

Metal
Antimony
Arsenic
Barium
Beryllium
Cadmium
Chromium
Colbalt
Copper
Lead
Manganese
Mercury
Nickel
Phosphorus
Selenium
Silver
Thallium
Zinc
A-U-315-1

0.0
2.8
5.4
0.02
0.31
5.2
0.0
4.9
8.1
5.1
0.0
1.1
15.0
2.0
0.0
0.9
31.0
A-U-315-1
Corrected
0.0
2.8
5.4
0.02
0.31
5.2
0.0
4.9
8.1
2.4
0.0
1.1
15.0
2.0
0.0
0.9
26.0
A-U-315-2

0.0
5.1
12.1
0.07
0.35
10.7
0.0
5.1
8.4
8.3
0.0
2.9
36.0
4.3
0.0
1.0
37.0
A-U-315-2
Corrected
0.0
5.1
12.1
0.07
0.35
10.7
0.0
5.1
8.4
5.6
0.0
2.9
36.0
4.3
0.0
1.0
32.0
A-U-315-3

0.0
4.1
7.8
0.03
0.45
6.7
0.0
4.6
4.3
5.5
0.0
1.9
18.0
4.5
0.0
0.6
34.0
A-U-315-3
Corrected
0.0
4.1
7.8
0.03
0.45
6.7
0.0
4.6
4.3
2.8
0.0
1.9
18.0
4.5
0.0
0.6
29.0
A-U-315-4

0.0
4.7
8.3
0.03
0.47
5.8
0.0
5.7
5.3
8.9
0.0
1.6
30.0
5.2
0.0
0.8
35.0
A-U-315-4
Corrected
0.0
4.7
8.3
0.03
0.5
5.8
0.0
5.7
5.3
6.2
0.0
1.6
30.0
5.2
0.0
0.8
30.0
Filter Blank
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
0.0
2.7
0.0
0.0
0.0
0.0
0.0
0.0
5.0

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - Metals
Underfire Stack
Page 1 of 6




Sb
csb
CSb @ 7% O2
Esb
Esb
Charge

As
CA$
CSb @ 7% O2
EM
EAS
Charge

Ba
CBa
CBa @ 7% O2
EBa
EBa
Charge
RUN NUMBER
RUN DATE
RUN TIME
Antimony
Target Catch, ug
Concentration, ug/dscm
Concentration, |jg/dscm @ 7% O2
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
Arsenic
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% 02
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
Barium
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% 02
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
A-U-315-1
9/24/98
1025-1344

0.0
O.OOE+00
0.0000
0.000
O.OOE+00
O.OOE+00

2.8
2.56E-03
5.73E-03
184,021
3.70E-07
7.28E-09

5.4
4.93E-03
1.11E-02
354,897
7.13E-07
1.40E-08
A-U-315-2
9/24/98
1443-1806

0.0
O.OOE+00
0.0000
0.000
O.OOE+00
O.OOE+00

5.1
4.40E-03
1.04E-02
354,377
6.73E-07
1.24E-08

12.1
1.04E-02
2.46E-02
840,777
1.60E-06
2.93E-08
A-U-315-3
9/25/98
0738-1029

0.0
O.OOE+00
0.0000
0.000
O.OOE+00
O.OOE+00

4.1
3.44E-03
6.22E-03
292,841
5.41 E-07
O.OOE+00

7.8
6.55E-03
1.18E-02
557,113
1.03E-06
O.OOE+00
A-U-315-4
9/25/98
1110-1428

0.0
O.OOE+00
0.0000
0.000
O.OOE+00
O.OOE+00

4.7
4.08E-03
7.67E-03
324,476
6.20E-07
1.67E-08

8.3
7.21E-03
1.35E-02
573,011
1.10E-06
2.95E-08

Average


0.0
O.OOE+00
0.0000
0.000
O.OOE+00
O.OOE+00

4.20
3.68E-03
7.93E-03
287,625
5.54E-07
1.21E-08

8.60
7.53E-03
1.64E-02
589,562
1.14E-06
2.43E-08
*Run A-U-315-3 is not included in averages. This Test was conducted under non-push conditions

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - Metals
Underfire Stack
Page 2 of 6





Be
CBe
CBe @ 7% O2
EBe
EBe
Charge

Cd
Ccd
CCd @ 7% O2
Ecd
Ecd
Charge

Cr
CCr
CCr @ 7% O2
ECr
Ecr
Charge
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA - Continued
Beryllium
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% O2
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
Cadmium
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% 02
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
Chromium
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% 02
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
A-U-315-1
09/24/98
1025-1344


0.0
1.83E-05
4.09E-05
1,314
2.64E-09
5.20E-11

0.3
2.83E-04
6.34E-04
20,374
4.09E-08
8.06E-10

5.2
4.75E-03
1.06E-02
341,753
6.86E-07
1.35E-08
A-U-315-2
09/24/98
1443-1806


0.1
6.04E-05
1.42E-04
4,864
9.24E-09
1.70E-10

0.4
3.02E-04
7.12E-04
24,320
4.62E-08
8.49E-10

10.7
9.24E-03
2.18E-02
743,497
1.41E-06
2.60E-08
A-U-315-3
09/25/98
0738-1029


0.0
2.52E-05
4.55E-05
2,143
3.96E-09
O.OOE+00

0.5
3.78E-04
6.82E-04
32,141
5.94E-08
O.OOE+00

6.7
5.63E-03
1.02E-02
478,545
8.84E-07
O.OOE+00
A-U-315-4
09/25/98
1110-1428


0.0
2.61 E-05
4.90E-05
2,071
3.96E-09
1.07E-10

0.5
4.08E-04
7.67E-04
32,448
6.20E-08
1.67E-09

5.8
5.04E-03
9.47E-03
400,417
7.66E-07
2.06E-08

Average



0.04
3.49E-05
7.74E-05
2,750
5.28E-09
1.09E-10

0.4
3.31E-04
7.05E-04
25,714
4.97E-08
1.11E-09

7.23
6.34E-03
1.40E-02
495,223
9.55E-07
2.00E-08
*Run A-U-315-3 is not included in averages. This Test was conducted under non-push conditions

-------
Summary of Stack Gas Parameters and Test
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - Metals
Underfire Stack
Page 3 of 6
Results
RUN NUMBER A-U-315-1 A-U-315-2 A-U-315-3
RUN DATE 09/24/98 09/24/98 09/25/98
RUNTIME 1025-1344 1443-1806 0738-1029


C






C






C



Co
Ceo
Co @ 7% O2
ECO
ECO
Charge

Cu
Ccu
Cu @ 7% O2
ECU
ECU
Charge

Pb
Cpb
Pb @ 7% O2
EPb
Epb
Charge
EMISSIONS DATA - Continued
Colbalt
Target Catch, pg
Concentration, pg/dscm
Concentration, pg/dscm @ 7% 02
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
Copper
Target Catch, pg
Concentration, pg/dscm
Concentration, pg/dscm @ 7% 02
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
Lead
Target Catch, ug
Concentration, pg/dscm
Concentration, ug/dscm @ 7% 02
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged

0.
0.

0.
0.


0.0
OOE+00
OOE+00
0
OOE+00
OOE+00

4.9
4.47E-03
1
.OOE-02
322,036
6
1


7
1
.47E-07
.27E-08

8.1
.39E-03
.66E-02
532,346
1
2
.07E-06
.11E-08

0.
0.

0.
0.


0.0
OOE+00
OOE+00
0
OOE+00
OOE+00

5.1
4.40E-03
1
.04E-02
354,377
6
.73E-07
1.24E-08


7
1

8.4
.25E-03
.71E-02
583,680
1
.11E-06
2.04E-08

0.0
O.OOE+00
0.

0.
OOE+00
0
OOE+00
O.OOE+00


3
6

4.6
.86E-03
.98E-03
328,554
6
0.


3
.07E-07
OOE+00

4.3
.61E-03
6.52E-03
307,126
5
0.
.68E-07
OOE+00
A-U-315-4
09/25/98
1110-1428

0.
0.

0.
0.


4
9
0.0
OOE+00
OOE+00
0
OOE+00
OOE+00

5.7
.95E-03
.31E-03
393,514
7
2


4
8
.52E-07
.02E-08

5.3
.61E-03
.65E-03
365,899
7
1
.OOE-07
.88E-08
Average
0.00
O.OOE+00
O.OOE+DO
0
O.OOE+00
O.OOE+00

5.23
4.61 E-03
9.90E-03
356,642
6.91 E-07
1.51E-08

7.3
6.42E-03
1.41E-02
493,975
9.59E-07
2.01 E-08
*Run A-U-315-3 is not included in averages. This Test was conducted under non-push conditions

-------
Summary of Stack Gas Parameters and Test
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - Metals
Underfire Stack
Page 4 of 6
RUN NUMBER
RUN DATE
RUN TIME
A-U-315-1
09/24/98
1025-1344
A-U-315-2
09/24/98
1443-1806
Results
A-U-315-3
09/25/98
0738-1029

A-U-315-4
09/25/98
1110-1428

Average
EMISSIONS DATA - Continued
Manganese


C






C






Mn
CMn
Mn @ 7% 02
EMn
EMH
Charge

Hg
CHg
Hg @ 7% 02
EH9
EHg
Charge

Ni
CNI
CNi @ 7% O2



ENi
ENi
Charge
Target Catch, ug
Concentration,
Concentration,
Emission Rate,
Emission Rate,
ug/dscm
pg/dscm @ 7% O2
ug/hr
Ib/hr
Pounds per Ton of Coal Charged
Mercury

2
4
2.4
.19E-03
.91 E-03
157,732
3
6

Target Catch, ug
Concentration,
Concentration,
Emission Rate,
Emission Rate,
ug/dscm
pg/dscm @ 7% 02
pg/hr
Ib/hr
Pounds per Ton of Coal Charged
Nickel

.17E-07
.24E-09

0.0
O.OOE+00
0.

0.
0.

Target Catch, ug
Concentration,
Concentration,
Emission Rate,
Emission Rate,
pg/dscm
pg/dscm @ 7% 02
pg/hr
Ib/hr
Pounds per Ton of Coal Charged
1
2

OOE+00
0
OOE+00
OOE+00

1.1
.OOE-03
.25E-03
72,294
1.45E-07
2
.86E-09

4
1
5.6
.84E-03
.14E-02
389,120
7
1


0.
0.

0.
.39E-07
.36E-08

0.0
OOE+00
OOE+00
0
OOE+00
O.OOE+00


2

2.9
.50E-03
5.90E-03
201,509
3
7
.83E-07
.03E-09
2.8
2.35E-03
4.25E-03
199,989
3.70E-07
O.OOE+00

0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

1.9
1.60E-03
2.88E-03
135,707
2.51 E-07
O.OOE+00
6.2
5.39E-03
1.01E-02
428,032
8.18E-07
2.20E-08

0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

1.6
1.39E-03
2.61 E-03
110,460
2. 11 E-07
5.68E-09
4.73
4.14E-03
8.81 E-03
324,962
6.25E-07
1.39E-08

0.00
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

1.87
1.63E-03
3.59E-03
128,087
2.46E-07
5.19E-09
*Run A-U-315-3 is not included in averages. This Test was conducted under non-push conditions

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke • Birmingham, Alabama
US EPA Test Method 315 - Metals
Underfire Stack
Page 5 of 6





P
Cp
Cp @ 7% O2
EP
EP
Charge

Se
Cse
CSe @ 7% O2
Ese
Ese
Charge

Ag
Cag
CAg @ 7% O2
'-Ag
^Ag
Charge
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA - Continued
Phosphorus
Target Catch, pg
Concentration, pg/dscm
Concentration, pg/dscm @ 7% 02
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
Seleniurn
Target Catch, pg
Concentration, pg/dscm
Concentration, pg/dscm @ 7% 02
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
Silver
Target Catch, pg
Concentration, pg/dscm
Concentration, pg/dscm @ 7% 02
Emission Rate, pg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
A-U-315-1
09/24/98
1025-1344


15.0
1.37E-02
3.07E-02
985,826
1.98E-06
3.90E-08

2.0
1.83E-03
4.09E-03
131,443
2.64E-07
5.20E-09

0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00
A-U-315-2
09/24/98
1443-1806


36.0
3.11E-02
7.32E-02
2,501,486
4.75E-06
8.73E-08

4.3
3.71 E-03
8.75E-03
298,789
5.68E-07
1 .04E-08

0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00
A-U-315-3
09/25/98
0738-1029


18.0
1.51E-02
2.73E-02
1,285,644
2.38E-06
O.OOE+00

4.5
3.78E-03
6.82E-03
321,411
5.94E-07
O.OOE+00

0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00
A-U-315-4
09/25/98
1110-1428


30.0
2.61 E-02
4.90E-02
2,071,125
3.96E-06
1.07E-07

5.2
4.52E-03
8.49E-03
358,995
6.86E-07
1.85E-08

0.0
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00

Average



27.00
2.36E-02
5.10E-02
1,852,812
3.56E-06
7.76E-08

3.83
3.35E-03
7. 11 E-03
263,076
5.06E-07
1.14E-08

0.00
O.OOE+00
O.OOE+00
0
O.OOE+00
O.OOE+00
*Run A-U-315-3 is not included in averages. This Test was conducted under non-push conditions

-------
Summary of Stack Gas Parameters and Test Results
S51 2.000
ABC Coke - Birmingham, Alabama
US EPA Test Method 315 - Metals
Underfire Stack
Page 6 of 6





Tl
On
C-n @ 7% O2
En
En
Charge

Zn
Czn
CZn @ 7% 02
Ezn
Ezn
Charge
RUN NUMBER
RUN DATE
RUN TIME
EMISSIONS DATA - Continued
Thallium
Target Catch, |jg
Concentration, ug/dscm
Concentration, |jg/dscm @ 7% 02
Emission Rate, (jg/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
Zinc
Target Catch, ug
Concentration, ug/dscm
Concentration, ug/dscm @ 7% O2
Emission Rate, ug/hr
Emission Rate, Ib/hr
Pounds per Ton of Coal Charged
A-U-315-1
09/24/98
1025-1344


0.9
8.22E-04
1.84E-03
59,150
1.19E-07
2.34E-09

26.0
2.37E-02
5.32E-02
1,708,764
3.43E-06
6.76E-08
A-U-315-2
09/24/98
1443-1806


1.0
8.63E-04
2.03E-03
69,486
1.32E-07
2.43E-09

32.0
2.76E-02
6.51 E-02
2,223,543
4.22E-06
7.76E-08
A-U-315-3
09/25/98
0738-1029


0.6
5.04E-04
9.10E-04
42,855
7.92E-08
O.OOE+00

29.0
2.44E-02
4.40E-02
2,071,316
3.83E-06
O.OOE+00
A-U-315-4
09/25/98
1110-1428


0.8
6.95E-04
1.31E-03
55,230
1.06E-07
2.84E-09

30.0
2.61 E-02
4.90E-02
2,071,125
3.96E-06
1.07E-07

Average



0.90
7.93E-04
1.73E-03
61,288
1.19E-07
2.54E-09

29,33
2.58E-02
5.58E-02
2,001,144
3.87E-06
8.39E-08
*Run A-U-315-3 is not included in averages. This Test was conducted under non-push conditions.

-------
Summary of Stack Gas Parameters and Test Results
ABC Coke - Birmingham, Alabama
CARS Method 429 - PAH's
Baghouse Inlet





Y
AH
Pbar
vm
Tm
P*.tic
T,
Vte
CO2
02
N2
Cp
AP1/2

As
e
Dn




A,
Vm(«|d)
Vmfrtd)
Qm
B*.
Bws(t«t)
V«td
1-Bw.
Md
M,
V.
A
Q,
Q.
Q.IC™,)
1

RUN NUMBER
RUN DATE
RUN TIME
MEASURED DATA
Meter Box Correction Factor
Avg. Meter Orifice Pressure, in. H2O
Barometric Pressure, inches Hg
Sample Volume, ft3
Average Meter Temperature, *F
Stack Static Pressure, inches H2O
Average Stack Temperature, *F
Condensate Collected, ml
Carbon Dioxide content, % by volume
Oxygen content, % by volume
Nitrogen content, % by volume
Pilot Tube Coefficient
Average Square Root Dp, (in. H2O)1/!
Circular Stack? 1=Y.O=N:
Diameter or Dimensions, inches:
Sample Run Duration, minutes
Nozzle Diameter, inches
Tons of Coke pushed
Total Test Time, hours
Tons of Coke per Hour
CALCULATED DATA
Nozzle Area, ft2
Standard Meter Volume, dscf
Standard Meter Volume, dscm
Average Sampling Rate, dscfm
Moisture, % by volume
Moisture (at saturation), % by volume
Standard Water Vapor Volume, ft3
Dry Mole Fraction
Molecular Weight (d.b.), Ib/lb-mole
Molecular Weight (w.b.), Ib/lb-mole
Stack Gas Velocity, ft/s
Stack Area, ft2
Stack Gas Volumetric flow, acfm
Stack Gas Volumetric flow, dscfm
Stack Gas Volumetric flow, dscmm
Isokinetic Sampling Ratio, %
Page 1 of 1
A-l -429-1
9/21/98
1128-1912

1.002
0.8588
29.70
176.494
99
-5.90
120
121.3
0.2
20.30
79.50
0.84
0.6439
0
4680
458
0.183
257.46
7.73
33.3

0.000183
166.098
4.703
3.63E-01
3.3
11.8
5.710
0.967
28.84
28.48
38.6
32.5
75.215
64,724
1,833
99.7

A-l-429-2
9/22/98
1018-1816

1.002
0.4392
29.74
99.075
103
-4.50
136
63.0
0.2
20.30
79.50
0.84
0.4436
0
4680
422
0.183
281.98
7.97
35.4

0.000183
92.605
2.622
2.19E-01
3.1
18.0
2.965
0.969
28.84
28.51
26.9
32.5
52,375
44,174
1,251
88.4

A-l -429-3
9/23/98
1019-1810

1.002
0.5672
29.80
155.926
107
-5.80
135
92.3
0.2
20.30
79.50
0.84
0.5096
0
4680
435
0.183
269.72
7.85
34.4

0.000183
145.053
4.107
3.33E-01
2.9
17.5
4.345
0.971
28.84
28.53
30.8
32.5
60.131
50.842
1,440
116.7


Average


1.002
0.6217
29.75
143.832
103
-5.40
130
92.200
0.20
20.30
79.50
0.84
0.5324

4680
438
0.183
269.72
7.85
34.3

0.000183
134.585
3.811
3.05E-01
3.1
15,766
4.340
0.969
28.84
28.51
32.1
32.50
62,574
53.246
1,508
101.6

-------
   quantdata
Baghouse Inlet
Trunc'd CMPD
Naphtha! cmpdl
2-Methyl cmpd2
Acenaph cmpd3
Acenaph cmpd4
Fluorene cmpdS
Phenant cmpdG
Anthranc cmpd7
Fluorant cmpdS
Pyrene cmpd9
Benzo (a cmpdl 0
Chrysen cmpd11
Benzo (b cmpdl 2
Benzo (k cmpdl 3
Benzo (e cmpdl 4
Benzo (a cmpdl 5
Perylene cmpdl 6
lndeno( cmp17
Dibenz( cmpd18
Benzo (g cmpd19
Quanterra Compound Name Mol. Wt. Method Blank
Naphthalene 1 128.16 340
2-Methylnaphlhalene 2 142.2 25
Acenaphthylene 3 154.21 0
Acenaphthene 4 154.21 0
Fluorene 5 166.21 0
Phenanthrene 6 178.22 24
Anthrancene 7 178.22 0
Fluoranthene 8 202.26 0
Pyrene 9 202.24 0
Benzo (a) anthrancene 10 228.29 0
Chrysene 11 228.28 0
Benzo (b) fluoranthene 12 252.32 0
Benzo (k) fluoranthene 13 252.32 0
Benzo (e) pyrene 14 252.3 0
Benzo (a) pyrene 15 252.3 0
Perylene 16 202.24 0
lndeno(1,2,3-cd) pyrene 17 290.34 0
Dibenz (a,h) anthracene 18 278.33 .0
Benzo (g.h.i) perylene 19 276.34 0
A-l-429-1 Blank Adjusted
360,000 359,660
76,000 75,975
88,000 88,000
15,000 15,000
3,400 3,400
160,000 159,976
16,000 16,000
50,000 50,000
33,000 33,000
15,000 15,000
26,000 26,000
17,000 17.000
9,200 9,200
6,500 6,500
6,300 6,300
1,100 1,100
11,000 11,000
2,500 2,500
11,000 11,000
A-l-429-2 Blank Adjusted
120,000 119,660
24,000 23,975
36,000 36,000
4,300 4,300
16,000 16,000
53,000 52,976
4,300 4,300
18.000 18,000
13,000 13,000
7,000 7,000
12,000 12,000
5,200 5,200
3,700 3,700
2,600 2,600
1,900 1,900
330 330
4,300 4,300
1,100 1,100
3.800 3.800
A-l-429-3 Blank Adjusted
160,000 159,660
41,000 40,975
33,000 33,000
6,300 6,300
18,000 18,000
66,000 65,976
9,100 9,100
25,000 25,000
18,000 18,000
11,000 11,000
18,000 18,000
6,100 6,100
3,600 3,600
3,300 3,300
1,800 1,800
280 280
3,900 3,900
980 980
4,000 4,000

-------
Baghouse Inlet

Naphthalene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, (ig/dscm '
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
2-Methylnaphthalene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Acenaphthylene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Acenaphthene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Fluorene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ng/dscm *
Emission Rate, |ig/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
A-I-429-1

128.16
359,660
359.66
76.5
8,408,972
1.85E-02
5.57E-04

142.20
75,975
75.98
16.15
1,776,321
3.92E-03
1.18E-04

154.21
88,000
88.00
18.71
2,057,470
4.54E-03
1.36E-04

154.21
15000.00
15.00
3.189
350,705
7.73E-04
2.32E-05

166.21
3,400
3.40
0.723
79,493
1.75E-04
5.26E-06
A-I-429-2

128.16
119,660
119.66
45.6
3,424,793
7.55E-03
2.13E-04

142.20
23,975
23.98
9.14
686,189
1.51E-03
4.28E-05

154.21
36,000
36.00
13.73
1,030,357
2.27E-03
6.42E-05

154.21
4300.00
4.30
1.640
123,070
2.71E-04
7.67E-06

166.21
16,000
16.00
6.102
457,937
1.01E-03
2.85E-05
A-I-429-3

128.16
159,660
159.66
38.9
3,357,695
7.40E-03
2.15E-04

142.20
40,975
40.98
9.98
861,716
1.90E-03
5.53E-05

154.21
33,000
33.00
8.03
693,999
1.53E-03
4.45E-05

154.21
6300.00
6.30
1.534
132,491
2.92E-04
8.50E-06

166.21
18,000
18.00
4.382
378,545
8.35E-04
2.43E-05
Average


212,993
212.99
53.7
5,063,820
1.12E-02
3.28E-04


46,975
46.98
11.76
1,108,075
2.44E-03
7.19E-05


52,333
52.33
13.49
1,260,609
2.78E-03
8.16E-05


8533.33
8.53
2.121
202,089
4.46E-04
1.31E-05


12,467
12.47
3.736
305,325
6.73E-04
1.94E-05

-------

Phenanthrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, jig/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Anthrancene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm "
Emission Rate, ug/hr b
Emission Rate, Ib/hr e
Pounds per Ton of Coke Pushed
Fluoranthene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Pyrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Benzo (a) anthrancene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
A-I-429-1

178.22
159,976
160.0
34.01
3,740,293
8.25E-03
2.48E-04

178.22
16000
16.00
3.402
374,085
8.25E-04
2.48E-05

202.26
50,000
50.00
10.63
1,169,017
2.58E-03
7.74E-05

202.24
33,000
33.00
7.016
771,551
1.70E-03
5.11E-05

228.29
15000
15.00
3.1892
350,705
7.73E-04
2.32E-05
A-I-429-2

178.22
52,976
53.0
20.20
1,516,228
3.34E-03
9.45E-05

178.22
4300
4.30
1.640
123,070
2.71E-04
7.67E-06

202.26
18,000
18.00
6.86
515,179
1.14E-03
3.21E-05

202.24
13,000
13.00
4.958
372,073
8.20E-04
2.32E-05

228.29
7000
7.00
2.6694
200,347
4.42E-04
1.25E-05
A-I-429-3

178.22
65,976
66.0
16.06
1,387,494
3.06E-03
8.90E-05

178.22"
9100
9.10
2.215
191,376
4.22E-04
1.23E-05

202.26
25,000
25.00
6.09
525,757
1.16E-03
3.37E-05

202.24
18,000
18.00
4.382
378,545
8.35E-04
2.43E-05

228.29
11000
11.00
2.6781
231,333
5.10E-04
1.48E-05
Average


92,976
93.0
23.43
2,214,672
4.88E-03
1.44E-04


9800
9.80
2.419
229,510
5.06E-04
1.49E-05


31,000
31.00
7.86
736,651
1.62E-03
4.77E-05


21,333
21.33
5.452
507,390
1.12E-03
3.28E-05


11000
1 1 .00
2.8456
260,795
5.75E-04
1.68E-05

-------

Chrysene
Molecular Weight, g/g-raole
Target Catch, ng
ng to ug
Concentration, ng/dscm a
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Benzo (b) fluoranthene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Benzo (k) fluoranthene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, (ig/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr °
Pounds per Ton of Coke Pushed
Benzo (e) pyrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Benzo (a) pyrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
A-I-429-1

228.28
26,000
26.00
5.53
607,889
1.34E-03
4.02E-05

252.32
17,000
17.00
3.61
397,466
8.76E-04
2.63E-05

252.32
9,200
9.20
1.96
215,099
4.74E-04
1.42E-05

252.30
6,500
6.50
1.382
151,972
3.35E-04
1.01E-05

252.30
6300
6.30
1.339
147,296
3.25E-04
9.75E-06
A-I-429-2

228.28
12,000
12.00
4.58
343,452
7.57E-04
2.14E-05

252.32
5,200
5.20
1.98
148,829
3.28E-04
9.27E-06

252.32
3,700
3.70
1.41
105,898
2.33E-04
6.60E-06

252.30
2,600
2.60
0.992
74,415
1.64E-04
4.64E-06

252.30
1900
1.90
0.725
54,380
1.20E-04
3.39E-06
A-I-429-3

228.28
18,000
18.00
4.38
378,545
8.35E-04
2.43E-05

252.32
6,100
6.10
1.49
128,285
2.83E-04
8.23E-06

252.32
3,600
3.60
0.876
75,709
1.67E-04
4.86E-06

252.30
3,300
3.30
0.803
69,400
1.53E-04
4.45E-06

252.30
1800
1.80
0.438
37,855
8.35E-05
2.43E-06
Average


18,667
18.67
4.83
443,295
9.77E-04
2.86E-05


9,433
9.43
2.36
224,860
4.96E-04
1.46E-05


5,500
5.50
1.414
132,235
2.92E-04
8.56E-06


4,133
4.13
1.059
98,596
2.17E-04
6.38E-06


3333
3.33
0.834
79,844
1.76E-04
5.19E-06

-------
  	A-I-429-1       A-I-429-2       A-I-429-3      Average
Perylene
     Molecular Weight, g/g-mole                202.24          202.24          202.24
     Target Catch, ng                          1100.00          330.00          280.00            570.00
     ngtoug                                     1.10            0.28            0.28              0.55
     Concentration, ug/dscm °                   0.2339            0.11            0.07            0.1363
     Emission Rate, ug/hrb                    25,718          8013.89         5888.48           13206.9
     Emission Rate, Ib/hrc                    5.67E-05        1.77E-05        1.30E-05          2.91E-05
     Pounds per Ton of Coke Pushed           1.70E-06        4.99E-07        3.78E-07          8.60E-07
Indeno (1,2,3-cd) pyrene
     Molecular Weight, g/g-mole                290.34          290.34          290.34
     Target Catch, ng                          11,000           4,300           3,900             6,400
     ngtoug                                   11.00            4.30            3.90              6.40
     Concentration, ug/dscm'                     2.34            1.64           0.949             1.643
     Emission Rate, ug/hrb                   257,184         123,070          82,018           154,091
     Emission Rate, Ib/hrc                    5.67E-04        2.71E-04        1.81E-04          3.40E-04
     Pounds per Ton of Coke Pushed           1.70E-05        7.67E-06        5.26E-06          9.98E-06
Dibenz (a,h) anthracene
     Molecular Weight, g/g-mole                278.33          278.33          278.33
     Target Catch, ng                           2,500           1,100              980              1527
     ngtoug                                    2.50            1.10           0.980             1.527
     Concentration, ug/dscm *                    0.532           0.419           0.239             0.397
     Emission Rate, ug/hrb                    58,451          31,483          20,610            36,848
     Emission Rate, Ib/hrc                    1.29E-04        6.94E-05        4.54E-05          8.12E-05
     Pounds per Ton of Coke Pushed           3.87E-06        1.96E-06        1.32E-06          2.38E-06
Benzo (g,h,i) perylene
     Molecular Weight, g/g-mole                276.34          276.34          276.34
     Target Catch, ng                          11,000           3,800           4,000             6,267
     ngtoug                                   11.00            3.80            4.00              6.27
     Concentration, ug/dscm *                    2.339           1.449           0.974             1.587
     Emission Rate, ug/hrb                   257,184         108,760          84,121           150,022
     Emission Rate, Ib/hrc                    5.67E-04     .   2.40E-04        1.85E-04          3.31E-04
     Pounds per Ton of Coke Pushed           1.70E-05        6.78E^06        5.40E-06          9.73E-06
    Milligrams per dry standard cubic meter at 68° F (20° C) and 1 atm.
    Micrograms per hour.
    Pounds per hour.
ND  Not Detectable - Results are below target analyte detection limit.  Values are counted as zero (0) in averages.
{ }   Estimate - Analyte results are below the quantitation limit and above the detection limit.

-------
Summary of Stack Gas Parameters and Test Results
ABC Coke - Birmingham, Alabama
CARB Method 429 - PAH's
Baghouse Outlet
Page 1 of 1


Y
AH
Pbar
vm
Tm
P«talic
T,
W
C02
02
N2
CP
Ap<"

As
0
Dn




A,
Vm(std)
Vm
-------
    quantdata
Baghouse Outlet
Trunc'd Name CMPD
Naphthalene cmpdl
2-Methylnaphthalene cmpd2
Acenaphthylene cmpd3
Acenaphthene cmpd4
Fluorene cmpdS
Phenanthrene cmpd6
Anthrancene cmpd?
Fluoranthene cmpdS
Pyrene cmpd9
Benzo (a) anthrancene cmpdl 0
Chrysene cmpdl 1
Benzo (b) fluoranthene cmpd 1 2
Benzo (k) fluoranthene cmpdl 3
Benzo (e) pyrene cm pd 1 4
Benzo (a) pyrene cmpdl 5
Perylene cmpd16
Indeno (1 ,2,3-cd) pyren cmpl 7
Dibenz (a,h) anthracen cmpdl 8
Benzo (g,h,i) perylene cmpdl 9
Quanterra Compound Name Mol. Wt. Method Blank
Naphthalene 1 128.16 340
2-Methylnaphthalene 2 142.2 25
Acenaphthylene 3 154.21 0
Acenaphthene 4 154.21 0
Fluorene 5 166.21 0
Phenanthrene 6 178.22 24
Anthrancene 7 178.22 0
Fluoranthene 8 202.26 0
Pyrene 9 202.24 0
Benzo (a) anthrancene 10 228.29 0
Chrysene 11 228.28 0
Benzo (b) fluoranthene 12 252.32 0
Benzo (k) fluoranthene 13 252.32 0
Benzo (e) pyrene 14 252.3 0
Benzo (a) pyrene 15 252.3 0
Perylene 16 202.24 0
Indeno (1,2,3-cd) pyrene 17 290.34 0
Dibenz (a,h) anthracene 18 278.33 0
Benzo (g,h,i) perylene 19 276.34 0
A-O-429-1 Blank Adjusted
290,000 289,660
55,000 54,975
50,000 50,000
7,000 7,000
21,000 21,000
66,000 65,976
20,000 20,000
32,000 32,000
16,000 16,000
290 290
740 740
200 200
200 200
130 130
0 ND
0 ND
0 ND
0 ND
0 ND
A-O-429-2 Blank Adjusted
95,000 94.660
24,000 23,975
22,000 22,000
2,500 2,500
7,500 7,500
45,000 44,976
3,300 3,300
14,000 14.000
8,100 8,100
240 240
640 640
180 180
160 160
0 ND
0 ND
0 ND
0 ND
0 ND
0 ND
A-O-429-3 Blank Adjusted
110,000 109,660
36,000 35,975
17,000 17,000
3,500 3,500
8,800 8,800
27,000 26,976
5,100 5,100
12,000 12,000
6,400 6,400
240 240
690 690
210 210
140 140
110 110
0 ND
0 ND
0 ND
0 ND
0 ND

-------
Baghouse Outlet

Naphthalene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ng/dscm "
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
2-Methylnaphthalene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ng/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Acenaphthylene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Acenaphthene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ng/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Fluorene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
A-O-429-1

128.16
289,660
289.7
65.1
7,098,639
1.56E-02
4.71E-04

142.20
54,975
55.0
12.36
1,347,261
2.97E-03
8.94E-05

154.21
50,000
50.0
11.24
1,225,340
2.70E-03
8.13E-05

154.21
7,000
7.00
1.574
171,548
3.78E-04
1.14E-05

166.21
21,000
21.00
4.72
514,643
1.13E-03
3.42E-05
A-O-429-2

128.16
94,660
94.7
34.6
2,352,729
5.19E-03
1.44E-04

142.20
23,975
24.0
8.77
595,887
1.31E-03
3.66E-05

154.21
22,000
22.0
8.05
546,799
1.21E-03
3.36E-05

154.21
2,500
2.50
0.914
62,136
1.37E-04
3.81E-06

166.21
7,500
7.50
2.74
186,409
4.11E-04
1.14E-05
A-O-429-3

128.16
109,660
109.7
26.5
2,692,659
5.94E-03
1.71E-04

142.20
35,975
36.0
8.71
883,352
1.95E-03
5.61E-05

154.21
17,000
17.0
4.11
417,429
9.20E-04
2.65E-05

154.21
3,500
3.50
0.847
85,941
1.89E-04
5.46E-06

166.21
8,800
8.80
2.13
216,081
4.76E-04
1.37E-05
Average


164,660
164.7
42.1
4,048,009
8.92E-03
2.62E-04


38,308
38.3
9.95
942,167
2.08E-03
6.07E-05


29,667
29.7
7.80
729,856
1.61E-03
4.71E-05


4,333
4.33
1.112
106,542
2.35E-04
6.89E-06


12,433
12.43
3.20
305,711
6.74E-04
1.98E-05

-------

Phenanthrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Anthrancene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ng/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Fluoranthene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, fig/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Pyrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to (ig
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr °
Pounds per Ton of Coke Pushed
Benzo (a) anthrancene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
A-O-429-1

178.22
65,976
66.0
14.8
1,616,861
3.56E-03
1.07E-04

178.22
20,000
20.00
4.50
490,136
1.08E-03
3.25E-05

178.22
20,000
20.00
4.50
490,136
1.08E-03
3.25E-05

202.24
16,000
16.00
3.60
392,109
8.64E-04
2.60E-05

228.29
290
0.290
0.0652
7,107
1.57E-05
4.72E-07
A-O-429-2

178.22
44,976
45.0
16.5
1,117,857
2.46E-03
6.86E-05

178.22
3,300
3.30
1.21
82,020
1.81E-04
5.03E-06

178.22
3,300
3.30
1.21
82,020
1.81E-04
5.03E-06

202.24
8,100
8.10
2.96
201,322
4.44E-04
1.24E-05

228.29
240
0.240
0.0878
5,965
1.32E-05
3.66E-07
A-O429-3

178.22
26,976
27.0
6.5
662,385
1.46E-03
4.21E-05

178.22
5,100
5.10
1.23
125,229
2.76E-04
7.95E-06

178.22
5,100
5.10
1.23
125,229
2.76E-04
7.95E-06

202.24
6,400
6.40
1.55
157,150
3.46E-04
9.98E-06

228.29
240
0.240
0.0581
5,893
1.30E-05
3.74E-07
Average


45,976
46.0
12.6
1,132,368
2.50E-03
7.27E-05


9,467
9.47
2.31
232,461
5.12E-04
1.52E-05


9,467
9.47
2.31
232,461
5.12E-04
1.52E-05


10,167
10.17
2.70
250,193
5.52E-04
1.61E-05


257
0.257
0.0704
6,322
1.39E-05
4.04E-07

-------

Chrysene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Benzo (b) fluoranthene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Benzo (k) fluoranthene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Benzo (e) pyrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm "
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Benzo (a) pyrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm "
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
A-O-429-1

228.28
740
0.740
0.166
18,135
4.00E-05
1.20E-06

252.32
200
0.200
0.0450
4,901
1.08E-05
3.25E-07

252.32
200
0.200
0.0450
4,901
1.08E-05
3.25E-07

252.30
130.0
0.1300
0.0292
3,186
7.02E-06
2.11E-07

252.30
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00
A-O-429-2

228.28
640
0.640
0.234
15,907
3.51E-05
9.76E-07

252.32
180
0.180
0.0658
4,474
9.86E-06
2.75E-07

252.32
160
0.160
0.0585
3,977
8.77E-06
2.44E-07

252.30
ND
0.0000
0.0000
0
O.OOE+00
O.OOE+00

252.30
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00
A-O-429-3

228.28
690
0.690
0.167
16,943
3.74E-05
1.08E-06

252.32
210
0.210
0.0508
5,156
1.14E-05
3.27E-07

252.32
140
0.140
0.0339
3,438
7.58E-06
2.18E-07

252.30
110.0
0.1100
0.0266
2,701
5.95E-06
1.72E-07

252.30
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00
Average


690
0.690
0.189
16,995
3.75E-05
1.09E-06


197
0.197
0.0539
4,844
1.07E-05
3.09E-07


167
0.167
0.0458
4,105
9.05E-06
2.63E-07


80.0
0.0800
0.0186
1,962
4.33E-06
1.28E-07


0.00
0.00
0.00000
0
O.OOE+00
O.OOE+00

-------
A-O-429-1
Perylene
Molecular Weight, g/g-mole
Target Catch, ng
ng to fig
Concentration, ng/dscm *
Emission Rate, ng/hr
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Indeno (1,2,3-cd) pyrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ug/dscm a
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Dibenz (a,h) anthracene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr °
Pounds per Ton of Coke Pushed
Benzo (g,h,i) perylene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ng/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coke Pushed
Milligrams per dry standard cubic meter at 68° F (20
Micrograms per hour.
Pounds per hour.

202.24
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00

290.34
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00

278.33
ND
0.00
0.00000
0.0
O.OOE+00
O.OOE+00

276.34
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00
A-O-429-2

202.24
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00

290.34
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00

278.33
ND
0.00
0.00000
0.00
O.OOE+00
O.OOE+00

276.34
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00
A-O-429-3 Average

202.24
ND
0.00
0.00000
0.00
O.OOE+00
O.OOE+00

290.34
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00

278.33
ND
0.00
0.00000
0.00
O.OOE+00
O.OOE+00

276.34
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00


0.00
0.00
0.00000
0
O.OOE+00
O.OOE+00


0.00
0.00
0.00000
0
O.OOE+00
O.OOE+00


0.00
0.00
0.00000
0.00
O.OOE+00
O.OOE+00


0.00
0.00
0.00000
0
O.OOE+00
O.OOE+00
0 C) and 1 atm.


ND Not Detectable - Results are below target analyte detection limit.






Values are counted as zero (0) in averages.
{ } Estimate - Analyte results are below the quantitation limit and above the detection limit.

-------
Summary of Stack Gas Parameters and Test Results
ABC Coke - Birmingham, Alabama
CARB Method 429 - PAH's
Underfire Stack





T
AH
vf
Tm
P«*
T,
Vic
CO,
02
N2
Cp
Ap"2

As
e
Dn
Charge



An
Vm(*(|
V^tfd)
CU
Bw,
IT
1-B«
Md
M.
V.
A
Q.
Q.
O*™*)
I

RUN NUMBER
RUN DATE
RUN TIME
MEASURED DATA
Meter Box Correction Factor
Avg. Meter Orifice Pressure, in. H2O
Barometric Pressure, inches Hg
Sample Volume, ft3
Average Meter Temperature, °F
Stack Static Pressure, inches H2O
Average Stack Temperature, °F
Condensate Collected, ml
Carbon Dioxide content, % by volume
Oxygen content, % by volume
Nitrogen content, % by volume
Pilot Tube Coefficient
Average Square Root Dp, (in. H2O)1/2
Circular Stack? 1=Y,0=N:
Diameter or Dimensions, inches:
Sample Run Duration, minutes
Nozzle Diameter, inches
Tons of Coal Charged
Total Test Time, hours
Tons of Coal per Hour
CALCULATED DATA
Nozzle Area, ft2
Standard Meter Volume, dscf
Standard Meter Volume, dscm
Average Sampling Rate, dscfm
Moisture, % by volume
Moisture (at saturation), % by volume
Standard Water Vapor Volume, ft3
Dry Mole Fraction
Molecular Weight (d.b.), Ib/lb-mole
Molecular Weight (w.b.), Ib/lb-mole
Stack Gas Velocity, ft/s
Stack Area, ft2
Stack Gas Volumetric flow, acfrn
Stack Gas Volumetric flow, dscfm
Stack Gas Volumetric flow, dscmm
Isokinetic Sampling Ratio, %
Page 1 of
A-U-429-1
9/24/98
1026-1345

1.002
1.396
29.85
109.964
99
-1.00
435
429.8
2.7
14.70
82.60
0.84
0.0994
1
187
180
0.740
168.63
3.33
50.6

0.002987
104.145
2.949
5.79E-01
16.3
2571.5
20.231
0.837
29.02
27.23
7.5
190.7
85,825
42,176
1,194
87.6
1
A-U-429-2
9/24/98
1443-1812

1.002
1.344
29.85
117.850
103
-1.00
454
408.8
2.95
15.00
82.05
0.84
0.0924
1
187
180
0.740
183.96
3.48
52.9

0.002987
110.807
3.138
6.16E-01
14.8
3131.8
19.242
0.852
29.07
27.43
7.0
190.7
80,320
39,328
1,114
100.0

A4M29-3
9/25/98
0738-1029

1.002
1.034
29.85
97.169
87
-1.00
465
325.8
2.65
13.20
84.15
0.84
0.0830
1
187
172.5
0.740
0.00
2.85
0.0

0.002987
93.963
2.661
5.45E-01
14.0
3496.5
15.335
0.860
28.95
27.42
6.3
190.7
72,571
35,427
1,003
98.2

A-U-429-4
9/25/98
1110-1427

1.002
1.340
29.85
118.132
102
-1.00
460
370.2
2.8
13.50
83.70
0.84
0.0941
1
187
180
0.740
122.64
3.28
37.4

0.002987
111.269
3.151
6.18E-01
13.5
3326.9
17.425
0.865
28.99
27.50
7.2
190.7
81,966
40,461
1,146
97.6


Average*


1.002
1.360
29.85
115.315
101
-1.00
450
402.9
2.82
14.40
82.78
0.84
0.0953
1.0000
187
180
0.740
158.41
3.36
47.0

0.002987
108.740
3.079
6.04E-01
14.9
3010.1
18.966
0.851
29.03
27.39
7.2
190.73
82,704
40,655
1,151
951
* Averages do not include A-U-429-3.  This was a non-pushing baseline test run.

-------
   quantdata
Underfire Stack
Trunc'd CMPD
Naphthal cmpdl
2-Methyl cmpd2
Acenaph cmpd3
Acenaph cmpd4
Fluorene cmpdS
Phenant cmpd6
Anthranc cmpd7
Fluorant cmpdB
Pyrene cmpd9
Benzo(a cmpdIO
Chrysen cmpdl 1
Benzo(b cmpdl 2
Benzo(k cmpdl 3
Benzo (e cmpdl 4
Benzo(a cmpdl 5
Perylene cmpdl 6
lndeno( cmp17
Dibenz( cmpdl 8
i Benzo (g cmpdl 9
Quanterra Compound Name Mol. Wl. Method Blank
Naphthalene 1 126.16 340
2-Methylnaphthalene 2 142.2 25
Acenaphthylene 3 154.21 0
Acenaphlhene 4 154.21 0
Fluorene 5 166.21 0
Phenanthrene 6 178.22 24
Anthrancene 7 178.22 0
Fluoranthene 8 202.26 0
Pyrene 9 202.24 0
Benzo (a) anlhrancene 10 228.29 0
Chrysene 11 228.28 0
Benzo (b) nuoranthene 12 252.32 0
Benzo (k)tluoranlhene 13 252.32 0
Benzo (e)pyrene 14 252.3 0
Benzo (a) pyrene 15 252.3 0
Perylene 16 202.24 0
lndeno(1.2,3-cd) pyrene 17 290.34 0
Dibenz (a,h) anthracene 18 278.33 0
Benzo (g,h,i) perytene 19 276.34 0
A-U-429-1 Blank Adjusted
100,000 99,660
2,900 2,875
16,000 16,000
280 280
930 930
11,000 10,976
310 310
5,400 5,400
2,700 2,700
160 160
380 380
270 270
0 ND
290 290
230 230
0 ND
0 ND
0 ND
0 ND
A-U-429-2 Blank Adjusted
130,000 129,660
2,300 2,275
68,000 68,000
240 240
690 690
20,000 19,976
460 460
12,000 12,000
21,000 21,000
100 100
460 460
420 420
130 130
1,400 1,400
210 210
0 ND
0 ND
0 ND
0 ND
A-U-429-3 Blank Adjusted
76,000 75,660
1,600 1,575
13,000 13,000
120 120
360 360
9,900 9,876
220 220
4,800 4,800
3,300 3,300
0 ND
290 290
210 210
0 ND
350 350
0 ND
0 ND
0 ND
0 ND
0 ND
A-U-429-4 Blank Adjusted
99,000 98,660
4,400 4,375
NC NC
240 240
1,300 1,300
1,800 1,776
280 280
7,100 7,100
4,600 4,600
150 150
520 520
260 260
110 110
300 300
160 160
0 ND
0 ND
0 ND
0 ND

-------
Underfire Stack

Naphthalene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ng/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
2-Methylnaphthalene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ng/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Acenaphthylene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ng/dscm "
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Acenaphthene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ng/dscm "
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Fluorene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ng/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
A-U-429-1

128.16
99,660
99.66
33.79
2,421,573
5.34E-03
1.05E-04

142.20
2,875
2.88
0.97
69,858
1.54E-04
3.04E-06

154.21
16,000
16.00
5.425
388,774
8.57E-04
1.69E-05

154.21
280.00
0.28
0.0949
6,804
1.50E-05
2.96E-07

166.21
930
0.93
0.3154
22,597
4.98E-05
9.84E-07
A-U-429-2

128.16
129,660
129.66
41.32
2,761,196
6.09E-03
1.15E-04

142.20
2,275
2.28
0.725
48,448
1.07E-04
2.02E-06

154.21
68,000
68.00
21.672
1,448,105
3.19E-03
6.04E-05

154.21
240.00
0.24
0.0765
5,111
1.13E-05
2.13E-07

166.21
690
0.69
0.2199
14,694
3.24E-05
6.13E-07
A-U-429-3

128.16
75,660
75.66
28.44
1,711,580
3.77E-03
O.OOE+00

142.20
1,575
1.58
0.59
35,630
7.85E-05
O.OOE+00

154.21
13,000
13.00
4.886
294,086
6.48E-04
O.OOE+00

154.21
120.00
0.12
0.0451
2,715
5.98E-06
O.OOE+00

166.21
360
0.36
0.1353
8,144
1.80E-05
O.OOE+00
A-U-429-4

128.16
98,660
98.66
31.31
2,152,550
4.75E-03
1.27E-04

142.20
4,375
4.38
1.39
95,453
2.10E-04
5.63E-06

154.21
NC
NC
NC
NC
NC
O.OOE+00

154.21
240.00
0.24
0.0762
5,236
1.15E-05
3.09E-07

166.21
1,300
UO
0.4126
28,363
6.25E-05
1.67E-06
Average*


109,327
109.33
35.48
2,445,106
5.39E-03
1.16E-04


3,175
3.18
1.03
71,253
1.57E-04
3.56E-06


42,000
42.00
13.549
918,439
2.02E-03
2.58E-05


253.33
0.25
0.0825
5,717
1.26E-05
2.73E-07


973
0.97
0.3160
21,885
4.82E-05
1.09E-06

-------

Phenanthrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm "
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Anthrancene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Fluoranthene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Pyrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, |ig/dscm '
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Benzo (a) anthrancene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
A-TJ-429-1

178.22
10,976
10.98
3.722
266,699
5.88E-04
1.16E-05

178.22
310.00
0.31
0.10512
7,532
1.66E-05
3.28E-07

202.26
5400.00
5.40
1.8311
131,211
2.89E-04
5.71E-06

202.24
2700.00
2.70
0.9155
65,606
1.45E-04
2.86E-06

228.29
160.00
0.16
0.05425
3,888
8.57E-06
1.69E-07
A-U-429-2

178.22
19,976
19.98
6.366
425,402
9.38E-04
1.77E-05

178.22
460.00
0.46
0.14660
9,796
2.16E-05
4.09E-07

202.26
12000.00
12.00
3.8245
255,548
5.63E-04
1.07E-05

202.24
21000.00
21.00
6.6928
447,209
9.86E-04
1.87E-05

228.29
100.00
0.10
0.03187
2,130
4.69E-06
8.88E-08
A-U-429-3

178.22
9,876
9.88
3.712
223,415
4.93E-04
O.OOE+00

178.22
220.00
0.22
0.08268
4,977
1.10E-05
O.OOE+00

202.26
4800.00
4.80
1.8040
108,586
2.39E-04
O.OOE+00

202.24
3300.00
3.30
1.2403
74,653
1.65E-04
O.OOE+00

228.29
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00
A-U-429-4

178.22
1,776
1.78
0.564
38,749
8.54E-05
2.28E-06

178.22
280.00
0.28
0.08887
6,109
1.35E-05
3.60E-07

202.26
7100.00
7.10
2.2534
154,907
3.42E-04
9.13E-06

202.24
4600.00
4.60
1.4600
100,362
2.21E-04
5.92E-06

228.29
150.00
0.15
0.04761
3,273
7.22E-06
1.93E-07
Average6


10,909
10.91
3.55!
243,616
5.37E-04
1.05&05


350,00
0.35
0.11353
7,812
1.72E-05
3.66E-0^


8166.67
8.17
2.6363
180,555
3.98E-04
8.50E-06


9433.31
9.43
3.022i
204,392;
4.51E-04
9.14E-06


136.67
0.14
0.04458
3,097-
6.83E-06
« 1.50E-07

-------

Chrysene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, jig/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Benzo (b) fluoranthene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ^g
Concentration, ng/dscm a
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Benzo (k) fluoranthene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ug/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Benzo (e) pyrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, ug/dscm *
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Benzo (a) pyrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ug/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr °
Pounds per Ton of Coal Charged
A-U-429-I

228.28
380.00
0.38
0.1289
9,233
2.04E-05
4.02E-07

252.32
270.00
0.27
0.0916
6,561
1.45E-05
2.86E-07

252.32
ND
0.00
0.0000
0
O.OOE+00
O.OOE+00

252.30
290.00
0.29
0.0983
7,047
1.55E-05
3.07E-07

252.30
230.00
0.23
0.0780
5,589
1.23E-05
2.43E-07
A-U-429-2

228.28
460.00
0.46
0.1466
9,796
2.16E-05
4.09E-07

252.32
420.00
0.42
0.1339
8,944
1.97E-05
3.73E-07

252.32
130.00
0.13
0.0414
2,768
6.10E-06
1.15E-07

252.30
1400.00
1.40
0.4462
29,814
6.57E-05
1.24E-06

252.30
210.00
0.21
0.0669
4,472
9.86E-06
1.87E-07
A-U-429-3

228.28
290.00
0.29
0.1090
6,560
1.45E-05
O.OOE+00

252.32
210.00
0.21
0.0789
4,751
1.05E-05
O.OOE+00

252.32
ND
0.00
0.0000
0
O.OOE+00
O.OOE+00

252.30
350.00
0.35
0.1315
7,918
1.75E-05
O.OOE+00

252.30
ND
0.00
0.0000
0
O.OOE+00
O.OOE+00
A-U-429-4

228.28
520.00
0.52
0.1650
11,345
2.50E-05
6.69E-07

252.32
260.00
0.26
0.0825
5,673
1.25E-05
3.34E-07

252.32
110.00
0.11
0.0349
2,400
5.29E-06
1.42E-07

252.30
300.00
0.30
0.0952
6,545
1.44E-05
3.86E-07

252.30
160.00
0.16
0.0508
3,491
7.70E-06
2.06E-07
Average1*


453.33
0.45
0.1468
10,125
2.23E-05
4.93E-07


316.67
0.32
0.1026
7,059
I.56E-05
3.31E-07


80.00
0.08
0.0254
1,723
3.80E-06
8.57E-08


663.33
0.66
0.2132
14,469
3.19E-05
6.45E-07


200.00
0.20
0.0652
4,517
9.96E-06
2.12E-07

-------

Perylene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ng/dscm *
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Indeno (1,2,3-cd) pyrene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ug/dscm "
Emission Rate, ug/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Dibenz (a,h) anthracene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ug
Concentration, (ig/dscm '
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
Benzo (g,h,i) perylene
Molecular Weight, g/g-mole
Target Catch, ng
ng to ng
Concentration, ug/dscm "
Emission Rate, ng/hr b
Emission Rate, Ib/hr c
Pounds per Ton of Coal Charged
A-U-429-1

202.24
ND
0.00
0.00
0
O.OOE+00
O.OOE+00

290.34
ND
0.00
0
0
O.OOE+00
O.OOE+00

278.33
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00

276.34
ND
0.00
0.0000
0
O.OOE+00
O.OOE+00
" Milligrams per dry standard cubic meter at 68° F (20° C) and 1
Micrograms per hour.
Pounds per hour.
Averages do not include A-U-429-3.


A-U-429-2

202.24
ND
0.00
0.00
0.00
O.OOE+00
O.OOE+00

290.34
ND
0.00
0
0
O.OOE+00
O.OOE+00

278.33
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00

276.34
ND
0.00
0.0000
0
O.OOE+00
O.OOE+00
atm.


A-U-429-3

202.24
ND
0.00
0.00
0.00
O.OOE+00
0

290.34
ND
0.00
0
0
O.OOE+00
0

278.33
ND
0.00
0.00000
0
O.OOE+00
0

276.34
ND
0.00
0.0000
0
O.OOE+00
0



A-U-429-4

202.24
ND
0.00
0.00
0.00
O.OOE+00
O.OOE+00

290.34
ND
0.00
0
0
O.OOE+00
O.OOE+00

278.33
ND
0.00
0.00000
0
O.OOE+00
O.OOE+00

276.34
ND
0.00
0.0000
0
O.OOE+00
O.OOE+00



Average*1


0.06
0.00
0.00

O.OOE+00
O.OOE+QO


o.oo
0.00
0
°!
O.OOE+00
O.OOE+OQ


0.01
0.01
0.00001
(
O.OOE+OI
O.OOE+fl(


O.Of
o.ot
0.0001
;
01
O.OOE+OI
O.OOE+OI



This was a non-pushing baseline test run.
ND Not Detectable - Results are below target analyte detection limit.
Values are counted as zero (0) in averages.
{ } Estimate - Analyte results are below the quantitation limit and above the detection limit.

-------
APPENDIX F




QA/QC DATA

-------
                    PROCEDURES AUDIT FOR METHOD 315
                            ERG LABORATORIES
       The following is a record of a visit to ERG Labs to evaluate their procedures and
handling of Method 315 samples of emission tests from coke ovens. The work was performed by
ERG chemist Mr. Linh Nguyen under the direction of Dr. Joan T. Bursey, Laboratory Director.

       The first objective was to observe the procedure for weighing the samples. After the
samples were logged in, they were transferred to the weighing room, which is temperature and
humidity controlled. The samples were then put in desiccators to desiccate for twenty-four hours
before being weighed. The samples were then weighed on a laboratory balance. The balance
was located on a weighing table, which is especially designed to add stability and provide more
accurate weight measurements.

       Because the analysis of Method 315 samples for Methylene Chloride Extractable Matter
(MCEM) is done over a period of about seven to eight working days, it was not possible to
observe the analysis in its entirety. It was decided to observe two segments of the analysis on
separate visits. During the first visit the procedures handling of the filters for MCEM analysis,
were observed to verify that the analyses were  done according to section 11.2.1.2 of the method.
The chemist was very meticulate in his work and explained the procedures as they were
occurring and answered questions as they were raised. The second visit was about four days later
or midway into the analysis. This segment included the MCEM analysis of the impinger
solutions.  This was done following the procedures in section 11.2.4.1 of the method. This
involved the adding of a known quantity of methylene chloride to the impinger water in a
separatory funnel and extracting off the phase that had separated. This was done a total of three
times.  The extracts were then heated to near dryness, transferred to an aluminum dish where the
extract was allowed to dry and reach equilibration in the balance room. The sample was then
weighed to the nearest 0.1 mg. After analysis was completed and data computed, the data was
reviewed by the laboratory director for accuracy and completeness.

       This observer did not notice any sample handling or analytical procedures outside the
procedures of Method 315 that would result in the invalidation of data for the above referenced
project.

-------
                                                              Pacific Environmen
                                                              Services, Inc.
Memo
        To:     PES Project File S511.000

        From:  Franklin Meadows, Project Manager

        CC:

        Date:   12/15/98

        Re:     First Analytical Laboratory Visit
               The PM and MCEM sample residues were hand delivered by the PES Project Manager to
        First Analytical Laboratory (FAL) for subsequent analysis for 17 trace metals.  The samples were
        received in a dedicated sample receiving area where they were  unpacked and  arranged by Run
        Number and sample fraction. The samples were inspected for integrity, damage, and chain-of-custody
        documentation.  All of the samples were received in good condition and all were accounted for.

               Once the samples were  accounted for, Dr.  William A. Wadlin,  FAL Laboratory Manager,
        assigned a project number to the PES project and logged  the samples into FAL's sample tracking
        system.  Each sample and sample  fraction was assigned  a unique  identification number and the
        samples were again compared to the sample chain-of-custody document.

               During the  sample preparation stage, each sample digestate was labelled with the original
        sample identification code. These numbers were used to track  the sample through the sample
        preparation and digestion process. All raw data printouts and calibration curves are labelled with the
        identification number. These numbers were used throughout the preparation and analysis to the final
        report of the results, so that a paper trail could be generated for each analytical result that tracks the
        result back to the original sample.

               A walk-through of the laboratory indicated that the laboratory was well organized, clean, and
        well maintained. The samples were prepared and analyzed by Dr. Wadlin. Standard FAL procedure is
        to analyze the samples progressively first using the procedure having the least analytical sensitivity
        followed by the procedure having the next  best analytical  sensitivity. The laboratory continuously
        monitors instrument performance and makes necessary  instrument repairs in advance of instrument
        failure  so that samples do not need to be re-analyzed  due to instrument performance outside the
        method QC requirements.

               FAL has been participating in the EPA's quarterly audit for  metals analysis (lead) for the past
        three years.  FAL is also approved by EPA Region I for  EPA Method  29 analyses.
        • Page 1

-------
                          PERFORMANCE AUDIT

Laboratory: Quanterra Environmental Services, Inc.
Address:   880 Riverside Parkway
           West Sacramento, California
Telephone: 916-374-4333
INTRODUCTION
       On December 16, 1998, Mr. Dennis Becvar of Pacific Environmental Services,
Inc. (PES), Baldwin Park, California, conducted a performance audit of laboratory work
just completed by Quanterra Laboratories (Project No. 301802) for PES.  The audit was
conducted at the request of the PES office in Research Triangle Park, North Carolina, for
samples collected by PES under contract to US EPA at ABC Coke, Birmingham,
Alabama (PES Project No. S512.000). The source testing and sample analysis for
polyaromatic hydrocarbons was conducted following the procedures of California Air
Resources Board Method 429 as published on August 9,  1996.

       The audit included a review of quality assurance and quality control procedures,
sample handling, sample analysis, and data reporting.  During this audit the laboratory
was represented by Mr. Eric Redman, Manager of Advanced Technology.  All of the
analytical data and other documentation for this project were available for review by the
auditor at the time of this audit. Also, Quanterra Project Manager, Mr. Robert
Weidenfeld, was available during this audit.

OVERVIEW OF LABORATORY MANAGEMENT AND QUALITY
ASSURANCE PROGRAM

Sample receiving and log-in

       The samples for this project were delivered at 1530 hours on September 29,1998,
directly from the field to the laboratory by PES. A review of the sample log-in sheet
indicated sample temperatures had exceeded the temperature range specified by the

-------
method.  Sample temperatures ranged from 8°C to 23°C. The method specifies that the
temperatures of the samples upon receipt are to be 4°C ± 2°C. No other anomolies were
recorded by the laboratory upon sample receipt. The sample log-in or "project receipt
checklist" (copy attached) used by Quanterra allows for the early "flagging" of problems
with samples when received by the laboratory.  After the samples were logged into the
laboratory information management system (LIMs) they were immediately transferred
and stored in a refrigerator until sample recovery. The temperature of the refrigerator
housing the samples was maintained within the allowable range.

       It should be noted that the PES project manager was not notified by the laboratory
that the sample temperatures of the samples received were outside the allowable range.
The laboratory indicated that they did inform the PES technician of the sample
temperatures.

Sample extraction and concentration

       The samples were extracted on October 3,1998, within the 21 day period after
sample collection as specified by CARB Method 429. The various fractions from the
Modified Method 5 sampling train were combined into one composite sample per test
run.  In order to determine matrix effects each sample was spiked with a PAH surrogate
13c-fluorene. After extraction each sample was concentrated on a rotary evaporator to a
volume of 10 mis. Each sample was then equally split: a total of 5 mis were set aside as
a sample retain, and the remaining 5 mis were further concentrated in preparation for
analysis. The final concentration step was conducted with a turbo extractor using
nitrogen. The extraction laboratory technician did not encounter any special problems
nor did he note any anomolies with the samples. The standard laboratory practice is to
maintain a sample split of each sample received for a period of thirty days.

-------
Analysis
       The analysis for this project work was conducted on GC/MS identified as "VA-4"
equipped with column "DB-5".  The Method Detection Level (MDL) for this analytical
procedure was established approximately one year ago. According to Mr. Redman the
MDL was established by following the procedures of CARB Method 429.  The practical
quantification level (PQL) is based on 5X the MDL as stated by the method.  Prior to
analysis the instrument was standardized with known standards of 10, 50,100, 200 and
500 ug to establish a five point calibration for each of the polyaromatic hydrocarbons
included in Method 429. Each standard was injected at least five times, and from this
data the average response factor, relative response factor, standard deviation and relative
standard deviation were calculated for each PAH. For each analyte, a deutorated
surrogate in the same concentration was used.  Also, each sample contained an internal
standard to which each analysis  was normalized. During instrument standardization a
response factor was established  for each analyte based on the five point calibration just
described.  A relative response factor was also determined based on the internal standard
of di4-Terphenyl.

       The standards for calibrating the instrument were prepared by diluting a stock
standard prepared and certified by the National Institute of Standards and Technology
(NIST). When a new standard is prepared, it is standard  laboratory practice to compare it
to the previous standard to assure the correct dilution was achieved. Since the laboratory
has a sufficiently high volume of analytical work, the standards are generally expended
within a month.

       The concentration of PAH's in the inlet samples were sufficiently high that
several dilutions with iso-octane were required to dilute the sample concentrations within
the standardized range of the instrument. The internal standard was used to determine the
accuracy of any dilutions.

-------
Data Reporting

       All of the calibration and sample information are retained by the LIMs. Also,
printouts are made of the instrument standardizations and the various sample
chromatograms.  Each PAH analyte has an accompanying deutorated surrogate. All of
the final results are normalized to the internal standard and the deutorated surrogates.
The reported data of several samples were evaluated during the audit.  The following
equation is used to calculate the final concentration of a detected analyte:

       CTA=  (AT/AIS) x (Mis ng/(Response Factor x AF))]
       Where: CTA = concentration of analyte to be reported
              AT  =  area of analyte peak
              AIS =  area of internal standard
              MIS  =  mass of the internal standard in ng
              RF  =  response factor of analyte compared to the internal standard
              AF  =  aliquot factor (the analysis is based on a 50:50 split of the sample)

       If two compounds co-elute, both compounds are reported and the analyst makes
an assessment regarding the identity and concentration of each compound and flags the
data for the final reviewer.

       The quality control range for back-to-back injections of samples is ± 30%, and the
internal standards is ± 40%

STAFF EXPERIENCE

       The analyst for this project was Saleh Argunrhtin who has more than twenty years
of experience in gc/ms work, and more than five years of experience with PAH's.

       The analytical assist was Adriana Mesman who has eight years  of analytical
experience with more than five years in PAH work.

-------
       The data reviewer for this project was Teri Stone who has eight years of
experience working in an analytical laboratory with five years of experience directly with
PAHs.

       The report was assembled by Clark Pickell and approved by Eric Redman.  Both
scientists have more than twenty years of experience in analytical laboratory work.

OBSERVATIONS

       The samples from this project had a significant amount of naphthalene, however,
according to the laboratory the naphthalene concentrations did not interfere with the
analysis for the other PAH's. The inlet samples did require a significant amount of
dilution, however, it appears the laboratory made every effort to minimize any additional
error introduced through dilutions. The samples upon receipt at the laboratory were
outside the acceptable temperature range, however, since the samples were not exposed
to elevated temperatures the samples should be representative for this source. The
highest temperature recorded by the laboratory  was 23°C with most of the samples
averaging 11°C.
       The laboratory did follow the quality control requirements specified by the
method as well as the quality control criteria developed by the laboratory.
       The laboratory does employ  qualified staff to conduct PAH analysis. The results
reported by Quanterra should be considered representative of the samples collected in the
field.

FINDINGS
       The PES project manager was not notified regarding the deviation in sample
temperatures upon arrival of the samples at Quanterra. It is recommended the laboratory
incorporate into its LIMs the name and telephone of the PES project manager in order to
quickly notify PES of any concerns regarding the quality of the samples or problems with
the analysis.

-------
                    PACIFIC ENVIRONMENTAL SERVICES.INC.
                                 4700 Duke Drive,
                                       Suite 150
                                     Mason, Ohio
                              Phone: (513) 398-2556
                                Fax: (513)3983342
                                   www.pes.com
                 TEMPERATURE SENSOR CALIBRATION DATA
                         FOR STACK THERMOCOUPLES
THERMOCOUPLE NUMBER:
T4A
 DATE:
12/22/97
BAROMETRIC PRES.(ln.Hg):
AMBIENT TEMP. °F:
29.52
 72
 REFERENCE:
 Mercury-in-glass:

 Other:

'CALIBRATOR:
                                                                  ASTM-3F
                                                                    J.C.
Reference
point
number
1
2
3
4
Source3
(Specify)
Ambient Air
Cold Bath
Hot Bath
Hot Oil
Reference
Thermometer
Temperature,°F
72
52
195
284
Thermocouple
Potentiometer
Temperature, °F
72
51
194
283
Temperature
Difference,"
%
0.00
0.20
0.15
0.13
Type of calibration used.

"fref. temp.aF+460Wtest thermometer temp aF+46Q)   X100
           reftemp,°F+460

Comments:
                            100<1.5%
                      STACK THERMOCOUPLE CALIBRATION FORM      1998 Yearly Calibration

-------
                    PACIFIC ENVIRONMENTAL SERVICES.INC.
                                 4700 Duke Drive,
                                       Suite 150
                                    Mason, Ohio
                             Phone: (513) 398-2556
                                Fax: (513)3983342
                                   www.pes.com
                 TEMPERATURE SENSOR CALIBRATION DATA
                        FOR STACK THERMOCOUPLES
THERMOCOUPLE NUMBER:
 4B
 DATE:
12/23/97
BAROMETRIC PRES.(ln.Hg):
AMBIENT TEMP. °F:
29.52
 74
 REFERENCE:
 Mercury-in-glass:

 Other:

'CALIBRATOR:
                                                                 ASTM-3F
                                                                   J.C.
Reference
point
number
1
2
3
4
Source3
(Specify)
Ambient Air
Cold Bath
Hot Bath
Hot Oil
Reference
Thermometer
Temperature,°F
74
36
208
307
Thermocouple
Potentiometer
Temperature,°F
74
42
204
309
Temperature
Difference,"
%
0.00
1.21
0.60
0.26
"Type of calibration used.
"tefJejniLgF+46QWtest thermometer temp
           reftemp,°F+460

Comments:
      X100
                 100<1.5%
                      STACK THERMOCOUPLE CALIBRATION FORM       1998 Yearly Calibration

-------
                    PACIFIC ENVIRONMENTAL SERVICES.INC.
                                 4700 Duke Drive,
                                       Suite 150
                                     Mason, Ohio
                             Phone:(513)398-2556
                                Fax: (513)3983342
                                   www.pes.com
                 TEMPERATURE SENSOR CALIBRATION DATA
                        FOR STACK THERMOCOUPLES
THERMOCOUPLE NUMBER:
 4E
 DATE:
12/23/97
BAROMETRIC PRES.(ln.Hg):
AMBIENT TEMP. °F:
29.52
 74
 REFERENCE:
 Mercury-in-glass:

 Other:

'CALIBRATOR:
                                                                  ASTM-3F
                                                                   G.Gay
Reference
point
number
1
2
3
4
Source3
(Specify)
Ambient Air
Cold Bath
Hot Bath
Hot Oil
Reference
Thermometer
Temperature,°F
74
38
203
339
Thermocouple
Potentiometer
Temperature,°F
74
38
202
340
Temperature
Difference,"
%
0.00
0.00
0.15
0.13
"Type of calibration used.

"(ref. temo.aF+460Wtest thermometer temp.aF+4601
      X100
           reftemp,°F+460
Comments:
                 100<1.5%
                      STACK THERMOCOUPLE CALIBRATION FORM       1998 Yearly Calibration

-------
                    PACIFIC ENVIRONMENTAL SERVICES.INC.
                                  4700 Duke Drive,
                                       Suite 150
                                     Mason, Ohio
                              Phone: (513) 398-2556
                                Fax: (513) 3983342
                                    www.pes.com
                 TEMPERATURE SENSOR CALIBRATION DATA
                        FOR STACK THERMOCOUPLES
THERMOCOUPLE NUMBER:
 5E
 DATE:
12/23/97
BAROMETRIC PRES.(ln.Hg):
AMBIENT TEMP. °F:
29.52
 74
 REFERENCE:
 Mercury-in-glass:

 Other:

"CALIBRATOR:
                                                                  ASTM-3F
                                                                    J.C.
Reference
point
number
1
2
3
4
Source3
(Specify)
Ambient Air
Cold Bath
Hot Bath
Hot Oil
Reference
Thermometer
Temperature,°F
74
46
200
318
Thermocouple
Potentiometer
Temperature,°F
74
46
200
318
Temperature
Difference,1"
%
0.00
0.00
0.00
0.00
"Type of calibration used.

"(ref. temp.°F+46QHtest thermometer temp.°F+46Q)   X100
           ref temp,°F+460

Comments:
                            100<1.5%
                      STACK THERMOCOUPLE CALIBRATION FORM       1998 Yearly Calibration

-------
                    PACIFIC ENVIRONMENTAL SERVICES,INC.
                                  4700 Duke Drive,
                                        Suite 150
                                     Mason, Ohio
                              Phone: (513) 398-2556
                                Fax:(513)3983342
                                    www.pes.com
                  TEMPERATURE SENSOR CALIBRATION DATA
                         FOR STACK THERMOCOUPLES
THERMOCOUPLE NUMBER:
 12A
 DATE:
12/24/97
BAROMETRIC PRES.(ln.Hg):
AMBIENT TEMP. °F:
29.44
 72
 REFERENCE:
 Mercury-in-glass:

 Other:

"CALIBRATOR:
                                                                  ASTM-3F
                                                                   S.Simon
Reference
point
number
1
2
3
4
Source8
(Specify)
Ambient Air
Cold Bath
Hot Bath
Hot Oil
Reference
Thermometer
Temperature,°F
72
31
205
352
Thermocouple
Potentiometer
Temperature,°F
72
32
206
352
Temperature
Difference,"
%
0.00
0.20
0.15
0.00
"Type of calibration used.

"fref. temp.°F+46QWtest thermometer temp.°F+460^
      X100
           reftemp,°F+460
Comments:
                 100<1.5%
                       STACK THERMOCOUPLE CALIBRATION FORM      1998 Yearly Calibration

-------
              TEMPERATURE SENSOR CALIBRATION FORM
Temperature Sensor No.
Ambient Temp. °F
Sensor Type
                                              -~e    Length
                                       Barometric Pressure, "Hg
Reference Temp. Sensor:
Date
|-Zt^
« i
••















Ref.
Point
No.
1
2
3
1
2
3
1
2
3
1
2
3
1
2
3
1
2
3
Temp.
Source
ICvL
%!?£'
*H£"O















Temp. °F
Ref.
Sensor
•2»t
"IZ-
tio















Test
Sensor
3z,
6^
zc-s















Temp.
Duf. %
o
-.«
-.7^V















Within
Limits
Y/N
X
X
M















Calibrated
By
\LJ3>
YOi
\l&
tj








"






-------
                    PACIFIC ENVIRONMENTAL SERVICES, INC.

               TEMPERATURE SENSOR CALIBRATION DATA FORM
                               FOR METER BOX
DATE:
10-16-97
AMBIENT TEMPERATURE:

CALIBRATOR:	G. Gay
           75
THERMOCOUPLE NUMBER:
BAROMETRIC PRES.(ln.Hg):
                                           Other:
MB-1
29.59
                               REFERENCE:
                                       Mercury-in-giass:     ASTM 3F
Reference
point
number
INLET
1
2
3
OUTLET
1
2
3
Source3
(Specify)
Ambient Air
Cold Bath
Hot Bath

Ambient Air
Cold Bath
Hot Bath
Reference
Thermometer
Temperature,°F
75
38
190

75
37
190
Thermocouple
Potentiometer
Temperature,°F
75
38
190

74
37
190
Temperature
Difference,"
°F
0
0
0

-1
0
0
"Type of calibration used.
Allowable tolerance ±5°F
Comments:
                                  METER BOX

-------
                    PACIFIC ENVIRONMENTAL SERVICES, INC.


               TEMPERATURE SENSOR CALIBRATION DATA FORM
                               FOR METER BOX
DATE:
10-17-97
AMBIENT TEMPERATURE:    71   °F

CALIBRATOR:      R.Kolde
THERMOCOUPLE NUMBER:
                               BAROMETRIC PRES.(ln.Hg):
                                           Other:
MB-02
                           29.5
                               REFERENCE:
                                      Mercury-in-glass:     ASTM 3F
Reference
point
number
INLET
1
2
3
OUTLET
1
2
3
Source3
(Specify)
Ambient Air
Cold Bath
Hot Bath
Ambient Air
Cold Bath
Hot Bath
Reference
Thermometer
Temperature,°F
70
34
160
70
34
160
Thermocouple
Potentiometer
Temperature,°F
69
34
159
70
33
160
Temperature
Difference."
°F
-1
0
-1
0
-1
0
"Type of calibration used.

"Allowable tolerance ±5°F


Comments:
                                  METER BOX

-------
                    PACIFIC ENVIRONMENTAL SERVICES, INC.


               TEMPERATURE SENSOR CALIBRATION DATA FORM
                               FOR METER BOX
DATE:
10-16-97
AMBIENT TEMPERATURE:    74  °F

CALIBRATOR:       G. Gay
THERMOCOUPLE NUMBER:    MB-13 in/out

BAROMETRIC PRES.(ln.Hg):      29.59

REFERENCE:
       Mercury-in-glass:     ASTM 3F
                                           Other:
Reference
point
number
INLET
1
2
3
OUTLET
1
2
3
Source3
(Specify)
Ambient Air
Cold Bath
Hot Bath

Ambient Air
Cold Bath
Hot Bath
Reference
Thermometer
Temperature,°F
74
30
190

73
32
190
Thermocouple
Potentiometer
Temperature,°F
74
31
190

72
31
190
Temperature
Difference,1"
°F
0
1
0

-1
-1
0
"Type of calibration used.
 Allowable tolerance +5°F
Comments:
                                  METER BOX

-------
                    PACIFIC ENVIRONMENTAL SERVICES, INC.

               TEMPERATURE SENSOR CALIBRATION DATA FORM
                               FOR METER BOX
DATE:
10-16-97
AMBIENT TEMPERATURE:    74  °F
CALIBRATOR:
     G. Gay
THERMOCOUPLE NUMBER:    MB-14 in/out

BAROMETRIC PRES.(ln.Hg):       29.59

REFERENCE:
       Mercury-in-glass:     ASTM 3F
                                           Other:
Reference
point
number
INLET
1
2
3
OUTLET
1
2
3
Source3
(Specify)
Ambient Air
Cold Bath
Hot Bath
Ambient Air
Cold Bath
Hot Bath
Reference
Thermometer
Temperature,°F
74
30
190
73
32
190
Thermocouple
Potentiometer
Temperature,°F
74
30
191
72
30
191
Temperature
Difference,"
°F
0
0
1
-1
-2
1
aType of calibration used.

"Allowable tolerance ±5°F


Comments:
                                  METER BOX

-------
                    PACIFIC ENVIRONMENTAL SERVICES, INC.


                TEMPERATURE SENSOR CALIBRATION DATA FORM
                                FOR METER BOX
DATE:
12-29-97
AMBIENT TEMPERATURE:    71
CALIBRATOR:
     R.Kolde
THERMOCOUPLE NUMBER:

BAROMETRIC PRES.(ln.Hg):

REFERENCE:
       Mercury-in-glass:

Other:
MB-15
                                                           29.5
                                                                    ASTM 3F
Reference
point
number
INLET
1
2
3
OUTLET
1
2
3
Source3
(Specify)
Ambient Air
Cold Bath
Hot Bath
Ambient Air
Cold Bath
Hot Bath
Reference
Thermometer
Temperature,°F
70
34
160
70
34
160
Thermocouple
Potentiometer
Temperature,°F
69
34
159
71
33
161
Temperature
Difference,"
°F
-1
0
-1
1
-1
1
"Type of calibration used.
 Allowable tolerance ±5°F
Comments:
                                   METER BOX

-------
                   PACIFIC ENVIRONMENTAL SERVICES, INC.


               TEMPERATURE SENSOR CALIBRATION DATA FORM
                               FOR METER BOX
DATE:
17-Oct-97
AMBIENT TEMPERATURE:    68  °F

CALIBRATOR:      R. Kolde
THERMOCOUPLE NUMBER:
                              BAROMETRIC PRES.(ln.Hg):
                                          Other:
RMB-13
                           29.5
                              REFERENCE:
                                     Mercury-in-glass:      ASTM-3F
Reference
point
number
INLET
1
2
3
OUTLET
1
2
3
Source3
(Specify)

Ambient Air
Cold Bath
Hot Bath

Ambient Air
Cold Bath
Hot Bath
Reference
Thermometer
Temperature,°F

68
33
155

68
33
155
Thermocouple
Potentiometer
Temperature,°F

67
34
155

68
34
156
Temperature
Difference,"
°F

-1
1
0

0
1
1
'Type of calibration used.
 Allowable tolerance ±5°F
Comments:
                                  METER BOX

-------
                     PACIFIC ENVIRONMENTAL SERVICES, INC.
DATE:   10-16-97
OPERATOR:
THERMOCOUPLE DIGITAL INDICATOR
       CALIBRATION DATA SHEET

                     INDICATOR NO.
R. Kolde
CALIBRATION DEVICE Digital simulator
SERIAL NO.:
                      MANUFACTURER:
                           MB-1
207
                          Omega
TEST POINT
NO.
1
2
3
4
5
6
7
8
9
10
MILLIVOLT
SIGINAL
-0.692
1.520
3.819
6.092
8.314
10.560
22.251
29.315
36.166
42.732
EQUIVALENT
TEMP °F
0
100
200
300
400
500
1000
1300
1600
1900
DIGITAL INDICATOR
TEMP READING °F
-1
99
200
300
398
500
1001
1300
1601
1900
DIFFERENCE %
0.217391304
0.18
0.00
0.00
0.23
0.00
-0.07
0.00
-0.05
0.00
        Percent difference must be less than or equal to 0.5

        Percent difference:
       (Equivalent temp..°R - Digital indicator tern, °R) * ( 100%)
                         (Equivalent temp, °R)
        Where °R = °F + 460
                                   DIGITAL INDICATOR

-------
                     PACIFIC ENVIRONMENTAL SERVICES, INC.
DATE:   10-17-97
OPERATOR:
CALIBRATION DEVICE Digital simulator
                         THERMOCOUPLE DIGITAL INDICATOR
                               CALIBRATION DATA SHEET
             INDICATOR NO.:

             SERIAL NO.:

               MANUFACTURER:
R. Kolde
                                               MB-02
207
                                               Omega
TEST POINT
NO.
1
2
3
4
5
6
7
8
9
10
MILLIVOLT
SIGINAL
-0.692
1.520
3.819
6.092
8.314
10.560
22.251
29.315
36.166
42.732
EQUIVALENT
TEMP °F
0
100
200
300
400
500
1000
1300
1600
1900
DIGITAL INDICATOR
TEMP READING °F
1
102
203
302
400
503
1004
1304
1604
1905
DIFFERENCE %
-0.217391304
-0.36
-0.45
-0.26
0.00
-0.31
-0.27
-0.23
-0.19
-0.21
        Percent difference must be less than or equal to 0.5 %
        Percent difference:
        Where °R = °F + 460
(Equivalent temp,."R - Digital indicator tem, "R) * ( 100%)
                  ( Equivalent temp, °R)
                                   DIGITAL INDICATOR

-------
                     PACIFIC ENVIRONMENTAL SERVICES, INC.
DATE:   10-16-97
OPERATOR:
                         THERMOCOUPLE DIGITAL INDICATOR
                               CALIBRATION DATA SHEET
R. Kolde
CALIBRATION DEVICE Digital simulator
INDICATOR NO.:

SERIAL NO.:

  MANUFACTURER:
                                               MB-13
207
                                               Omega
TEST POINT
NO.
1
2
3
4
5
6
7
8
9
10
MILLIVOLT
SIGINAL
-0.692
1.520
3.819
6.092
8.314
10.560
22.251
29.315
36.166
42.732
EQUIVALENT
TEMP °F
0
100
200
300
400
500
1000
1300
1600
1900
DIGITAL INDICATOR
TEMP READING °F
0
99
201
301
398
499
999
1298
1598
1900
DIFFERENCE %
0
0.18
-0.15
-0.13
0.23
0.10
0.07
0.11
0.10
0.00
        Percent difference must be less than or equal to 0.5

        Percent difference:
       (Equivalent temp,.°R - Digital indicator tem. °R) * ( 100%)
                         ( Equivalent temp, °R)
        Where °R = °F + 460
                                   DIGITAL INDICATOR

-------
                     PACIFIC ENVIRONMENTAL SERVICES, INC.
DATE:
OPERATOR:
10-17-97
THERMOCOUPLE DIGITAL INDICATOR
      CALIBRATION DATA SHEET

                    INDICATOR NO.:
        R. Kolde
CALIBRATION DEVICE Digital simulator
                    SERIAL NO.:
                              MANUFACTURER:
MB-14
 207
                                              Omega
TEST POINT
NO.
1
2
3
4
5
6
7
8
9
10
MILLIVOLT
SIGINAL
-0.692
1.520
3.819
6.092
8.314
10.560
22.251
29.315
36.166
42.732
EQUIVALENT
TEMP °F
0
100
200
300
400
500
1000
1300
1600
1900
DIGITAL INDICATOR
TEMP READING °F
0
99
199
301
399
499
999
1298
1599
1901
DIFFERENCE %
0
0.18
0.15
-0.13
0.12
0.10
0.07
0.11
0.05
-0.04
        Percent difference must be less than or equal to 0.5
        Percent difference:
        Where °R = °F + 460
               (Equivalent temp,."R - Digital indicator tem, °R) * ( 100%)
                                 ( Equivalent temp, °R)
                                   DIGITAL INDICATOR

-------
                     PACIFIC ENVIRONMENTAL SERVICES, INC.
DATE:
OPERATOR:
                         THERMOCOUPLE DIGITAL INDICATOR
                               CALIBRATION DATA SHEET
12-29-97
CALIBRATION DEVICE
        R. Kolde
         Digital simulator
INDICATOR NO.:

SERIAL NO.:

  MANUFACTURER:
MB-15
 207
Omega
TEST POINT
NO.
1
2
3
4
5
6
7
8
9
10
MILLIVOLT
SIGINAL
-0.692
1.520
3.819
6.092
8.314
10.560
22.251
29.315
36.166
42.732
EQUIVALENT
TEMP °F
0
100
200
300
400
500
1000
1300
1600
1900
DIGITAL INDICATOR
TEMP READING °F
1
101
203
300
400
502
1004
1303
1604
1903
DIFFERENCE %
-0.22
-0.18
-0.45
0.00
0.00
-0.21
-0.27
-0.17
-0.19
-0.13
        Percent difference must be less than or equal to 0.5

        Percent difference:
               (Equivalent temp,."R - Digital indicator tem, °R) * ( 100%)
                                 (Equivalent temp, °R)
        Where °R = °F + 460
                                   DIGITAL INDICATOR

-------
4A
PACIFIC ENVIRONMENTAL SERVICES, INC.
                        4700 Duke Drive,
                               Suite 150
                       Mason, Ohio 45040
                    Phone: (513) 398-2556
                       Fax (513) 398-3342
                           www.pes.com
Pilot Tube Number: 4A Date:
Effective Length: 49" Calibrated By:

Pilot Tube Openings Damaged? YES | NO |

Pilot Tube Assembly Level? [ YES | NO
a , = l.l °(< 10°) a , =
3 , = 0.5 "(<5°) 32 =
Y= 0.8 B = 0.7 A =
z = A sin Y = 0.014 cm (in.) 0.32 cm ( < 1/8 in.)
w = A sin 0 = 0.012 cm (in.) 0.08 cm ( < 1/32 in.)
PA = 0.484 cm (in.)
12/23/97
S. Simon
0.8 °(< 10°)
0.3 °(<5°)
0.967

                                               0.483
                                           cm (in.)
                          D,=
                       0.375
cm (in.)
                                                                          ±L
                                                              •—-•^yq;-"—^j.—	
                                                              	>	.>"i2(*or-)
                                                              	asr-;^g—	
                                                              ^=s^K-r™	-A.?.!*..."' -)
                                                                                      Flow

                                                                  (O)

           The types of face-opening misalignmert shown above wil not affect thebasefne value of Cp(s) so
           long as a, and**, Is less than or equal to 10*,a,and aa is less than or equal to 5". z is loss than or
           equal to O.32 cm (1/8 In.), andw is toss than or equal too.08 cm(1>32 in.) (reference 11.O In
                                      Pitot Tube Calibration Form
                                                                                       1998 Yearly Calibration

-------
4B
PACIFIC ENVIRONMENTAL SERVICES, INC.
                        4700 Duke Drive,
                               Suite ISO
                       Mason, Ohio 45040
                    Phone: (513) 398-2556
                       Fax (513) 398-3342
                           www.pes.com
Pitol Tube Number: 4B Dale:
Effeclive Len£th: 48" Calibrated By:
Pitot Tube Openings Damaeed? YES 1 NO 1

Pilol Tube Assembly Level? | YES | NO
a , 3 °« 10°) a , =
3, - 0 °(<5°) P2 =
Y- 1 9= 1 A =
z = A sin Y = 0.017 cm (in.) 0.32 cm ( < 1/8 in.)
w = A sin 9 = 0.017 cm (in.) 0.08 cm ( < 1/32 in.)
PA = 0.475 cm (in.)
12/23/97
S. Simon
2
!
0.949

                                                                                                  '(< 10°)
                          Pn =
                        0.474
cm (in.)
                          D,=
                         (d)
                        0.375
                                           TK.
cm (in.)
                                            ™::;;	>'	
                                            =^:::::::::ik?!±..°:->
                                                     5j.fc..«-
                                                                    (a)
                                                                                        Flow

                                                                                     (c)
            The types of face-opening mis alignment shown above wi I not affect the baseSne value of Cp(s) so
            long as a1andcSis less than or equal to 1O', B, and Q2 is less than or equal to S*, z Is less than or
            equal to a32 cm (1/8 in.), andw Is less than or equal to O.OB cm(1/32 In.) (reference-! 1.O in
            S&CHcn 16 OV	.		
                                       Pitot Tube Calibration Form
                                                                 1998 Yearly Calibration

-------
4E
PACIFIC ENVIRONMENTAL SERVICES, INC.
                         4700 Duke Drive,
                                Suite ISO
                        Mason, Ohio 45040
                     Phone:(513)398-2556
                        Fax (513) 398-3342
                            www.pes.com
Pitoi
Tube Number: 4E Date:
Effective Length: 49" Calibrated By:
Pilol
Pilot

lube Openings Damaged? YES | NO |
Tube Assembly Level? | YES | NO
a , = o "(< 10°) a , =
3, = 1 °(<5°) (32 =
Y= 0 6= 1 A =
z = A sin Y = 0 cm (in.) 0.32 cm ( < 1/8 in.)
w = A sin 6 = 0.017 cm (in.) 0.08 cm ( < 1/32 in.)
PA = 0.487 cm (in.)
12/23/97
S. Simon
I
3
0.973

                                                                                                     '(< 10°)
                           Pp =
                        0.486
cm (in.)
                           D,=
                        0.375
cm (in.)
            Tha typas of fact-open Ing m it •lignment shown abova will not a ff act In a bssalina valua ofCp(t) «o
            long ii a, a n d a, l> !• 11 than or tqualto 10*, B, and 0, ii ltd than oraqualto 5*. I it la si than or
            aqualto 0.32  cm (1/6 In.), and w is lass than oraqualto 0.08 cm (1/3 2 In.) (rafarance11.0 in
            Sactlon 16.0).	  	
                                       Pitot Tube Calibration Form
                                                                 1998 Yearly Calibration

-------
5C
PACIFIC ENVIRONMENTAL SERVICES, INC.
                        4700 Duke Drive,
                               Suite 150
                       Mason, Ohio 45040
                    Phone: (513) 398-2556
                       Fax (513) 398-3342
                           www.pes.com
Pitot Tube Number: 5C Date:
Effective Length: 61" Calibrated By:

Pitot Tube Openings Damaged? YES 1 NO |

Pitot Tube Assembly Level? | YES | NO
'a , - o °(< 10°) a 2 =
(3, - l °«5°) P2 =
Y= 1 6=1 A =
z = A sin Y = 0.017 cm (in.) 0.32 cm ( < 1/8 in.)
w = A sin 9 = 0.017 cm (in.) 0.08 cm ( < 1/32 in.)
PA = 0.474 cm (in.)
12/23/97
S. Simon
I
!
0.948

                                                                                                  '(< 10°)
                          PH =
                        0.474
                                                0.375
cm (in.)

cm (in.)
                                                                                        Row
               \ B
                         (d)
                                                                                     (c)
                                 t  ~/T
                              	V^	 i
                          ff)
                                                                    (0)
            The types of face-opening misalignment shown above will not affect the baseine value of Cp(s) so
            long as a, and Ojis less than or equal to 10'. B, and Us is less than or equal to 5*. z Is less than or
            equal to O.32 cm (1/8 in.), and w is less than or equal to O.OB cm(1/32 In.) (reference 11.0 In
                                       Pitot Tube Calibration Form
                                                                                        1998 Yearly Calibration

-------
5E
PACIFIC ENVIRONMENTAL SERVICES, INC.
   4700 Duke Drive,
         Suite 150
  Mason, Ohio 45040
Phone: (513) 398-2556
  Fax (513) 398-3342
      www.pes.com
Pitol Tube Number: 5E Date: 12/22/97
Effective Len
Pilot Tube Op
$&'• 64" Calibrated By: S.Simon

emngs Damaged1.' YES j NO |
Pilot Tube Assembly Level? | YES | NO
3,
z = A
w = A
1 °« 10°) a , = 1 °(< 10°)
1 °(<5°) (32 = 3 "(<5°)
Y= 0 0= i A= K122
siny = 0 cm (in.) 0.32 cm (< 1/8 in.)
sin 6 = 0.02 cm (in.) 0.08 cm ( < 1/32 in.)
PA = 0.561 cm (in.)
Pp = 0.561 cm (in.)
D, = 0.375 cm (in.)
^ ! ^ 	 £ _
7 ^V^ / V \ ^B Flowf^/
L! * s\. B L^ * /\ B iy ~1 "A 	 iiil 	 iZTx
\ \ ^-?
\ <•> 1 (b> (c)
-A' 7 . ^ ^.--j,.,...;. 	 - • •• •
^B Flow'^X )l B _^X 	 ^I12(«»f.|
iA 	 «L\ r A _ .> 	 %«....,,
^1,.)
(SI (.)
^2 	 ^
.-X-A- 	 	 <^- 	 ^5t^- 	 	 X-T 	 ««=^==S^ 	 .^feriS) 	 !Z_.l
to B (g)
The typee of fece -opening mil alignment shown above will not affect the baseline value ofCp(s) so
long es a, end a, is less then orequelto 10*, a, and (, is less then or equel lo S*,z Is less then or
equal to 0.32 cm (1/8 In.), and w Is less than or equal to 0.08 cm (1/3 Z In.) (reference 11 .0 In
Section 16.0).
                                  Pitot Tube Calibration Form
                                                       1998 Yearly Calibration

-------
 12A
                        PACIFIC ENVIRONMENTAL SERVICES, INC.
                                             4700 Duke Drive,
                                                    Suite ISO
                                            Mason, Ohio 45040
                                         Phone: (513) 398-2556
                                            Fax (513) 398-3342
                                                www.pes.com
Pilot Tube Number:

Effective Length:
                           12A
                           145"
Pilot Tube Openings Damaged?

Pilot Tube Assembly Level?
       a
       P.
                                        YES
                                     |   YES

                                     °(< 10°)
                                                      1
                            Date:_     12/23/97

                  Calibrated By:
                  NO
                                                                      a ,  =
                                                                                      S. Simon
5
0
°(< 10°)
D«5°)
0.936
      z = A sin Y =

     w = A sin 6 =
             \  ~.
           	A X
                                0.033
                                0.016
                           PA =
                           Pn =
cm (in.)   0.32 cm ( < 1/8 in.)

cm (in.)   0.08 cm ( < 1/32 in.)

0.468                cm (in.)
                                                0.468
                                                0.375
                     cm (in.)
                                                                     cm (in.)
                                                                    (g)
                                                                              - or-}
                                                                                        Flow
             The types of face-opening misalignment shown above will not affect the baseine value of Cp(s) so
             long as a, and °^is less than or equal to 1O*, a, and Q2 is less than or equal to 5*. z is less than or
             equal to 0.32 cm (1/8 in.), and w is less than or equal to O.OB cm(1S2 in.) (reference 11.0 in
             Section
                                       Pitot Tube Calibration Form
                                                                                         1998 Yearly Calibration

-------
                                                                                   9/30/94: CD2-1
                                    CALIBRATION DATA SHSET 2
                                     Type S Phot Tube Inspection

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                                                                        (Signatur«/D«t«t

-------
                  PACIFIC ENVIRONMENTAL SERVICES,  INC.
Box No.:

Date:

Calibrated By :

Plant:


•

DH

inHg

Vw,

Vw2

Vd,

Vd2


Tw

Td

t
                  9-29-98

                    am

                 EPA Coke


                 •

             Delta H

             Vacuum

             Initial RTM

             Final RTM

             Initial DGM

             Final DGM

             Ave. Temp RTM UF

             Ave. Temp DGM "F

             Time (min.)
Bar. Press.(Ps):

Pretest Gamma:

 Pretest dH@:



   RUN1

    2.30

    10.00

   543.645

   555.028

   318.370

   329.663

    71.0

    72.0

    14.0
AVERAGE Y
% Difference from Yearly Y =
                                     1.003
                                    -0.893
                                     1.908
 29.80

 1.012

 1.954



 RUN 2

 2.30

 10.00

555.028

567.630

329.663

342.205

 70.0

 72.0

 15.0
                                                                  in. Hg
 RUNS

 2.30

 10.00

567.630

579.845

342.205

354.466

 70.0

 76.0

 15.0
Vw2 - Vw,
Vd2 - Vd,


Net Volume RTM
Net Volume DGM
Y
dH@
11.383
11.293
1.004
1.962
12.602
12.542
1.003
1.830
12.215
12.261
1.002
1.934
                           ACCEPT
AVERAGE dH@ =

Calculations

Y = (Vw * Pb * (Td + 460)) / (Vd * (Pb + (dHd / 13.6)) * (Tw +460))

dH@ = 0.0317 » dHd / (Pb (Td + 460)) * (((Tw +460) * time) / Vw)'2
                                                                                          4700 Duke Drhre,
                                                                                                Suite ISO
                                                                                        Mason, Ohio 45040 f
                                                                                       Phone:(513)398-2556'
                                                                                         Fax: (513)398-3342
                                                                                             www.pes.com
                            Posttest Dry Gas Meter Calibration Form (English Units)
                                                                                                12/2/98

-------
PACIFIC ENVIRONMENTAL SERVICES, INC.
  4700 Duke Drive.
        Suite ISO
 Mason. Ohio 45040
Phone:(513)398-2556
 Fax:(513)398-3342
    www.pes.com
Box No.: MB-1
Date: 10-27-97
uHBIHHH^m^^^HB
DH Delta H
in Hg Vaccum
Vw, Initial RTM
Vw, Final RTM
VJ, Initial DGM
Vd, Final DGM
Tw Avc. Temp RTM "F
Td Ave. Temp DGM "F
i Time (mm. i
Bar. Press. (Pb):
Calibrated By :
| RUN 1
0.50
10
934.200

-------
     PACIFIC ENVIRONMENTAL SERVICES, INC.
Box No.:

Date:

Calibrated By :

Plant:


•

DH

inHg

Vw,

Vw2

Vd,

Vd2


Tw

Td
      MB 02

      9-29-98

       am

    EPA Coke


   •

Delta H

Vacuum

Initial RTM

Final RTM

Initial DGM

Final DGM

Ave. Temp RTM "F

Ave. Temp DGM "F

Time (min.)
Bar. Press.(Pb):

Pretest Gamma:

 Pretest dH@:




   RUN i

    2.00

    12.00

   581.580

   592.959

   313.545

   325.154


    70.0

    70.0

    15.0
AVERAGE Y
% Difference from Yearly Y =
AVERAGE dH@
                       0.986


                       -1.620


                       1.860
 29.80

 1.002

 1.797




 RUN 2

 2.00

 12.00

592.959

604.663

325.154

337.005


 71.0

 76.0

 15.0
in. Hg
      RUN 3

      2.00

      12.00

     604.663

     618.175

     337.005

     350.664


      72.0

      75.0

      17.0
d^^^^^^^Hfli^Hi^M
Vw2 - Vw,
Vd, - Vd,


•••••MIMB^^H^^HBBHHMVMHMB
Net Volume RTM
Net Volume DGM
Y
dH@
P^HMM^H*^MOHH^^^^^^^^HM1
11.379
11.609
0.975
1.959
•^•^^^^^^••^•••^^^^^^^M
11.704
11.851
0.992
1.838
^^•^^••••^^^••^••^^^H
13.512
13.659
0.990
1.782
                          ACCEPT
                                                                                          4700 Duke Drive,
                                                                                                Suite 150
                                                                                        Mason, Ohio 45040
                                                                                        Phone:(513)398-2556
                                                                                         Fax: (513)398-3342
                                                                                             www.pes-com
Y = (Vw • Pb • (Td + 460)) / (Vd * (Pb + (dHd / 13.6)) * (Tw +460))

dH@ = 0.0317 * dHd / (Pb (Td + 460)) * (((Tw +460) * time) / Vw)'2
                            Posttest Dry Gas Meter Calibration .Form (English Units)

-------
                PACIFIC ENVIRONMENTAL SERVICES, INC.
                                                                             4700 Duke Drive.
                                                                                    Suite 150
                                                                            Mason. Ohio 45040
                                                                           Phone:(513)398-2556
                                                                            Fax: (513)398-3342
                                                                                www.pes.com
Box No.:

Date:
        2          ar. Press.! Pb):

      10-17-97      Calibrated By :
      DH

     inHg

      Vw,

      Vw,

      Vd,

      Yd,

      Tw

      TJ
Delta H

Vacuum

Initial RTM

Final RTM

Initial DGM

Final DGM

Ave. Temp RTM "F

Ave. Temp DGM "F

Time (mm.)
 RUN 1

 0.50

  10

558.612

569.029

I OX.182

118.634

  75

  75

 25.5
 RUN 2

 0.75

  10

574.095

585.906

123.684

135.517

  76

  78

 24.0
 29.50

  RJK


 RUN 3

  1.00

  10

586.200

598.741

135.800

148.334

  78

  80

 22.0
 in. Hg





 RUN 4

  1.50

  10

598.965

f> 12.032

14X.548

161.596

  78

  82

  19.0
 RUNS

 2.00

  10

612.242

030.414

161.792

179.920

  79

  83

 23.0
 RUN 6

 4.00

  10

630.900

M6.492

180.404

195.932

  80

  85

 14.0
Vw?-Vw, Net Volume RTM 10.417 11.811 12.541 13.067 18.172 15.592
Vil, - Vd, Net Volume UGM 10.452 11.833 12.534 13.048 18.128 15.528
Y 0.996 0.999 1-003 1.004 1.006 1.003
dH® 1.719 1.779 1.769 1.822 1.839 1.852
AVERAGE Y = 1.002
Average Y Range = 0.982 TO 1.022
AVERAGE JH@ 1.797
Average dH@ Range = 1.597 TO 1.997

ACCEPT

ACCEPT
Calculations
Y • (Vw • Pb • (Td + 460)) / (Vd • (Pb + (dHd / 13.6)) • (Tw +460))
dH® = 0.0317 » dHd / (Pb (Td + 460)) • (((Tw +460) • t) / Vw)*2

-------
                 PACIFIC ENVIRONMENTAL SERVICES, INC.
Box No.:

Date:

Calibrated By :

Plant:


•

DH

inHg

Vw,

Vw2

Vd,

Vd2


Tw

Td
      3(13)

     9-29-98

       am

    EPA Coke


   •

Delta H

Vacuum

Initial RTM

Final RTM

Initial DGM

Final DGM

Ave. Temp RTM °F

Ave. Temp DGM °F

Time (min.)
Bar. Press.(Ps):

Pretest Gamma:

 Pretest dH@:




   RUN1

    1.90

    6.00

   506.810

   518.900

   954.527

   966.713


    91.0

    97.0

    15.0
AVERAGE Y
% Difference from Yearly Y
AVERAGE dH@ =
                       0.997

                       -0.697

                       1.655
 29.80

 1.004

 1.784




 RUN 2

  1.90

  6.00

518.900

530.308

966.713

978.289


  90.0

  100.0

  15.0
in. Hg
     RUN 3

      1.90

      6.00

     530.308

     543.644

     978.289

     991.885


      90.0

      100.0

      15.0
Vw, - Vw,
Vdj - Vd,


Net Volume RTM
Net Volume DGM
Y
dH@
12.090
12.186
0.998
1.696
11.408
11.576
0.999
1.888
13.336
13.596
0.994
1.381
                          ACCEPT
                                                                           4700 Duke Drive,
                                                                                 Suite 150
                                                                         Mason, Ohio 45040
                                                                        Phone:(513)398-2556
                                                                          Fax: (513)398-3342
                                                                              www.pes.com
Y = (Vw * Pb * (Td + 460)) / (Vd * (Pb + (dHd / 13.6)) * (Tw +460))

dH@ = 0.0317 * dHd / (Pb (Td + 460)) * (((Tw +460) * time) / Vw)'2
                           Posttest Dry Gas Meter Calibration Form (English Units)

-------
                 PACIFIC ENVIRONMENTAL SERVICES, INC.
                                                                               4700 Duke Drive.
                                                                                      Suite [SO
                                                                              Mason. Ohio 45040
                                                                             Phone:(513)398-2556
                                                                              Fax: (513)398-3342
                                                                                  www.pes.com
Box No.:

Date:
      DH

     mHg

      Vw,

      Vw,

      Vd,

      VJ,

      Tw

      Td
        13

      10-16-97


     I

Delta H

Vacuum

Initial RTM

Final RTM

Initial DGM

Final DGM

Ave. Temp RTM "F

Ave. Temp DGM "F

Time (mm.)
Bar. Press.(Pb):

Calibrated By :


    RUN 1

    0.50

     10

   474.707

   484.514

   70.442

   80.267

     90

     95

    24.0
 RUN 2

 0.75

  10
     .w
4H4.860


493.318


 S0.600

 H9.087


  89


  95

  17.0
 29.59

R. Kolde


 RUNS

  1.00

  10

493.733

505.845

 S9.500

101.668

  89

  94

  21.0
 in. Hg




 RUN 4

  1.50

  10

506.082

517.191

101.900

113.061

  89

  95

  16.0
 RUNS

 2.00

  10

517.525

527.985

113.405

123.902

  90

  98

 13.0
 RUN 6

 4.00

  10

528.376

539.639

124.306

135.615

  91

  99

 10.0
Vw, - Vw, Net Volume RTM ').807 X.458 12.112 11.109 10.460 11.263
Vd, - Vd, Net Volume DGM ') 825 X.487 12.168 11.161 10.497 11.309
Y 1.006 1.006 1.002 1.002 1.006 1.000
dH® 1.749 1.763 1.752 1.810 1.794 1.835
AVERAGE Y = 1.004
Average Y Range = 0.984 TO 1.024
AVERAGE dH@ 1.784
Average dH@ Range = 1.584 TO 1.984

ACCEPT

ACCEPT
Calculations
Y m (Vw • Pb • (Td + 460)) / (Vd • (Pb + (dHd / 13.6)) • (Tw +460))
dH® = 0.0317 • dHd / (Pb (Td + 460)) • (((Tw +460) • t) / Vw)*2

-------
                PACIFIC ENVIRONMENTAL SERVICES, INC.
Box No.:
Date:
Calibrated By
Plant:
BBB
DH
inHg
Vw,
Vw,
Vd,
Vd2
Tw
Td
t
1BH
•B9
Vw, - Vw,
Vd, - Vd,


AVERAGE Y
15(5)
9-29-98
: gg
EPA Coke
•••••
Delta H
Vacuum
Initial RTM
Final RTM
Initial DOM
Final DOM
Ave. Temp RTM "F
Ave. Temp DGM "F
Time (min.)
•HB
B^B^B
Net Volume RTM
Net Volume DGM
Y
dH@
=
% Difference from Yearly Y =
AVERAGE dH@ =
Calculations

Bar. Press. (Ps):
Pretest Gamma:
Pretest dH@:

RUN1
1.80
5.00
214.453
230.230
608.315
624.400
72.0
81.0
20.6
HHB|
BBB^I
15.777
16.085
0.993
1.696
0.994
1.296
1,728

30.00
0.981
1.710

RUN 2
1.80
5.00
230.230
245.365
624.400
639.854
72.0
84.0
20.0
••
••
15.135
15.454
0.997
1.728




in. Hg



RUN 3
1.80
5.00
245.365
260.368
639.854
655.294
73.0
86.0
20.0
•••
15.003
15.440
0.991
1.759

ACCEPT


  4700 Duke Drive,
        Suite 150
 Mason, Ohio 45040
Phone:(513)398-2556
 Fax: (513)398-3342
     www.pes.com
Y = (Vw * Pb * (Td + 460)) / (Vd * (Pb + (dHd / 13.6)) * (Tw +460))

dH@ = 0.0317 * dHd / (Pb (Td + 460)) * (((Tw +460) * time) / Vw)'2
                         Posttest Dry Gas Meter Calibration Form (English Units)
        12/2/98

-------
PACIFIC ENVIRONMENTAL SERVICES, INC.
  4700 Duke Drive.
        Suite 150
 Mason. Ohio 45040
Phone:(513)398-2556
 Fax: (513)398-3342
    www.pes.com
Box No.: MB 15
Date: 12-29-97
?•••••••••
DH Delia H
in Hg Vaccum
Vw, Initial RTM
Vw, Final RTM
Vd, Initial DGM
Vd, Final DGM
Tw Ave. Temp RTM "F
Td Ave. Temp DGM "F
l Time (mm.)
ar. Press. (Pb):
ahbrated By :
| RUN 1
0.50
10
150.884
157.026
564.125
570.432
73
76
15.000


RUN 2
0.75
10
157.349
164.869
570.758
578.496
75
MO
15.000
29.15
GGAY
RUN 3
1.00
10
165.074
173.741
578.795
587.643
75
82
IS.O
in. Hg

RUN 4
1.50
10
173.960
1X4.259
5X7.860
598.511
76
K4
15.0
                                                       RUN 5    RUN 6

                                                       2.00      4.00

                                                        10       10

                                                      184.521    197.212

                                                      196.465    :i4.019

                                                      598.779    hi 1.999

                                                      611.127    629.263

                                                        76       78

                                                        H6       88

                                                       15.0      15.0
.^^^•^^^••••i
Vw, - Vw, Net
Vil, - Vd, Net


AVERAGE Y =
iHiSliSSSSIHHI
Volume RTM
Volume UGM
Y
dH®
0.981
Average Y Range =
AVERAGE dH
Average dH®
1.770
Range =
•••••••••••^^••^^•^•••••^Mi^BB^HH^B^^^^^HH^^H
6.142 7.520 H.667 10.299 11.944 16.807
d.307 7738 S.H4X 10.651 12.348 17.264
0.978 0.979 0.990 0.978 0.980 0.982
1.719 1.720 1.720 1.827 1.805 1.830

0.961 TO 1.001

1.570 TO 1.970

ACCEPT

ACCEPT
Calculations


Y -(Vw
dH® *
• Pb • (Td + 460)) / (Vd • (Pb + (dHd / 13.6)) • (Tw +460))
0.0317 • dHd / (Pb (Td + 460)) • (((Tw +460) • t) / Vw)*2

-------
                  PACIFIC ENVIRONMENTAL SERVICES, INC.
Box No.:

Date:

Calibrated By :

Plant:


•

DH

inHg

Vw,

Vw2

Vd,

Vd2


Tw

Td

t
                  6(Rmb 13)

                   9-29-98

                    am

                  EPA Coke
             Delta H

             Vacuum

             Initial RTM

             Final RTM

             Initial DGM

             Final DGM

             Ave. Temp RTM "F

             Ave. Temp DGM "F

             Time (min.)
Bar. Press. (Ps):

Pretest Gamma:

 Pretest dH@:



   RUN 1

    2.30

    4.00

   455.655

   473.310

   223.936

   241.899

    70.0

    71.0

    20.0
Vw, - Vw,     Net volume RTM          17.655

Vd2 - Vd,      Net volume DGM          17.963

                     Y              0.979

                   dH@             1.661
AVERAGE Y =
% Difference from Yearly Y =
                                    0.992
                                    -1.334
                                    1.775
 29.80

 1.005

 1.778



 RUN 2

 2.30

 4.00

473.310

490.345

241.899

259.085

 74.0

 82.0

 20.0
                                                     17.035

                                                     17.186

                                                      1.000

                                                      1.774
in. Hg
      RUNS

      2.30

      4.00

     490.345

     506.805

     259.085

     275.869

      74.0

      85.0

      20.0
                                      16.460

                                      16.784

                                      0.995

                                      1.890
                           ACCEPT
AVERAGE dH@ =

Calculations

Y = (Vw * Pb * (Td + 460)) / (Vd * (Pb + (dHd /13.6)) * (Tw +460))

dH@ = 0.0317 * dHd / (Pb (Td + 460)) * (((Tw +460) * time) / Vw)'2
                                                                                          4700 Duke Drive,
                                                                                                Suite 150
                                                                                        Mason, Ohio 45040
                                                                                       Phone:(513)398-2556
                                                                                        Fax: (513)398-3342
                                                                                             www.pes.com
                           Posttest Dry Gas Meter Calibration Form (English Units)

-------
                   PACIFIC ENVIRONMENTAL SERVICES, INC.
                                                       4700 Duke Drive.
                                                              Suite ISO
                                                      Mason, Ohio 45040
                                                     Phone:(513)398-2556
                                                      Fax: (513)398-3342
                                                          www.pes.com
Box No.:

Date:
      DH

      inHg

      Vw,

      Vw2

      Vd,

      Vd2


      Tw

      Td

       t
      RMB-13 i

      10-17-97



     I

Delta H

Vacuum

Initial RTM

Final RTM

Initial DGM

Final DGM

Ave. Temp RTM "F

Ave. Temp DGM "F

Time (min.)
Bar. Press.(Pb):

Calibrated By :
 29.50

R.Kolde
   RUN 1       RUN 2      RUN 3


    0.50        0.75        1.00


     10          10         10

   669.271    680.835    691.078


   680.326    690.74S    701.245


     23.196     34.797     45.097


     34.289     44.775     55.330
 in. Hg





 RUN 4

 1.50

  10

701.618

713.109

 55.700

 67.254
                      RUNS

                      2.00

                       10

                     713.486

                     723.578

                      67.635

                      77.774
 RUN 6

 4.00

  10

724.113

735.099

 78.300


 89.309
     68.500     67.500     67.000     67.000     67.500     68.500


     73.000     73.500     75.000     75.500     76.500     78.000

     27.000     20.000       18.0       17.0       13.0       10.0
Vwj-Vw, Net Volume RTM 11.055 9.910 10.167 11.491 10.092 10.986
Vdj-Vd, Net Volume DGM 11.093 9.978 10.233 11.554 10.139 11.009
Y 1.004 1.003 1.006 1.007 1.007 1.006
dH@ 1.680 1.712 1.748 1.830 1.850 1.849
AVERAGE Y = 1.005
Average Y Range = 0.985 TO 1.025
AVERAGE dH@= 1.778
Average dH@ Range = 1.578 TO 1.978
ACCEPT
ACCEPT
Calculations
Y = (Vw * Pb * (Td + 460)) / (Vd * (Pb + (dHd / 13.6)) * (Tw +460))
*
dH@ = 0.0317 * dHd / (Pb (Td + 460)) * (((Tw +460) * t) / Vw)"2
                             Initial Dry Gas Meter Calibration Form (English Units)
                                               1998 Yearly Calibration

-------
Pacific Environmental Services VOST Box Calibration
Date: 7/19-98
Vost Box Number: V-2


Bubble Meter
1005 1007
1007 1009
1007 1012
1008

Average: 1007.86



Bubble Meter
1007 1008
1006 1009
1006 1010
1012

Average: 1008.29



1005 1003
1004 1002
1003 1004
1005

Average: 1003.71


Flow Rate: 1.0 l/min
Rotameter Setting:
Bubble Meter Temp. :
Run 1

Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=
Run 2

Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=
Run 3
Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=

0.95
91

Meter Box
8883.5
8903.5
105
104
104.5
18.49
1055.798
0.9546

Meter Box
8903.5
8923.5
105
105
105
18.5
1054.293
0.9564

8924
8944
105
105
105
18.6
1048.624988
0.9572
                               Average Y=
0.9560

-------
Pacific Environmental Services VOST Box Calibration
Date: 7-19-98
Vost Box Number: V-2


Bubble Meter
499.9 498.7
500.9 501.3
498.9 499.8
500.2

Average: 499.96



Bubble Meter
500.2 500.0
501.0 499.8
500.8 499.6
499.8

Average: 500.17



500.0 500.9
500.6 500.7
501.0 500.1
499.5

Average: 500.40


Flow Rate: 0.5 1/min
Rotameter Setting:
Bubble Meter Temp. :
Run 1
Meter Box
Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y—
Run 2
Meter Box
Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=
Run 3
Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=

0.4
91


8837
8852
104
104
104
27.6
530.951
0.9416


8852.25
8867.25
104
104
104
27.5
532.882
0.9386

8867.5
8882.75
105
104
104.5
27.6
539.322345
0.9278
                           Average Y=
0.9360

-------
Pacific Environmental Services VOST Box Calibration
Date: 7-19-98
Vost Box Number: V-2


Bubble Meter
238.5 240.9
239.4 241.0
240.1 240.5
240.8

Average: 240.17



Bubble Meter
238.0 240.1
239.5 240.4
239.6 240.4
240.0

Average: 239.71



240.6 240.8
240.8 240.0
240.2 239.6
239.0

Average: 240.14


Flow Rate: 0.25 1/min
Rotameter Setting:
Bubble Meter Temp. :
Run 1
Meter Box
Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=
Run 2
Meter Box
Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=
Run 3
Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=

0.2
91


8815.5
8822
103
102
102.5
27.3
233.228
1.0298


8822.5
8829
103
103
103
27.35
232.594
1.0306

8829.5
8836
104
104
104
27.3
232.6072273
1.0324
                             Average Y=
1.0309

-------
Pacific Environmental Services VOST Box Calibration
Date: 7/19-98
Vost Box Number: V-l


Bubble Meter
1012 1007
1010 1007
1010 1008
1009

Average: 1009.00



Bubble Meter
1008 1010
1010 1009
1011 1007
1003

Average: 1008.29



1009 1005
1008 1003
1006 1005
1008

Average: 1006.29


Flow Rate:
Rotameter Setting:
Bubble Meter Temp. :
Run 1

Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=
Run 2

Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=
Run 3
Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=
1.0 I/min
l.OS
91

Meter Box
9829
9855
104
104
101
26.25
972.821
1.0372

Meter Box
9855.5
9881.5
104
103
103.5
26.25
968.505
1.0411

9882
9908
104
103
103.5
26.26
968.1358553
1.0394
                               Average Y=
1.0392

-------
Pacific Environmental Services VOST Box Calibration
Date: 7-19-98
Vost Box Number: V-l


Bubble Meter
500.5 501.9
501.9 502.0
500.9 501.7
501.3

Average: 501.46



Bubble Meter
501.5 500.2
501.6 500.2
501.9 500.3
500.5

Average: 500.89



501.8 501.9
502.0 501.5
502.2 501.3
500.8

Average: 501.64


Flow Rate:
Rotameter Setting:
Bubble Meter Temp. :
Run 1

Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=
Run 2

Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=
Run 3
Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=
0.5 I/min
0.6
91

Meter Box
9783
9797.5
101
100
100.5
28.3
503.683
0.9956

Meter Box
9798
9812.5
102
100
101
28.4
501.462
0.9988

9813
9827.5
103
103
103
28.4
499.6810347
1.0039
                           Average Y=
0.9995

-------
Pacific Environmental Services VOST Box Calibration
Date: 7-19-98
Vost Box Number: V-l


Bubble Meter
232.9 232.8
233.0 232.9
233.1 232.9
232.9

Average: 232.93



Bubble Meter
233.0 232.8
233.0 232.8
233.2 232.4
232.2

Average: 232.77



232.8 233.0
232.7 233.2
232.5 233.6
234.0

Average: 233.11


Flow Rate: 0.25 I/min
Rotameter Setting:
Bubble Meter Temp. :
Run 1
Meter Box
Initial Volume
Final Volume
Initial Temp.
Final Temp,
Average Temp.
Time:
QDGM=
Y=
Run 2
Meter Box
Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=
Run 3
Initial Volume
Final Volume
Initial Temp.
Final Temp.
Average Temp.
Time:
QDGM=
Y=

0.32
90


9761.5
9768
99
99
99
28.2
226.785
1.0271


9768.25
9774.75
100
100
100
28.18
226.541
1.0275

9775
9781.5
100
too
100
28.2
226.3804458
1.0297
                             Average Y=
1.0281

-------
        ABC COKE
COKE OVEN EMISSION TEST
 BIR1N1INGHAM, ALABAMA
              /-°a?   AlffUJ
            •vi G~w    Ai6 <5
                                     A.OU^
                                    1 cf 2
Qoaiity Control Check
Mar to Stat of Tests




Viaafly inspect each train for proper anembiy
* . .



.— .. . i. * ^ ,_.
W ••••^HA^ •••M^V^^^v ^^i^^^^^^^^^ MI • «^^ ^^••JA*
Vismflyniip-ctTypeSPftDttnbe
Leak check each leg ofTypoSRtot tube
T,fflfr «4MMA» •inim ^nf «ling «raig
**
DuriiHt Tffitflig

r • ^^^^^*


datasheets
rTfm«.| oprmrrnrr p^"4 ^i tnt log
~™

ra^f«mri tmmiing iitttlJB

T 	 «- 1 	 t- *——£^ L^^H^I^ ^M^rf «A|^» MIM^ M.^^_
uC8K COCGK iZHB OODBw flu* JMBB "•* co^^DQQfQK
rhiniBM iliiiiiiit leg



JyfUOQmi JCJB IB ICB WBIBT OflD flDB IBHBB^K XBDOflSP

accnncy
Data sheeo reviewed by PMdaflydnrin^ testing
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-------
                                                                      Date
                                                                      Page     2 of  2
 Quality Control Cheek
                  Aficr Testing
 Visually 1

 Visually inspect Type SPitot tube
                                                  a
 Leak check
         i leg of the Type S Pint tube
                                                   u
 Leak check tne.
                     uSIE
 Record observations if any
                                                 4£4-
                   FiddLog
 Proji
      sdD and location
                                               j(ao^jt>»xA .  /A*Mnfrt****JtA
                riannefadn
                           «map
 S8IDDx6 ^VB u^DBS 8DB uflvBS
Deviadoua fiom QAPP
DlfficuMes in sampling on

Sample ID
^j2*B AfliQ TDDC Of COU6COOO
                                                                                             L\
I^teetaidanmtols
Analytical pi
Pi C
V Alive

-------
COKE OVEN EMISSION TEST
 BIRMINGHAM, ALABAMA
                                    X J-tf/f-
>3%/-
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-------
2 of 5

Date
R - Recotmended
H » Mandatory

4. M-3 sampling train check: >jj>
initial- (M-) 	 -"-A- •
(should hold
10 in* vacuum rxnai \MJ 	
for- 1/2- mm.; 	 	
Puree sample train- with- stack- eas 	
Constant' rate- samel ing 	 1- per 	
5. Time- test- started- • 	
• Time test- ended- 	
6. Drv zas (• • )* port" initial 	
meter ...... f£nm£ 	
volume: 1' ' * )' port- initial 	 :•• •

• •)• port- initial 	
' • * • final 	
• • rport initial 	
	 • final 	 	
7. Train operation Nozzle changed
during ran during run —

pitch- and- yaw of- probe- o-.k-. 	
nozzle* not scraped* on- nipple 	 •£••
effective- seal* around- pro >e 	
probe moved- at- proper- time 	
probe .heated 	 • •
calculator constants or nomograph
changed when TS and /or TM
chances- significantlv
average time to sec
isokenetics after probe

Average values:
impinger temperature
should- be-< 70*F 	
Post filter gas streamer or
Filter box temperACU-MFv — ,
• *F- c"ircie~"one- • •'• 	
barometric- P taken- and- value

from filter holder while in
stack?
was filter chanced durins run?

f-Ztfg
Test
Run
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-------
3 of 5
Date
R - Reconaended
H - Mandatory

Check on filter holder loosening of
clan-Dine device holder
during run? • :

Accurate IP 	 f\^^ f. 7^~ l^^LLA \
reading ofr 	 *« &**«**, C~ni~ U^U-JH

i*Boin*-e*r temperature 	
'-\jfc~ <****' Minimum sample time of • 37bA' min mat
^ \ ^xHinununi s-unpie volume oz 	 dscf collected
S. Post cest: -• All* openings- smmlmd 	
- recovery- area- clean- sheltered 	
•.l1,1--"!. handled- -with* aioves-.- forceps*
- -jetri- dish sealed, labeled 	
- an*r sample lose 	
grad cyl.
weighed
water- measured- iSid. • • EBB •
- silica ge'l weighed*. • net- ems 	
- condition — color- 	 .* • • • •
	 k- spent 	
- probe* cooled- sufficiently 	
- noaszie removed* and- brushed* 	
- probe brushed1 6* ci™?-- 	
- nozzle* brushes* clean* 	
i „ . J M iJl 1 ." acetone clean 	
/ * Ij_-T~v_ *-*'r'~ **"° *-J" "•innee* *mr**;e 	
-blank taken: acetone-. • vater*. • other-
Capped*
Uaoeien
' sealed 	
	 .., ..._ Liauid* level- raarteed-
. J*fL>uv~& t / I I
9-3/ft
Test
Run
1
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-------
of 5
Date
R » Recomended
M " Mandatory

9. Post test Orsat Analysis of fciitial (MJ
integrated bag sample Ursat '
analyzer - Analyzer leak check
(levels should not fall below Final (M)
0.2 raL in- bnrrette for- 2- inin-. ) 	
Orsat* samples? • Each bar anaivzed- 3- tines-
,M-£P^..aJ5S-£a" within- Ov2I 	
-tlP?.?.?.**68' within 0-.2X 	
*" CO"iSBea" within- 0-.2X 	
Analysis at end ot Cesc. Orsac analyzer
checked against air- (20; 9- +• 0-.3) 	
CO-,* 	 	 .
FO • ZQ-. 9 -• Z- Off
;.t,con 	

grange £M- fuel
uraat- analysis- valid-
orsac solutions changed
when calculated Fo
exceeds fue 1 type • range •
ID. All samples locked uo ~
1L. All data- sheets suomxtted to- observer-^- • •
- Run- isoicenetic- • • • Tamn'obsarver- 	 t
- Particuiate- recoverv 	

?-J/-?«
Teat
Run
1

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Test
Run
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• •



-------
                                                                  Page  5 of 5
J.   NOTES:  Care should be taken, when sampling for organic  compounds,  Co
     follow stringent quality control guidelines to avoid contamination  of  the
     sample and sampling train.  Take note of any occurences  which  could bias
     the sample in any manner.

     Include: (1) General comments; (2) Changes to pretest agreement with
     justification;  (3)  Identify (manufacturer) and describe  condition of
     sampling equipment;  (4)  any abnormal occurrences/during  test program.
     (Additional page(s)  attached:  Yes •••  .No
 Signature of Observer            Affiliation or Observer          Dace

-------
             ABC COKE
   COKE OVEN EMISSION TEST
    BIRMINGHAM,ALABAMA
         //U/ef  /.dCe-f'^AJ      .
                                 3/J
                                                          -
                                                             1 of 2


Mar to Slut of Tests


AMMMM m' j m jlmi fi^g t-iiiiiimiiimii
AUOnOUuaiudlar _ 	 T=rl
Vbmttjr inspect each train fir proper asembiy

Lcmaod^Bi> r-r '"







i
CMrw-R^
J
Ci^fvvjg^
CXwvo^
1
OU«vt<_

CLwv>~^

Cuirv»-t_
 Vbnfly inspect Typo S Fttottnbe
 Lok check acfa leg ofTVpe S Ptettufaa
                                                                     :
Rodl
             DdtfifibOBBi
^JOUDB!
             i mad la
Prepcfiy mjoim tbo nil cod pncix of BCB of TVpe S
dngesdn
         :tea

Muntni ice inksuurtaharti
edttopennB
rgiih
                 fnr
acomcy
Data sheen reviewed by PMdafly during tiKti^g
Wd&^  SA9 - ^1(3^ Z
      r-'-°6
      ^ H - /.'
             -  J.
                                        -  /.o 6 y
                                         j:  A7flV

-------
Date
Page    2 of 2
Quality Control Cheek
Axosf lestmSi

visually inspect sampling name
Visually inspect TypoS Pilot tube
Leak check each leg of the Type SPitot tube




Field Log


Ckoiogicdobsavttonsmdndingmap


Sttpfedescriptfcos
Descripooo of QG samples




Smmi* Labels

Sample ID


r -ah tIMthMmm tnitnll

Analytical parameter

<->ii. . I, .1
umetmioB


<*1AA

'VL**
•


^*4

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SW4

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-------
COKE OVEN EMISSION TEST
 BIRMINGHAM,
Page  1 of 5
I. Test Run Obaefvationa Dcee
B « Becosnended
If • Mandatory
1. Train. see-up- ' filter ID
filter weight
filter checiced for hole*
filter centered
	 - - nozzle- clean- • • •
nozzle • undamaged
nozzle diamacer (in*;}
probe liner eln«i
probe markings correct
probe heeted 4 lone
entire- length* • • •""•
	 ismingers* cnarnd 	
• ' 	 iBBJiasjera- iced 	
	 meeer- box leva-lad* 	

	 filter- oo-c or- Voider- arc- teno*.
ell bell joints Lightly
	 greaaed 	
2. Train leak check Lg 	
to«
Test
Ptrti
A}//}
tU/Pl
•**JLJ*
-^•C!
^ aA
' g^dl^' o A
Jw3

AJJ*
****
JU*A '
'J4-4AA '
'JtiSJ


•tifo-
'•$?&
at nozzles initial- A '
• tJ • •
i /^J"
St4ts4
jLltA
IS
^Lt^\ '
' 'f/bbLA '
' rC^^fy


jo/A-
?$$y
' /j"*/&
• *—^* *
• •«— f •
• T— '
*— - •
Vacuum during LC . 	 j « — >
teat nm. ) intermediate (R) VAC


cneck: necetiTe- tine (R*- • •

( 1 S ••» ^ .... . , . ,_ , •
115 SBC.; MMg-fTm- H-nm- { g-1-

Tedlar bag: Should hold 2 to 4 in. HjO
pressure- far- lO-trinces* or- 	

uimpleceAylTu bag and let
^ P^-bv Urf. UrUti Q^3-"^
ffi-— ~~
•&(J /


•>3*o^
">3V0^

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Test
Run
3
6-7
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• •

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1
1

-------
Date
R « Recommended
M • Mandatory
4. M-3 sampling train check: y
initial- (M-) 	 -j^
(should hoia
lu in* vacuum ixnai \rij 	 	
Purge sample train* with* stack* gas 	
Constant- rate- sampling 	 1- tar 	

• Tine test- ended- 	
6. Dry gas (' • )* port- initial 	 •
meter • 	 final 	
volume: I* ' • ;* port* initial 	
( ) • port* initial 	
•• -final 	
• ; * port initial 	
	 • fii-g} 	
7. Train operation Nozzle changed
during ran during run —

pitch- and* yatr of* probe* o.k*. 	
nozzle- not scraped* on* nxppie 	
er receive- seal- around- probe 	
probe moved- at* proper- tine 	 i
probe .heated* • 	 • • • • •
calculator constants or nomograph
changed when TS and /or TH
changes- significantly-
average tine to set
isokenetics after probe
moved- to- next* point 	
Average values:
• • ^
inpinger temperature

Filter box eemperaeure
^2S6-F"+ 23tX320"r.

* circle one 	

barometric* P taken* and* value

from filter holder while in
stack?
was filter chanced durine run?
1-i*e
Test
Run
/if
/7-/A
J.I/A
* ' 'fiJ/H-'
J. ~
££_
//A
' fo U(t M




• • r 	 •• .
•• '^— ' '
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A) O

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• -,^0- • •
• -^&^' •
s*4£* I
• *sytj&
u
<./o
-------
                               •*""&
#<
	 • 0 -

Date
R - Recomatended
M " Mandatory

Check on filter holder loosening of
damning device holder
waa silica gel changed
during run?
waa "any p'artxculate lost?
Accurate ^P^^^^Qj-tAAo f Cc»»yt. ' tirti^m LJi*i ^
reading of 7 AH f^^JL. ffj-,mY 'fir^-^i '
meter temoej-atixre 	 ' 	 	
stack* temoeratnre 	
AJrfL*/- meter- vacuum- • •S*2cm*ti*d; 	
:;¥£. tine- per* point 	
"^ urn-anger- te-aoeratnre 	
filter* box temoerature 	 • —
Minimum nanp1-* time of 	 min nr*c
Minimum sampl-* volume of •••-•. Amff collected


8. Post test: — All- openings* sealed 	
- recovery area- clean* sheltered- 	
-• filter handled- with* gloves*. • forceps- • •
- petri- dish sealed, labeled 	
• any samole lost 	
grad cyl.
weighed
w«uci lucaouccu *>nu* B"** 	
- "silica- gel- weighed*. • net* BBS 	
- condition - color* 	
	 k* spent* • • 	 * 	
- probe- cooled- sufficiently 	
- nozzle- removed* and* brushed 	
- probe brushed- 6- ein»« • • • 	
— nozzle* brushes* cit$sn 	
Mrtf3M**>. - wash bottles clean* 	
•**"*•*• CNMrtMSx** acetone clean 	 	 ...
*~ M""Q i.5 minute* out1 tie 	
- blank taken: acetone-, water*, other*


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-------
Page
Dace
R " Reconoended
M - Mandatory

9. Post test Orsat Analysis of Initial (MJ
analyzer - Analyzer leak check
(levels should not fall below Final (M)
0.2 nuY in- burrette for- 2- min*. )
Orsat- samples? • Each bar analyzed- 3- tines-
I'- CO-* agrees- vichin- 0;2Z 	
1 u? agrees- within Q-.2X 	
Analysis at end of teac. Orsat analyzer
checked against air- (20-.9- +• 0-.3) 	
co->z 	 .'....

euer • "• 	
F^range- fov fuel
ursar analysis- valid
Ora«c solutions changed
when calculated F0
exceeds foe 1 • type - range •
iu. All samples locxea up
All sampling- components- clean- and- sealed-
( ^£ All data- sheets submit ted- CD* observer —
- Run- isoicenetxc- Team/Obierver- 	
- Particuiate- recovery 	 - 	
/ -7^ 5"
-------
                                                                 Page   5 «* 3

J.   NOTES:  Care  should be  taken,  when sampling  for organic compounds,  Co
     follow stringent quality control guidelines  to avoid contamination  of the
     sample and sampling train.   Take note of any occurences which could bias
     the sample in any manner.

     Include: (1)  General comments; (2) Changes to pretest agreement with
     justification;  (3) Identify (manufacturer) and describe condition of
     sampling equipment; (4)  any abnormal occurrences during test program.
     (Additional page(s) attached:   Yes  ; •  , No  _;tX»)
  Signature of Observer             Affiliation  or Observer

-------
             ABC COKE

  COKE OVEN EMISSION TEST
    BIRMINGHAJVALABAMA
            1^1*
              4, r
                                                          Page    l of z
                                     \N>i/vv>.
Qomitty Control Check
            Mar to Sine of Tests
                                         <3Mr>^A_
Aaioiibte urn in duu flee taaiu
Vfamily inspect each tan for proper assembly
Levgjaadianimfnnmrttr
VtaailymspeasinipiingnaaziB fir drips
                              
-------
         Date
         Page  2of 2
Quality Control Cteek
After Testing


Visnaily inspect Type SRtot tube
Leak check each leg of the Type SPitot tube




Field Log
Project name/ID and location


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COKE OVEN EMISSION TEST
                                              iof
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I. Teat Ron Observations Date
R • Recoanended
M • Mandatory
1. Train, set- up- ' filter ID







entire* length 	




	 orifice- -aanimBtM- zeroed 	
	 filter- bar- f»-t»riri.*-ac. team-.
	 greaaed 	
	 all- ODeninRa-caiiMd 	

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-------
• to «
Page
Date
R «• Reconnended
M - Mandatory

4. M-3 sampling train check:

(should hold

for* 1/2- min. ) 	
Purse samoie train- with* stack* eaa • • 	
• Constant- rate- sampling 	 1- tmr 	
5. Time- test* started* 	
• Time tear ended 	
6. Dry zas (' * >' port* in-Leiai 	
meter • • 	 finai 	
volume: (• • • )• port* initial 	 :•• *
	 final 	 • *
( " ')' pore* ini.CTxi 	
' -final 	

7. Train operation Nozzle changed
during ran during nm —

pitch* and* yaw of* probe* o-.Ic*. 	

probe .heated* *. 	 • • • • •
calculator cons cants or nomograph
changed when TS and /or TM
changes- significantly*
isokenetics after probe
moved* to* next* point 	
iopinger temperature
should- be-< 70-F 	


• *T* c"ircie""one- -•'••• 	


from filter holder while in
scack?

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-------
                                                                                               Page
                                                                                                       3 of 5
ftkdjL
Dace
R « Recommended
M » Mandatory
Check on filter holder loosening of
cla-Boing device holder
during run?
w«» any Particuiate lost*
Accurate AP /j-trtAx^^ fjou^: L)a2*.fiJ\


- recovery area- clean- sheltered 	
- petri* dish sealed T labeled 	
ft — anv* samole lost* • 	
W,v «rad cyl.
/weighed
water- measured* • mL • • m* 	
- silica- gel* weighed*. • net* pip* 	
- condition - color- * * * - LMij^Vtiife. \ffl i^
	 ii* spent- : 	
- probe- cooled* suff icientiv 	
- nozzie* removed- and* bnnhed* 	
- probe brushed' 6* Cim»« • • • 	
— nozzle* brushes* clean* 	
- blank taken: acetone*, water*, other*

Caooed*
Laoeled
sealed 	
Liouid- lev-si- -narked* |
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-------
Page •* of 3
	 	 :SjutoT«P3'/y
Dace
R * Recommended
M « Handacory
9. Pose test Orsac Analysis of Initial (M*
analyzer - Analyzer leak check
(levels should not fall below Final (M-)
0.2 mL in- burrette for- 2'min-. ) 	
Orsat- samples?- Each bag- analyzed- 3- tines-
Z CO-» aerees- virhin- 0-.2Z- • ' •
S' CP" afTBea' within- 0-.2X 	
checked aeainse air- (20-.9- •*•• 0-.3) 	
0^* 	 	 	 '
Fo » 2U-.9 -Z 07 ~~~
Fuel- • • - - ' - • 	 	
UrsaC* analm» v v*4it4-
Orsac aoluciona changed
when calcnlaeed F0
exceeds f»« 1 type -ranee
-^t-All data- sheecs subnet cceo- to- at>«ervetr
- Run- isoieeneeic 	 ^•^Obnmmr 	

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-------
                                                                  Page   5 of  5

 J.   NOTES:  Care should be  taken, when sampling  for organic compounds, to
      follow stringent quality control guidelines  to avoid contamination of the
      sample and sampling train.   Take note of any occurences which could bias
      Che sample in any manner.

      Include: (1) General  comments; (2) Changes to pretest agreement with
      justification;  (3) Identify (manufacturer) and describe condition of
      sampling equipment; (4)  any abnormal occurrences during test program.
      (Additional page(s) attached:  Yea • ••  . No  t/ «J
S).
•C^Uu/J
                       _
   Signature of  Observer             Affiliation of Observer          Dace

-------
        ABC COKE
COKE OVEN EMISSION TEST
 BIRMINGHAM. ALABAMA
    Oof/e/  £•£<*//«xJ

       Date
       Page
                                              1 of 2
~^r*~"
Quality Control duck
Prior to Start of Tests




Visually inspect each train for proper assembly
wit ,





Visually inspect Typo SPitot tube
Leak check each leg of Type SPitot tube
T mmlf rlianlr ^M«M»» 	 untiling 4ffWtft

^.pQUDJC XCSt^Dff



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-------
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-------
COKE OVEN EMISSION TEST
 BIRMINGHAM, ALABAMA
1 of 5
£. Teat Run ObaerVationa Date
R - Reconnended
H - Mandatory
* • "... . .
1. Train, see- TIP- " filter ID
filter weight

filter centered
	 * ' nozzle clean* • • •
nozzle • undan«Mfi
nozzle diameter (isa*
probe Liner clean
probe aarkinxa correct
probe heated ilonc
entire* length 	
	 mpxttgers* eaareed* 	 •'
	 •UHpinsjers" iced 	 • • • •
	 meter* box leveled* • • • 	
• • • • ... nri f*? rrr Tnano"» * n i zeroitd' • • • •
	 filter- ooar or- hoida-r- ar- reonr.
all ball joints Lightly
	 Kreaaed 	
	 •U-oaaBUBn-anpaa 	 •
2. Train leak check LC 	
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-------
                                        Page
                                              2 of 5
Date
R ** RecoDBended
M • Mandatory

4. M-3 sampling train check:

(should hold

for- 1/ 2- -Bin.; 	
Pnr^e sample train* with* stack- gas • * • • 	
• • • Constant* race* sampling 	 1* par 	
5* Time* test* scarred* • • 	 	
* Time tesc* ended* 	
6. Dry gas (* • )• port' initial 	 	
meter * * 	 final 	
volume: (' * * )- port- initial 	 •• •
	 finMi 	 .- • •
* •;* port- initial 	
• ' ' "final 	
* ' ; • port iniri»l 	
	 * final 	
7. Train operation Nozzle changed
during ran during ran —

pitch- and- yaw of- probe- o*.Ir. 	
nozzle* not scraned- on- nip >ie 	
effective- seal* around- pro; m 	
probe moved- at- pronex- time 	
probe .heated* • 	 • • • •
calculator constants or nomograph
changed when TS and /or TM
chances* significantly
average cine to set
isokenetics after probe

Average values:
inpinger temperature
should- be-< 70*»F 	
Post filter gas streamer or
 <320~F,
* cxrcie one 	

barometric- P taken- and- value

from filter holder while in
stack?

t**i
Test
Run
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-------
                                                                                Page
                                                                                       3 of 5
<
^    ,
Date
R « RecoBttnended
M - Mandatory

Check on filter holder loosening of
elamoin*-* device holder
was silica gel changed
during run? • • •
was any parciculate lost?
Accurace A p. _ .,..„,,,, Jf Sff***^ l*W&
reading oft AH * • . T. • i \, / ,39 p
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Test
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stack temoerature 	
A ^jneter* vacuum- 	
* tome- per* goine 	
imoinger* temoerature 	
f/J'l*-
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Test
Run
3
• • > • • •
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filter- box temperature 	 * 	 ffflfFZ ' 5r-2J-FP^ #37-' "\ 	 1
Minimum sample time of ' * - TLX* min nee
Minimum sample volume of * ;;/• dae£ collected

8. Post test: -• All- openings- seal-Mi 	 	
- recovery area- clean- sheltered 	
- filter handled- -with- ftioveav forcens- * *
- petri* dish sealed, labeled 	
- any samel e Lose 	
grad cyl.
, weighed
water* measured* i/mL • • R-B-I 	
- silica gel- weighed*. • nee- ama 	
- condition — color- 	
	 *• spent 	
- probe- cooled* sufficiently 	
- nozzle- removed- and* brushed 	
- probe brushed- 6* tin-en 	
- nozzle* brushes* clean* 	
, — wash bottles clean* 	 	
-blank taken: acetone*, • vacer*. * other*
uanped*
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-------
• • ~ • •-•• a,,+A
Date
R » Recommended
H * Mandatory
• . . ...
9. Post test Orsat Analysis of Initial (M*
analyzer - Analyzer leak, check
(levels should not fall below Final (H)
0.2 mL in- barret te f or- 2- min-. )
Orsat- samples?- Each bar analyzed- 3- tines-


checked against air- (20;9- «•• Qi3) 	
CQ-Z 	 . .

uu* 	

r^ranae- for fuel
ygg'C- analysis- valid
Orsat solutions changed
when calculated F0
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-------
                                                                  Page
                                                                        5 of 5
J.   NOTES:  Care should be  taken,  when sampling  for organic compounds,  Co
     follow stringent quality control guidelines  to avoid contamination  of the
     sample and  sampling train.   Take note  of any occurences which could bias
     the sample  in any manner.

     Include: (1) General comments; (2) Changes to pretest agreement with
     justification; (3) Identify (manufacturer) and describe condition of
     sampling equipment; (4)  any abnormal occurrences during test program.
     (Additional page(s) attached:   Yes • ••  . No
 Signacure of Observer            Affiliation of Observer          Date

-------
        ABC COKE

COKE OVEN EMISSION TEST

 BmMINGHAM^ALABAMA
          X. a-C. ajk-jfvO     f t
Page
                                             l of 2
Quality Control Check
Prior to Start of Teas
Keep all dented gimme sokd omii train astemUy


Vlsoily inspect each train fir proper assembly
> • _-__



VR_lt.. ^— .^ .•i.niKn» niijila fhr rMn*

Vbadty mpeet Type S Fftttnbe
Leak dieeke«di leg ofTypeSPtetnbe

Leak cnedc eonre snquing mn
Dnriog Testing




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-------
            33,
Page   2 of 2
Quality Control Check
After Testing


Visually inspect Type SRtot tube




Record onset viuuim or any
FieULog








dIEDDlfi QC9CRDQOOS
Dcsci ipuuu of QC mnpiBs

Dcviaoou Jzom QAPP


Sample Labels
Sample ID
Date *"*d *""* of coilectxon
Ubtedmirnmnrirtal.
Analytical panmeKT

OtMfTttto.

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-re

-------
  COKE OVEN EMISSION TEST
    BIRMINGHAM, ALABAMA
I.   Test Ran Observations

     R • Reconeended
     M - Mandatory
                                        Qace
                                              Test
Test
Bitti
         Test
          ii-
          3
Test
Ran
 4
1.    Train. set-up- * filter ID
                   filteT
                                                   AI
                                                 /A
M«*?y
                                                      m
      20
                   filter efaMfc..4 £or hoiea
                   filter centered
                                                     ^Lfi^L
                                                     ifcrf'

                                                    14JL
                   nozzle clean-
                                              ^£
-------
P«ge   2 of
Date
R • Reconnended
M - Mandatory

4. M-3 nampling train cheek:
«•»• »• —4 • f\M.\. . ... . ......
initial \MJ 	 - 	
(should hold
10 in. vacuum rinai in) 	
for- 1/2- min. ) 	
Puree sample train- with- stack* en • 	
Constant- rate- sampling 	 1- per 	
5. Time- tear started- • • 	
• Time test- ended 	
6. Dry zaa t" • )• port- initial 	 	
meter ..... fy^^ 	
volume: (•••;• port' initial 	 :•• •
	 final 	 • •
1 • J- port- initial 	
• • • final 	
<• -)-port initial 	

Test
/ " yL •/'
~*>/A
t .

' 'AJ/'A '
y^fl^
/IJQyS
+M8
Test
Run
2
fly /-'
A)/A'-
J

' fli/A:
' v^*** " '
• :x4i>* •
• "/b.^A ' /013'ffA
••$'./f?M f.'ftPfi
^J!w£I
• *_^-*-
, ._•. • -.-, • •
. -*~- ,• -
. -.-, - :...- • •
C?7/.S961
— ._±. .
' • -*- •
. -jj —
— ••
• — ^j- -j- • •- 	
. ..„• • •_ • •)• • -j- • • •
	 • final 	 VlfSfiS&WXhtftQ
7. Train operation Nozzle changed
during run during run —
MOT ALLOWED 	
pitch- and- yaw of- probe* o-.k-. 	
nozzle- not scraped- on* nipple 	
effective- seal- around* probe 	 	 	
probe moved- at* proper- cine 	
probe .heated 	 • • -
calculator constants or nomograph
changed when TS and /or TM
chances- significantlv
average time to set
isokenetics after probe

Average values:
unpinger temperature
should- be-< 70T 	
Filter box temperature. _.

' *T' c~ircie~"one- • •" 	 • • •

barometric- P taken* and- value

from filter holder while in
stack?

MO. ..

•s*4ijr\ ' '
rfygA
" 'Jfcf ' ' '
l&fclA
• •Jzi^
u
M/A-

+if U«W<.
^
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'W-CA ' ' '
'j2tett

Test
Run
3

..



Test
Sun






	
to • '
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. . . .
. • . »

• • •
•>... • . ..




	






	 !•••
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39^ V \ ^79/ 1- • • i

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-------
'^•-
  3 of  5
Date
R • Reconnended
M » Mandatory

Check on filter holder loosening of
clamoine device holder
during run?
was any particulate lost? v
Accurate 6* 	 	 Au-*^. t^ ^wW|



Minimum sample volume of ~ i/- • daef collected
8. Post cest: — • All* ODeninrcs* scaled 	
- recovery area- clean* sheltered 	
- filter handled- with* zlovea*.- forcens-
- petri- dish sealed, labeled 	
- any samoie lost 	
grad cyi.
, weighed
water- measured- «XmL • • ems • •
- "silica- gel- weighed*. • nee* prs 	
- condition — color* 	 	
	 M* spent- • 	
- probe- cooled- sufficiently 	
•* nozzle removed* and* brushed* 	
- probe brushed- b- eim>« 	
- nozzle- brushes- clean 	
- blank taken: acetone*, water*, other-
Canoed-
Laoeied
Sealed 	
Liouid- ieve-i- ™«T-*M-
%&n
Test
Run
\
M-W
\
(£>**
•'Too

,ai3-i
•*y/t. •
^Htf
\n*lM
• r«,f . .
iztnsz
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Run
3




Test
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4




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-------
                                                    4 pf
... * V
Dace
R « Reconaended
M - Mandatory

9. Post test Orsac Analysis of Initial (M)
integrated bag sample orsat
analyzer - Analyser leak check
(levels should not fall below Final (M)
cap. tubing and noc more than
0.2 mL in-bnrrette for- 2-min-.) 	
Orsaf samples;- Each bag- analyzed- 3* times-
£j S2?..2i5rees'wiehin- 0-.2X 	
f' 9?.25£?*»' within 0-.2X 	
S- CO- agrees- within- 0-.2I 	
Analysis ac end of tesc. Orsac analyzer
checked against air- (20i 9- «•• 0-.3) 	
Orsat Analysis:
CO-,* 	 	
o«>* 	
cox 	
Fo * _ZO»9' *•' Z' Of

Fuel 	
Fm range- for- fuel
Orsac- analysis- valid-
Orsac solucions changed
when calcalated F0
exceeds fne 1 • type • range •
IU. All samoles locked un
All samniing- comoonencs- clam* and' sealed' • •
/ -5^- All data- sheets submxcced- tn- observer-
- Run- isoitenecxc 	 TuM/observer- 	



Tesc
Run
^\^'
J
^ __
<~Us\
•^tjj^

Tesc
Run
2
M-Ztf-
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• • u/0//Qs
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Test
Run
3

.


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Tesc
Run
4




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	 ••!•• ••*

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	 \

1



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   |(
-------
                                                                 Page  5 of 5

J.   NOTES:  Care should be taken, when stapling for organic compounds,  Co
     follow stringent quality control guidelines to avoid contamination  of the
     sample and  sampling train.  Take note of any occurences which could bias
     the sample  in any manner.

     Include:  (13 General comments;  (2) Changes to pretest agreement with
     justification; (3) Identify (manufacturer) and describe condition of
     sampling  equipment; (4) any abnormal occurrences^during test  program.
     (Additional page(s) attached:  Yes  •     No
                                         P-Ei
 Signature of Observe?            Affiliation or Observer          Date

-------
              ABC COKE

   COKE OVEN EMISSION TEST

     BIRMINGHAM. ALABAMA,
                                ^oCo-T/
                                   l\ U fcl
                           3 i-T
 QmJftjr COBtrai Cheek
             Mar to Start of Tests
 Keep aildgmtdgtowceaqkd until ttan assembly
            i IB dost fico esvnc
                                 "2
 Vbntiy inspect each train fir proper ssseabfy
 Lew

                                 
-------
                Date  SLja?, ffl &
                Page   2 of 2
Quality Control Cheek
After Testing


Visually inspect Type SRtot tube
Leak check each leg of the Type SPitot tube




Field Log



~auipliug peisuiwel (uames/puailiun)
(leotafftOti pliminariiini im-liidma mm



Sample descriptions
DesBipiiuii of QC samples


HtfflntMM in cmnnlhw nrmnMrnl «w»4M.~..

Sample Labds
Sample ID
n IB J«' C tteasai
0
T ah farhnirimi tnifnlt

Analytical pamnev


<->ii.i _, -jin _
uiueivaum


U^o
^io
H^o
G
MAA

UG^

A XJ i n \ A \
A^fiC. CoRe \J\riwiH«Ka»M K oLt

OUscUM . lfl*Jf«*54) 7 M*»-t«JL. (2

"IXj^A^iLU luM>» "t: AJUl, /O f Mfert PL
a • J •J
//>.'£oAnt L (*:oc,fa 9-33-9A
i^ueU CuL.*/« MJ 5icr /U/drA
A)/X\

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-\jtn>i 0 aA*»3t«vi cL*xR5 |J*ft>**\ \fr**«ia<4
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f-

-------
COKE OVEN EMISSION TEST
                                            Page
.U AXV1Y JLJJ. 1 \JJJLI~V1YJL*; A» l-/x\ Jjj\J.TJjrjL »
I. Teat Run Observations Date
H " Mandatory
1. Train. see-up- * filter ID -
filter weight
filter checked for holes
filter centered • •
	 - ' nozzle" clean,* • • •
nozzle -undamaged

probe Liner cla-m
probe oarkinga correct
• • entire- length 	
	 unpingera* charged* 	 -'

pitot nezuneter* ABI oed 	

	 filter* boar or* holder- a*r tenrr.
all ball joints Lightly
	 greaaed 	
ail ooeninga' naoueii 	
2. Train leak check jj* 	
~ Cy^CTtfXunxl
T*«
Test
n-/A
/u//-
^\j>j\
&tS\
S*%£S\
'faesi
. oil 3
stUA
/fc£e/s

*$V\' ,

>^&& '
Z&iJLX1 '
• ff>&L>>
vtf/A-
1 ^%*^ ^X* '
ac nozzle: uxxtxai- (R-J* • • • VAC" 	 t • /J^Xfe
( /A'
MtS> '
•&4&^
/&eA' '
' #^*<3' "
it)l (f>
I*ALA


i r-M Irl

x*-il' '
" ^^ '
'S&&&\ '
M •
*t>69'
' /S~V/A
• 

test nm.; intermeduee fRJ VAC | -^—

•VAC
cbeeis.: negativ-r line CU- • •
final- • po«it~fTr». M«^ (Mi- • •

^ 15 aec. i nevero-re* line*  » jv i * 1 i /


^fV-
wV-
•^"LdxA.
. X^
Vi^
f^/?

.66?



-------
Page
2 of 5
Date
R - Reconnended
H « Mandatory

4. M-3 sampling train check:
^nitiai \nj
(should bold
1U in* vacuuni tznaz \nj 	
for- 1/2* mm.) 	
PntTjje sample train* with* stack* gas 	
• • ' Constant* rate* sampling 	 l- -jar 	
5. Time* test- started- • * 	
• Time tear ended 	
6. Dry gas (* • )j5ort* initial 	
meter ...... ffrM,^ 	
volume: (• * * )• port- initial 	 *.-• *
	 final 	 • * •
( * )• port- initial 	
• • * final 	
'")-'•)•> Q*
/ yj'lo
Test
/n*** 7i» /
•AJ/4
-A) /A •
• • yf/yp
LL»_>»
• -vT^c^
'/ft'ZLJD ^M
fStfK
Test
Pitn
/ i^^y »J
so/rf-
•fi)//r -
• 'A) f ft •
' ' u'^>1 ' '
• • •Kfoji'
• SofLb'Ad

Test
Run
3









/^Zo'3/9

• •^->--
• •—•• • •

ft*9', 6/1-
1 "*""*.'!'

. . . ._._. .

Test
Run
4










^.'..' : : ::H

	
BVVii-seisU-IMHIUBiHM

7. Train operation Nozzle changed
during run during run —
AtO
pitch- and- yaw of- probe- o*.k-. 	 j- -s~te& '
nozzle* not scraped* on* nipple 	
effective- seal- around- probe 	
prooe moved- at- proper- tune 	
probe .heated* * 	 • • • •
calculator constants or nomograph
changed when TS and /or TM
changea- significantly*
average time to set
isokenetics after probe

Average values:
impinger temperature
should* be-< 70T 	





from filter holder while in
stack?

" **?*&' '
~ ~<**L>*' '
•^Pexj
- -->*lj>_A
V

\ / t*1***-
>•
^ .


**MZS —
' ?%~f\ ' '
• '^t^LA '1
' -ty*A '






	 i ....
	 t • - • •


< AoJiit
.^.
**,











-
398 t J?^ h .,-.
/JO
AJ o
Ad

*Jfi ' 	



-------
                                                                          Page
                                                                          uUsHwwSi,
                                                                          3 of 5
                                                    Dace
            R • Recommended
            M - Mandatory
       Check on filter holder loosening of
       damning device holder
                       was silica gel changed
                       during run?
                was any partieuiate lost?
Accurate       /IP
readine of?     AH
                               -Q-CA*£) '
            Test
            Run
                                                                  Af-3-lf
                                                            -/oo
Tesc
Run
 3
                                                                  t
 . AA/Miniamm sample tine of • • • y-  mia. nee
' <*VN. Minimum sample volume of  • \y- dacf collected
       8.   Post test:   -• Al' openings- sealed
                 - recovery area- clean- sheltered .........
                 - filter handled- with- gloves-.- foreens- •
                 - petri- dish sealed, labeled
                 - anv samoe lose
                   vater- measured-
                              grad cyl.
                               weighed
                              si,
                                     v nee-
                 - condition - color-
                 4.

tHLw_*^
                                                                     0

- probe- cooled- surtlcienely 	
- nozzle* removed- and* br«*h«d 	
• probe brushed* 6- cin»« 	
— nozzle* brushes* clean 	
. , - vash bottles clean* 	 	
r-> - M-8 15- mxnnte- -ouree 	
"^-^ - blank taken: acetone-, vacer- other* *

cao-ped-
l-aoeied
Sealed 	


*-M
•ji
•^
"A


•^
*

• ^

r%T
jW *
iJ»' "

•64 ' *


Sh1

77"




•






• A
Ji

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* • • • • •
• 	




• •

...



. . . .
	 •








                                                                      euw^  kartO

                                                                   — «--»>U-uuJl  OS&

-------
-

Dace
R " Reconaended
M " Mandatory
9. Post test Orsat Analysis of Initial (M*
analyzer - Analyzer leak check
(levels should not fall below Final (M)
0.2 mL in- bnrrette for- 2- min-.) •
Orsaf samples? • Each bar analyzed- 3- times-
Z CO-> agrees- trir.nin- Q-.2I 	
S- CO- agrees- within- 0-.2X 	
checked against air- (20; 9- +• 0-.3) 	
COoZ 	
cox-"r 	
' Z C0»» 	

^range-for- fuel
Orsat- analysis- valid
Orsac aoluciona changed
«hen calcalated F0
exceeds fuel type -range •
All samoiing* comoonents* clem- anrf- •••4o«4- • •
- Orsac 	 "
- Run- isoicenetic 	 TeaWobmerver- 	



1-m
Test
Run
$W
v
• VLM
a

-rfn
l^e^- -

-*f-


UJ2>4
V
A>/A

cfA: ^-J
-^


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Test
Run
3 ^
•M-3t*
]W
V-U^

UJL/ • •
:%**::
"v^~
•d,?. •
-^-
•ti/A •
•/J//f- •
UU>, '



•^M.
w-«--p_^
Page


Test
Run
3
.


'•

	 1
	 f


	 r
\


'• 	 r
	 !•

y it IT?*
4 of 5


Test
4


l
• -
K • •








. ...

1^
*-v^Ai<
                  RT I  f
                                  U


-------
                                                                  Page
                                                                        o of 5
J.   NOTES:  Care  should be  taken,  when sampling for organic compounds,  to
     follow stringent quality control guidelines to avoid contamination  of the
     sample and sampling train.   Take note of any occurences which could bias
     the sample in any manner.

     Include: (1)  General comments; (2) Changes  to pretest agreement vith
     justification;  (3) Identify (manufacturer)  and describe condition of
     sampling equipment; (4)  any abnormal occurrences during test program.
     (Additional page(s) attached:   Yes _;	,  No
  Signature of  Observer
                                         CD
                                         ~ K /j_
Affiliation of Observer
Date

-------
 APPENDIX G




PARTICIPANTS

-------
PROJECT PARTICIPANTS
Affiliation
USEPA
EMC
BSD
PES




ATS
DEECO
ERG
FAL
Quanterra
LabCorp
RTI
ABC Coke
Name

John C. Bosch, Jr.
Alfred E. Vervaert
Lula H. Melton
John T. Chehaske
Franklin Meadows
Daniel F. Scheffel
Dennis P. Holzschuh
Ron Kolde
Dennis P. Becvar
Dennis D. Holzschuh
Troy A. Abernathy
Gary M. Gay
Amanda Richcreek
Steven B. Blaine
Paul T. Siegel
Steve Terrell
Richard Durham
Marc Hamilton
Joan T. Bursey
William H. Wadlin
Robert Weidenfeld

Marvin Branscome
Sandy George
Stacy Molinich
John Pearson
Mark Poling
Bruce Wise
Responsibility

Work Assignment Manager
Group Leader
Process Monitor and Observer
Program Manager
Project Manager
Field Team Leader
QA Coordinator
Sample Recovery
Laboratory Audit
Field Team Member
Field Team Member
Field Team Member
Field Team Member
Field Team Member
Field Team Member
CARB Method 429 Sample Transport
Sample Recovery
QAPP
PM/MCEM Analysis
Metals Analysis
PAH Analysis
NIOSH PAH Analysis
EPA/ESD Contractor
EPA/ESD Contractor (Observer)
EPA/ESD Contractor (Observer)
President
Manager, Engineering Environmental Compliance
Facility Testing Coordinator

-------
            APPENDIX H




SAMPLING AND ANALYTICAL PROCEDURES

-------
        EMISSION MEASUREMENT TECHNICAL INFORMATION CENTER
                         NSPS  TEST METHOD
 Method 1 - Sample and Velocity Traverses for Stationary Sources
1.  PRINCIPLE AND APPLICABILITY

1.1   Principle.   To  aid in  the  representative  measurement of
pollutant  emissions  and/or  total  volumetric flow  rate  from a
stationary source,  a  measurement site where the effluent stream is
flowing in a known  direction is selected, and the cross-section of
the  stack is divided  into a  number of equal  areas.   A traverse
point is then located  within each of these equal areas.

1.2   Applicability.   This  method  is  applicable  to  flowing gas
streams  in  ducts,  stacks, and flues.   The method  cannot be  used
when:  (1)  flow  is  cyclonic or swirling  (see  Section  2.4),  (2) a
stack  is  smaller than about 0.30 meter  (12  in.)  in diameter, or
0.071 m2  (113 in.2)  in cross-sectional area, or  (3) the measurement
site is  less than  two stack  or duct diameters downstream or  less
than a half diameter upstream from a flow disturbance.

The  requirements  of  this  method  must  be  considered  before
construction  of a new  facility  from which  emissions will be
measured; failure  to do  so may require subsequent alterations to
the  stack  or  deviation from  the  standard  procedure.    Cases
involving variants are subject  to  approval by the Administrator,
U.S. Environmental Protection Agency.

2.  PROCEDURE

2.1    Selection  of  Measurement  Site.    Sampling  or  velocity
measurement  is performed  at a site located at least eight stack or
duct diameters downstream and two diameters upstream from any  flow
disturbance  such as a bend, expansion, or contraction in the stack,
or from a visible flame.   If necessary,  an alternative location may
be  selected,  at a  position at least two  stack or duct diameters
Prepared by Emission Measurement Branch              EMTIC TM-001
Technical Support Division, OAQPS, EPA

-------
        EMISSION MEASUREMENT TECHNICAL INFORMATION CENTER
                        NSPS TEST METHOD
downstream and a half diameter upstream from any flow disturbance.
For a rectangular  cross section, an equivalent diameter  (De) shall
be  calculated  from the  following  equation,  to  determine  the
upstream and downstream distances:

                           p=   2LW
                            e  (L + W)

                                                       Eq. 1-1

     Where
          L    =    Length and W = width.

An   alternative   procedure   is   available   for   determining  the
acceptability  of  a  measurement location  not meeting the criteria
above.  This procedure,
determination  of gas  flow  angles at  the  sampling points  and
comparing the results with acceptability criteria, is described in
Section 2.5.

2.2  Determining the Number of Traverse Points.

2.2.1   Particulate  Traverses.  When  the eight-  and two-diameter
criterion can be met, the minimum number of traverse points shall
be:  (1) twelve, for circular or rectangular stacks with diameters
(or  equivalent diameters)  greater than 0.61 meter  (24  in.);   (2)
eight,  for  circular stacks with diameters  between  0.30 and 0.61
meter  (12  and 24  in.);  and (3)  nine,  for rectangular stacks with
equivalent diameters between 0.30 and 0.61 meter (12 and 24 in.).

When  the eight-  and two-diameter criterion  cannot be  met,  the
minimum  number of traverse  points  is  determined  from Figure 1-1.
Before  referring  to the  figure,  however,  determine the distances
from the  chosen  measurement site  to the  nearest  upstream and
downstream  disturbances,  and divide  each  distance  by  the stack
Prepared by Emission Measurement Branch              EMTIC TM-001
Technical Support  Division, OAQPS, EPA

-------
EMTIC TM-001          EMTIC NSPS TEST METHOD                Page 3
diameter or equivalent  diameter, to determine the distance in terms
of the number of duct  diameters.  Then, determine  from  Figure 1-1
the minimum number  of traverse points that  corresponds:  (1)  to the
number  of  duct  diameters  upstream;  and   (2)  to  the  number  of
diameters downstream.  Select the higher of the two  minimum numbers
of traverse points,  or  a  greater value,  so that for  circular stacks
the number is a multiple  of 4, and for  rectangular stacks,  the
number is  one of those shown in Table 1-1.

2.2.2   Velocity (Non-Particulate)  Traverses.   When velocity  or
volumetric flow rate  is to be determined  (but not particula'te
matter) ,  the same procedure  as that used for particulate traverses
(Section  2.2.1)  is followed,  except that Figure   1-2 may be used
instead of  Figure  1-1.

2.3  Cross-Sectional Layout and Location of Traverse Points.

2.3.1    Circular  Stacks.    Locate the  traverse  points  on  two
perpendicular  diameters  according  to  Table  1-2 and the  example
shown in  Figure  1-3.   Any equation  (for examples,  see Citations 2
and 3 in  the Bibliography)  that gives the  same  values as  those  in
Table 1-2  may be used  in lieu of Table 1-2.

For particulate traverses, one of the diameters  must  be  in a plane
containing  the  greatest expected  concentration variation,  e.g.,
after bends, one diameter shall be in the plane  of  the bend.   This
requirement  becomes   less  critical  as   the   distance   from  the
disturbance increase's; therefore, other diameter locations may  be
used,  subject to the approval of the Administrator.

In addition,  for stacks  having  diameters  greater than  0.61  m (24
in.),  no traverse points  shall be within 2.5 centimeters  (1.00 in.)
of the stack walls;  and for stack diameters equal  to or less than
0.61 m (24 in.),  no traverse points shall be located  within 1.3  cm
(0.50 in.) of the stack walls.  To meet these criteria, observe the
procedures given below-
2.3.1.1   Stacks With Diameters Greater Than 0.61  m  (24 in.).   When
any of the traverse points as located in Section 2.3.1 fall within
2.5 cm (1.00 in.) of the
stack walls,  relocate  them away  from  the  stack walls  to:  (1)  a
distance of
2.5 cm  (1.00  in.);  or  (2)   a distance equal to the  nozzle inside
diameter,  whichever is  larger.  These relocated traverse  points (on
each end  of a  diameter)  shall  be the "adjusted" traverse points.

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EMTIC TM-001          EMTIC NSPS TEST METHOD                Page 4
Whenever  two  successive traverse points  are combined  to form  a
single  adjusted  traverse point, treat the  adjusted point as  two
separate  traverse  points,  both  in  the  sampling  (or  velocity
measurement) procedure, and in recording the data.

2.3.1.2   Stacks  With Diameters Equal To or Less Than 0.61 m  (24
in.).   Follow the procedure in Section 2.3.1.1, noting only that
any "adjusted" points  should be relocated away from the stack walls
to: (1)  a distance of  1.3 cm (0.50 in.); or  (2)  a distance  equal to
the nozzle inside diameter, whichever is larger.

2.3.2  Rectangular Stacks.  Determine the number  of traverse points
as explained in Sections 2.1 and 2.2 of this method.   From  Table 1-
1,  determine  the grid configuration.   Divide  the  stack cross-
section into as many equal rectangular elemental  areas as  traverse
points,  and then locate a  traverse  point at the centroid of each
equal area according to the example in Figure 1-4.
If  the  tester desires to use more  than  the  minimum  number of
traverse  points,  expand the "minimum  number of traverse points"
matrix  (see Table 1-1)  by  adding  the extra traverse points along
one or the other  or  both legs of the matrix;  the  final matrix need
not  be  balanced.   For example,  if a 4 x 3  "minimum  number of
points" matrix were expanded to 36 points,  the  final matrix could
be  9  x  4  or 12  x 3, and would  not  necessarily  have to be 6 x 6.
After constructing the  final matrix,  divide  the  stack  cross-section
into as many equal rectangular,  elemental areas  as traverse points,
and locate a traverse point at the centroid  of each equal area.  The
situation of traverse points being too close to  the stack  walls is
not expected to  arise with rectangular stacks.   If this problem
should  ever  arise,  the  Administrator  must   be  contacted   for
resolution of the matter.

2.4  Verification of Absence of Cyclonic Flow.   In most stationary
sources, the direction  of stack gas flow is  essentially parallel to
the stack walls.   However,  cyclonic flow may exist  (1) after such
devices  as cyclones   and  inertial  demisters  following  venturi
scrubbers, or  (2) in stacks having tangential inlets  or other duct
configurations which tend to induce swirling; in these instances,
the presence or absence of cyclonic flow at the  sampling  location
must be determined.   The following  techniques are acceptable  for
this determination.  Level and zero the manometer.  Connect a Type
S pitot tube to the manometer.   Position the Type S  pitot tube at
each traverse point, in succession, so that the  planes of  the face
openings of the  pitot  tube are perpendicular to the stack cross-

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EMTIC TM-001          EMTIC NSPS TEST METHOD                Page  5
sectional plane;  when the  Type S pitot tube is in this position,  it
is at "0° reference."  Note the differential  pressure (Ap)  reading
at each traverse  point.  If a null  (zero) pitot reading is obtained
at  0°  reference  at  a given  traverse point,  an acceptable  flow
condition exists  at  that  point.   If  the pitot  reading is not  zero
at  0°  reference,  rotate  the  pitot tube  (up to ±90°  yaw  angle),
until a null reading  is obtained.  Carefully determine and record
the value of the  rotation angle  (a)  to  the nearest  degree.  After
the null technique
has been applied  at  each  traverse  point,  calculate  the average  of
the absolute values  of a;  assign a  values of 0°  to those points for
which no rotation was required,  and include these  in the  overall
average.    If  the average  value  of  a  is greater  than 20°,  the
overall   flow   condition   in  the  stack  is   unacceptable,  and
alternative  methodology,  subject   to  the   approval  of  the
Administrator,  must  be used to perform accurate sample and velocity
traverses.  The alternative procedure  described in Section  2.5 may
be used to  determine  the  rotation  angles  in  lieu of the procedure
described above.
2.5    Alternative Measurement  Site  Selection  Procedure.    This
alternative applies  to sources where measurement locations are  less
than 2 equivalent or duct diameters downstream  or  less  than  one-
half  duct  diameter  upstream  from  a  flow  disturbance.   The
alternative should   be  limited to ducts larger than  24  in.  in
diameter  where   blockage and  wall  effects   are   minimal.    A
directional flow-sensing  probe is used to  measure  pitch  and yaw
angles of the gas flow at  40 or more traverse points; the resultant
angle is calculated  and compared with  acceptable criteria for  mean
and standard deviation.

NOTE:   Both the  pitch  and yaw  angles  are  measured from a  line
passing through the  traverse point  and parallel to the stack axis.
The pitch angle is the angle of the gas flow component in the plane
that INCLUDES the traverse line and is parallel to the stack axis.
The yaw angle is  the  angle of the  gas flow component in the plane
PERPENDICULAR  to  the traverse line  at  the  traverse  point  and  is
measured  from the  line   passing  through the  traverse  point and
parallel to the stack axis.

2.5.1  Apparatus.

2.5.1.1  Directional Probe.  Any directional  probe,  such as United
Sensor  Type DA  Three-Dimensional Directional Probe,  capable  of
measuring both the pitch and yaw angles of gas  flows  is acceptable.

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EMTIC TM-001          EMTIC NSPS TEST METHOD                Page 6
 (NOTE:    Mention of  trade  name  or  specific  products does  not
 constitute   endorsement  by   the   U.S.   Environmental  Protection
 Agency.)  Assign an identification  number to the directional probe,
 and  permanently mark  or engrave  the  number on  the body  of  the
 probe.  The pressure holes  of directional probes are susceptible to
 plugging when used in particulate-laden  gas  streams.   Therefore,  a
 system  for  cleaning  the  pressure holes by  "back-purging"  with
 pressurized  air  is  required.

 2.5.1.2  Differential Pressure Gauges.   Inclined manometers,  U-tube
 manometers, or other differential pressure gauges (e.g.,  magnehelic
 gauges) that meet the specifications described in Method 2,  Section
 2.2.

 NOTE:   If the differential pressure gauge produces  both negative
 and  positive readings, then  both  negative  and positive pressure
 readings  shall  be  calibrated at  a minimum  of  three   points  as
 specified in  Method 2, Section 2.2.

 2.5.2   Traverse  Points.   Use a minimum of 40 traverse  points  for
 circular ducts and 42  points  for rectangular ducts for the gas flow
 angle determinations.   Follow Section 2.3 and Table  1-1  or  1-2  for
 the location and  layout of  the traverse points.   If the measurement
 location is determined to be  acceptable
 according  to  the criteria  in this alternative procedure,  use  the
 same traverse point  number  and locations for sampling and velocity
measurements.

2.5.3  Measurement Procedure.

2.5.3.1   Prepare the  directional  probe and differential pressure
gauges  as  recommended by the manufacturer.   Capillary  tubing or
surge tanks  may  be used to  dampen  pressure  fluctuations.    It is
recommended,  but not  required,  that  a  pretest  leak  check be
conducted.  To perform a leak check, pressurize or use  suction on
the impact opening until a reading  of at least  7.6  cm  (3 in.J  H20
registers on the  differential pressure gauge, then plug  the  impact
opening.  The pressure  of a leak-free system will remain  stable  for
at least 15 seconds.

2.5.3.2  Level and zero the manometers.  Since the manometer level
and. zero may drift because of vibrations and temperature changes,
periodically check the level and zero during the traverse.

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EMTIC TM-001          EMTIC NSPS TEST METHOD                Page 7
2.5.3.3  Position the  probe  at the appropriate locations in the gas
stream, and rotate until  zero deflection  is  indicated for the yaw
angle pressure gauge.   Determine  and  record the  yaw angle.  Record
the pressure gauge readings  for the pitch  angle,  and determine the
pitch angle from the  calibration  curve.  Repeat  this procedure for
each traverse point.   Complete a  "back-purge" of the pressure lines
and  the  impact  openings  prior   to measurements  of  each  traverse
point .

A post-test check as  described in Section  2.5.3.1 is required.  If
the  criteria  for a  leak-free   system  are  not  met,  repair  the
equipment, and  repeat  the flow angle measurements.

2.5.4  Calculate the  resultant  angle at each traverse  point, the
average  resultant angle,  and the  standard  deviation using the
following equations.   Complete the calculations  retaining  at least
one  extra significant  figure  beyond that of the  acquired data.
Round the values  after the  final calculations.

2.5.4.1   Calculate the resultant angle  at each  traverse point:

                R.. = arc cosine [ (cosineYi) (cosinePi) ]
                                                        Eq.  1-2
Where:
          RA   =     resultant  angle  at  traverse  point i,  degree.
          Yi   =     yaw  angle  at  traverse  point  i,  degree.
          Pi   =     pitch  angle at traverse  point  i,  degree.

2.5.4.2  Calculate the average resultant for the measurements:
                                                             Eq. 1-3
Where:
          Ravg  =    average  resultant  angle,  degree.
          n    =    total number  of  traverse  points.

2.5.4.3  Calculate the  standard deviations:

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EMTIC TM-001
                     EMTIC NSPS TEST METHOD
Page 8
                                  (n-1)
Where:
                    standard deviation, degree.
2.5.5  The measurement  location is acceptable if Ravg
s 10°.
                                                             B3[. 1-4
                                                        20° and Sd
2.5.6   Calibration.   Use a flow  system as described in  Sections
4.1.2.1 and  4.1.2.2  of Method  2.   In  addition,  the flow  system
shall have the .capacity to generate two test-section velocities:
one  between  365  and 730  m/min  (1200  and 2400  ft/min)  and  one
between 730 and 1100 m/min  (2400 and 3600  ft/min) .

2.5.6.1  Cut  two entry ports in the test section.   The axes through
the entry ports shall be perpendicular to each other  and intersect
in the centroid of the test section.  The ports should be elongated
slots parallel to the  axis of the test section and  of sufficient
length to allow measurement of pitch angles while maintaining  the
pitot head position  at  the test-section centroid.   To facilitate
alignment of  the  directional probe during calibration,   the test
section  should  be  constructed  of  plexiglass  or some  other
transparent material.  All calibration measurements should be made
at the same point in the test section, preferably at the  centroid
of the test section.

2.5.6.2  To  ensure that the gas  flow  is  parallel to the  central
axis of the test section, follow the procedure in Section 2.4  for
cyclonic flow determination to measure the gas flow  angles  at  the
centroid of the test  section from two test ports  located 90°  apart.
The  gas flow  angle measured in  each port  must be  ±2° of  0°.
Straightening vanes should be installed, if necessary, to meet this
criterion.

2.5.6.3  Pitch Angle Calibration.  Perform a  calibration  traverse
according  to  the  manufacturer's  recommended   protocol  in   5°
increments for angles from  -60°  to  +60° at  one velocity in each of
the two ranges specified above.  Average the pressure ratio values
obtained  for each angle  in the  two  flow  ranges, and  plot  a

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EMTIC TM-001          EMTIC NSPS TEST METHOD               Page  9
calibration curve with  the average values of the pressure ratio  (or
other   suitable  measurement   factor  as   recommended   by   the
manufacturer) versus the pitch angle.   Draw  a  smooth line through
the  data  points.   Plot also  the  data values  for  each traverse
point.  Determine the  differences between the measured datavalues
and  the  angle  from  the calibration  curve  at  the  same pressure
ratio.   The difference at  each  comparison  must be  within 2°  for
angles between 0° and 40°  and within 3°  for  angles between 40°  and
60°.

2.5.6.4  Yaw Angle Calibration.  Mark the three-dimensional probe
to allow the determination of the yaw position  of the probe.  This
is  usually a line extending the length of  the probe and aligned
with the impact  opening.  To determine the accuracy of measurements
of the yaw angle, only  the zero or null position need be calibrated
as follows:  Place the directional  probe in  the test section,  and
rotate  the  probe until  the  zero  position  is found.   With a
protractor  or  other  angle  measuring  device,  measure  the  angle
indicated  by the  yaw angle  indicator on  the three-dimensional
probe.  This should  be within 2° of 0°.  Repeat this measurement
for any other points  along the length of the  pitot where yaw angle
measurements could be  read  in order to account for variations in
the pitot markings used to  indicate pitot head positions.

BIBLIOGRAPHY

1.   Determining Dust Concentration  in   a  Gas   Stream,   ASME
     Performance Test  Code  No. 27.  New York.  1957.

2.   DeVorkin,  Howard,  et  al.  Air Pollution Source Testing Manual.
     Air Pollution Control  District.   Los  Angeles,  CA.   November
     1963.

3.   Methods  for Determining of Velocity,  Volume,  Dust and Mist
     Content  of Gases.   Western  Precipitation Division  of  Joy
     Manufacturing Co.  Los Angeles, CA.  Bulletin WP-50.  1968.

4.   Standard Method'for  Sampling  Stacks for Particulate Matter.
     In: 1971 Book of ASTM Standards, Part 23.  ASTM Designation D
     2928-71.   Philadelphia, PA.  1971.

5.   Hanson,  H.A.,  et al.   Particulate Sampling  Strategies  for
     Large  Power Plants Including  Nonuniform  Flow.   USEPA,  ORD,
     ESRL,  Research  Triangle Park,  NC.   EPA-600/2-76-170.   June

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EMTIC TM-001          EMTIC  NSPS  TEST METHOD              Page  10
     1976.

6.   Entropy Environmentalists, Inc.  Determination of the Optimum
     Number of Sampling Points: An Analysis of Method 1 Criteria.
     Environmental  Protection Agency.  Research Triangle Park, NC.
     EPA Contract No. 68-01-3172, Task 7.

7.   Hanson, H.A.,  R.J.  Davini,  J.K.  Morgan, and  A.A.  Iversen.
     Particulate  Sampling  Strategies  for  Large  Power  Plants
     Including  Nonuniform Flow.  USEPA,  Research Triangle Park, NC.
     Publication No. EPA-600/2-76-170.   June 1976.  350 p.

8.   Brooks,  E.F.,   and  R.L.   Williams.    Flow and  Gas  Sampling
     Manual.   U.S.  Environmental  Protection  Agency.   Research
     Triangle  Park,  NC.   Publication No.  EPA-600/2-76-203.  July
     1976.   93 p.

9.   Entropy Environmentalists,  Inc.   Traverse Point Study.  EPA
     Contract No. 68-02-3172.   June 1977.  19 p.

10.  Brown,  J.  and  K.  Yu.    Test  Report:  Particulate  Sampling
     Strategy  in Circular  Ducts.   Emission  Measurement  Branch.
     Emission   Standards    and  Engineering   Division.      U.S.
     Environmental Protection  Agency,  Research Triangle  Park, NC
     27711.  July 31, 1980.  12 p.

11.  Hawksley,  P.G.W., S. Badzioch, and J.H. Blackett.  Measurement
     of Solids in  Flue Gases.   Leatherhead,  England, The British
     Coal Utilisation Research Association.  1961.  p. 129-133.

12.  Knapp,  K.T.    The  Number  of  Sampling  Points Needed  for
     Representative Source  Sampling.  In:  Proceedings  of the Fourth
     National Conference on Energy and Environment.  Theodore, L.
     et al. (ed).  Dayton,  Dayton Section of the American Institute
     of Chemical Engineers.  October 3-7, 1976.  p. 563-568.

13.  Smith, W.S.  and D.J.  Grove.   A  Proposed Extension  of EPA
     Method 1  Criteria.    Pollution Engineering.    XV (8):36-37.
     August 1983.

14.  Gerhart,   P.M. and M.J. Dorsey.   Investigation of Field Test
     Procedures for Large Fans.  University of Akron.  Akron, OH.
     (EPRI  Contract CS-1651) .   Final Report (RP-1649-5).  December
     1980.

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EMTIC TM-001          EMTIC NSPS TEST METHOD               Page  11
15.  Smith, W.S.  and D.J.  Grove.  A New Look at Isokinetic Sampling
        Theory  and  Applications.    Source  Evaluation  Society
     Newsletter.  VIII(3):19-24.  August 1983.

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EMTIC TM-001
EMTIC NSPS TEST METHOD
Page 12
              Table  1-1.  CROSS-SECTION LAYOUT  FOR
                       RECTANGULAR STACKS

               	Number of  traverse  points
               Matrix layout

9 	
12 	
16 	
20 	
25 	
30 	
36 	
42 	
49 	

	 3x3
	 4x3
, 	 4x4
	 5x4
	 5x5

	 6x6
, 	 7x6
	 7x7

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EMTIC TM-001
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                            TABLE 1-2
          LOCATION OF TRAVERSE POINTS  IN CIRCULAR STACKS
              (Percent of stack diameter from inside
                     wall to  traverse point)
Traverse
Point
Number on a
Diameter
1 	

2 	

3 	

4 	

5 	

6 .....

7 	

8 	

9 	

10 ....
11 ....
12 ....
13 ....
Number of traverse points on a diameter
2
14
.6
85
.4











4
6.
7
25
.0
75
.0
93
.3









6
4.
4
14
.6
29
.6
70
.4
85
.4
95
.6







8
3.
2
10
.5
19
.4
32
.3
67
.7
80
.6
89
.5
96
.8





10
2.6
8.2
14.
6
22.
6
34.
2
65.
8
77.
4
85.
4
91.
8
97.
4


•
12
2.1
6.7
11.
8
17.
7
25.
0
35.
6
64.
4
75.
0
82.
3
88.
2
93.
3
97.
9

14
1.8
5.7
9.9
14.
6
20.
1
26.
9
36.
6
63.
4
73.
1
79.
9
85.
4
90.
1
94.
3
16
1.6
4.9
8.5
12.
5
16.
9
22.
0
28.
3
37.
5
62.
5
71.
7
78.
0
83.
1
87.
5
18
1.
4
4.
4
7.
5
10
.9
14
.6
18
.8
23
.6
29
.6
38
.2
61
.8
70
.4
76
.4
81
.2
20
1.
3
3.
9
6.
7
9.
7
11
2.
9 .
16
.5
20
.4
25
.0
30
.6
38
.8
61
.2
69
.4
75
.0
22
1.1
3.5
6.0
8.7
11.
6
14.
6
18.
0
21.
8
26.
2
31.
5
39.
3
60.
7
68.
5
24
1.1
3.2
5.5
7.9
10.
5
13.
2
16.
1
19.
4
23.
0
27.
2
32.
3
39.
8
60.
2

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EMTIC TM-001
EMTIC NSPS TEST METHOD
Page 14
14 ....

15 ....

16 ....

17 ....

18 ....

19 ....

20 ....

21 ....

22 ....

^ O • • • •

24 ....





































































































































98.
2




















91.
5
95.
1
98.
4
















85
.4
89
.1
92
.5
95
.6
98
.6












79
.6
83
.5
87
.1
90
.3
93
.3
96
.1
98
.7








73.
8
78.
2
82.
0
85.
4
88.
4
91.
3
94.
0
96.
5
98.
9




67.
7
72.
8
77.
0
80.
6
83.
9
86.
8
89.
5
92.
1
94.
5
96.
8
98.
9

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EMTIC  TM-001
EMTIC  NSPS TEST  METHOD
Page 15
                  50
                    0.5
                             Dud Diameters Upstream from Row Disturbance* (Distance A)

                                  1.0             1.5             2.0
                                                                             2.5
                  40
                  30
                  20
                  10
                           Higher Number i» for
                           Rectangular Stacks or Duds
                           * From Point of Any Type of
                           Dlsturbanc* (B«nd, Expansion, Contraction. «tc.)
                            I
                                   I
                                          J_
                                                  I
                                S.  ^^Diaturtanca
                               J   I MaMurament
                               1   L  si-
                                                              T
                                                               B
                                                                    Disturbance
                                                     16   Slack Diameter > 0.61 m (24 in.)

                                                         I       «
                        Stack Diameter » 0.30 to 0.81 m (12-24 in.)

                        I	I	I	
                            345678

                             Duct Diameters Downstream from Flow Disturbance* (Distance B)
                                                                       0
                                                                              10
           Figure  1-1.  Minimum  number  of  traverse  points   for
           particulate  traverses.

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EMTIC NSPS TEST METHOD
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          50
          40
          30
          20
          10
            0.5
                     Duct Diameters Upstream from Flow Disturbance* (Distance A)

                          1.0            1.5           2.0
                                                                   2.5
II I I I I
8 Higher Number is for
Rectangular Stacks or Ducts
16 Stack Die

I
_X
j.
1


1
\
/Disturbance
Measurement
Site
Disturbance

-
imeter > 0.61 m (24 in.)
12
— * From Point of Any Type of
Disturbance (Bend, Expansion, Contraction, etc.)
Stack Diameter
I I I I I I
8or9a
•0.30 to 0.61 m (12-24 in.)
|
                    3      4      5      6      78

                    Duct Diameters Downstream from Flow Disturbance* (Distance B)
                                         10
    Figure  1-2. Minimum number  of traverse points  for  velocity
     (nonparticulate)  traverses.

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EMTIC  TM-001
         EMTIC NSPS TEST METHOD
Page 17
       Traverse
        Point

         1
         2
         3
         4
         5
         e
 Distance
% of diameter

  4.4
  14.7
  29.5
  70.5
  85.3
  95.6
    Figure  1-3.  Example showing circular  stack  cross section
    divided  into 12  equal  areas,   with location of  traverse
    points indicated.

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EMTIC TM-001
EMTIC NSPS TEST METHOD
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o

o
	
o
o
1 	 1
o
I 	 4
0
o
	 1
o
I- 	 1
o
0
	
o
	
o
  Figure  1-4.  Example showing rectangular stack  cross  section
  divided into 12 equal areas, with a traverse point at centroid
  of each area.

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               EMISSION MEASUREMENT TECHNICAL INFORMATION CENTER
                               NSPS TEST METHOD
         Method 2 - Determination of Stack Gas Velocity and Volumetric
                         Flow Rate (Type S Pitot Tube)


1.  PRINCIPLE AND APPLICABILITY

1.1  Principle.   The average gas velocity  in a  stack is determined from the gas
density  and  from  measurement  of  the  average  velocity  head  with a  Type  S
(Stausscheibe or  reverse type) pitot tube.

1.2  Applicability.  This  method is applicable for measurement of  the average
velocity of a gas  stream and  for  quantifying gas flow.

This procedure  is  not applicable at measurement sites that  fail  to meet the
criteria of Method 1, Section 2.1.  Also,  the  method cannot be  used for direct
measurement in  cyclonic or swirling gas streams; Section 2.4  of Method 1 shows
how  to  determine cyclonic or  swirling  flow  conditions.    When unacceptable
conditions  exist,  alternative  procedures,  subject  to the  approval  of  the
Administrator,  U.S. Environmental Protection Agency,  must be employed to make
accurate flow rate determinations;  examples of  such alternative  procedures are:
(1) to install  straightening  vanes;  (2) to calculate the total  volumetric flow
rate stoichiometrically, or (3) to move to  another measurement  site at which the
flow is  acceptable.

2.  APPARATUS

Specifications for the apparatus are given below.  Any other apparatus that has
been demonstrated (subject to approval of the Administrator)  to be capable of
meeting  the specifications will be considered  acceptable.

2.1  Type S Pitot Tube.  Pitot tube made of metal tubing  (e.g., stainless steel)
as shown in Figure  2-1.   It  is  recommended that the external  tubing diameter
(dimension  Dt,  Figure 2-2b)  be between 0.48 and 0.95  cm  (3/16 and 3/8 inch).
There shall be an equal distance  from the  base  of each leg of  the pitot tube to
its  face-opening plane  (dimensions PA and PB,  Figure  2-2b); it is  recommended
that this distance be between  1.05 and  1.50 times the external tubing diameter.
The  face openings of the pitot tube shall, preferably, be aligned  as shown in
Figure 2-2; however,  slight misalignments of the openings are permissible  (see
Figure 2-3) .

The Type S pitot tube shall have a known coefficient, determined as  outlined in
Section  4.  An  identification number shall be  assigned to the pitot tube; this
number  shall  be  permanently  marked or engraved on  the body of the tube.   A
standard pitot tube may be  used instead of a Type S, provided  that it meets the
specifications of Sections  2.7 and 4.2;  note, however, that the static and impact
pressure holes  of  standard pitot  tubes  are  susceptible  to  plugging  in
particulate-laden gas streams.  Therefore,  whenever a standard pitot  tube  is used
to perform a traverse, adequate proof must  be  furnished that  the  openings of the
Prepared by Emission Measurement Branch                             EMTIC M-002
Technical Support Division, OAQPS,  EPA

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               EMISSION MEASUREMENT TECHNICAL INFORMATION CENTER
                               NSPS TEST METHOD
pitot tube have not plugged up during the traverse period; this can  be  done by
taking a velocity head  (Ap) reading at the final traverse point,  cleaning  out the
impact  and static  holes  of the  standard pitot  tube by  "back-purging"  with
pressurized air, and then taking  another Ap  reading.   If the Ap readings  made
before  and after  the  air purge  are  the same  (±5 percent),  the  traverse  is
acceptable.  Otherwise, reject the run.  Note that if Ap at the final traverse
point is unsuitably low,  another  point  may be selected.   If "back-purging"  at
regular intervals is part of the procedure,  then comparative Ap readings shall
be taken,  as  above, for  the  last two  back  purges at which  suitably high  Ap
readings are observed.

2.2  Differential Pressure Gauge.   An inclined manometer or equivalent  device.
Most  sampling trains are equipped with a  10-in.  (water column) inclined-vertical
manometer,  having  0.01-in. H20 divisions on the 0- to 1-in. inclined  scale,  and
0.1-in.  H20 divisions on the 1- to 10-in. vertical  scale.  This type of manometer
(or other gauge of equivalent sensitivity)  is satisfactory for the measurement
of Ap values as  low as  1.3 mm  (0.05 in.) H20.   However, a differential pressure
gauge of  greater sensitivity shall  be used  (subject  to the  approval  of  the
Administrator),  if  any of the following is found to be true:  (1) the  arithmetic
average  of all  Ap readings at  the traverse  points in the  stack  is less  than
1.3 mm  (0.05 in.) H20; (2)  for traverses of 12  or more  points,  more than  10
percent of the  individual Ap readings are below  1.3 mm  (0.05  in.)  H20;  (3)  for
traverses  of  fewer than 12 points, more  than one Ap reading  is  below  1.3  mm
(0.05 in.)  H20.   Citation 18 in the  Bibliography describes commercially available
instrumentation for the measurement of low-range gas velocities.

As an alternative to criteria (1)   through (3) above, the following calculation
may  be  performed  to   determine   the  necessity  of  using  a  more  sensitive
differential pressure gauge:
                             i. +K
Where:
        Api   =    Individual velocity head reading at a traverse point, mm (in.)
                  H20.

        n    =    Total number of traverse points.

        K    =    0.13 mm H20 when metric  units  are  used and 0.005 in. H20 when
                  English units are used.
Prepared by Emission Measurement Branch                            EMTIC H-002
Technical Support Division, OAQPS, EPA

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EMTIC TM-002                     NSPS TEST METHOD                        Page 3


If T is  greater than 1.05, the velocity head data are unacceptable  and  a  more
sensitive differential pressure gauge must be used.

NOTE:  If differential pressure gauges  other than inclined  manometers  are  used
(e.g.,  magnehelic  gauges), their calibration must  be checked after each  test
series.  To check  the calibration of a  differential  pressure  gauge,  compare Ap
readings of the gauge with  those of  a gauge-oil manometer  at a minimum  of three
points, approximately representing  the  range of  Ap values in  the  stack.  If,  at
each point,  the values  of Ap as read  by  the  differential  pressure gauge and
gauge-oil manometer agree  to  within 5 percent, the differential pressure gauge
shall be  considered to be in proper calibration.   Otherwise, the test  series
shall either be voided, or  procedures to adjust the measured  Ap values and final
results shall be used, subject to the approval of the Administrator.

2.3    Temperature  Gauge.    A thermocouple,  liquid-filled bulb  thermometer,
bimetallic thermometer, mercury-in-glass thermometer,  or other gauge  capable of
measuring  temperature to  within 1.5  percent of  the minimum  absolute stack
temperature.   The  temperature  gauge shall be attached  to the pitot tube such  that
the sensor tip does not touch  any metal; the gauge shall be  in an  interference-
free arrangement with respect  to the pitot tube face openings (see Figure 2-1 and
also Figure 2-7 in Section 4).  Alternative positions may be  used if the pitot
tube-temperature gauge system  is calibrated according  to the procedure  of Section
4.  Provided that  a difference of not more than 1  percent in the average  velocity
measurement  is introduced, the temperature gauge need  not  be attached  to the
pitot tube; this alternative  is subject to the approval of  the Administrator.

2.4  Pressure Probe and Gauge.  A piezometer tube and mercury- or water-filled
U-tube manometer capable of measuring stack pressure  to within 2.5 mm (0.1  in.)
Hg.  The static tap of a standard type  pitot tube or one  leg  of a Type S pitot
tube with the  face opening planes positioned parallel to  the  gas  flow  may  also
be used as the pressure probe.

2.5  Barometer.   A mercury,  aneroid,  or  other  barometer capable of measuring
atmospheric  pressure  to within 2.5 mm (0.1 in.) Hg.  See NOTE  in Method  5,
Section 2.1.9.

2.6  Gas Density  Determination Equipment.   Method 3  equipment,  if needed  (see
Section  3.6),  to  determine the stack  gas  dry  molecular  weight,  and Reference
Method 4 or Method 5 equipment for moisture  content determination;  other methods
may be used subject to approval of  the  Administrator.

2.7  Calibration  Pitot Tube.  When calibration of  the  Type S  pitot  tube  is
necessary (see Section 4),  a standard pitot tube  for  a reference.  The  standard
pitot  tube shall, preferably,  have a  known coefficient, obtained either (1)
directly from the  National  Bureau of Standards, Route  70 S, Quince  Orchard Road,
Gaithersburg,  Maryland, or  (2)  by calibration against  another standard  pitot  tube
with an NBS-traceable coefficient.   Alternatively, a standard pitot  tube  designed
according  to  the  criteria given  in  Sections 2.7.1 through 2.7.5  below  and
illustrated in Figure 2-4  (see also  Citations 7,  8, and 17 in  the  Bibliography)
may be used.   Pitot tubes  designed  according to  these specifications will  have
baseline coefficients of about 0.99 ± 0.01.

2.7.1  Hemispherical  (shown in Figure 2-4) ellipsoidal, or  conical tip.

2.7.2   A minimum  of  six  diameters straight  run (based  upon D,  the  external
diameter of the tube) between the tip and  the static pressure holes.

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EMTIC TM-002                     NSPS TEST METHOD                       Page 4
2.7.3  A minimum of eight diameters  straight run between  the  static pressure
holes and the centerline of the external  tube,  following the 90-degree bend.

2.7.4  Static pressure holes of equal size (approximately 0.1 D),  equally spaced
in a piezometer ring configuration.

2.7.5  Ninety-degree bend, with curved  or mitered junction.

2.8  Differential  Pressure Gauge for Type S Pitot Tube  Calibration.   An inclined
manometer  or  equivalent.    If the  single-velocity  calibration technique  is
employed (see Section 4.1.2.3), the calibration differential  pressure gauge shall
be  readable  to  the  nearest  0.13  mm  (0.005 in.)  H20.    For  multivelocity
calibrations, the  gauge shall be readable to the nearest 0.13 mm  (0.005  in.)  H20
for Ap values between 1.3 and  25  mm (0.05 and 1.0 in.) H20, and to the nearest
1.3 mm (0.05 in.) H20  for Ap values above 25 mm (1.0 in.) H20.   A special, more
sensitive gauge will be  required  to read Ap values below 1.3 mm  (0.05  in.)  H20
(see Citation 18  in the Bibliography).


3.  PROCEDURE

3.1   Set up the apparatus as  shown in  Figure 2-1.  Capillary  tubing or surge
tanks installed between  the  manometer and pitot tube may be used to dampen Ap
fluctuations.  It  is'recommended, but not required,  that a pretest leak-check be
conducted as follows:  (1) blow through  the  pitot  impact opening until at least
7.6 cm (3 in.)  H20 velocity pressure registers on the manometer;  then, close off
the impact opening.  The pressure shall remain stable for at least 15 seconds;
(2) do the same for the static pressure side, except using suction to obtain the
minimum  of 7.6 cm  (3  in.)  H20.    Other leak-check procedures,  subject to'the
approval of  the Administrator, may be used.

3.2   Level and zero the manometer.   Because the manometer level  and zero may
drift due to vibrations and temperature changes,  make periodic checks during the
traverse.    Record  all  necessary  data  as  shown in  the  example  data  sheet
(Figure  2-5).

3.3  Measure the  velocity head  and temperature at  the  traverse  points specified
by Method 1.  Ensure that the  proper  differential pressure  gauge is being used
for the range of  Ap values encountered (see Section 2.2).  If it  is necessary to
change to a  more  sensitive  gauge, do so, and  remeasure the Ap  and temperature
readings at each  traverse point.  Conduct a post-test leak-check (mandatory),  as
described in Section 3.1 above, to validate the traverse run.

3.4  Measure the  static pressure in the stack.  One reading is usually adequate.

3.5  Determine the atmospheric pressure.

3.6  Determine the stack gas dry molecular weight.  For combustion processes or
processes that emit essentially C02,  02, CO, and N2,  use Method 3.  For processes
emitting essentially air, an analysis need not be conducted;  use a dry molecular
weight of 29.0.   For other processes,  other  methods,  subject to the approval 6>f
the Administrator, must be used.

3.7  Obtain the moisture content from Reference Method  4 (or equivalent) or from
Method 5.

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EMTIC TM-002                     NSPS TEST METHOD                        Page 5


3.8   Determine the cross-sectional area  of  the stack or duct at  the  sampling
location.   Whenever possible, physically measure  the stack dimensions rather than
using blueprints.

4.  CALIBRATION

4.1  Type  S Pitot Tube.  Before its initial use, carefully examine the  Type S
pitot tube in top,  side, and end views  to verify that  the face openings  of the
tube are aligned within  the  specifications  illustrated in Figure 2-2 or  2-3.  The
pitot tube  shall not be  used if it fails to meet  these alignment specifications.

After verifying the face opening alignment,  measure  and record the  following
dimensions of the  pitot tube:   (a)  the external tubing diameter  (dimension  Dt,
Figure 2-2b); and (b)  the base-to-opening plane  distances  (dimensions PA and  PB,
Figure  2-2b) .   If Dt  is between 0.48 and  0.95 cm (3/16 and  3/8  in.),  and if ^
and  PB are equal  and  between 1.05 and  1.50  C\.,  there are two  possible  options:
(1)  the pitot  tube may be  calibrated  according to  the procedure outlined  in
Sections 4.1.2 through 4.1.5 below,  or (2)  a  baseline  (isolated tube) coefficient
value of 0.84 may be assigned to the  pitot  tube.   Note, however, that  if the
pitot tube  is part of an assembly,  calibration may still be  required, despite
knowledge of  the  baseline coefficient  value  (see Section  4.1.1).

If  Dt,  PA,   and g  are  outside  the  specified limits,  the pitot  tube must  be
calibrated as outlined  in Sections  4.1.2  through 4.1.5 below.

4.1.1  Type S Pitot Tube Assemblies.  During  sample and velocity traverses,  the
isolated Type S  pitot  tube is not always used; in many instances, the pitot tube
is  used in  combination with other  source-sampling  components  (thermocouple,
sampling probe,  nozzle)  as part of an "assembly." The presence of  other  sampling
components  can  sometimes affect the baseline value of  the  Type  S pitot tube
coefficient (Citation  9  in the Bibliography);  therefore  an assigned (or  otherwise
known) baseline  coefficient  value may or may  not be valid for  a given assembly.
The  baseline and assembly  coefficient  values will  be  identical  only  when the
relative placement of the  components in the assembly  is such that aerodynamic
interference effects  are  eliminated.    Figures 2-6  through  2-8 illustrate
interference-free component  arrangements for  Type S pitot tubes having  external
tubing diameters between 0.48 and 0.95 cm (3/16 and 3/8  in.).   Type  S pitot tube
assemblies  that fail to meet any or all  of the specifications of Figures 2-6
through 2-8 shall be calibrated according  to  the procedure outlined in  Sections
4.1.2  through  4.1.5 below,  and  prior  to  calibration,  the  values  of  the
intercomponent  spacings (pitot-nozzle,  pitot-thermocouple, pitot-probe sheath)
shall be measured  and recorded.

NOTE:  Do not use any  Type S pitot tube  assembly which  is constructed  such that
the impact  pressure opening  plane of the pitot tube is  below the entry  plane of
the nozzle  (see  Figure  2-6B).

4.1.2  Calibration Setup. If the Type S pitot tube is to be calibrated, one leg
of the tube shall be permanently marked  A, and the other, B.   Calibration shall
be done in a  flow  system having the following essential design features:

4.1.2.1  The flowing gas stream must be confined to a duct of definite  cross-
sectional area,  either circular or rectangular.   For circular cross sections, the
minimum duct diameter  shall  be 30.5 cm (12  in.);  for rectangular cross  sections,
the width  (shorter  side) shall be at least 25.4 cm  (10 in.).

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EMTIC TM-002                      NSPS TEST METHOD                        Page  6


4.1.2.2  The cross-sectional  area  of  the  calibration duct must be constant  over
a distance  of  10  or more  duct  diameters.   For a rectangular cross section,  use
an equivalent diameter,  calculated from the following equation, to determine the
number of duct diameters:

                                 D  -    2LW
                                  e     (L + W)


                                                                Eq. 2-1

Where:

         De   =   Equivalent diameter.
         L    =   Length.
         W    =   Width.

To  ensure  the presence  of  stable,  fully  developed  flow patterns  at   the
calibration site,  or  "test section,"  the  site must be located  at least eight
diameters downstream and  two diameters upstream from the nearest disturbances.

NOTE:  The eight-  and two-diameter criteria are not absolute;  other test section
locations may be used  (subject  to  approval  of  the Administrator), provided  that
the flow at the test site  is  stable and demonstrably parallel to the duct axis.

4.1.2.3   The  flow system shall have  the  capacity to generate  a test-section
velocity around 915 m/min  (3,000  ft/min).   This velocity must be constant  with
time to  guarantee steady  flow  during calibration.   Note  that Type S pitot  tube
coefficients obtained by single-velocity calibration at 915 m/min (3,000 ft/min)
will generally be  valid  to ±3 percent for the measurement of velocities above  305
m/min (1,000 ft/min) and  to  ±5  to 6  percent for the measurement of velocities
between 180 and 305 m/min  (600 and 1,000 ft/min).   If a more precise correlation
between  Cp and velocity is desired,   the flow  system shall have  the capacity to
generate  at least  four distinct, time-invariant test-section velocities covering
the velocity range from  180 to 1,525  m/min (600 to 5,000 ft/min), and calibration
data shall be taken at regular velocity intervals over this range (see Citations
9 and 14 in the Bibliography for details).

4.1.2.4  Two entry ports, one each for the standard and Type S pitot tubes,  shall
be cut  in  the test  section;  the standard pitot  entry  port shall  be  located
slightly downstream of  the Type S port, so that  the standard and Type S impact
openings will  lie in the same cross-sectional  plane during calibration.   To
facilitate alignment of  the pitot tubes during  calibration,  it is  advisable that
the test  section be constructed of plexiglas or some other  transparent material.

4.1.3  Calibration Procedure.   Note that this procedure is a general one and must
not be used without first referring  to the special considerations presented in
Section  4.1.5.  Note also that this  procedure applies only  to  single-velocity
calibration.   To  obtain calibration data  for  the A and  B sides  of  the Type S
pitot tube, proceed as  follows:

4.1.3.1   Make sure that  the manometer  is properly filled and that the oil is  free
from contamination and  is of the proper  density.  Inspect  and  leak-check all
pitot lines; repair or  replace  if necessary.

4.1.3.2  Level and zero the manometer.  Turn  on the fan,  and allow the flow to

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EMTIC  TM-002                      NSPS TEST METHOD                       Page 7


stabilize.  Seal  the Type S entry port.

4.1.3.3   Ensure that the manometer is level and zeroed.  Position the standard
pitot  tube at the calibration point  (determined as outlined in Section 4.1.5.1),
and align the tube so that its tip is pointed directly into the flow. Particular
care should be  taken in aligning the tube to avoid yaw and pitch angles.  Make
sure that the  entry port surrounding the tube is properly sealed.

4.1.3.4  Read Apstd,  and  record its value in a data  table  similar to the one shown
in Figure 2-9.  Remove the standard pitot tube from the duct, and disconnect it
from the manometer.  Seal the standard entry port.

4.1.3.5  Connect the Type S pitot tube to the manometer.  Open the Type S entry
port.   Check the manometer  level and  zero.   Insert and align the Type S pitot
tube so  that its A side impact opening is at the same point as was the standard
pitot  tube and  is pointed directly into the flow.  Make sure that the entry port
surrounding the tube is properly sealed.

4.1.3.6  Read  Ap5,  and enter its value in the data  table.   Remove the Type S
pitot  tube from the duct, and disconnect it from the manometer.

4.1.3.7  Repeat  Steps 4.1.3.3  through  4.1.3.6 above until  three  pairs of Ap
readings have been obtained.

4.1.3.8  Repeat Steps 4.1.3.3 through 4.1.3.7 above for the B side of the Type
S pitot tube.

'4.1.3.9  Perform calculations, as described in Section 4.1.4 below.

4.1.4   Calculations.

4.1.4.1  For  each of the six pairs of Ap readings  (i.e., three from side A and
three  from side B)  obtained in Section 4.1.3 above, calculate the value of
the Type S pitot  tube coefficient as follows:
                              C    =C
                              ^p(s)   p(std),
                                                                         Eq. 2-2
         Where:

         Cp(s)       =    Type S pitot tube coefficient.

         Cp,,td)      =    Standard  pitot  tube  coefficient;  use  0.99  if   the
                        coefficient  is  unknown and the tube is designed according
                        to  the criteria  of Sections 2.7.1  to 2.7.5  of  this
                        method.

         ApBtd       =    Velocity head  measured by the standard pitot tube,  cm
                        (in.) H20.

         Ap,        =    Velocity head measured by the Type S pitot tube, cm  (in.)
                        H20.

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EMTIC TM-002
                                 NSPS TEST METHOD                        Page 8
4.1.4.2  Calculate Cp (side A), the mean A-side coefficient,  and C"p  (side B),  the
mean  B-side  coefficient;  calculate  the  difference between  these two  average
values.

4.1.4.3  Calculate the deviation of each of the three A-side  values  of
Cp(s) from Up (side A), and the deviation of each B-side values of Cp(s) from
Cp (side B).   Use the following equation:


                        Deviation  = C    ~C~(A or B)
                                       P(s)    r
                                                                  Eq. 2-3

4.1.4.4  Calculate  a, the average deviation from the mean, for both the A and B
sides of the pitot tube.  Use the following equation:
                  a(side A or  B)  =
                                     t|Cp(s)
                                                                  Eq. 2-4

4.1.4.5  Use the Type S pitot tube only if the values of  o  (side A)  and a (side
B)  are  less than or equal to 0.01 and if the absolute value of the difference
between C~p (A) and Up  (B)  is 0.01 or  less.

4.1.5  Special Considerations.

4.1.5.1  Selection of Calibration Point.

4.1.5.1.1  When an isolated Type S pitot  tube  is calibrated,  select a calibration
point at or near  the center of the duct, and follow the  procedures  outlined in
Sections  4.1.3 and 4.1.4 above.  The Type  S pitot coefficients so  obtained,
i.e., Cp  (side  A) and (Jj  (side B),  will be valid,  so  long as  either:  (1)  the
isolated pitot tube  is used; or (2)  the pitot  tube  is used with  other components
(nozzle,  thermocouple,   sample  probe)   in  an  arrangement  that is free  from
aerodynamic interference  effects  (see Figures 2-6  through  2-8) .

4.1.5.1.2   For  Type  S  pitot  tube-thermocouple  combinations   (without  sample
probe),  select a calibration point at or  near  the center of  the  duct, and follow
the procedures outlined in Sections 4.1.3 and 4.1.4 above.   The coefficients so
obtained will be valid so  long as the pitot tube-thermocouple combination is used
by itself or with other components in an interference-free  arrangement (Figures
2-6 and 2-8).

4.1.5.1.3   For assemblies with sample  probes,  the calibration point should be
located at or near the center of the  duct; however,  insertion  of a  probe sheath"
into a small duct may cause significant cross-sectional area blockage and yield
incorrect  coefficient values  (Citation  9 in the Bibliography). Therefore, to
minimize  the  blockage  effect,  the calibration point may be a  few  inches off-

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EMTIC TM-002                      NSPS TEST METHOD                       Page 9


center  if  necessary.  The actual  blockage effect will be  negligible when the
theoretical  blockage, as  determined by  a projected-area  model of  the probe
sheath,  is 2 percent or less  of the duct cross-sectional  area  for assemblies
without  external sheaths (Figure 2-lOa), and 3 percent or  less  for assemblies
with external  sheaths (Figure  2-10b).

4.1.5.2  For those  probe assemblies  in which pitot tube-nozzle interference is
a factor (i.e., those in  which  the pitot-nozzle separation distance fails to meet
the specification illustrated in  Figure 2-6A), the  value of Cp(s) depends upon the
amount of free-space between the  tube and nozzle, and therefore is a function of
nozzle size.  In these instances,  separate calibrations  shall be  performed with
each of the commonly used nozzle  sizes in place.   Note that  the single-velocity
calibration  technique is acceptable  for  this purpose,  even  though the larger
nozzle  sizes  (>0.635 cm or 1/4  in.)  are not  ordinarily  used  for isokinetic
sampling at velocities around 915 m/min  (3,000 ft/min), which is the calibration
velocity; note also that  it is  not necessary to draw an isokinetic sample during
calibration  (see Citation  19 in  the  Bibliography).

4.1.5.3  For a probe assembly constructed such that its pitot tube is always used
in the same orientation,  only one side of the pitot tube  need be calibrated (the
side which will face the flow) .  The pitot  tube  must still meet the alignment
specifications of Figure  2-2 or 2-3, however, and must have an average deviation
(o) value  of 0.01  or less  (see Section 4.1.4.4.)

4.1.6  Field Use and Recalibration.

4.1.6.1  Field Use.

4.1.6.1.1  When a Type S  pitot  tube  (isolated or in an assembly)  is used in the
field,  the  appropriate coefficient  value  (whether assigned  or  obtained  by
calibration) shall be used  to perform velocity calculations.  For calibrated Type
S pitot tubes,  the A side coefficient  shall be used when the A side of the tube
faces the  flow,  and the  B  side coefficient shall  be used when the B side faces
the flow; alternatively,  the arithmetic average  of the A and B side coefficient
values may be  used,  irrespective of  which side  faces the flow.

4.1.6.1.2  When a probe assembly  is used to sample  a small duct,  30.5 to 91.4 cm
(12 to 36 in.)  in diameter, the probe sheath sometimes blocks a significant part
of the  duct cross-section, causing a reduction in  the effective  value of Cp(,).
Consult Citation 9 in the Bibliography for details.   Conventional  pitot-sampling
probe assemblies are not recommended for use in  ducts having inside diameters
smaller  than 30.5  cm (12 in.)  (see Citation 16  in the Bibliography).

4.1.6.2  Recalibration.

4.1.6.2.1  Isolated Pitot Tubes.   After each field use,  the  pitot tube shall be
carefully reexamined in top, side, and end views.   If the pitot face openings are
still aligned within the  specifications illustrated in Figure 2-2  or 2-3, it can
be assumed that the baseline coefficient of the pitot tube has not changed.  If,
however,  the tube has been damaged  to the extent that it  no longer meets the
specifications of the Figure 2-2  or 2-3,  the damage shall either be repaired to
restore proper alignment of the  face  openings,  or the tube  shall be discarded.

4.1.6.2.2  Pitot Tube Assemblies.  After each field use, check the face opening
alignment  of  the  pitot tube,  as in  Section  4.1.6.2.1;  also,   remeasure the
intercomponent spacings of  the  assembly.  If the intercomponent spacings have not

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EMTIC TM-002                     NSPS TEST METHOD                       Page 10


changed and the face  opening alignment is acceptable, it can be  assumed that the
coefficient of the assembly has not  changed.  If the  face opening  alignment is
no  longer within the  specifications of Figure 2-2 or 2-3,  either repair the
damage or  replace the  pitot tube (calibrating the new assembly,  if necessary).
If the intercomponent  spacings have  changed, restore  the original  spacings,  or
recalibrate the assembly.

4.2  Standard  Pitot Tube (if applicable).  If a standard pitot  tube  is  used for
the velocity traverse, the tube shall be constructed  according to  the  criteria
of Section 2.7 and shall be assigned a baseline coefficient value  of  0.99.  If
the standard pitot tube is used as part of an assembly, the tube  shall  be in an
interference-free arrangement (subject to the approval of the  Administrator) .

4.3   Temperature Gauges.   After each field  use,  calibrate  dial thermometers,
liquid-filled bulb thermometers, thermocouple-potentiometer systems,  and other
gauges  at  a   temperature  within  10 percent  of the average  absolute  stack
temperature.   For temperatures up to 405°C  (761°F), use an ASTM  inercury-in-glass
reference thermometer, or equivalent, as a reference; alternatively,  either
a reference thermocouple and potentiometer (calibrated by NBS) or  thermometric
fixed  points,  e.g.,  ice bath  and  boiling  water  (corrected  for barometric
pressure)  may be used.   For  temperatures  above  405°C  (761°F),  use  an  NBS-
calibrated  reference  'thermocouple-potentiometer  system  or  an   alternative-
reference, subject to  the approval of the Administrator.

If, during calibration, the absolute temperature measured with the  gauge being
calibrated and the reference gauge agree  within 1.5 percent, the  temperature data
taken in the field shall be considered valid.  Otherwise,  the pollutant  emission
test shall either be considered invalid or adjustments (if appropriate)  of the
test results shall be made,  subject  to the approval of the Administrator.

4.4  Barometer.  Calibrate the barometer used against a mercury barometer.

5.  CALCULATIONS

Carry out calculations, retaining at  least one extra decimal  figure  beyond that
of the acquired data.  Round off figures after final calculation.

5.1  Nomenclature.

          A    =    Cross-sectional  area of stack,  m2  (ft2) .

          Bws   =    Water vapor in the  gas stream  (from  Method 5 or Reference
                    Method 4),   proportion by volume.

          CP    =    Pitot tube coefficient,  dimensionless.

          Kp    =    Pitot tube constant,

                                                       1/2
for the metric system.
34 07 m
sec
(g/g-mole) (mmHg)
(°K) (mmH20)

-------
EMTIC TM-002
             NSPS TEST METHOD
Page 11
                    85.49
       ft
      sec
                                Ib/lb-mole)  (in.Hg)
                                          (in.H20)
                                                        1/2
for the English system.
          M.
Molecular weight of stack gas,  dry basis (see Section 3.6),
g/g—mole  (Ib/lb-mole).

Molecular weight of stack gas,  wet basis,  g/g-mole (Ib/lb-
mole) .

        = Md(l-Bws)  +18.0Bws
          PS
                                             Eq. 2-5

Barometric pressure at measurement site,  mm Hg (in.  Hg)

Stack static pressure, mm Hg (in.  Hg).

Absolute stack pressure,  mm Hg (in.  Hg),
                                      v.
                                      bar
          P.t
          t.
                                             Eq. 2-6
Standard absolute pressure,  760 mm Hg (29.92 in. Hg) .

Dry  volumetric  stack gas flow rate  corrected  to standard
conditions, dsmVhr (dscf/hr).

Stack temperature, °C (°F) .

Absolute stack temperature,  °K (°R).


              = 273  + t.
for metric.
                                  = 460  + t
                                                                  Eq.  2-7
for English.
                                                                  Eq.  2-8
                    Standard absolute temperature, 293°K (528°R).

                    Average stack gas velocity, m/sec  (ft/sec).

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EMTIC TM-002
                                 NSPS TEST METHOD
                                                                   Page  12
          Ap   =    Velocity head of stack gas, mm H20 (in.  H20).

          3,600=    Conversion factor, sec/hr.

          18.0 =    Molecular weight of water, g/g-mole  (Ib/lb-mole) .

5.2  Average Stack Gas Velocity.
                             = KG  (,/Sp)
                                         avg
                                            *
                                           s(avg)
5.3  Average Stack Gas Dry Volumetric Flow Rate

                                              T
                    Qsd  =  3,600(l-Bws)vsA
                                                std
                                             T         P
                                              s(avg)     std
                                                                  Eq.  2-9
                                                                  Eq.  2-10
BIBLIOGRAPHY
1.


2.


3.




4.



5.


6.


7.

8.

9.
Mark, L.S.   Mechanical  Engineers'  Handbook.   New York.  McGraw-Hill  Book
Co., Inc.  1951.

Perry.  J.H.   Chemical Engineers' Handbook.   New York.  McGraw-Hill  Book
Co., Inc.  1960.

Shigehara,  R.T.,  W.F. Todd, and W.S.  Smith.  Significance  of Errors  in
Stack  Sampling  Measurements.     U.S.   Environmental   Protection  Agency,
Research Triangle Park, N.C.  (Presented at the Annual Meeting of the Air
Pollution Control Association,  St. Louis, MO., June 14-19, 1970).

Standard Method for Sampling Stacks for Particulate Matter.  In: 1971  Book
of ASTM  Standards,  Part 23.  Philadelphia,  PA.   1971.  ASTM Designation
D 2928-71.

Vennard,  J.K.  Elementary Fluid  Mechanics.  New York.  John Wiley and Sons,
Inc.  1947.
Fluid  Meters  -  Their  Theory  and  Application.
Mechanical Engineers, New York, N.Y.  1959.
American  Society  of
ASHRAE Handbook of Fundamentals.  1972.  p. 208.

Annual Book of ASTM Standards, Part 26.  1974.  p. 648.

Vollaro,  R.F.   Guidelines for Type S Pitot Tube  Calibration.   U.S.
Environmental Protection Agency, Research Triangle Park, N.C.   (Presented
at   1st  Annual   Meeting,   Source   Evaluation  Society,   Dayton,   OH,
September 18, 1975.)

-------
EMTIC TM-002                     NSPS TEST METHOD                      Page  13


10.  Vollaro, R.F-  A Type S Pitot Tube Calibration Study.  U.S. Environmental
     Protection Agency,  Emission Measurement  Branch,  Research Triangle  Park,
     N.C.  July 1974.

11.  Vollaro, R.F.  The Effects of Impact Opening Misalignment on the Value  of
     the Type S Pitot Tube Coefficient.  U.S.  Environmental Protection Agency,
     Emission Measurement Branch, Research Triangle Park, NC.  October 1976.

12.  Vollaro, R.F.  Establishment of a Baseline Coefficient Value for Properly
     Constructed  Type S Pitot Tubes.   U.S.  Environmental Protection Agency,
     Emission Measurement Branch, Research Triangle Park, NC.  November  1976.

13.  Vollaro, R.F.  An Evaluation of Single-Velocity Calibration Technique as a
     Means  of  Determining Type S Pitot Tube Coefficients.  U.S. Environmental
     Protection Agency,  Emission Measurement Branch, Research Triangle Park, NC.
     August  1975.

14.  Vollaro,  R.F.   The Use of Type S  Pitot Tubes  for the Measurement  of Low
     Velocities.   U.S. Environmental  Protection  Agency,  Emission Measurement
     Branch, Research  Triangle Park, NC.  November 1976.

15.  Smith,  Marvin  L.   Velocity Calibration  of EPA Type Source Sampling  Probe.
     United Technologies Corporation, Pratt and Whitney Aircraft Division, East
     Hartford, CT.   1975.

16.  Vollaro, R.F.  Recommended Procedure for Sample Traverses  in Ducts Smaller
     than 12 Inches in Diameter.  U.S. Environmental Protection Agency, Emission
     Measurement  Branch,  Research Triangle Park, NC.  November 1976.

17.  Ower, E. and R.C.  Pankhurst.  The Measurement of Air  Flow, 4th Ed. London,
     Pergamon Press.   1966.

18.  Vollaro, R.F.   A  Survey of Commercially Available Instrumentation for the
     Measurement  of Low-Range Gas Velocities.   U.S.  Environmental Protection
     Agency,   Emission  Measurement  Branch,  Research   Triangle  Park,  NC.
     November 1976.  (Unpublished Paper).

19.  Gnyp,  A.W.,  C.C.  St.  Pierre,  D.S.  Smith, D.  Mozzon, and J. Steiner. An
     Experimental Investigation of the Effect of  Pitot  Tube-Sampling Probe
     Configurations on the  Magnitude of the S Type Pitot Tube Coefficient for
     Commercially Available  Source Sampling Probes.  Prepared by the University
     of  Windsor   for   the  Ministry   of  the  Environment,  Toronto,  Canada.
     February 1975.

-------
EMTIC TM-002
           NSPS  TEST METHOD
Page  14
   1.90-2.54 cm*
   (0.75 -1.0 in.)
     I   c
           7.62 cm (3 in.)'
Temperature Sensor
                          /	I
                                TypeS Pilot Tube
                * Suggested (Interference Free)
                Pilot tube/Thermocouple Spacing
Figure  2-1.   Type  S  pitot  tube  manometer  assembly.

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EMTIC  TM-002
NSPS TEST METHOD
Page  15
                 Transverse
                 Tube Axis
          Longitudinal
          Tube Axis
                                                Face
                                               Opening
                                               Planes


                                                 (a)
                                                      A-Side Plane
                                                      B-Slde Plane
                   T
                                          /TOTE
                                                 (c)
                             (a) end view; face opening planes perpendicular
                               to transverse axis;

                             (b) lop view; face opening planes parallel to
                               longrtudna! axis:

                             (c) side view; both legs of equal length and
                               oentertines coincident, when viewed from
                               botfisides. Baseline coeffident values of
                               0.64 may be assigned to pitot lubes con-
                               •ductedthitway
 Figure   2-2.    Properly   constructed  Type   S  pitot  tube.

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EMTIC TM-002
NSPS TEST METHOD
Page 16
                                    -
Figure 2-3.  Types of face-opening misalignment that can  result  from field use
or improper  construction of  Type  S pitot  tubes.   These  will  not  affect  the
baseline  value of Cp(s) so long  as a1 and a2  *10°, P1 and (J2 s5°, i <;0.32  cm (1/8
in.)  and w *0.08 cm (1/32 in.)  (citation 11 in Bibliography).

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EMTIC TM-002
NSPS TEST METHOD
Page 17
                                                   Curved or
                                                  Mitered Junction
                                                   HwnUpnerical
                                                      Tip
   Figure 2-4.   Standard  pitot  tube design  specifications.

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EMTIC TM-002                     NSPS TEST METHOD                      Page 18

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EMTIC TM-002
NSPS TEST METHOD
Page 19
PLANT
DATE
               RUN NO.
      STACK DIA. OR
DIMENSIONS, m (in.)  	  BAROMETRIC PRESS., mm Hg
(in. Hg) 	CROSS SECTIONAL AREA, m2 (ft2)	
OPERATORS 	
PITOT TUBE I.D. NO. 	
  AVG. COEFFICIENT, Cp
  LAST DATE CALIBRATED
                                 SCHEMATIC OF STACK
                                  CROSS SECTION
Traverse
Pt. No.













Vel. Hd., Ap
mm (in. ) H20













Stack Temperature
T.,
°C (°F)













Average
T.,
°K (°R)














Pg
mm Hg
(in.Hg)














Up)1'2














                     Figure 2-5.  Velocity traverse data,

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EMTIC  TM-002
                                    NSPS TEST METHOD
                        Page  20
                                    TypeS Pilot Tube
                                   I »>1.ncn>(KI>i)fcrD lUaiKHta.)
                              Sampling Nozzle
                           A. Bottom View; showing minimum pilot tubs-nozzle separation
                                    Sampling
                                     Nozzle
Static Pressure
Opening Plane
                          Types       Nozzle Entry
                         Pilot Tube
                           B. Side View; to prevent pilot tube from interfering with gai
                            flow streamlines approaching the nozzle, the Impact pressure
                            opening plane of the pilot tube shall be even with or above the
                            nozzle entry plane.
  Figure 2-6.   Proper  pitot  tube-sampling nozzle  configuration  to
  prevent   aerodynamic   interference;   button-hook  type   nozzle;
  centers of nozzle and pitot  opening aligned;  Dt between  0.48 and
  0.95  cm  (3/16  and  3/8 in.).

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EMTIC TM-002
NSPS TEST METHOD
Page 21
                             I w.ja-
                Teirperature S«nsor
                    p.  Types Blot Tube
              Simple Probe
                                             Temperature Senior
                                                   Type S Pilot Tub.
                                           SenpUF
   Figure   2-7.     Proper   thermocouple   placement   to  prevent
   interference; Dt between  0.48 and 0.95  cm  (3/16 and 3/8  in.).

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EMTIC TM-002
NSPS TEST METHOD
Page  22
                                 TypeS Pilot Tube
  Figure 2-8.   Minimum  pitot-sample  probe separation needed to
  prevent interference; Dt between 0.48 and  0.95 cm (3/16  and 3/8
  in.) .

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EMTIC TM-002
           NSPS TEST METHOD
Page 23
PITOT TUBE IDENTIFICATION NUMBER: DATE: CALIBRATED BY:


RUN NO.
1
2
3

RUN NO.
1
2
3



"A" SIDE CALIBRATION
cm H2O
(in H2O)




cm H2O
(in H20)



(SIDE"' A)
CD,.,





"B" SIDE CALIBRATION
cm H2O
(in H20)



ftTT-Q-rarrfi Dpi\H a +- -i nn = n
cm H20
(in H20)



^p, ovg
(SIDE B)





EC - C
. ^p(s) ^p(AorB)
- 1=i 	 _ -Mii«

Deviation
C.,., - CD(A)




Deviation
CD(., - CD(B)



=5t:R^<0 . 01
Cp(SideA)-Cp
                                      -MustBe^O.Ol
             Figure 2-9.   Pitot tube calibration data.

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EMTIC TM-002
           NSPS TEST METHOD
Page 24
          t  ^^
   Figure 2-10
   assemblies.
Projected-area  models for  typical pitot tube

-------
                  EMISSION MEASUREMENT TECHNICAL INFORMATION CENTER
                                   NSPS TEST METHOD
                  Method 3B - Gas Analysis for the Determination of
                    Emission Rate Correction Factor or Excess Air
1.  APPLICABILITY AND PRINCIPLE

1.1  Applicability.

1.1.1  This method is applicable for determining carbon dioxide (COZ). oxygen  (02),
and carbon monoxide (CO) concentrations of a sample from a gas stream of a fossil -
fuel combustion process for excess air or emission rate correction factor
calculations.

1.1.2  Other methods, as well as modifications to the procedure described herein.
are also applicable for all of the above determinations. Examples of specific
methods and modifications include:  (1) a multi-point sampling method using an Orsat
analyzer to analyze individual grab samples obtained at each point,  and  (2) a method
using C02 or 02 and stoichiometric calculations to determine excess air.   These
methods and modifications may be used, but are subject to the approval of the
Administrator. U.S. Environmental Protection Agency (EPA).

1.1.3  Note.  Mention of trade names or specific products does not constitute
endorsement by EPA.

1.2  Principle.  A gas sample is extracted from a stack by one of the following
methods:  (1) single-point, grab sampling; (2) single-point, integrated  sampling;  or
(3) multi-point, integrated sampling.  The gas sample is analyzed for percent C02.
percent 02.  and.  if necessary,  percent CO.   An Orsat  analyzer  must be used  for  excess
air or emission rate correction factor determinations.

2.  APPARATUS

The alternative sampling systems are the same as those mentioned in Section 2 of
Method 3.

2.1  Grab Sampling and Integrated Sampling.  Same as in Sections 2.1 and 2.2.
respectively, of Method 3.

2.2  Analysis.  An Orsat analyzer only.  For low C02 (less than 4.0  percent)  or high
02 (greater than 15.0 percent)  concentrations,  the measuring burette of  the Orsat
must have at least 0.1 percent subdivisions.  For Orsat maintenance and operation
procedures, follow the instructions recommended by the manufacturer, unless
otherwise specified herein.

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Prepared by Emission Measurement Branch                                 EMTIC TM-003B
Technical Support Division,  OAQPS.  EPA                                   May 15.  1990


EMTIC TM-003B                  EMTIC NSPS TEST METHOD                          Page 2


3.  PROCEDURES

Each of the three procedures below shall be used only when specified in an
applicable subpart of the standards.   The use of these procedures for other purposes
must have specific prior approval  of the Administrator.
Note:  A Fyrite-type combustion gas analyzer is not acceptable for excess air or
emission rate correction factor determinations,  unless approved by the
Administrator.  If both percent C02 and  percent 02 are measured, the analytical
results of any of the three procedures given below may also be used for calculating
the dry molecular weight (see Method 3).

3.1  Single-Point. Grab Sampling and Analytical  Procedure.

3.1.1  The sampling point in the duct shall  be as described in Section 3.1 of Method
3.

3.1.2  Set up the equipment as shown in Figure 3-1 of Method 3, making sure all
connections ahead of the analyzer are tight.  Leak check the Orsat analyzer
according to the procedure described in Section 6 of Method 3.  This leak check is
mandatory.

3.1.3  Place the probe in the stack,  with the tip of the probe positioned at the
sampling point; purge the sampling line long enough to allow at least five
exchanges.  Draw a sample into the analyzer.  For emission rate correction factor
determinations, immediately analyze the sample,  as outlined in
Sections 3.1.4 and 3.1.5, for percent C02 or percent 02.   If excess air is desired.
proceed as follows: (1) immediately analyze the sample,  as in Sections 3.1.4 and
3.1.5, for percent C02.  02, and CO;  (2) determine the percentage of the gas that is N2
by subtracting the sum of the percent C02, percent 02,  and percent CO from 100
percent, and (3) calculate percent excess air as outlined in Section 4.2.

3.1.4  To ensure complete absorption of the C02, 02, or if applicable, CO, make
repeated passes through each absorbing solution until  two consecutive readings are
the same.  Several passes (three or four) should be made between readings.  (If
constant readings cannot be obtained after three consecutive readings, replace the
absorbing solution.)  Note:   Since this single-point,  grab sampling and analytical
procedure is normally conducted in conjunction with a single-point, grab sampling
and analytical procedure for a pollutant, only one analysis is ordinarily conducted.
Therefore, great care must be taken to obtain a valid sample and analysis.  Although
in most cases, only C02 or 02 is required, it is recommended that both C02 and 02 be
measured, and that Section 3.4 be used to validate the analytical data.             *

3.1.5  After the analysis is completed,  leak check (mandatory) the Orsat analyzer
once again, as described in Section 6 of Method 3.  For the results of the analysis

-------
to  be  valid,  the Orsat analyzer must  pass  this  leak  test  before  and  after  the
analysis.
 EMTIC  TM-003B                  EMTIC NSPS TEST METHOD                         Page 3
 3.2  Single-Point.  Integrated Sampling and Analytical  Procedure.

 3.2.1  The sampling point in the duct shall be located as  specified
• in Section 3.1.1.

 3.2.2  Leak check  (mandatory) the flexible bag as  in Section  2.2.6 of
 Method 3.   Set up  the equipment as shown in Figure 3-2 of  Method  3. Just  before
 sampling,  leak check (mandatory) the train as  described in Section 4.2  of Method  3.

 3.2.3  Sample at a constant rate, or as specified  by the Administrator.   The
 sampling run must  be simultaneous with,  and for the same total length of  time  as,
 the pollutant emission rate determination.   Collect at least  30 liters  (1.00 ft3) of
 sample gas.  Smaller volumes may be collected,  subject to  approval of the
 Administrator.

 3.2.4  Obtain-one  integrated flue gas sample during each pollutant emission rate
 determination.  For emission rate correction factor determination, analyze the
 sample within 4 hours after it is taken for percent C02 or percent 02  (as  outlined in
 Sections 3.2.5 through 3.2.7). The Orsat analyzer  must be  leak checked  (see Section
 6 of Method 3) before the analysis.  If excess air is  desired, proceed  as follows:
 (1) within 4 hours after the sample is taken,  analyze  it (as  in Sections  3.2.5
 through 3.2.7) for percent C02,  02. and CO; (2) determine the  percentage of the gas
 that is N2 by subtracting  the sum of the percent C02. percent  02.  and percent CO from
 100 percent; and (3) calculate percent excess  air.  as  outlined in Section 4.2.

 3.2.5  To ensure complete absorption of the C02. 02. or if  applicable. CO. follow the
 procedure described in Section 3.1.4.   Note:   Although in  most instances  only  C02 or
 02  is  required,  it  is  recommended that both C02 and 02  be measured, and that Section
 3.4.1 be used to validate the analytical  data.

 3.2.6  Repeat the  analysis until the following criteria are met:

 3.2.6.1  For percent C02.  repeat the analytical procedure until the results of any
 three analyses differ by no more than (a)  0.3  percent  by volume when C02  is greater
 than 4.0 percent or (b) 0.2 percent by volume  when C02  is  less than or equal  to 4.0
 percent.  Average  three acceptable values  of percent C02, and report the  results to
 the nearest 0.1 percent.

 3.2.6.2  For percent 02.  repeat  the analytical  procedure until the results of  any
 three analyses differ by no more than (a)  0.3  percent  by volume when 02 is less than
 15.0 percent or (b) 0.2 percent by volume when 02  is greater than or equal to  15.0
 percent.  Average  the three acceptable values  of percent 02. and  report the results

-------
to the nearest 0.1 percent.

3.2.6.3  For percent CO, repeat the analytical procedure until the results of any
three analyses differ by no more than 0.3 percent.  Average the three acceptable
values of percent CO, and report the results to the nearest 0.1 percent.
EMTIC TM-003B                   EMTIC NSPS TEST METHOD                          Page 4
3.2.7  After the analysis is completed, leak check (mandatory) the Orsat analyzer
once again, as described in Section 6 of Method 3.  For the results
of the analysis to be valid, the Orsat analyzer must pass this leak test before and
after the analysis.

3.3  Multi-Point, Integrated Sampling and Analytical Procedure.

3.3.1  The sampling points shall be determined as specified in Section 5.3 of Method
3.

3.3.2  Follow the procedures outlined in Sections 3.2.2 through 3.2.7, except for
the following:  Traverse all sampling points,  and sample at each point for an equal
length of time.  Record sampling data as shown in Figure 3-3 of Method 3.

3.4  Quality Control Procedures.

3.4.1  Data Validation When Both C02  and 02 Are Measured.  Although in most
instances, only C02 or 02 measurement is required, it is recommended that both C02 and
02 be  measured to provide  a  check  on  the quality  of  the  data.   The  following  quality
control procedure is suggested. Note:  Since the method for validating the C02 and 02
analyses is based on combustion of organic and fossil  fuels and dilution of the gas
stream with air, this method does not apply to sources that (1) remove C02  or 02
through processes other than combustion, (2) add 02  (e.g.,  oxygen enrichment) and N2
in proportions different from that of air. (3) add C02  (e.g.,  cement or  lime  kilns).
or (4) have no fuel factor.  F0.  values  obtainable (e.g., extremely  variable waste
mixtures).  This method validates the measured proportions of C02 and  02 for  fuel
type,  but the method does not detect  sample dilution resulting from leaks during or
after sample collection.  The method  is applicable for samples collected downstream
of most lime or limestone flue-gas desulfurization units as the C02 added or  removed
from the gas stream is not significant in relation to the total C02 concentration.
The C02 concentrations from  other  types of
scrubbers using only water or basic slurry can be significantly affected and would
render the F0 check  minimally  useful.

3.4.1.1  Calculate a fuel  factor,  F0, using  the following  equation:

                      20.9 - *02
                FO	                                             Eq. 3B-1
                        *C02

where:

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       $02 = Percent 02 by volume,  dry basis.

      XC02 = Percent C02 by volume,  dry basis.

      20.9 = Percent 02 by volume in ambient air.
EMTIC TM-003B                   EMTIC NSPS TEST METHOD                          Page 5
If CO is present in quantities measurable by this method, adjust the 02 and C02
values before performing the calculation for F0 as follows:
       *C02(adj)  =

        *02(adj)  = *02 - 0.5

where:

       %CO = Percent CO by volume, dry basis.
3.4.1.2  Compare the calculated F0 factor with the expected F0 values.  The following
table may be used in establishing acceptable ranges for the expected F0 if the fuel
being burned is known.  When fuels are burned in combinations, calculate the
combined fuel Fd and Fc  factors  (as defined  in Method 19) according to the procedure
in Method 19. Section 5.2.3.  Then calculate the F0 factor  as  follows:

                        0.209 Fd
                 F0	                                             Eq.  3B-2
           Fuel type                                       F0  range
   Coal:   Anthracite and lignite 	  1.016 - 1.130
           Bituminous	1.083 - 1.230

   Oil:    Distillate	1.260 - 1.413
           Residual	1.210 - 1.370

   Gas:    Natural	1.600 - 1.836
           Propane	1.434 - 1.586
           Butane	1.405 - 1.553

   Wood	1.000  -  1.120
   Wood bark	1.003  -  1.130

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3.4.1.3  Calculated F0 values,  beyond the acceptable ranges  shown in this table.
should be investigated before accepting the test results.  For example, the strength
of the solutions  in the gas analyzer and the analyzing technique should be checked
by sampling and analyzing a known concentration, such as air; the fuel factor should
be reviewed and verified.  An acceptability range of ±12 percent is appropriate for
the F0 factor of mixed fuels with variable fuel  ratios.   The level  of the emission
rate  relative to  the compliance level should be considered in determining if a
retest is appropriate, i.e.; if the measured emissions are much lower or much
greater than the  compliance limit,

EMTIC TM-003B                  EMTIC NSPS TEST METHOD                          Page 6
 repetition of the test would not significantly change the compliance status of the
 source and would be unnecessarily time consuming and costly.

 4.  CALCULATIONS

 4.1  Nomenclature.  Same as Section 5 of Method 3 with the addition of the
 following:
               Percent excess air.

       0.264 = Ratio of 02 to N2 in air. v/v.

4.2  Percent Excess Air.  Calculate the percent excess air (if applicable) by
substituting the appropriate values of percent 02. CO. and N2 (obtained from Section
3.1.3 or 3.2.4) into Equation 3B-3.

                        X02 -  0.5  *CO
          *EA -  -   x 100                        Eq.  3B-3
                  0.264 *N2 -  (*02 - 0.5 SCO)


Note:  The equation above assumes  that ambient air is used as  the  source of 02 and
that the fuel does not contain appreciable amounts of N2 (as do coke oven  or blast
furnace gases).  For those cases when  appreciable amounts  of N2 are present  (coal.
oil, and natural  gas do not contain appreciable amounts of N2) or when oxygen
enrichment is used, alternative methods,  subject to  approval of the Administrator.
are required.

5.  BIBLIOGRAPHY

Same as Method 3.

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        EMISSION MEASUREMENT TECHNICAL INFORMATION  CENTER
                         NSPS TEST METHOD
           Method 4 - Determination of Moisture Content
                          in Stack Gases
1.  PRINCIPLE AND APPLICABILITY

1.1  Principle.   A gas  sample is extracted at a constant  rate  from
the  source;  moisture  is  removed  from  the  sample  stream  and
determined  either volumetrically or gravimetrically.

1.2  Applicability.   This  method is applicable for determining the
moisture content of  stack gas.

1.2.1  Two procedures are  given.  The first is a reference method,
for accurate determinations  of moisture content  (such  as are  needed
to  calculate emission data).   The  second  is  an  approximation
method,  which  provides estimates  of  percent moisture  to aid  in
setting  isokinetic sampling rates prior  to  a  pollutant  emission
measurement run.   The approximation method described  herein is  only
a  suggested approach;  alternative means  for  approximating  the
moisture content,  e.g.,  drying tubes,  wet bulb-dry bulb techniques,
condensation  techniques,   stoichiometric calculations,  previous
experience, etc., are  also  acceptable.

1.2.2  The reference  method  is often conducted simultaneously  with
a pollutant emission measurement  run;  when  it  is,  calculation  of
percent  isokinetic,  pollutant emission  rate,  etc.,  for the  run
shall  be based  upon the  results  of  the  reference  method or  its
equivalent;  these calculations shall not be based upon the results
of  the approximation method,  unless  the  approximation method  is
shown,  to the satisfaction of the Administrator,  U.S.  Environmental
Protection  Agency,   to  be  capable of  yielding results  within  1
percent H20  of  the reference method.

1.2.3  Note:  The reference method may yield questionable results
Prepared by Emission Measurement Branch              EMTIC  TM-004
Technical Support Division, OAQPS, EPA               July  11,  1989

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        EMISSION MEASUREMENT TECHNICAL INFORMATION CENTER
                        NSPS TEST METHOD
when applied to saturated gas  streams  or  to streams that contain
water droplets.   Therefore, when  these  conditions  exist  or  are
suspected,  a second determination of the moisture content shall be
made simultaneously with the reference method, as follows:  Assume
that the  gas stream is  saturated.   Attach  a  temperature sensor
[capable of measuring to within 1°C  (2°F) ]  to the reference method
probe.   Measure the stack gas  temperature at each traverse point
(see Section 2.2.1) during the reference method  traverse; calculate
the average  stack gas  temperature.   Next, determine the moisture
percentage, either by:   (1) using a psychrometric chart and making
appropriate corrections if stack pressure  is different from that of
the chart,  or (2) using saturation vapor pressure  tables.  In cases
where the  psychrometric chart  or  the saturation  vapor pressure
tables  are not applicable  (based on  evaluation  of the process),
alternative methods, subject to the approval  of the Administrator,
shall be used.

2.  REFERENCE METHOD

The  procedure  described in  Method  5  for  determining moisture
content is  acceptable as a reference method.

2.1  Apparatus.   A schematic of the  sampling  train used in  this
reference  method is shown in Figure 4-1.  All  components shall be
maintained and calibrated according to the procedures in Method 5.

2.1.1  Probe.  Stainless  steel or glass tubing,  sufficiently heated
to prevent water condensation, and  equipped  with a  filter, either
in-stack  (e.g., a plug of glass wool  inserted  into  the  end of the
probe)  or  heated  out-stack (e.g.,  as  described  in Method 5), to
remove  particulate  matter.   When  stack  conditions permit,  other
metals or plastic  tubing  may be used for the  probe,  subject to the
approval of the Administrator.

2.1.2   Condenser.  See Method  5, Section  2.1.7,  for a  description
 Prepared  by Emission Measurement Branch               EMTIC TM-004
 Technical Support  Division,  OAQPS,  EPA               July 11, 1989

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EMTIC TM-004                     EMTIC NSPS TEST METHOD
                                                           Page 3
of an acceptable type  of  condenser and for alternative measurement
systems.

2.1.3  Cooling System.   An ice bath container and crushed ice  (or
equivalent), to aid in condensing moisture.

2.1.4  Metering System.   Same as in Method 5,  Section  2.1.8, except
do not  use sampling systems designed for  flow  rates higher than
0.0283  mVmin   (1.0  cfm) .    Other metering  systems,  capable  of
maintaining  a constant  sampling  rate  to  within 10  percent and
determining  sample  gas  volume to within 2 percent,  may be used,
subject to the approval  of the Administrator.

2.1.5  Barometer.   Mercury, aneroid, or other barometer capable of
measuring atmospheric  pressure to within 2.5 mm  (0.1 in.) Hg.  See
NOTE in Method 5, Section 2.1.9.

2.1.6   Graduated Cylinder and/or Balance.   To  measure condensed
water and moisture caught in the silica gel to within 1 ml or 0.5
g.  Graduated cylinders  shall have subdivisions no greater than 2
ml.   Most  laboratory balances  are  capable  of weighing  to the
nearest 0.5  g or less.   These balances are suitable for use here.

2.2  Procedure.   The  following procedure  is  written for a condenser
system  (such as the impinger system described in Section 2.1.7 of
Method  5)   incorporating  volumetric  analysis  to  measure  the
condensed  moisture,  and silica  gel  and gravimetric  analysis  to
measure the moisture leaving the condenser.

2.2.1  Unless otherwise  specified by the Administrator, a minimum
of eight traverse points shall be used for circular stacks having
diameters less than  0.61  m  (24 in.),  a minimum of nine points shall
be used for  rectangular  stacks
having  equivalent  diameters  less  than  0.61 m  (24  in.),  and a
minimum of twelve traverse points shall be used in all other cases.
The traverse points  shall  be located according  to Method 1.  The
use  of   fewer   points   is  subject  to   the  approval  of  the
Administrator.   Select a  suitable probe and probe length such that
all  traverse points  can  be  sampled.    Consider sampling  from
opposite sides
of the  stack  (four  total  sampling  ports)  for large  stacks,  to
permit  use  of shorter probe  lengths.   Mark  the  probe  with heat
resistant  tape  or  by  some  other method to  denote  the proper
distance  into  the  stack or duct for  each  sampling  point.  Place

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EMTIC TM-004                     EMTIC NSPS TEST METHOD
                                                           Page  4
known  volumes of water  in the first  two impingers.   Weigh  and
record the  weight of the  silica  gel  to  the nearest  0.5  g,  and
transfer  the silica gel to the fourth impinger; alternatively,  the
silica gel may first be transferred to the  impinger, and the weight
of the silica gel plus impinger recorded.

2.2.2  Select a total sampling time such that a minimum total  gas
volume of 0.60 scm (21 scf) will be collected,  at a rate no greater
than  0.021  mVmin (0.75  cfm) .   When  both moisture  content  and
pollutant  emission  rate  are  to  be  determined,  the  moisture
determination shall be simultaneous  with,  and for the same  total
length  of  time   as,  the  pollutant  emission rate   run,  unless
otherwise specified in an applicable subpart of the standards.

2.2.3  Set up the sampling train as shown in Figure 4-1.  Turn on
the probe heater and (if applicable)  the filter heating system to
temperatures of about 120°C  (248°F), to prevent water condensation
ahead  of the condenser;  allow  time  for  the  temperatures  to
stabilize.   Place  crushed ice in  the ice  bath container.    It is
recommended,  but  not required,  that  a  leak  check  be  done,  as
follows:    Disconnect the  probe from  the  first  impinger  or  (if
applicable)   from  the filter  holder.   Plug the inlet  to the  first
impinger  (or filter holder), and pull a 380 mm (15 in.) Hg vacuum;
a lower vacuum may be used, provided that it is not exceeded during
the test.   A leakage rate in excess of 4  percent  of the average
sampling rate or 0.00057 mVmin (0.02 cfm), whichever is less, is
unacceptable.   Following the leak check,  reconnect the probe to  the
sampling train.

2.2.4  During the  sampling run, maintain a sampling rate within 10
percent  of  constant  rate,  or as specified by the Administrator.
For each  run, record the  data required on the example data  sheet
shown in Figure 4-2.   Be sure to record the dry gas meter reading
at  the  beginning  and  end  of each  sampling time increment  and
whenever sampling is halted.   Take other  appropriate readings at
each sample  point, at least once during each time increment.

2.2.5   To  begin  sampling,  position the  probe tip at  the  first
traverse  point.  Immediately start  the pump,  and adjust the flow to
the desired rate.  Traverse  the cross  section, sampling  at each
traverse  point for an equal length of time.  Add more ice and, if
necessary, salt to maintain a  temperature  of  less than 20°C  (68°F<)
at the silica gel outlet.

2.2.6  After collecting the sample, disconnect the probe from  the

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EMTIC TM-004                      EMTIC NSPS TEST METHOD
                                                            Page 5
filter  holder  (or from  the first  impinger),  and conduct  a  leak
check  (mandatory) as described in  Section 2.2.3.   Record the leak
rate.   If the leakage  rate  exceeds the  allowable  rate,  the tester
shall  either reject  the  test results or  shall  correct  the sample
volume as in Section  6.3  of  Method  5.  Next,  measure the volume of
the moisture condensed to the  nearest ml.  Determine the increase
in weight of the silica gel (or silica gel  plus  impinger)  to the
nearest 0.5 g.  Record this information  (see example data sheet,
Figure 4-3), and calculate the  moisture percentage, as described in
2.3 below.

2.2.7  A quality control  check  of the volume metering system at the
field site is  suggested before  collecting  the sample following the
procedure in Method  5, Section 4.4.

2.3  Calculations. Carry out the following calculations, retaining
at least one extra decimal figure beyond that of the acquired data.
Round  off figures after  final  calculation.

2.3.1   Nomenclature.

   Bws  = Proportion of  water vapor, by volume, in the gas stream.

    Mw  = Molecular weight  of  water,  18.0  g/g-mole  (18.0  Ib/lb-
         mole).

    Pm  = Absolute pressure  (for this method,  same  as  barometric
         pressure)       at  the  dry gas meter, mm Hg  (in. Hg).

   Pstd  = Standard absolute pressure, 760 mm Hg  (29o92 in. Hg)  .

     R  = Ideal  gas constant, 0.06236  (mm  Hg) (m3) / (g-mole) (°K)  for
         metric  units   and  21.85  (in.  Hg) (ft3) / (Ib-mole) (°R)  for
         English  units.

    Tm  = Absolute temperature at meter,  °K (°R) .

   Tstd  = Standard absolute temperature,  293°K (528°R) .

    Vm  = Dry gas  volume measured by dry gas meter, dcm  (dcf).

   AVm  = Incremental  dry gas volume measured by  dry gas  meter at
         each traverse  point,  dcm (dcf).

       = DrY 9as  volume measured by the dry gas meter, corrected to

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EMTIC  TM-004                      EMTIC NSPS TEST METHOD
                                                             Page 6
         standard conditions, dscm  (dscf).

 vwcistd) = Volume  of  water vapor  condensed,  corrected to  standard
         conditions, scm  (scf).

vwsg(std) = Volume  of water  vapor  collected .in silica gel,  corrected
         to standard  conditions, scm  (scf) .

    Vf = Final volume of condenser water, ml.

    Vi = Initial volume, if any, of condenser  water,  ml.

    Wf = Final weight of silica gel or silica gel plus impinger,  g.

    Wi = Initial weight  of silica gel or silica gel plus  impinger,


     Y = Dry gas meter calibration factor.

    pw = Density of water, 0.9982 g/ml  (0.002201 Ib/ml).


2.3.2  Volume of Water  Vapor Condensed.

            v    =(v  -v )p   RTstd
             «=(.*.,    t   iJP»PstdMw                         Eq.  4-1
Where:

    K! =  0.001333  mVml for metric  units,

      =  0.04707 ftVml for English units.


2.3.3  Volume of Water Collected in Silica Gel

                     RT
           v
                      f -  i     std
                                                          Eq. 4-2
                  = K2(Wf - W.)

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EMTIC TM-004                      EMTIC NSPS TEST  METHOD

                                                             Page 7
Where:




    K2 = 0.001335 m3/g for metric units,




       = 0.04715 ftVg for English units.






2.3.4   Sample  Gas Volume.





                        (PJ (Tstd)




                               11                           Eq.
V     = V Y-
 m(std)    m
                         v p

                   = K Y  m m


                      3

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EMTIC TM-004                      EMTIC NSPS TEST METHOD
                                                            Page 8
Where:

    K3 =  0.3858  °K/mm  Hg  for  metric units,

      =  17.64  °R/in.  Hg  for  English units.
NOTE:   If  the  post-test leak  rate  (Section  2.2.6)  exceeds  the
allowable  rate,  correct the  value  of Vra  in Equation 4-3,  as
described in Section 6.3 of Method  5.

2.3.5  Moisture Content.
          3       wc(std)   wsg(std)                           Eq. 4~4
           ws  V     +V      +V
               wc(std)  wsg(std)   m(std)
NOTE:   In saturated  or moisture  droplet-laden gas  streams,  two
calculations  of the moisture  content of the  stack gas  shall be
made, one using a  value based upon the saturated  conditions  (see
Section 1.2),  and  another based upon the results  of  the impinger
analysis.   The lower of  these two values of Bws  shall be considered
correct.

2.3.6   Verification of Constant  Sampling  Rate.   For  each time
increment,  determine the AVm.  Calculate the  average.  If the value
for  any time increment differs from  the  average by more than 10
percent, reject  the results, and repeat the  run.

3.  APPROXIMATION METHOD

The  approximation  method described below  is presented  only as a
suggested method (see Section  1.2).

3.1  Apparatus.  See Figure 4-4.

3.1.1  Probe.  Stainless steel  or glass tubing,  sufficiently heated
to prevent water condensation and equipped  with a filter  (either
in-stack or heated  out-stack) to remove particulate matter.  A plu*g
of  glass  wool,  inserted  into  the  end  of  the  probe,  is  a
satisfactory  filter.

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EMTIC TM-004                      EMTIC NSPS TEST METHOD
                                                            Page 9
3.1.2  Impingers.  Two midget  impingers,  each  with  30-ml  capacity,
or equivalent.

3.1.3  Ice Bath.  Container  and  ice,  to aid in condensing moisture
in impingers.

3.1.4  Drying Tube.  Tube  packed with new or regenerated  6-  to 16-
mesh indicating-type  silica gel (or  equivalent desiccant),  to dry
the sample gas  and to protect the  meter and pump.

3.1.5  Valve.  Needle valve, to  regulate the sample gas flow rate.

3.1.6  Pump.   Leak-free, diaphragm  type,  or equivalent,  to pull the
gas sample through the train.

3.1.7   Volume  Meter.  Dry gas meter,  sufficiently accurate  to
measure the sample volume  to within 2 percent,  and  calibrated over
the range of flow rates and  conditions actually encountered  during
sampling.

3.1.8  Rate Meter.  Rotameter, to measure the  flow  range  from 0 to
3 liters/min  (0  to 0.11 cfm) .

3.1.9  Graduated Cylinder.  25-ml.

3.1.10    Barometer.   Mercury,   aneroid,  or  other barometer,  as
described in  Section  2.1.5  above.

3.1.11   Vacuum Gauge.  At  least 760-mm (30-in.)  Hg gauge,  to be
used for the  sampling leak  check.

3.2  Procedure.

3.2.1  Place  exactly  5 ml water in each impinger.   Leak  check the
sampling train as follows:   Temporarily  insert  a vacuum  gauge at or
near the probe inlet;  then,  plug the  probe inlet, and pull a  vacuum
of at least  250  mm (10 in.) Hg.  Note  the  time rate of  change of
the dry gas meter dial; alternatively, a  rotameter  (0 to 40 cc/min)
may  be  temporarily  attached  to  the  dry gas  meter outlet  to
determine the leakage rate.  A leak rate  not in excess of  2 percent
of  the  average  sampling  rate  is  acceptable.   NOTE:    Carefully
release the probe  inlet plug  before  turning off the pump.

3.2.2  Connect the  probe, insert it  into the  stack,  and  sample at

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EMTIC TM-004                      EMTIC NSPS TEST METHOD
                                                           Page 10
a constant  rate  of 2 liters/min  (0.071 cfm) .   Continue sampling
until  the  dry gas meter registers about  30 liters  (1.1 ft3)  or
until  visible liquid  droplets are  carried over  from  the  first
impinger to the second.   Record temperature,  pressure,  and dry gas
meter readings as required by  Figure  4-5.

3.2.3  After collecting  the sample, combine the contents of the two
impingers,  and measure  the volume to  the nearest  0.5 ml.

3.3  Calculations.  The  calculation method presented is  designed to
estimate the  moisture  in  the  stack  gas;  therefore,   other  data,
which are only necessary for accurate  moisture determinations,  are
not  collected.   The following equations  adequately estimate  the
moisture  content,  for  the  purpose  of   determining   isokinetic
sampling rate settings.

3.3.1  Nomenclature.

    B^ = Approximate  proportion by volume of water vapor in the gas
         stream leaving  the second impinger, 0.025.

    BHS = Water vapor in  the gas stream, proportion by  volume.

     Mw = Molecular weight of  water,  18.0  g/g-mole  (18.0  Ib/lb-
         mole).

     Pm = Absolute pressure  (for this method,  same as  barometric
         pressure)  at the dry  gas meter, mm  Hg  (in. Hg).

   Pstd = Standard absolute pressure,  760 mm  Hg  (29.92  in.  Hg) .

     R = Ideal gas constant, 0.06236  [(mm  Hg) (m3) ] / [ (g-mole) (°K) ]
         for metric units and 21.85  [(in. Hg) (ft3) ] / [(Ib-mole) (°R)]
         for English units.

     Tm = Absolute temperature  at meter, °K  (°R) .

   Tstd = Standard absolute temperature, 293°R (528°R) .

     Vf = Final volume of impinger contents, ml.

     VA = Initial volume of impinger contents, ml.                ,

     vm = Dry gas volume measured by dry gas meter, dcm (dcf).

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EMTIC TM-004                     EMTIC NSPS TEST METHOD
                                                           Page 11
 vm(stdj = DrY  gas volume measured  by  dry gas meter,  corrected to
         standard conditions,  dscm (dscf) .


     Y = Dry  gas meter  calibration factor.


     pw = Density of water, 0.9982 g/ml  (0.002201  Ib/ml) .


3.3.2  Volume of Water  Vapor  Collected.
                      Pstc,Mw                               Eq.  4-5
Where :


     K! = 0.001333 m3/ml for metric units,


       = 0.04707 ftVml for English units


3.3.3  Gas Volume.
                              T

                       P   I I  T
                                                          Eq.  4-6
                         Pm                                M
                  = K. V  -S
                    2  mm
Where:


     K2 = 0.03858  °K/mm Hg for metric units,


       = 17.64  °R/in. Hg for English units.


3.3.4  Approximate Moisture Content.

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EMTIC TM-004                     EMTIC NSPS TEST METHOD
                                                           Page 12
             B   = 		+B
              ws    V +V       wm
                    wcv m(std)                               Eq. 4-7
                      wc  -+(0.025)
                  V  +V
                   we  m(std)
4.  CALIBRATION
4.1   For  the  reference  method,  calibrate  the  metering  system,
temperature gauges, and barometer according  to Sections 5.3,  5.5,
and 5.7,  respectively,  of  Method 5.  The recommended  leak check of
the metering system  (Section 5.6 of Method 5) also applies to the
reference method.   For  the approximation method,  use  the procedures
outlined in Section  5.1.1 of Method  6  to calibrate the metering
system,  and the procedure of  Method 5,  Section 5.7, to calibrate
the barometer.

5.   BIBLIOGRAPHY

1.  Air Pollution Engineering Manual (Second  Edition).   Danielson,
   J.A.  (ed.).   U.S.  Environmental Protection Agency,  Office of Air
   Quality Planning  and Standards.    Research Triangle  Park,  NC.
   Publication No. AP-40.  1973.

2.  Devorkin,  Howard,  et al.   Air Pollution Source Testing Manual.
   Air Pollution Control District,  Los Angeles, CA.  November 1963.

3.  Methods for  Determination  of Velocity, Volume,  Dust  and  Mist
   Content  of   Gases.    Western  Precipitation  Division  of  Joy
   Manufacturing Co.   Los Angeles,  CA.  Bulletin WP-50.   1968.

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EMTIC TM-004
                    EMTIC NSPS TEST METHOD
                                                                       Page  13
       Filter
     (Either In Stack)
     or Out of Stack)
 Stack
/ Wall
Condenser-Ice Bath System Including Silica Gel Tube

            I
  method.
                       Figure 4-1.   Moisture  sampling train reference

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EMTIC TM-004                     EMTIC NSPS TEST METHOD
                                                          Page 14

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                Figure 4-2.   Field Moisture Determination Reference Method.
Plant 	
Location.
Operator.
Date	
Run No. 	
Ambient temperature.
Barometric pressure.
Probe Length	
                                      SCHEMATIC OF STACK CROSS SECTION
Traverse
Pt. No.










Sampling
Time
(9) , min










Stack
Temperature
°C (°F)










Average
Pressure
differential across
orifice meter AH
mm (in.) H20











Meter
Reading gas
sample
volume
m3 (ft3)











AVn
m3
(ft3)











Gas sample
temperature at
dry gas meter
Inlet
Tmln
°C(°F)











Outlet
Tnw
°C(°F)











Temperature
of gas
leaving
condenser or
last
impinger
°C(°F)












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EMTIC TM-004                          EMTIC NSPS TEST METHOD
                                                                       Page  16
                Figure 4-3.  Analytical data - reference method.

                                  Impinger           Silica gel
               	volume.  ml	weight,  o
           Final
           Initial
           Difference

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EMTIC TM-004
EMTIC NSPS TEST METHOD
                                                          Page 17
  Figure 4-4,,  Moisture Samping Train - Approximation Method.

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EMTIC TM-004
EMTIC  NSPS  TEST METHOD
                                                                        Page 18
           Figure 4-5.  Field Moisture Determination - Approximation Method.
Location.
Test	
Date	
Operator	
Barometric pressure.
                                  Comments:
Clock Time






Gas volume
through
meter, (VB) ,
m3 (ft3)






Rate meter
setting mVmin
(ftVmin)






Meter
temperature
0 C (° F)







-------
APPENDIX A TO PART 63--TEST METHODS
* *  *  * *
METHOD 315 - DETERMINATION OF PARTICULATE AND METHYLENE CHLORIDE
EXTRACTABLE MATTER (MCEM) FROM SELECTED SOURCES
AT PRIMARY ALUMINUM PRODUCTION FACILITIES
       NOTE: This method does not include all of the specifications (e.g., equipment and supplies) and
procedures (e.g., sampling and analytical) essential to its performance.  Some material is incorporated by
reference from other methods in this part. Therefore, to obtain reliable results, persons using this method
should have a thorough knowledge of at least the following additional test methods: Method 1, Method
2, Method 3, and Method 5 of 40 CFR part 60, appendix A.
1.0    Scope and Application.
        1.1 Analytes.  Particulate matter (PM).  No CAS number assigned.  Methylene chloride
extractable matter (MCEM). No CAS number assigned.
        1.2 Applicability. This method is applicable for the simultaneous determination of PM and
MCEM when specified in an applicable regulation. This method was developed by consensus with the
Aluminum Association and the U.S. Environmental Protection Agency (EPA) and has limited precision
estimates for MCEM; it should have similar precision to Method 5 for PM in 40 CFR part 60, appendix
A since the procedures are similar for PM.
        1.3 Data quality objectives. Adherence to the requirements of this method will enhance the
quality of the data obtained from air pollutant sampling methods.
2.0    Summary of Method.
       Particulate matter and MCEM are withdrawn isokinetically from the source. PM is collected on
a glass fiber filter maintained at a temperature in the range of 120 ± 14°C (248 ± 25°F) or such other
temperature as specified by an applicable subpart of the standards or approved by the Administrator for a
particular application.  The PM mass, which includes any material that condenses on the probe and is
subsequently removed in an acetone rinse or on the filter at or above the filtration temperature, is
determined gravimetrically after removal of uncombined water.  MCEM is then determined by adding a
methylene chloride rinse of the probe and filter holder, extracting the condensable hydrocarbons
collected in the impinger water, adding an acetone rinse followed by a methylene chloride rinse of the
sampling train components after the filter and before the silica gel impinger, and determining residue
gravimetrically after evaporating the solvents.
1Q_    Definitions.  [Reserved]
4.0    Interferences.  [Reserved]
10    Safety.
       This method may involve hazardous materials, operations, and equipment.  This method does not
purport to address all of the safety problems associated with its use. It is the responsibility of the user of
this method to establish appropriate safety and health practices and determine the applicability of
regulatory limitations prior to performing this test method.
6.0 Equipment and Supplies.
       NOTE: Mention of trade names or specific products does not constitute endorsement by the
EPA.
       6.1  Sample collection. The following items are required for sample collection:
       6.1.1 Sampling train.  A schematic of the sampling train used in this method is shown in Figure
5-1, Method 5,40 CFR part 60, appendix A. Complete construction details are given in APTD-0581
(Reference 2 in section 17.0 of this method); commercial models of this train are also available. For
changes from APTD-0581 and for allowable modifications of the train shown in Figure 5-1, Method 5,40
CFR part 60, appendix, A see the following subsections.
       NOTE: The operating and maintenance procedures for the sampling train are described in
APTD-0576 (Reference 3 in section 17.0 of this method). Since correct usage is important in obtaining

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valid results, all users should read APTD-0576 and adopt the operating and maintenance procedures
outlined in it, unless otherwise specified herein. The use of grease for sealing sampling train components
is not recommended because many greases are soluble in methylene chloride. The sampling train
consists of the following components:
       6.1.1.1  Probe nozzle. Glass or glass lined with sharp, tapered leading edge. The angle of taper
shall be <30°, and the taper shall be on the outside to preserve a constant internal diameter.  The probe
nozzle shall be of the button-hook or elbow design, unless otherwise specified by the Administrator.
Other materials of construction may be used, subject to the approval of the Administrator. A range of
nozzle sizes suitable for isokinetic sampling should be available.  Typical nozzle sizes range from 0.32 to
1.27 cm (1/8 to 1/2 in.) inside diameter (ID) in increments of 0.16 cm (1/16 in.). Larger nozzle sizes are
also available if higher volume sampling trains are used. Each nozzle shall be calibrated according to the
procedures outlined in section 10.0 of this method.
       6.1.1.2 Probe liner. Borosilicate or quartz glass tubing with a heating system capable of
maintaining a probe gas temperature at the exit end during sampling of 120 ± 14°C (248 ± 25°F), or such
other temperature as specified by an applicable subpart of the standards or approved by the
Administrator for a particular application. Because the actual temperature at the outlet of the probe is
not usually monitored during sampling, probes constructed according to APTD-0581 and using the
calibration curves of APTD-0576 (or calibrated according to the procedure outlined in APTD-0576) will
be considered acceptable. Either borosilicate or quartz glass probe liners may be used for stack
temperatures up to  about 480°C (900°F); quartz liners shall be used for temperatures between 480 and
900°C (900 and 1,650°F). Both types of liners may be  used at higher temperatures than specified for
short periods of time, subject to the approval of the Administrator. The softening temperature for
borosilicate glass is 820°C (1,500°F) and for quartz glass it is 1,500°C (2,700°F).
       6.1.1.3 Pitot tube.  Type S, as described in section 6.1 of Method 2, 40 CFR part 60, appendix A,
or other device approved by the Administrator. The pitot tube shall be attached to the probe (as shown in
Figure 5-1 of Method 5, 40 CFR part 60, appendix A) to allow constant monitoring of the stack gas
velocity. The impact (high pressure) opening plane of the pitot tube shall be even  with or above the
nozzle entry plane (see Method 2, Figure 2-6b, 40 CFR part 60, appendix A) during sampling. The Type
S pitot tube assembly shall have a known coefficient, determined  as outlined in section 10.0 of Method 2,
40 CFR part 60, appendix A.
       6.1.1.4 Differential pressure gauge. Inclined manometer or equivalent device (two), as described
in section 6.2 of Method 2, 40 CFR part 60, appendix A. One manometer shall be used for velocity head
(Dp) readings, and  the other, for orifice differential pressure readings.
       6.1.1.5 Filter holder. Borosilicate glass, with a glass frit filter support and a silicone rubber
gasket. The holder design shall provide a positive seal against leakage from the outside or around the
filter. The holder shall be attached immediately at the  outlet of the probe (or cyclone, if used).
       6.1.1.6 Filter heating system. Any heating system capable of maintaining  a temperature around
the filter holder of 120 ± 14°C (248 ± 25°F) during sampling, or such other temperature as specified by an
applicable subpart of the standards or approved by the Administrator for a particular application.
Alternatively, the tester may opt to operate the equipment at a temperature lower than that specified. A
temperature gauge capable of measuring temperature to within 3°C (5.4°F) shall be installed so that the
temperature around the filter holder can be regulated and monitored during sampling. Heating systems
other than the one shown in APTD-0581 may be used.
       6.1.1.7  Temperature sensor. A temperature sensor capable of measuring temperature to within
±3°C (5.4°F) shall  be installed so that the  sensing tip of the temperature sensor is  in direct contact with
the sample gas, and the temperature around the filter holder can be regulated and monitored during
sampling.                                                                                     *
       6.1.1.8 Condenser. The following system shall be used to determine the stack gas moisture
content: four glass impingers connected in series with leak-free ground glass fittings. The first, third,

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and fourth impingers shall be of the Greenburg-Smith design, modified by replacing the tip with a 1.3 cm
(1/2 in.) ID glass tube extending to about 1.3 cm (1/2 in.) from the bottom of the flask. The second
impinger shall be of the Greenburg-Smith design with the standard tip. The first and second impingers
shall contain known quantities of water (section 8.3.1 of this method), the third shall be empty, and the
fourth shall contain a known weight of silica gel or equivalent desiccant.  A temperature sensor capable
of measuring temperature to within 1°C (2°F) shall be placed at the outlet of the fourth impinger for
monitoring.
        6.1.1.9 Metering system. Vacuum gauge, leak-free pump, temperature sensors capable of
measuring temperature to within 3°C (5.4°F), dry gas meter (DGM) capable of measuring volume to
within 2 percent, and related equipment, as shown in Figure 5-1 of Method 5, 40 CFR part 60, appendix
A. Other metering systems capable of maintaining sampling rates within 10 percent of isokinetic and of
determining sample volumes to within 2 percent may be used, subject to the approval of the
Administrator. When the metering system is used in conjunction with a pitot tube, the system shall allow
periodic checks of isokinetic rates.
        6.1.1.10  Sampling trains using metering systems designed for higher flow rates than that
described in APTD-0581 or APTD-0576 may be used provided that the specifications of this method are
met.
        6.1.2 Barometer.  Mercury, aneroid, or other barometer capable of measuring atmospheric
pressure to within 2.5 mm (0.1 in.) Hg.
        NOTE: The barometric reading may be obtained from a nearby National Weather Service
station.  In this case, the station value (which is the absolute barometric pressure) shall be requested and
an adjustment for elevation differences between the weather station and sampling point shall be made at
a rate of minus 2.5 mm (0.1 in) Hg per 30 m (100 ft) elevation increase or plus 2.5 mm (0.1 in) Hg per 30
m (100  ft) elevation decrease.
        6.1.3 Gas density determination equipment. Temperature sensor and pressure gauge, as
described in sections 6.3 and 6.4 of Method 2, 40 CFR part 60, appendix A, and gas analyzer, if
necessary, as described in Method 3,40 CFR part 60, appendix A. The temperature sensor shall,
preferably, be permanently attached to the pitot tube or sampling probe in a fixed configuration, such that
the tip of the sensor extends beyond the leading edge of the probe sheath and does not touch any metal.
Alternatively, the sensor may be attached just prior to use in the field. Note, however, that if the
temperature sensor is attached in the field, the sensor must be placed in an interference-free arrangement
with respect to the Type S pitot tube openings (see Method 2, Figure 2-4,40 CFR part 60, appendix A).
As a second alternative, if a difference of not more than 1 percent in the average velocity measurement is
to be introduced, the temperature sensor need not be attached to the probe or pitot tube. (This alternative
is subject to the approval of the Administrator.)
        6.2  Sample recovery. The following items are required for sample recovery:
        6.2.1 Probe-liner and probe-nozzle brushes. Nylon or Teflon® bristle brushes with stainless
steel wire handles. The probe brush shall have extensions (at least as long as the probe) constructed of
stainless steel, nylon, Teflon®, or similarly inert material.  The brushes shall be properly sized and
shaped to brush out the probe liner and nozzle.
        6.2.2 Wash bottles.  Glass wash bottles are recommended. Polyethylene or tetrafluoroethylene
(TFE) wash  bottles may be used, but they may introduce a positive bias due to contamination from the
bottle. It is recommended that acetone not be stored in polyethylene  or TFE bottles for longer than a
month.
        6.2.3 Glass sample storage containers. Chemically resistant, borosilicate glass bottles, for
acetone and  methylene chloride washes and impinger water, 500 ml or 1,000 ml.  Screw-cap liners shall
either be rubber-backed Teflon® or shall be constructed so as to be leak-free and resistant to chemical
attack by acetone or methylene chloride.  (Narrow-mouth glass bottles have been found to be less prone
to leakage.)  Alternatively, polyethylene bottles may be used.
        6.2.4 Petri dishes. For filter samples, glass, unless otherwise specified by the Administrator.
        6.2.5 Graduated cylinder and/or balance.  To measure condensed water, acetone wash and

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methylene chloride wash used during field recovery of the samples, to within 1 ml or 1 g.  Graduated
cylinders shall have subdivisions no greater than 2 ml. Most laboratory balances are capable of weighing
to the nearest 0.5 g or less. Any such balance is suitable for use here and in section 6.3.4 of this method.
       6.2.6 Plastic storage containers.  Air-tight containers to store silica gel.
       6.2.7 Funnel and rubber policeman. To aid in transfer of silica gel to container; not necessary if
silica gel is weighed in the field.
       6.2.8 Funnel. Glass or polyethylene, to aid in sample recovery.
       6.3  Sample analysis. The following equipment is required for sample analysis:
       6.3.1 Glass or Teflon® weighing dishes.
       6.3.2 Desiccator.  It is recommended that fresh desiccant be used to minimize the chance for
positive bias due to absorption of organic material during drying.
       6.3.3 Analytical balance.  To measure to within 0.1 mg.
       6.3.4 Balance. To measure to within 0.5 g.
       6.3.5 Beakers. 250ml.
       6.3.6 Hygrometer. To measure the relative humidity of the laboratory environment.
       6.3.7 Temperature sensor.  To measure the temperature of the laboratory environment.
       6.3.8 Buchner fritted funnel. 30 ml size, fine (<50 micron)-porosity fritted glass.
       6.3.9 Pressure filtration apparatus.
       6.3.10 Aluminum dish. Flat bottom, smooth sides, and flanged top, 18 mm deep and with an
inside diameter of approximately 60 mm.
7.0 Reagents and Standards.
       7.1  Sample collection. The following reagents are required for sample collection:
       7.1.1 Filters.  Glass fiber filters, without organic binder, exhibiting at least 99.95 percent
efficiency (<0.05 percent penetration) on 0.3 micron dioctyl phthalate smoke particles. The filter
efficiency test shall be conducted in accordance with ASTM Method D 2986-95A (incorporated by
reference in § 63.841 of this part).  Test data from the supplier's quality control program are sufficient for
this purpose. In sources containing S02 or S03, the filter material must be of a type that is unreactive to
S02 or S03.  Reference 10 in section 17.0 of this method may be used to select the appropriate filter.
       7.1.2 Silica gel.  Indicating type, 6 to 16 mesh. If previously used, dryatl75°C(350°F)for2
hours. New silica gel may be used as received. Alternatively, other types of desiccants (equivalent or
better) may be used, subject to the approval of the Administrator.
       7.1.3  Water. When analysis of the material caught in the impingers is required, deionized
distilled water shall  be used. Run blanks prior to field use to eliminate a high blank on test samples.
       7.1.4 Crushed ice.
       7.1.5  Stopcock grease. Acetone-insoluble, heat-stable silicone grease. This is not necessary if
screw-on connectors with Teflon® sleeves, or similar, are used. Alternatively, other types of stopcock
grease may be used, subject to the approval of the Administrator. [Caution: Many stopcock greases are
methylene chloride-soluble.  Use sparingly and carefully remove prior to recovery to prevent
contamination of the MCEM analysis.]
       7.2  Sample recovery. The following reagents are required for sample recovery:
       7.2.1 Acetone. Acetone with blank values < 1 ppm, by weight residue, is required. Acetone
blanks may be run prior to field use, and only acetone with low blank values may be used. In no case
shall a blank value of greater than 1E-06 of the weight of acetone used be subtracted from the sample
weight.
       NOTE: This is more restrictive than Method 5,40 CFR part 60, appendix A.  At least one
vendor (Supelco Incorporated located in Bellefonte, Pennsylvania) lists <1  mg/1 as residue for its
Environmental Analysis Solvents.
       7.2.2 Methylene chloride. Methylene chloride with a blank value <1.5 ppm, by weight, residue.
Methylene chloride blanks may be run prior to field use, and only methylene chloride  with low blank *
values may be used. In no case shall a blank value of greater than 1.6E-06  of the weight of methylene
chloride used be subtracted from the sample weight.

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       NOTE: A least one vendor quotes <1 mg/1 for Environmental Analysis Solvents-grade
methylene chloride.
       7.3  Sample analysis. The following reagents are required for sample analysis:
       7.3.1 Acetone. Same as in section 7.2.1 of this method.
       7.3.2 Desiccant.  Anhydrous calcium sulfate, indicating type. Alternatively, other types of
desiccants may be used, subject to the approval of the Administrator.
       7.3.3 Methylene chloride.  Same as in section 7.2.2 of this method.
8.0 Sample Collection. Preservation. Storage, and Transport.
       NOTE: The complexity of this method is such that, in order to obtain reliable results, testers
should be trained and experienced with the test procedures.
       8.1 Pretest preparation. It is suggested that sampling equipment be maintained according to the
procedures described in APTD-0576.
       8.1.1 Weigh several 200 g to 300 g portions of silica gel in airtight containers to the nearest 0.5
g. Record on each container the total weight of the silica gel plus container. As an alternative, the silica
gel need not be preweighed but may be weighed directly in its impinger or sampling holder just prior to
train assembly.
       8.1.2 A batch of glass fiber filters, no more than 50 at a time, should placed in a soxhlet
extraction apparatus  and extracted using methylene chloride for at least 16 hours. After extraction, check
filters visually against light for irregularities, flaws,  or pinhole leaks. Label the shipping containers
(glass or plastic petri dishes), and keep the filters in  these containers at all times except during sampling
and weighing.
       8.1.3 Desiccate the filters at 20 ± 5.6°C (68 ± 10°F) and ambient pressure for at least 24 hours
and weigh at intervals of at least 6 hours to a constant weight, i.e., <0.5 mg change from previous
weighing; record  results to the nearest 0.1 mg. During each weighing the filter must not be exposed to
the laboratory atmosphere for longer than 2 minutes and a relative humidity above 50 percent.
Alternatively (unless otherwise specified by the Administrator), the filters may be oven-dried at 104°C
(220°F) for 2 to 3 hours, desiccated for 2 hours, and weighed. Procedures other than those described,
which account for relative humidity effects, may be  used, subject to the approval of the Administrator.
       8.2  Preliminary determinations.
       8.2.1 Select the sampling site and the minimum number of sampling points according to Method
1,40 CFR part 60, appendix A or as specified by the Administrator. Determine the stack pressure,
temperature, and the range of velocity heads using Method 2,40 CFR part 60, appendix A; it is
recommended that a  leak check of the pitot lines (see section 8.1 of Method 2,40 CFR part 60, appendix
A) be performed. Determine the moisture content using Approximation Method 4 (section 1.2 of
Method 4, 40 CFR part 60, appendix A) or its alternatives to  make isokinetic sampling rate settings.
Determine the stack gas dry molecular weight, as described in section 8.6 of Method 2,40 CFR part 60,
appendix A; if integrated  Method 3  sampling is used for molecular weight determination, the integrated
bag sample shall be taken simultaneously with, and for the same total length of time as, the particulate
sample run.
       8.2.2 Select  a nozzle size based on the range of velocity heads such that it is not necessary to
change the nozzle size in order to maintain isokinetic sampling rates. During the run, do not change the
nozzle size. Ensure that the proper differential pressure gauge is chosen for the range of velocity heads
encountered (see section 8.2 of Method 2, 40 CFR part 60, appendix A).
       8.2.3 Select  a suitable probe liner and probe length such that all traverse points can  be sampled.
For large stacks, consider sampling from opposite sides of the stack to reduce the required probe length.
       8.2.4 Select  a total sampling time greater than or equal to the minimum total sampling time
specified in the test procedures for the-specific industry such that:  (1) The sampling time per point is not
less than 2 minutes (or some greater time interval  as specified by the Administrator); and (2) the sample
volume taken (corrected to standard conditions) will exceed the required minimum  total gas sample
volume. The latter is based on an approximate average sampling rate.
       8.2.5 The sampling time at each point shall  be the same. It is recommended that the number of

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minutes sampled at each point be an integer or an integer plus one-half minute, in order to eliminate
timekeeping errors.
       8.2.6 In some circumstances (e.g., batch cycles), it may be necessary to sample for shorter times
at the traverse points and to obtain smaller gas sample volumes. In these cases, the Administrator's
approval must first be obtained.
       8.3 Preparation of sampling train.
       8.3.1 During preparation and assembly of the sampling train, keep all openings where
contamination can occur covered until just prior to assembly or until sampling is about to begin. Place
100 ml of water in each of the first two impingers, leave the third impinger empty, and transfer
approximately 200 to 300 g of preweighed silica gel from its container to the fourth impinger. More
silica gel may be used, but care should be taken to ensure that it is not entrained and carried out from the
impinger during sampling. Place the container in a clean place for later use in the sample recovery.
Alternatively, the weight of the silica gel plus impinger may be determined to the nearest 0.5 g and
recorded.
       8.3.2 Using a tweezer or clean disposable surgical gloves, place a labeled (identified) and
weighed filter in the filter holder. Be sure that the filter is properly centered and the gasket properly
placed so as to prevent the sample gas stream from circumventing the filter. Check the filter for tears
after assembly is completed.
       8.3.3 When glass liners are used, install the selected nozzle using a Viton A 0-ring when  stack
temperatures are less than 260°C (500°F) and an asbestos string gasket when temperatures are higher.
See APTD-0576 for details. Mark the probe with heat-resistant tape or by some other method to denote
the proper distance into the stack or duct for each sampling point.
       8.3.4 Set up the train as in Figure 5-1 of Method 5,40 CFR part 60, appendix A, using (if
necessary) a very light coat of silicone grease on all ground glass joints, greasing only the outer portion
(see APTD-0576) to avoid possibility of contamination by the silicone grease. Subject to the approval of
the Administrator, a glass cyclone may be used between the probe and filter holder when the total
particulate catch is expected to exceed 100 mg or when water droplets are present in the stack gas.
       8.3.5 Place crushed ice around the impingers.
       8.4 Leak-check procedures.
       8.4.1  Leak check of metering system shown in
Figure 5-1 of Method 5,40 CFR part 60, appendix A.  That portion of the sampling train from the  pump
to the orifice meter should be leak-checked prior to initial use and after each shipment. Leakage after the
pump will result in less volume being recorded than is actually sampled.  The following procedure is
suggested (see Figure 5-2 of Method 5, 40 CFR part 60, appendix A): Close the main valve on the meter
box. Insert a one-hole rubber stopper with rubber tubing attached into the orifice exhaust pipe.
Disconnect and  vent the low side of the orifice manometer.  Close off the low side orifice tap. Pressurize
the system to 13 to 18 cm (5 to 7 in.) water column by blowing into the rubber tubing. Pinch off the
tubing, and observe the manometer for 1 minute.  A loss of pressure on the manometer indicates a leak in
the meter box; leaks, if present, must be  corrected.
       8.4.2 Pretest leak check.  A pretest leak-check is recommended but not required. If the pretest
leak-check is conducted, the following procedure should be used.
       8.4.2.1  After the sampling train  has been assembled, turn on and set the filter and probe heating
systems to the desired operating temperatures. Allow time for the temperatures to stabilize.  If a Viton A
0-ring or other leak-free connection is used in assembling the  probe nozzle to the probe liner, leak-check
the train at the sampling site by plugging the nozzle and pulling a 380 mm (15 in.) Hg vacuum.
       NOTE:  A lower vacuum may be used, provided that it is not exceeded during the test.
       8.4.2.2  If an asbestos string is used, do not connect the probe to the train during the leak check.
Instead, leak-check the train by first plugging the inlet to the filter holder (cyclone, if applicable) and
pulling a 380 mm (15 in.) Hg vacuum. (See NOTE in section 8.4.2.1 of this method).  Then connect th*e
probe to the train and perform the leak check at approximately 25 mm (1  in.) Hg vacuum; alternatively,
the probe may be leak-checked with the rest of the sampling train, in one step, at 380 mm (15  in.) Hg

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vacuum. Leakage rates in excess of 4 percent of the average sampling rate or 0.00057 mVmin (0.02
cfm), whichever is less, are unacceptable.
        8.4.2.3  The following leak check instructions for the sampling train described in APTD-0576
and APTD-058I may be helpful. Start the pump with the bypass valve fully open and the coarse adjust
valve completely closed.  Partially open the coarse adjust valve and slowly close the bypass valve until
the desired vacuum is reached. Do not reverse the direction of the bypass valve, as this will cause water
to back up into the filter holder.  If the desired vacuum is exceeded, either leak-check at this higher
vacuum or end the leak check as shown below and start over.
        8.4.2.4  When the leak check is completed, first slowly remove the plug from the inlet to the
probe, filter holder, or cyclone (if applicable) and immediately turn off the vacuum pump.  This prevents
the water in the impingers from being forced backward into the filter holder and the silica gel from being
entrained backward into the third impinger.
        8.4.3 Leak checks during sample run.  If, during the sampling run, a component (e.g., filter
assembly or impinger) change becomes necessary, a leak check shall be conducted immediately before
the change is made. The leak check shall be done according to the procedure outlined in section 8.4.2 of
this method, except that it shall be done at a vacuum equal to or greater than the maximum value
recorded up to that point in the test. If the leakage rate is found to be no greater than 0.00057 mVmin
(0.02 cfm) or 4  percent of the average sampling rate (whichever is less), the results are acceptable, and
no correction will need to be  applied to the total volume of dry gas metered; if, however, a higher
leakage rate is obtained, either record  the leakage rate and plan to correct the sample volume as shown in
section 12.3 of this method or void the sample run.
       NOTE: Immediately after component changes, leak checks are optional; if such leak checks are
done, the procedure outlined  in section 8.4.2 of this method should be used.
        8.4.4 Post-test leak check.  A leak check is mandatory at the conclusion of each sampling run.
The leak check  shall be performed in accordance with the procedures outlined in section 8.4.2 of this
method, except that it shall be conducted at a vacuum equal to or greater than the maximum value
reached during the sampling  run. If the leakage rate is found to be no greater than 0.00057 mVmin
(0.02 cfm) or 4  percent of the average sampling rate (whichever is less), the results are acceptable, and
no correction need be applied to the total volume of dry gas metered. If, however, a higher leakage rate
is obtained, either record the  leakage rate and correct the  sample volume, as shown in section 12.4 of this
method, or void the sampling run.
        8.5 Sampling train operation. During the sampling run, maintain an isokinetic sampling rate
(within 10 percent of true isokinetic unless otherwise specified by the Administrator) and a temperature
around the filter of 120 ± 14°C (248 ± 25°F), or such other temperature as specified by an applicable
subpart of the standards or approved by the Administrator.
       8.5.1  For each run, record the data required on a data sheet such as the one shown  in Figure 5-2
of Method 5, 40 CFR part 60, appendix A. Be sure to record the initial reading. Record the DGM
readings at the beginning and end of each sampling time increment, when changes in flow rates are
made, before and after each leak-check, and when sampling is halted. Take other readings indicated by
Figure 5-2 of Method 5, 40 CFR part 60, appendix A at least once at each sample point during each time
increment and additional readings when significant changes (20 percent variation in velocity head
readings) necessitate additional adjustments in flow rate.  Level and zero the manometer. Because the
manometer level and zero may drift due to vibrations and temperature changes, make periodic checks
during the traverse.
       8.5.2 Clean the portholes prior to the test run to minimize the chance of sampling deposited
material. To begin sampling, remove  the nozzle cap and verify that the filter and probe heating systems
are up to temperature and that the pitot tube and probe are properly positioned.  Position the nozzle at the
first traverse point with the tip pointing directly into the gas stream. Immediately start the  pump and
adjust the flow to isokinetic conditions. Nomographs are available, which aid in the rapid adjustment of
the isokinetic sampling rate without excessive computations.  These nomographs are designed for use
when the Type S pitot tube coefficient (Cp) is 0.85 ± 0.02 and the stack gas equivalent density (dry

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molecular weight) is 29 ± 4.  APTD-0576 details the procedure for using the nomographs.  If Cp and Md
are outside the above-stated ranges, do not use the nomographs unless appropriate steps (see Reference 7
in section 17.0 of this method) are taken to compensate for the deviations.
        8.5.3 When the stack is under significant negative pressure (height of impinger stem), close the
coarse adjust valve before inserting the probe into the stack to prevent water from backing into the filter
holder. If necessary, the pump may be turned on with the coarse adjust valve closed.
        8.5.4 When the probe is in position, block off the openings around the probe and porthole to
prevent unrepresentative dilution of the gas stream.
        8.5.5 Traverse the stack cross-section, as required by Method 1,40 CFR part 60, appendix A or
as specified by the Administrator, being careful not to bump the probe nozzle into the stack walls when
sampling near the walls or when removing or inserting the probe through the portholes; this minimizes
the chance of extracting deposited material.
        8.5.6 During the test run, make periodic adjustments to keep the temperature around the filter
holder at the proper level; add more ice and, if necessary, salt to maintain a temperature of less than 20°C
(68°F) at the condenser/silica gel outlet. Also, periodically check the level and zero of the manometer.
        8.5.7 If the pressure drop across the filter becomes too high, making isokinetic sampling
difficult to maintain, the filter may be replaced in the midst of the sample run.  It is recommended that
another complete filter assembly be used rather than attempting to change the filter itself. Before a new
filter assembly is installed, conduct a leak check (see section 8.4.3 of this method).  The total PM weight
shall include the summation of the filter assembly catches.
        8.5.8 A single train shall be used for the entire sample run, except in cases where simultaneous
sampling is required in two or more separate ducts or at two or more different locations within the same
duct, or in cases where equipment failure necessitates a change of trains. In all other situations, the use
of two or more trains will be subject to the approval of the Administrator.
        NOTE: When two or more trains are used, separate analyses of the front-half and (if applicable)
impinger catches from each train shall be performed, unless identical nozzle sizes were used in all trains,
in which case the front-half catches from the individual trains may be combined (as may the impinger
catches) and one analysis of the  front-half catch and one analysis of the impinger catch may be
performed.
        8.5.9 At the end of the sample run, turn off the coarse adjust valve, remove the probe  and nozzle
from the stack, turn off the pump, record the final DGM reading, and then conduct a post-test leak check,
as outlined in section 8.4.4 of this method. Also leak-check the pitot lines as described in section 8.1 of
Method 2,40 CFR part 60, appendix A. The lines must pass this leak check in order to validate the
velocity head data.
        8.6  Calculation of percent isokinetic. Calculate percent isokinetic (see Calculations, section
12.12 of this method) to determine whether a run was valid or another test run should be made. If there
was difficulty in maintaining isokinetic rates because of source conditions, consult the Administrator for
possible variance on the isokinetic rates.
        8.7  Sample recovery.
        8.7.1 Proper cleanup procedure begins as soon as the probe is removed from the stack at the end
of the sampling period. Allow the probe to cool.
        8.7.2 When the probe can be safely handled, wipe off all external PM near the tip of the probe
nozzle and place a cap over it to  prevent losing or gaining PM.  Do not cap off the probe tip tightly while
the sampling train is cooling down.  This would create a vacuum in the filter holder, thus drawing water
from the impingers into the filter holder.
        8.7.3 Before moving the sample train to the cleanup site, remove the probe from the sample
train, wipe off the silicone grease, and cap the open outlet of the probe.  Be careful not to lose  any
condensate that might be present. Wipe off the silicone grease from the filter inlet where the probe was
fastened and cap it.  Remove the umbilical cord from the last impinger and cap the impinger.  If a
flexible line is used between the  first impinger or condenser and the filter holder, disconnect the line at
the filter holder and let any condensed water or liquid drain into the impingers or condenser. After

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wiping off the silicone grease, cap off the filter holder outlet and impinger inlet.  Ground-glass stoppers,
plastic caps, or serum caps may be used to close these openings.
        8.7.4 Transfer the probe and filter-impinger assembly to the cleanup area.  This area should be
clean and protected from the wind so that the chances of contaminating or losing the sample will be
minimized.
        8.7.5 Save a portion of the acetone and methylene chloride used for cleanup as blanks.  Take
200 ml of each solvent directly from the wash bottle being used and place it in glass sample containers
labeled "acetone blank" and "methylene chloride blank," respectively.
        8.7.6 Inspect the train prior to and during disassembly and note any abnormal conditions.  Treat
the samples as follows:
        8.7.6.1  Container No. 1. Carefully remove the filter from the filter holder, and place it in its
identified petri  dish container. Use a pair of tweezers and/or clean disposable surgical gloves to handle
the filter. If it is necessary to fold the filter, do so such that the PM cake is inside the fold. Using a dry
nylon bristle brush and/or a sharp-edged blade, carefully transfer to the petri dish any PM and/or filter
fibers that adhere to the filter holder gasket.  Seal the container.
        8.7.6.2 Container No. 2.  Taking care to  see that dust on the outside of the probe or other
exterior surfaces does not get into the sample, quantitatively recover PM or any condensate from the
probe nozzle, probe fitting, probe liner, and front half of the filter holder by washing these components
with acetone and placing the wash in a glass container. Perform the acetone rinse as follows:
        8.7.6.2.1  Carefully remove the probe nozzle and clean the inside surface by rinsing with acetone
from  a wash bottle and brushing with a nylon bristle brush. Brush until the acetone rinse shows no
visible particles, after which make a final rinse of the inside surface with acetone.
        8.7.6.2.2  Brush and rinse the inside parts of the Swagelok fitting with acetone in a similar way
until no visible particles remain.
        8.7.6.2.3  Rinse the probe liner with acetone by tilting and rotating the probe while squirting
acetone into its upper end so that all inside surfaces are wetted with  acetone. Let the acetone drain from
the lower end into the sample container. A funnel (glass or polyethylene) may be used to  aid in
transferring liquid washes to the container.  Follow the acetone rinse with a probe brush. Hold the probe
in an  inclined position, squirt acetone into the upper end as the probe brush is being pushed with a
twisting action  through the probe, hold  a sample container under the lower end of the probe, and catch
any acetone and PM that is brushed from the probe. Run the brush through the probe three times or more
until no visible PM is carried out with the acetone or until none remains in the probe liner on  visual
inspection. With stainless steel or other metal probes, run the brush through in the above-described
manner at least six times, since metal probes have small crevices in which PM can be entrapped. Rinse
the brush with acetone and quantitatively collect  these washings in the sample container.  After the
brushing, make a final acetone rinse of the probe as described above.
        8.7.6.2.4  It is recommended that two people clean the probe to minimize sample losses.
Between sampling runs, keep brushes clean and protected from contamination.
        8.7.6.2.5  After ensuring that all joints have been wiped clean of silicone grease, clean the inside
of the front half of the filter holder by rubbing the surfaces with a nylon bristle brush and rinsing with
acetone. Rinse each surface three times or more  if needed to remove visible particulate. Make a final
rinse  of the brush and filter holder. Carefully rinse out the glass cyclone also (if applicable).
        8.7.6.2.6  After rinsing the nozzle, probe, and front half of the filter holder with acetone, repeat
the entire procedure with methylene chloride and save in a separate No. 2M container.
        8.7.6.2.7  After acetone and methylene chloride washings and PM have been collected in the
proper sample containers, tighten  the lid on the sample containers so that acetone and methylene chloride
will not leak out when it is shipped to the laboratory.  Mark the height of the fluid level to determine
whether leakage occurs during transport.  Label each container to identify clearly its contents.
        8.7.6.3  Container No. 3.  Note the color of the indicating silica gel to determine whether it has
been completely spent, and make  a notation of its condition. Transfer the silica gel from the  fourth
impinger to its original container and seal the container. A funnel may make it easier to pour the silica

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gel without spilling. A rubber policeman may be used as an aid in removing the silica gel from the
impinger. It is not necessary to remove the small amount of dust particles that may adhere to the
impinger wall and are difficult to remove. Since the gain in weight is to be used for moisture
calculations, do not use any water or other liquids to transfer the silica gel.  If a balance is available in
the field, follow the procedure for Container No. 3 in section 1 1 .2.3 of this method.
        8.7.6.4 Impinger water. Treat the impingers as follows:
        8.7.6.4.1  Make a notation of any color or film in the liquid catch. Measure the liquid that is in
the first three impingers to within 1 ml by using a graduated cylinder or by weighing it to within 0.5 g by
using a balance (if one is available). Record the volume or weight of liquid present. This information is
required to calculate the moisture content of the effluent gas.
        8.7.6.4.2  Following the determination of the volume of liquid present, rinse the back half of the
train with water, add it to the impinger catch, and store it in a container labeled 3W (water).
        8.7.6.4.3  Following the water rinse, rinse the back half of the train with acetone to remove the
excess water to enhance subsequent organic recovery with methylene chloride and quantitatively recover
to a container labeled 3 S (solvent) followed by at least three sequential rinsings with aliquots of
methylene chloride.  Quantitatively recover to the same container labeled 3S. Record separately the
amount of both acetone and methylene chloride used  to the nearest 1  ml or 0.5g.
        NOTE: Because the subsequent analytical finish is gravimetric, it is okay to recover both
solvents to the same container. This would not be recommended if other analytical finishes were
required.
        8.8  Sample transport. Whenever possible, containers should be shipped in such a way that they
remain upright at all times.
9.0  Quality Control.
        9.1  Miscellaneous quality control measures.

  Section    Quality Control Measure         Effect

8.4,         Sampling and equipment         Ensure accurate
10.1-10.6    leak check and calibration        measurement of
                                            stack gas flow  rate,
_ sample volume             __
        9.2  Volume metering system checks. The following quality control procedures are suggested to
check the volume metering system calibration values  at the field test site prior to sample collection.
These procedures are optional.
        9.2. 1 Meter orifice check. Using the calibration data obtained during the calibration procedure
described in section 10.3 of this method, determine the AH@ for the metering system orifice.  The AH@ is
the orifice pressure differential in units of in. H20 that correlates to 0.75 cfm of air at 528°R and 29.92 in.
Hg.  The AH@ is calculated as follows:
                                 = 0.0319 AH
                             @                       P     v2  v2
                                                      rbar  T    vm
where
0.0319 = (0.0567 in. Hg/°R)(0.75 cfm)2;
AH       =   Average pressure differential across the orifice meter, in. H20;
Tm        =.   Absolute average DGM temperature, °R;
0         =   Total sampling time, min;
Pb«       =   Barometric pressure, in. Hg;

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Y         =    DGM calibration factor, dimensionless;
Vm        =    Volume of gas sample as measured by DGM, dcf.
        9.2.1.1 Before beginning the field test (a set of three runs usually constitutes a field test),
operate the metering system (i.e., pump, volume meter, and orifice) at the AH@ pressure differential for
10 minutes. Record the volume collected, the DGM temperature, and the barometric pressure. Calculate
a DGM calibration check value, Yc, as follows:
                                Ye"
                                         10
0.0319  T
                                                            m
                                                     bar
where
Yc      = DGM calibration check value, dimensionless;
10      = Run time, m in.
        9.2.1.2 Compare the Yc value with the dry gas meter calibration factor Y to determine that: 0.97
Y < Yc < 1.03Y. If the Yc value is not within this range, the volume metering system should be
investigated before beginning the test.
        9.2.2 Calibrated critical orifice. A calibrated critical orifice, calibrated against a wet test meter
or spirometer and designed to be inserted at the inlet of the sampling meter box, may be used as a quality
control check by following the procedure of section 16.2 of this method.
10.0 Calibration and Standardization.
        NOTE: Maintain a laboratory log of all calibrations.
        10.1 Probe nozzle.  Probe nozzles shall be calibrated before their initial use in the field. Using a
micrometer, measure the ID of the nozzle to the nearest 0.025 mm (0.001 in.). Make three separate
measurements using different diameters each time, and obtain the average  of the measurements.  The
difference between the high and low numbers shall not exceed 0.1  mm (0.004 in.). When nozzles
become nicked, dented, or corroded, they shall be reshaped, sharpened, and recalibrated before use.
Each nozzle shall be permanently and uniquely identified.
        10.2 Pitot tube assembly. The Type  S pitot tube assembly shall be calibrated according to the
procedure outlined in section 10.1 of Method  2, 40 CFR part 60, appendix  A.
        10.3 Metering system.
        10.3.1  Calibration prior to use.  Before its initial use in the field, the metering system shall be
calibrated as follows:  Connect the metering system inlet to the outlet of a wet test meter that is accurate
to within 1 percent. Refer to Figure 5-5  of Method 5, 40 CFR part 60, appendix A. The wet test meter
should have a capacity of 30 liters/revolution  (1 ffYrev).  A spirometer of 400 liters (14 ft3) or more
capacity, or equivalent, may be used for this calibration, although a wet test meter is usually more
practical. The wet test meter should be periodically calibrated with a spirometer or a liquid displacement
meter to ensure the accuracy of the wet test meter.  Spirometers or wet test meters of other sizes may be
used, provided that the specified accuracies of the procedure are maintained.  Run the metering system
pump for about 15 minutes with the orifice manometer indicating a median reading, as  expected in field
use, to allow the pump to warm up and to permit the interior surface of the wet test meter to be
thoroughly  wetted. Then, at each of a minimum of three orifice manometer settings, pass an exact
quantity of gas through the wet test meter and note the gas volume indicated by the DGM. Also note the
barometric  pressure and the temperatures of the wet test meter,  the inlet of the DGM, and the outlet of
the  DGM.  Select the highest and lowest orifice settings to bracket the expected field operating range of
the  orifice.  Use a minimum volume of 0.15 m3 (5 cf) at all orifice settings.  Record all the data on a form
similar to Figure 5-6 of Method 5,40 CFR part 60,  appendix A, and calculate Y (the DGM calibration
factor) and  AH@ (the orifice calibration factor) at each orifice setting, as shown on Figure 5-6 of Method
5, 40 CFR part 60, appendix A. Allowable tolerances for individual Y and AH@ values are given in

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Figure 5-6 of Method 5,40 CFR part 60, appendix A.  Use the average of the Y values in the calculations
in section 12 of this method.
        10.3.1.1. Before calibrating the metering system, it is suggested that a leak check be conducted.
For metering systems having diaphragm pumps, the normal leak check procedure will not detect
leakages within the pump. For these cases the following leak check procedure is suggested:  make a 10-
minute calibration run at 0.00057 mVmin (0.02 cfm); at the end of the run, take the difference of the
measured wet test meter and DGM volumes; divide the difference by 10 to get the leak rate. The leak
rate should not exceed 0.00057 mVmin (0.02 cfm).
        10.3.2 Calibration after use. After each field use, the calibration of the metering system shall be
checked by performing three calibration runs at a single, intermediate orifice setting (based on the
previous field test) with the vacuum set at the maximum value reached during the test series. To adjust
the vacuum, insert a valve between the wet test meter and the inlet of the metering system. Calculate the
average value of the DGM calibration factor.  If the value has changed by more than 5 percent,
recalibrate the meter over the full range of orifice settings, as previously detailed.
        NOTE: Alternative procedures, e.g., rechecking the orifice meter coefficient, may be used,
subject to the approval of the Administrator.
        10.3.3  Acceptable variation in calibration. If the DGM coefficient values obtained before and
after a test series differ by more than 5 percent, either the test series shall be voided or calculations for
the test series shall be performed using whichever meter coefficient value (i.e., before or after) gives the
lower value of total sample volume.
        10.4 Probe heater calibration.  Use a heat source to generate air heated to selected temperatures
that approximate those expected to occur in the sources to be sampled.  Pass this air through the probe at
a typical sample flow rate while measuring the probe inlet and outlet temperatures at various probe
heater settings. For each air temperature generated, construct a graph of probe heating system setting
versus probe outlet temperature. The procedure outlined in APTD-0576 can also be  used. Probes
constructed according to APTD-0581 need not be calibrated if the calibration curves  in APTD-0576 are
used. Also, probes with outlet temperature monitoring capabilities do not require calibration.
        NOTE: The probe heating system shall be calibrated before its initial use in the field.
        10.5 Temperature sensors.  Use the procedure in section 10.3 of Method 2, 40 CFR part 60,
appendix A to calibrate in-stack temperature sensors. Dial thermometers, such as are used for the DGM
and condenser outlet, shall be calibrated against mercury-in-glass thermometers.
        10.6 Barometer.  Calibrate  against a mercury barometer.
11.0 Analytical Procedure.
        11.1 Record the data required on a sheet such  as the one shown in Figure 315-1 of this method.
        11.2 Handle each sample container as follows:
        11.2.1  Container No. 1.
        11.2.1.1  PM analysis. Leave the contents in the shipping container or transfer the filter and any
loose PM from the sample container to a tared glass weighing dish.  Desiccate for 24 hours in a
desiccator containing anhydrous calcium sulfate.  Weigh to a constant weight and report the results to the
nearest 0.1 mg. For purposes of this section, the term "constant weight" means a difference of no more
than 0.5 mg or 1 percent of total weight less tare weight, whichever is greater, between two consecutive
weighings, with no less than 6 hours of desiccation time between weighings (overnight desiccation is a
common practice).  If a third weighing is required and  it agrees within ±0.5 mg, then the results of the
second weighing should be used.  For quality assurance purposes, record and report each individual
weighing; if more than three weighings are required, note this in the results for the subsequent MCEM
results.
        11.2.1.2 MCEM analysis. Transfer the filter and contents quantitatively into a beaker. Add 100
ml of methylene chloride and cover with aluminum foil.  Sonicate for 3 minutes then allow to stand for
20 minutes. Set up the filtration apparatus. Decant the solution into a clean Buchner fritted funnel.   *
Immediately pressure filter the solution through the tube into another clean, dry beaker. Continue
decanting and pressure filtration until all the solvent is transferred. Rinse the beaker and filter with 10 to

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20 ml methylene chloride, decant into the Buchner fritted funnel and pressure filter. Place the beaker on
a low-temperature hot plate (maximum 40°C) and slowly evaporate almost to dryness. Transfer the
remaining last few milliliters of solution quantitatively from the beaker (using at least three aliquots of
methylene chloride rinse) to a tared clean dry aluminum dish and evaporate to complete dryness.
Remove from heat once solvent is evaporated. Reweigh the dish  after a 30-minute equilibrium in the
balance room and determine the weight to the nearest 0.1 mg. Conduct a methylene chloride blank run
in an identical fashion.
        11.2.2 Container No. 2.
        11.2.2.1  PM analysis. Note the  level of liquid in the container, and confirm on the analysis
sheet whether leakage occurred during transport. If a noticeable amount of leakage has occurred, either
void the sample or use methods, subject to the approval of the Administrator, to correct the final results.
Measure the liquid in this container either volumetrically to ±1 ml or gravimetrically to ±0.5 g.  Transfer
the contents to a tared 250 ml beaker and evaporate to dryness at  ambient temperature and pressure.
Desiccate for 24 hours, and weigh to a constant weight.  Report the results to the nearest 0.1 mg.
        11.2.2.2 MCEM analysis. Add 25 ml methylene chloride to the beaker and cover with
aluminum foil. Sonicate for 3 minutes then allow to stand for 20  minutes; combine with contents of
Container No. 2M and pressure filter and evaporate as described for Container 1  in section 11.2.1.2 of
this method.
        NOTES FOR MCEM ANALYSIS:
        1. Light finger pressure only is necessary on 24/40  adaptor.  A Chemplast adapter #15055-240
has been found satisfactory.
        2. Avoid aluminum dishes made with fluted  sides, as these may promote solvent "creep,"
resulting in possible sample loss.
        3. If multiple samples are being run, rinse the Buchner fritted funnel twice between samples
with 5 ml solvent using pressure filtration. After the  second rinse, continue the flow of air until the glass
frit is completely dry. Clean the Buchner fritted funnels thoroughly after filtering five or six samples.
        11.2.3 Container No. 3.  Weigh  the spent silica gel  (or silica gel plus impinger) to the nearest 0.5
g using a balance.  This step may be conducted in the field.
        11.2.4 Container 3W (impinger  water).
        11.2.4.1  MCEM analysis. Transfer the solution into a 1,000 ml separatory funnel quantitatively
with methylene chloride washes.  Add enough solvent to total approximately 50 ml, if necessary. Shake
the funnel for 1 minute, allow the phases to separate,  and drain the solvent layer into a 250 ml beaker.
Repeat the extraction twice. Evaporate with low heat (less than 40°C) until near dryness. Transfer the
remaining few milliliters of solvent quantitatively with small solvent washes into a clean, dry, tared
aluminum dish and evaporate to dryness.  Remove  from heat once solvent is evaporated.  Reweigh the
dish after a 30-minute equilibration in the balance room and determine the weight to the nearest 0.1 mg.
        11.2.5 Container 3S (solvent).
        11.2.5.1  MCEM analysis. Transfer the mixed solvent to  250 ml beaker(s). Evaporate and weigh
following the procedures detailed for container 3W in section 11.2.4 of this method.
        11.2.6 Blank containers.  Measure the distilled water, acetone, or methylene chloride in each
container either volumetrically or gravimetrically.  Transfer the "solvent" to a tared 250 ml beaker, and
evaporate to dryness at ambient temperature and pressure. (Conduct a solvent blank on the distilled
deionized water blank in an identical fashion  to that described in section 11.2.4.1 of this method.)
Desiccate for 24 hours, and weigh to a constant weight. Report the results to the nearest 0.1 mg.
        NOTE: The contents of Containers No. 2,3W, and  3M as well as the blank containers may be
evaporated at temperatures higher than ambient.  If evaporation is done at an elevated temperature, the
temperature must be below the boiling point of the solvent; also, to prevent "bumping," the evaporation
process must be closely supervised, and the contents of the beaker must be swirled occasionally to
maintain an even temperature.  Use extreme care, as acetone and methylene chloride are highly
flammable and have a low flash point.

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12.0 Data Analysis and Calculations.
        12.1 Carry out calculations, retaining at least one extra decimal figure beyond that of the
acquired data.  Round off figures after the final calculation. Other forms of the equations may be used as
long as they give equivalent results.
        12.2 Nomenclature.
A,,      =       Cross-sectional area of nozzle, m3 (ft3).
Bws     =       Water vapor in the gas stream, proportion by volume.
C.      =       Acetone blank residue concentration, mg/g.
Cs      =       Concentration of particulate matter in stack gas, dry basis, corrected to standard
               conditions, g/dscm (g/dscf).
I       =       Percent of isokinetic sampling.
L,      =       Maximum acceptable leakage rate for either a pretest leak check or for a leak check
               following a component change; equal to 0.00057 mVmin (0.02 cfm) or 4 percent of the
               average sampling rate, whichever is less.
L,      =       Individual leakage rate observed during the leak check conducted prior to the "i"1"
               component change (I = 1,2,3...n), mVmin (cfm).
Lp      =       Leakage rate observed during the post-test leak check, mVmin (cfm).
ma      =       Mass of residue of acetone after evaporation, mg.
mn      =       Total amount of particulate matter collected, mg.
Mw     =       Molecular weight of water, 18.0 g/g-mole (18.0 Ib/lb-mole).
Pbar     =       Barometric pressure at the sampling site, mm Hg (in  Hg).
Ps      =       Absolute stack gas pressure, mm Hg (in. Hg).
Psld     =       Standard absolute pressure, 760 mm Hg (29.92 in. Hg).
R      =       Ideal gas constant, 0.06236 [(mm Hg)(m3)]/[(°K)
               (g-mole)] {21.85 [(in. Hg)(ft3)]/[(°R)(lb-mole)]}.
Tm      =       Absolute average dry gas meter (DGM) temperature (see Figure 5-2 of Method 5,40
               CFR part 60, appendix A), °K (°R).
Ts      =       Absolute average stack gas temperature (see Figure 5-2 of Method 5, 40 CFR part 60,
               appendix A), °K(°R).
Tstd     =       Standard absolute temperature, 293 °K (528°R).
V.      =       Volume of acetone blank, ml.
Vaw     =       Volume of acetone used in wash, ml.
V,      =       Volume of methylene chloride blank, ml.
Vw     =       Volume of methylene chloride used in wash, ml.
Vlc      =       Total volume liquid collected in impingers and silica gel (see Figure 5-3 of Method 5,
               40 CFR part 60, appendix A), ml.
Vm      =       Volume of gas sample as measured by dry gas meter, dcm(dcf).
        =       Volume of gas sample measured by the dry gas meter, corrected to standard conditions,
               dscm (dscf).
        =       Volume of water vapor in the gas sample, corrected to standard conditions, scm (scf).
Vs      =       Stack gas velocity, calculated by Equation 2-9 in Method 2,40 CFR part 60, appendix
               A, using data obtained from Method 5,40 CFR part 60, appendix A, m/sec (ft/sec).
Wa      =       Weight of residue in acetone  wash, mg.
Y      =       Dry gas meter calibration factor.
AH    =       Average pressure differential across the orifice meter (see Figure 5-2 of Method 5,40
               CFR part 60, appendix A), mm H20 (in H20).
P,      =       Density of acetone, 785.1 mg/ml (or see label on bottle).
pw      =       Density of water, 0.9982 g/ml (0.002201 Ib/ml).
Pi     =       Density of methylene chloride, 1316.8 mg/ml (or see label on  bottle).
0      =       Total sampling time, min.
®i      =       Sampling time interval, from the beginning of a run until the first component change,

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               mm.
©i        =    Sampling time interval, between two successive component changes, beginning with the
               interval between the first and second changes, min.
0p        =    Sampling time interval, from the final (n*) component change until the end of the
               sampling run, min.
13.6       =    Specific gravity of mercury.
60        =    Sec/min.
100       =    Conversion to percent.
       12.3 Average dry gas meter temperature and average orifice pressure drop. See data sheet
(Figure 5-2 of Method 5, 40 CFR part 60, appendix A).
       12.4 Dry gas volume.  Correct the sample volume measured by the dry gas meter to standard
conditions (20°C, 760 mm Hg or 68°F, 29.92 in Hg) by using Equation 315-1.

                           T   (p
                           1 std  rbar
                V  - V Y     v       13'6^                                   Ea. 315-1
                                T PM
                                  m  sto
                               =V  = K,VmY
where
K,   =  0.3858 °K/mm Hg for metric units,
     = 17.64 °R/in Hg for English units.
     NOTE: Equation 315-1 can be used as written unless the leakage rate observed during any of the
mandatory leak checks (i.e., the post-test leak check or leak checks conducted prior to component
changes) exceeds L,. If Lp or Li exceeds La, Equation 315-1 must be modified as follows:
     (a) Case I.  No component changes made during sampling run. In this case, replace V,,, in Equation
315-1 with the expression:
                                      [Vm-(Lp-LJ0]
     (b) Case II. One or more component changes made during the sampling run. In this case, replace
Vm in Equation
315-1 by the expression:
          [V,,  -  (L,  -  L.)  6,  -       (L,. - /..) 0,. -  (Lf -  /.,) 0p]
                                        /=2
and substitute only for those leakage rates (L; or Lp) which exceed Lt.
      12.5 Volume of water vapor condensed.

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where
K2     =  0.001333 mVml for metric units;
       =  0.04706 ftVml for English units.
       12.6 Moisture content.
                       B-         Vw(std)                                           -   _._ _
                       -  -                                    Eq. 315-3
                   wa     V        +  V
                          vm(std)     vw(std)
       NOTE: In saturated or water droplet-laden gas streams, two calculations of the moisture content
of the stack gas shall be made, one from the impinger analysis (Equation 315-3), and a second from the
assumption of saturated conditions. The lower of the two values of Bws shall be considered correct. The
procedure for determining the moisture content based upon assumption of saturated conditions is given
in section 4.0 of Method 4, 40 CFR part 60, appendix A. For the purposes of this method, the average
stack gas temperature from Figure 5-2 of Method 5, 40 CFR part 60, appendix A may be used to make
this determination, provided that the accuracy of the in-stack temperature sensor is ±1°C (2°F).
       12.7 Acetone blank concentration.

                                 M
                         c  -
                           ,
                                 a   a


        12.8 Acetone wash blank.
                                        W. = C.Vawp.                                Eq.315-5
        12.9 Total particulate weight. Determine the total PM catch from the sum of the weights
obtained from Containers 1 and 2 less the acetone blank associated with these two containers (see Figure
315-1).
       NOTE:  Refer to section 8.5.8 of this method to assist in calculation of results involving two or
more filter assemblies or two or more sampling trains.
        12.10 Particulate concentration.
                                        cs = K3mAra(s«d)                               Eq.315-6
where
K     = 0.001  g/mg for metric units;
       = 0.0154 gr/mg for English units.
        12.11  Conversion factors.
From
ft3
gr
gr/ft3
mg
gr






12.12
Io
m3
mg
mg/m3
g
Ib
Isokinetic variation.
Multiply by
0.02832
64.80004
2288.4
0.001
1.429X10-4


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        12.12.1 Calculation from raw data.
             ioo  r
        / =  —
                                    m  •  i  i  «     .AH
s   "   '"   '    Tm   J  I  •"    13.6;                        Ea. 315-7
                            60 0 vs Ps An
where
K4    =  0.003454 [(mm Hg)(m3)]/[(ml)(°K)] for metric units;
      =  0.002669 [(in HgXft3)]/[(mlX°R)] for English units.
        12.12.2  Calculation from intermediate values.
                       TV       P    100
           / = 	s   ms	2	                              Eg. 315-8
                 7.« ^s  © >A, Ps 60 (1 -Bws)
                                                ' s
where

K5     =   4.320 for metric units;
       =   0.09450 for English units.
       12.12.3 Acceptable results. If 90 percent <• I <; 110 percent, the results are acceptable. If the
PM or MCEM results are low in comparison to the standard, and "I" is over 110 percent or less than 90
percent, the Administrator may opt to accept the results. Reference 4 in the Bibliography may be used to
make acceptability judgments.  If "I" is judged to be unacceptable, reject the results, and repeat the test.
       12.13 Stack gas velocity and volumetric flow rate. Calculate the average stack gas velocity and
volumetric flow rate, if needed, using data obtained in this method and the equations in sections 5.2 and
5.3 of Method 2,40 CFR part 60,  appendix A.
       12.14 MCEM results. Determine the MCEM concentration from the results from Containers 1,
2,2M, 3W, and 3S less the acetone, methylene chloride, and filter blanks value as determined in the
following equation:

                              mmcem  = Zmtoto/  ~  WB  ~ Wt '  ft>
13.0 Method Performance.  [Reserved]
.1.4,0 Pollution Prevention. [Reserved]

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 15.0 Waste Management. [Reserved]
 16.0 Alternative Procedures.
        16.1 Dry gas meter as a calibration standard. A DGM may be used as a calibration standard for
 volume measurements in place of the wet test meter specified in section 16.1 of this method, provided
 that it is calibrated initially and recalibrated periodically as follows:
        16.1.1  Standard dry gas meter calibration.
        16.1.1.1.  The DGM to be calibrated and used as a secondary reference meter should be of high
 quality and have an appropriately sized capacity, e.g., 3 liters/rev (0.1 ftVrev). A spirometer (400 liters
 or more capacity), or equivalent, may be used for this calibration, although a wet test meter is usually
 more practical. The wet test meter should have a capacity of 30 liters/rev (1 ftVrev) and be capable of
 measuring volume to within  1.0 percent; wet test meters should be checked against a spirometer or a
 liquid displacement meter to ensure the accuracy of the wet test meter.  Spirometers or wet test meters of
 other sizes may be used, provided that the specified accuracies of the procedure are maintained.
        16.1.1.2 Set up the components as shown in Figure 5-7 of Method 5, 40 CFR part 60, appendix
 A.  A spirometer, or equivalent, may be used in place of the wet test meter in the system. Run the pump
 for at least 5 minutes at a flow rate of about 10 liters/min (0.35 cfm) to condition the interior surface of
 the wet test  meter. The pressure drop indicated by the manometer at the inlet side of the DGM should be
 minimized (no greater than 100 mm H2O [4 in. H2O] at a flow rate of 30 liters/min [1 cfin]). This can be
 accomplished by using large- diameter tubing connections and straight pipe fittings.
        16.1.1.3 Collect the data as shown in the example data sheet (see Figure 5-8 of Method 5,40
 CFR part 60, appendix A). Make triplicate runs at each of the flow rates and at no less than five different
 flow rates. The range of flow rates should be between 10 and 34 liters/min (0.35 and 1.2 cfm) or over
 the expected operating range.
        16.1.1.4 Calculate flow rate, Q, for each run using  the wet test meter volume, Vw, and the run
 time, q. Calculate the DGM  coefficient, Y^, for each run. These calculations are as follows:

                                 P    V
                        Qis         bar    w
                     =  K.  	—                                     Eg. 315-9
            Yd         Vw (Tds  + Tstd)  Pbar

                    Vds (Tw  + Tstd)(Pbar  + -^)                               Eg. 315-10
                                            1 o.b
where
K,    =   0.3858 for international system of units (SI);
           17.64 for English units;
Pbar   =   Barometric pressure, mm Hg (in Hg);
Vw   =   Wet test meter volume, liter (ft3);
tw    =   Average wet test meter temperature, °C (°F);
tsld    =   273°C for SI units; 460°F for English units;
0    =   Run time, min;
tds    =   Average dry gas meter temperature, °C (°F);
Vds   =   Dry gas meter volume, liter (ft3);
Ap   =   Dry gas meter inlet differential pressure, mm H2O (in H2O).
        16.1.1.5 Compare the three Y^ values at each of the flow rates and determine the maximum an4
minimum values.  The difference between the maximum and minimum values at each flow rate should
be no greater than 0.030. Extra sets of triplicate runs may be made in order to complete this requirement.
In addition, the meter coefficients should be between 0.95 and 1.05. If these specifications cannot be

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met in three sets of successive triplicate runs, the meter is not suitable as a calibration standard and
should not be used as such. If these specifications are met, average the three Y^ values at each flow rate
resulting in five average meter coefficients, Y^.
        16.1.1.6 Prepare a curve of meter coefficient, Y^, versus flow rate, Q, for the DGM. This curve
shall be used as a reference when the meter is used to calibrate other DGMs and to determine whether
recalibration is required.
        16.1.2  Standard dry gas meter recalibration.
        16.1.2,1 Recalibrate the standard DGM against a wet test meter or spirometer annually or after
every 200 hours of operation, whichever comes first. This requirement is valid provided the standard
DGM is kept in a laboratory and, if transported, cared for as any other laboratory instrument. Abuse to
the standard meter may cause a change in the calibration  and will require more frequent recalibrations.
        16.1.2.2 As an alternative to full recalibration, a two-point calibration check may be made.
Follow the same procedure and equipment arrangement as for a full recalibration, but run the meter at
only two flow rates (suggested rates are 14 and 28 liters/min [0.5 and 1.0 cfm]). Calculate the meter
coefficients for these two points, and compare the values with the meter calibration curve. If the two
coefficients are within 1.5 percent of the calibration curve values at the same flow rates, the meter need
not be recalibrated until the next date for a recalibration check.
        16.2  Critical orifices as calibration standards.  Critical orifices may be used as calibration
standards in place of the wet test meter specified  in section 10.3 of this method, provided that they are
selected, calibrated, and used as follows:
        16.2.1  Selection of critical orifices.
        16.2.1.1 The procedure that follows describes the use of hypodermic needles or stainless steel
needle tubing that has been found suitable for use as critical orifices.  Other materials and  critical orifice
designs may be used provided the orifices act as true critical orifices; i.e., a critical vacuum can be
obtained, as described in section 7.2.2.2.3 of Method 5,40 CFR part 60, appendix A.  Select five critical
orifices that are appropriately sized to cover the range of flow rates between 10 and 34 liters/min or the
expected operating range. Two of the critical orifices should bracket the expected operating range.  A
minimum of three critical orifices will be needed to calibrate a Method 5 DGM; the other two critical
orifices can serve as spares and provide better selection for bracketing the range of operating flow rates.
The needle sizes and tubing lengths shown in Table 315-1 give the approximate flow rates indicated in
the table.
        16.2.1.2 These needles can be adapted to a Method 5 type sampling train as follows: Insert a
serum  bottle stopper,  13 x 20 mm sleeve type, into a 0.5 in Swagelok quick connect. Insert the needle
into the stopper as shown in Figure 5-9 of Method 5,40 CFR part 60, appendix A.
        16.2.2  Critical orifice calibration.  The procedure described in this section uses the Method 5
meter box configuration with a DGM as described in section 6.1.1.9 of this method to calibrate the
critical orifices. Other schemes may be used, subject to the approval of the Administrator.
        16.2.2.1 Calibration of meter box.  The critical orifices must be calibrated in the same
configuration as they will be used; i.e., there should be no connections to the inlet of the orifice.
        16.2.2.1.1  Before calibrating the meter box, leak-check the system as follows: Fully open the
coarse adjust valve and completely close the bypass valve.  Plug the inlet.  Then turn on the pump and
determine whether there is any leakage.  The leakage rate shall be zero; i.e., no detectable  movement of
the DGM dial shall be seen for 1 minute.
        16.2.2.1.2 Check also for leakages in that portion of the sampling train between the pump and
the orifice meter. See section 5.6 of Method 5,40 CFR part 60, appendix A for the procedure; make any
corrections, if necessary.  If leakage is detected, check for cracked gaskets, loose fittings, worn 0-rings,
etc. and make the necessary repairs.
        16.2.2.1.3 After determining that the meter box is leakless, calibrate the meter box according to
the procedure given in section 5.3 of Method 5,40 CFR part 60, appendix A.  Make sure that the wet test
meter meets the requirements stated in section 7.1.1.1 of Method 5,40 CFR part 60, appendix A.  Check
the water level  in the wet test meter. Record the DGM calibration factor, Y.

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        16.2.2.2 Calibration of critical orifices.  Set up the apparatus as shown in Figure 5-10 of Method
5, 40 CFR part 60, appendix A.
        16.2.2.2.1  Allow a warm-up time of 15 minutes.  This step is important to equilibrate the
temperature conditions through the DGM.
        16.2.2.2.2  Leak-check the system as in section 7.2.2.1.1 of Method 5, 40 CFR part 60, appendix
A.  The leakage rate shall be zero.
        16.2.2.2.3  Before calibrating the critical orifice, determine its suitability and the appropriate
operating vacuum as follows: turn on the pump, fully open the coarse adjust valve, and adjust the bypass
valve to give a vacuum reading corresponding to about half of atmospheric pressure.  Observe the meter
box orifice manometer reading, DH. Slowly increase the vacuum reading until a stable reading is
obtained on the meter box orifice manometer. Record the critical vacuum for each orifice. Orifices that
do not reach a critical value shall not be used.
        16.2.2.2.4  Obtain the barometric pressure using a barometer as described in section 6.1.2 of this
method. Record the barometric pressure, Pbar, in mm Hg (in. Hg).
        1 6.2.2.2.5  Conduct duplicate runs at a vacuum of 25 to 50 mm Hg (1 to 2 in. Hg) above the
critical vacuum. The runs shall be at least 5 minutes each. The DGM volume readings shall be in
increments of complete revolutions of the DGM. As a guideline, the times should not differ by more
than 3.0 seconds (this includes allowance for changes in the DGM temperatures) to achieve ±0.5 percent
in K'.  Record the information listed in Figure 5-1 1 of Method 5, 40 CFR part 60, appendix A.
        1 6.2.2.2.6  Calculate K1 using Equation 315-11.
               ,  _
                                                 _

                                                                                  E. 315-11
where
K1     =  Critical orifice coefficient, [mJX0K)*]/
          [(mm Hg)(min)] {[(ft3)(°R)'^)]/[(in. Hg)(min)]};
Tarib   =  Absolute ambient temperature, °K (°R).
        16.2.2.2.7  Average the K1 values. The individual K1 values should not differ by more than ±0.5
percent from the average.
        16.2.3 Using the critical orifices as calibration standards.
        16.2.3.1  Record the barometric pressure.
        16.2.3.2  Calibrate the metering system according to the procedure outlined in sections 7.2.2.2.1
to 7.2.2.2.5 of Method 5, 40 CFR part 60, appendix A. Record the information listed in Figure 5-12 of
Method 5, 40 CFR part 60, appendix A.
        16.2.3.3  Calculate the standard volumes of air passed through the DGM and the critical orifices,
and calculate the DGM calibration factor, Y, using the equations below:
              Vm(sld)          = K, Vm [?„„ + (AH/i3.6)]/T.                              Eg. 315-12
              Vcl
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factors obtained from two adjacent orifices each time a DGM is calibrated; for example, when checking
orifice 13/2.5, use orifices 12/10.2 and 13/5.1.  If any critical orifice yields a DGM Y factor differing by
more than 2 percent from the others, recalibrate the critical orifice according to section 7.2.2.2 of Method
5,40 CFR part 60, appendix A.
17.0 References.
       1.  Addendum to Specifications for Incinerator Testing at Federal Facilities. PHS, NCAPC.
December 6,1967.
       2. Martin, Robert M. Construction Details of Isokinetic Source-Sampling Equipment.
Environmental Protection Agency. Research Triangle Park, NC.  APTD-0581. April 1971.
       3. Rom, Jerome J. Maintenance, Calibration, and Operation of Isokinetic Source Sampling
Equipment. Environmental Protection Agency. Research Triangle Park, NC.  APTD-0576. March 1972.
       4. Smith, W.S., R.T. Shigehara, and W.F. Todd.  A Method of Interpreting Stack Sampling Data.
Paper Presented at the 63rd Annual Meeting of the Air Pollution Control Association, St. Louis, MO.
June 14-19,1970.
       5. Smith, W.S., et al. Stack Gas Sampling Improved and Simplified With New Equipment.
APCA Paper No.  67-119. 1967.
       6. Specifications for Incinerator Testing at Federal Facilities. PHS, NCAPC. 1967.
       7. Shigehara, R.T. Adjustment in the EPA Nomograph for Different Pitot Tube Coefficients and
Dry Molecular Weights. Stack Sampling News 2:4-11.  October 1974.
       8. Vollaro, R.F. A Survey of Commercially Available Instrumentation for the Measurement of
Low-Range Gas Velocities.  U.S. Environmental Protection Agency, Emission Measurement Branch.
Research Triangle Park, NC. November 1976 (unpublished paper).
       9. Annual Book of ASTM Standards.  Part 26. Gaseous Fuels; Coal and Coke; Atmospheric
Analysis. American Society for Testing and Materials. Philadelphia, PA. 1974. pp. 617-622.
       10. Felix,  L.G., G.I. Clinard, G.E. Lacy, and J.D.  McCain. Inertial Cascade Impactor Substrate
Media for Flue Gas Sampling.  U.S. Environmental Protection Agency.  Research Triangle Park, NC
27711. Publication No. EPA-600/7-77-060. June 1977.  83 p.
       11. Westlin, P.R., and R.T. Shigehara. Procedure for Calibrating and Using Dry Gas Volume
Meters as Calibration Standards.  Source Evaluation Society Newsletter. 3_(I):17-30. February 1978.
       12. Lodge, J.P., Jr., J.B. Pate, B.E. Ammons, and  G.A.  Swanson. The Use of Hypodermic
Needles as Critical Orifices in Air Sampling. J. Air Pollution Control Association. 1&197-200. 1966.
18.0 Tables. Diagrams. Flowcharts, and Validation Data
TABLE 315-1. Flow Rates for Various Needle Sizes and Tube Lengths.
Gauge/length
(cm)
12/7.6
12/10.2
13/2.5
13/5.1
13/7.6
13/10.2
Flow rate
(liters/min)
32.56
30.02
25.77
23.50
22.37
20.67
Gauge/length
(cm)
14/2.5
14/5.1
14/7.6
15/3.2
15/7.6
15/10.2
Flow rate
(liters/min)
19.54
17.27
16.14
14.16
11.61
10.48

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Particulate analysis
Plant
Date
Run No.
Filter No.
Amount liquid lost during
transport
Acetone blank volume (ml)
Acetone blank concentration (Eq.315-4) (mg/mg)
Acetone wash blank (Eq.3 1 5-5) (mg)

Container
No. 1
Container
No. 2
Final weight
(mg)




,





Tare weight (mg)


Total
Less Acetone blank
Weight of particulate matter
Weight gain (mg)





Moisture analysis

Impingers
Silica gel
Final volume
(mg)
Note 1

Initial volume (mg)
Notel

Total
Liquid collected (mg)



FIGURE 315-1.  Particulate and MCEM Analyses




Note 1: Convert volume of water to weight by multiplying by the density of water (1 g/ml).

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                                     MCEM analysis
Container No.
 Final
weight
 (mg)
 Tare of
aluminum
dish (mg)
Weight
 gain
  Acetone
wash volume
    (ml)
Metflrjfanfe
    wash
   volume
    (ml)
  2+2M
  3W
  3S
                  Total
                                                  m
                                                    total
  Less acetone wash blank (mg)
  (not to exceed 1 mg/1 of
  acetone used)
                                      Wa = Ca Pa E Ve»
  Less methylene chloride wash
  blank (mg) (not to exceed
  1.5 mg/1 of methylene
  chloride used)
                                       w
                           t  = c A E
                                                     tw
  Less filter blank (mg)
  (not to exceed....
  (mg/filter)
  MCEM weight (mg)
                                                mMCEOM  ~ 2^ m total   Wa   Wt    'b
 FIGURE 315-1 CContinuedt.  Particulate And MCEM Analyses

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                    State of California
          California Environmental Protection Agency
                   Air Resources Board
                      Method 429

Determination of Poly cyclic Aromatic Hydrocarbon (PAH)
           Emissions from Stationary Sources
               Adopted: September 12, 1989
            Amended: [insert date of amendment]

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                          TABLE OF CONTENTS

1   INTRODUCTION			    1
1.1  APPLICABILITY		    1
1.2  PRINCIPLE	    1
1.3  DEFINITIONS AND ABBREVIATIONS		    1

2   THE PRE-TEST PROTOCOL		    4
2.1  RESPONSIBILITIES OF THE END USER, TESTER, AND ANALYST	    4
2.2  PRE-TEST REQUIREMENTS	    5
2.3  REQUIRED PRELIMINARY ANALYTICAL DATA	    6
2.4  EXPECTED RANGE IN TARGET PAH CONCENTRATIONS
     OF INDIVIDUAL PAHs	    7
2.5  SAMPLING RUNS, TIME, AND VOLUME	    7

3   INTERFERENCES . .				  10

4   SAMPLING APPARATUS, MATERIALS, AND REAGENTS	  11
4.1  SAMPLING APPARATUS	  11
4.2  SAMPLING MATERIALS AND REAGENTS  .	. .		  14
4.3  PRE-TEST PREPARATION	  18
4.4  SAMPLE COLLECTION		  21
4.5  CALCULATIONS	  26
4.6  ISOKINETIC CRITERIA	 .		  30

5   SAMPLE RECOVERY			  31
5.1  SAMPLE RECOVERY APPARATUS			  31
5.2  SAMPLE RECOVERY REAGENTS	  32
5.3  SAMPLE RECOVERY PROCEDURE		  32
5.4  SAMPLE PRESERVATION AND HANDLING		  34

6   ANALYTICAL PREPARATION		.		  34
6.1  SAFETY			  34
6.2  CLEANING OF LABORATORY GLASSWARE	  35
August 9, 1996                                     Proposed M-429 Page i

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6.3  APPARATUS	  35
6.4  SAMPLE PREPARATION: REAGENTS	  36
6.5  SAMPLE EXTRACTION	  37
6.6  COLUMN CLEANUP	  40

7    GC/MS ANALYSIS	  42
7.1  APPARATUS	  42
7.2  REAGENTS	  43
7.3  INITIAL CALIBRATION	  45
7.4  CONTINUING CALIBRATION	  48
7.5  GC/MS ANALYSIS	  49
7.6  QUALITATIVE ANALYSIS	  50
7.7  QUANTITATIVE ANALYSIS  	  51
8    QUALITY ASSURANCE/QUALITY CONTROL 	  52
8.1  QA SAMPLES	  52
8.2  ACCEPTANCE CRITERIA  	  54
8.3  ESTIMATION OF THE METHOD DETECTION LIMIT (MDL)
      AND PRACTICAL QUANTITATION LIMIT IPQL) 	  56
8.4  LABORATORY PERFORMANCE	T . .  57
9.    CALCULATIONS  	  57
9.1  ANALYST'S CALCULATIONS	  57
9.2  TESTER'S CALCULATIONS	  61

10   REPORTING REQUIREMENTS  	  64
10.1  SOURCE TEST PROTOCOL	  64
10.2  LABORATORY REPORT 	  65
10.3  EMISSIONS TEST REPORT	  68
11   BIBLIOGRAPHY	  70
August 9, 1996                                      Proposed M-429 Page ii

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TABLES
   1   Method 429 Target Analytes  	.................	    71
   2  Practical Quantitation Limits for Target PAHs	    72
   3  PAH Analysis by HRMS of Different Lots
        of Cleaned Resin	    73
   4  Composition of the Sample Spiking Solutions	    74
 4A  Composition of Alternative Sample Spiking Solutions	    75
   5  Concentrations of PAHs in Working GC/MS Calibration
        Standard Solutions for Low Resolution Mass Spectrometry  ,	    76
   6  Concentrations of PAHs in Working GC/MS Calibration
        Standard Solutions for High Resolution Mass Spectrometry  .	    78
 6A  Concentrations of PAHs in Alternative Working GC/MS Calibration
        Standard Solutions for High Resolution Mass Spectrometry	    80
   7  Spike Levels for Labelled Standards		    82
 7A  Spike Levels for Labelled Standards for Alternative
        HRMS Spiking Scheme	    83
   8  Target Concentrations for Labelled Standards in Sample Extract	    84
 8A  Target Concentrations f9r Labelled Standards in Sample Extract
        Obtained with Alternative HRMS Spiking Scheme	    85
   9  Concentrations of Compounds in Laboratory Control Spike Sample	    86
  10  Recommended Gas Chromatographic Operating Conditions
        for PAH Analysis	    87
  11   Assignments of Internal Standards for Calculation of RRFs
        and Quantitation of Target PAHs and Surrogate Standards .	    88
11A  Assignments of Internal Standards for Calculation of RRFs
        and Quantitation of Target PAHs and Surrogate
         Standards Using Alternative HRMS Spiking Scheme  ...............    89
  12  Assignments of Recovery Standards for Determination of Percent
        Recoveries of Internal Standards and the Alternate Standard  .	    90
12A  Assignments of Recovery Standards for Determination of
        Percent Recoveries of  Internal Standards and the Alternate Standard
         Using Alternative HRMS  Spiking Scheme	    91
  13  Quantitation and Confirmation Ions for Selected
        Ion Monitoring of PAHs by HRGC/LRMS	    92
  14  Mass Descriptors Used for Selected Ion Monitoring
        of PAHs by HRGC/HRMS	    94
August 9, 1996                                           Proposed M-429  Page iii

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FIGURES
   1   Method 429 Flowchart	   96
   2  PAH Sampling Train	   97
   3  Condenser and Sorbent Trap for Collection of Gaseous PAH	   98
   4  XAD-2 Fluidized Bed Drying Apparatus	   99
   5  Method 429 Field Data Record  	  100
   6  Recovery of PAH Sampling Train	  101
   7  Flowchart for Sampling, Extraction and Cleanup for  	  102
        Determination of PAH in a Split Sample
   8  Flowchart for Sampling, Extraction and Cleanup for
        Determination PAH in a Composite Sample	  103
   9  Example of Pre-Test Calculations for PAH Emissions Test	  104
  10  CARB Method 429 (PAHs) Sampling Train Setup Record	  105
  11   CARB Method 429 (PAHs) Sampling Train Recovery Record	  106
  12  Chain of Custody Sample Record	  107
  13  Chain of Custody Log Record  	  108
14A  Example of GC/MS Summary Report (HRMS) for
        Initial Calibration Solution #1   	  109
14B  Example of Initial Calibration (ICAL) RRF Summary  	  110
14C  Example of Continuing Calibration Summary .	  111
15A  Example of Summary  Report of LCS Results	  112
15B  LCS Recoveries for Benzo(a)pyrene	  113
16A  Example GC/MS Summary Report (HRMS) for Sample Run #32  	  114
16B  Example Laboratory Report of PAH Results for Sample Run #32  	  115
17A  Example of Tester's Summary of Laboratory Reports .	  116
17B   Field Data Summary for PAH Emissions Test  	  117
17C  Example of Emissions Test Report	  118
APPENDIX A
      Determination of the Method Detection Limit  	  119
August 9, 1996                                         Proposed M-429  Page iv

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                                    Method 429

              Determination of Polycyclic Aromatic Hydrocarbon (PAH)
                        Emissions From Stationary Sources
 1.       INTRODUCTION

 1.1      APPLICABILITY
         This method applies to the determination of nineteen polycyclic aromatic
         hydrocarbons (PAH) in emissions from stationary sources. These are listed in
         Table 1.  The sensitivity which can ultimately be achieved for a given sample will
         depend upon the types and concentrations of other chemical compounds in the
         sample as well as the original sample size and instrument sensitivity.

         Any modification of this  method beyond those expressly permitted shall be
         considered a major modification subject to approval by the Executive Officer of
         the California Air Resources Board or his or her authorized representative.

 1.2      PRINCIPLE

         Particulate and gaseous  phase PAH are extracted isokinetically from the stack
         and collected on XAD-2  resin, in impingers, or in upstream sampling train
         components (filter, probe, nozzle). Only the total amounts of each PAH in the
         stack emissions can be determined with this method. It has not been
         demonstrated that the partitioning in the different parts of the sampling train is
         representative of the partitioning in the stack gas sample for paniculate and
         gaseous PAH.

         The required analytical method is isotope dilution mass spectrometry combined
         with high resolution gas  chromatography. This entails the addition of internal
         standards to all samples in known  quantities, matrix-specific extraction of the
         sample with appropriate  organic solvents, preliminary fractionation and  cleanup
         of extracts and analysis of the processed extract for PAH using high-resolution
         capillary column gas chromatography coupled with either low resolution mass
         spectrometry (HRGC/LRMS), or high resolution mass spectrometry
         (HRGC/HRMS).  To ensure comparable  results, the same MS method must be
         used for samples collected at all tested locations at those sources where more
         than one location is tested.

         Minimum performance criteria are specified herein which must be satisfied to
         ensure the quality of the sampling and analytical data.

 1.3      DEFINITIONS AND ABBREVIATIONS

 1.3.1       Internal Standard

            An internal standard is a 2H-labelled PAH which is added to all field samples,
            blanks and other quality control samples before  extraction.  It is also present
            in the calibration solutions.  Internal standards are used to measure the
August 9, 1996                                              Proposed M-429  Page 1

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            concentration of the analyte and surrogate compounds.  There is one internal
            standard assigned to each of the target analytes and surrogates.
1.3.2       Surrogate Standard
            A surrogate standard is a labelled compound added in a known amount to the
            XAD-2 resin of the sampling train, and allowed to equilibrate with the matrix
            before the gaseous emissions are sampled. The surrogate standard has to be
            a component that can be completely resolved, is not present in the sample,
            and does not have any interference effects.  Its measured concentration in
            the extract is an  indication of the how effectively the sampling train retains
            PAH collected on the XAD-2 resin. The recovery of the surrogate standards
            in the field blanks can be used to determine whether there are 'any matrix
            effects caused by time or conditions under which the sample is transported
            and stored prior to analysis.
1.3.3       Alternate Standard
            An alternate standard is a  2H-labelled PAH compound which is added to the
            impinger contents prior to extraction to estimate the extraction efficiency for
            PAHs in the impinger sample.
1.3.4       Recovery Standard
            A recovery standard is a 2H-labelled PAH compound which is added to the
            extracts of all field samples, blanks, and quality control samples before
            HRGC/MS analysis.  It is also present in the calibration solution. The
            response of the internal standards relative to the recovery standard is used to
            estimate the recovery of the internal  standards. The internal standard
            recovery is an indicator of the overall performance of the analysis.
1.3.5       Relative Response Factor
            The relative response factor is the response of the mass spectrometer to a
            known amount of an analyte or labelled compound (internal standard or
            surrogate standard) relative to a known amount of an internal standard or
            another labelled compound (recovery standard  or internal standard).

1.3.6       Performance Standard

            A performance standard is a mixture of known amounts of selected standard
            compounds.  It is used to demonstrate continued acceptable performance of
            the GC/MS system.  These checks include system performance checks,
            calibration checks, quality checks, matrix recovery, and surrogate recoveries.

1.3.7       Performance Evaluation Sample

            A performance evaluation sample is one prepared by EPA or othsr
            laboratories that contains known concentrations of method analytes, and has-
            been analyzed by multiple laboratories to determine statistically the accuracy
            and precision that can be  expected when a method is performed by a


August 9, 1996                                              Proposed M-429 Page 2

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             competent analyst.  Concentrations must be in the same range as typical
             field samples.  Analyte concentrations are not known by the analyst.

1.3.8        Laboratory Control Sample

             A laboratory control sample is one that contains  known concentrations of
             method analytes that is analyzed by a laboratory to demonstrate that it can
             obtain acceptable identifications and measurements with procedures to be
             used to analyze field samples containing  the same analytes.  Analyte
             concentrations are known by the analyst. The laboratory must prepare the
             control sample from stock standards prepared independently from those used
             for calibration.

1.3.9        End User

             The regulating agency shall  be considered the end user if this test method is
             conducted for regulatory purposes, or the regulating agency shall designate
             the end user for the purposes of this method.  Otherwise the end user shall
             be the  party who defrays the cost of performing  this test method. In any
             case, the pre-test protocol (Section 2)  must identify the  end user.

1.3.10       Tester

             Usually the tester is a contract engineering firm that performs the sampling
             procedures and delegates responsibility for specific analytical procedures to
             an analytical group (usually  part of a subcontracting laboratory firm).  In
             some cases, the tester may be part of the regulating agency.  The tester shall
             be the  party ultimately responsible for the performance of this test method
             whether directly or indirectly through the co-ordination of the efforts of the
             analytical  group and the efforts of the sampling group.

1.3.11       Analyst

             This term  refers to the analytical group that performs the analytical
             procedures to generate the required analytical data.

1.3.12       Source Target Concentration

             This is  the target concentration for each emitted PAH of interest specified by
             the end user of the test results.  The target concentration shall be expressed
             in units of mass of target substance per volume of emissions; typical units
             are nanograms per dry standard cubic meter or micrograms per dry standard
             cubic meter (ng/dscm or /;g/dscm)

1.3.13       The Method Detection Limit

             The method detection limit (MDL) is based  on the precision of detection of
             the analyte concentration near the detection limit. It is the product of the
             standard deviation of seven  replicate analyses of resin samples spiked with
             low concentrations of the analyte and Student's  t value for 6 degrees  of
             freedom at a confidence level of 99 %.
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1.3.14      The Practical Quantitation Limit

            The practical quantitation limit (PQL) is a limit for each compound at or below
            which data must not be reported. It is the minimum sample mass that must
            be collected in the sampling train to allow detection during routine laboratory
            operation within the precision limits established by the MDL determination.
            The PQLs will be estimated at 5  times the MDL for those PAH that are not
            contaminants of the resin.  The PQL for the remainder will be  estimated at 5
            times the blank XAD-2 resin level.

2.       THE SOURCE TEST PROTOCOL

         Every performance  of this test method shall have an identified operator of the
         source  to be tested, an identified  end user of the test method results, and an
         identified tester who performs this test method.  Figure 1 is a summary of the
         responsibilities  of the  parties involved in the coordination and performance of the
         source  test.  The protocol for the entire test procedure should  be understood and
         agreed  upon by the responsible parties prior to the start of the test.

2.1      RESPONSIBILITIES  OF THE END USER AND THE TESTER

2.1.1       The End User

            Before testing may begin, the end user of the test results (1.3.9) shall specify
            a source target  concentration for each of the PAH to be determined by this
            method using the  guidelines of Section 2.2.1.

            The end user shall approve the source test protocol only after  reviewing the
            document and determining that the minimum pre-test requirements  (Sections
            2.2 to 2.5 ) have  been met.

2.1.2       The Tester

            The tester (1.3.10) shall have the primary responsibility for the performance
            of the test method, and shall co-ordinate the efforts of the analytical group
            and the efforts of  the sampling group.

            The tester shall be responsible for the selection of an analyst with
            documented experience in the satisfactory performance of the method.  The
            tester shall  obtain from the analyst all of the analytical data (Section 2.3)
            that are required for pre-test calculations of sampling parameters.

             Before performing the  rest of this method, the tester shall  develop and write
            a source test protocol (Section 2.2) to help ensure that useful  test method
            results are obtained.  The tester shall plan the test based on the  information
            provided by the end user, the results of pre-test survsys of the source, and
            the  tester's calculations of target source testing parameters (Section 2,2).

            The tester shall be responsible for ensuring that all of the sampling and
            analytical reporting requirements  (Section 10) are met.
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2.1.3        The Analyst

             The analyst shall be responsible for performing all of the required analytical
             procedures described in this test method and reporting the results as required
             by Sections 2.3, 4.2.1, 4.2.2, 10.1.1, 10.1.2,  10.1.3, and 10.2).

2.2      PRE-TEST REQUIREMENTS

         The source test protocol shall specify the test performance criteria of the end
         user and all assumptions, required data and calculated targets for the following
         testing parameters:

             (1)  source target concentration of each emitted PAH of interest (2.2.1),

             (2)  preliminary analytical data  (2.3) for each target PAH, and

             (3)  planned sampling parameters (2.5.4, 2.5.5, and 2.5.6).

         The protocol  must demonstrate that the testing parameters calculated by the
         tester will meet the needs of the end user.  The source test protocol shall
         describe the  procedures for all aspects  of the source test including information
         on supplies, logistics, personnel and other resources necessary for an efficient
         and coordinated test.

         The source test protocol shall identify the end user of the results, the tester, the
         analytical group, and the sampling group, and the protocol shall be signed by the
         end user of the results and the tester.

         The tester shall not proceed with the performance of the remainder of this
         method unless the source test protocol is signed by the tester and tha end user.

2.2,1        Source Target Concentration (STC)

             The tester shall not proceed with the test unless a target concentration has
             been chosen. This will be the primary reporting objective of the emissions
             test. The end user shall select  a basis for determining each target
             concentration from: a) regulatory limits, b) environmental risk assessments,
             and (c) the interests of the end  user, the tester, and the stationary source.

2.2.1.1          Regulatory Limits

                 The  regulatory limit shall be the basis for determining a target
                 concentration for stationary source emissions in those cases where the
                 purpose of the emissions test is to demonstrate compliance with the
                 established regulatory limit.

2.2.1.2          Environmental Risk Assessments

                 In some cases testing is conducted for an environmental risk
                 assessment. A pre-test estimate of the  permissible risk shall then  be
                 used to determine the target concentration for stationary source
                 emissions.

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                 Note that some risk assessment methodologies will assume that a PAH
                 is present at the detection limit or one half of the detection limit even
                 when the compound is not detected. This is inappropriate for planning
                 for the  performance of the test method because by definition a
                 substance cannot be detected at one half of its detection limit. In such
                 cases, the target sampling parameter must be the maximum practical
                 sample volume.

 2.2.1.3          Interests of the End User, the Tester and the Stationary Source

                 In cases where the emissions test is not being performed to demonstrate
                 compliance  with a regulation, nor is it required for a  risk assessment,
                 the end user may use emissions results from previous tests of the
                 facility  or from similar facilities.

                 If estimates of the emissions are not availble, the tester must conduct a
                 preliminary test at each emissions point of interest. This target
                 concentration is necessary for the calculation of the target sampling
                 parameters  required by Section 2.5. Therefore, the emissions measured
                 during the preliminary test must be representative of source operation.
                 The tester must document operating conditions, and know from
                 historical data, the extent to which the results of this preliminary run are
                 representative of emissions from the source. This will require
                 documentation of operating conditions during the preliminary test, and a
                 knowledge of the potential variability in emissions with differences in
                 source operation.

                 As an alternative to conducting a preliminary test, the end user may
                 specify, as a sampling target, the longest practical sampling time so as
                 to obtain the lowest practically achievable source reporting limit
                 (Section 2.5.6).

 2.3      REQUIRED PRELIMINARY ANALYTICAL DATA

 2.3.1       Results of Blank  Contamination Checks

            The tester must obtain from the analyst the results of the PAH contamination
            checks. The analytical report must satisfy the reporting requirements of
            Sections 10 and  10.1.

            The analyst shall use the procedures described in Sections 4.2.1 and 4.2,2 to
            clean the sampling media (filters and XAD-2 resin) and check for PAH
            contamination.

            Table 3 shows the results of analyses of different lots of re-cleaned XAD-2
            resin. The purpose of this table is to show typical variability.  Actual results
            may vary from one test to another.
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2.3.2        The Method Detection Limit

             The method detection limit (MDL) must be determined by the same analyst
             (1.3.11) that will perform the analyses subsequent to sampling.  Before
             estimating the method detection limit ( MDL), the analyst shall identify those
             PAH that are contaminants of the XAD-2 resin using the procedures
             described in Sections 4.2.2.1 to 4.2.2.4. The analyst shall determine the
             MDL as described in Section 8.3  and Appendix A.

2.3.3        The Practical Quantitation Limit

             The analyst shall calculate the practical quantitation limits (PQLs) for the
             target PAH.  This value will  be 5 times the MDL or 5 times the XAD-2
             background level for those compounds that have been identified  by the
             analyst as contaminants.

             Table 2 lists practical quantitation limits obtained during ARB's development
             of this method.  The values for the PQLs will vary with the performance of
             individual laboratories.  Therefore, the tester must obtain PQL values for all of
             the target analytes from the  analyst.

2.4      EXPECTED RANGE IN TARGET CONCENTRATIONS OF INDIVIDUAL PAHs

         The PAH compounds in a source test sample can show large differences in
         concentrations.  A sample that might provide sufficient analyte for the detection
         and quantitation of the lowest concentration PAH could contain levels of other
         PAHs that exceed the upper limit of the method.

         In some cases the solution is two GC/MS injections - first with the undiluted
         extract, and then again  after appropriate dilution of the extract.  At other times
         the required minimum dilution might be so large as to result in the reduction of
         the internal standard response below the minimum required by the method.  With
         prior notification of expected levels of the target analytes, the analyst can modify
         the preparation of the samples so that useful results might be obtained.  All
         major modifications  must be approved by the Executive Officer.

2.5      SAMPLING RUNS, TIME, AND VOLUME

2.5.1        Sampling Runs

             A test shall include at least three sampling runs in series and a blank
             sampling train.

2.5.2        Minimum Sample Volume (MSV)

             This is the minimum sample volume that must be collected in the sampling
             train to  provide the minimum reportable mass of PAH for quantitation.  It
             must be based on a) the practical quantitation limit (2.3.3), b) the source
             target concentration (2.2.1),  and c) sampling limitations. Use Equation
             429-1 to calculate the target MSV for each PAH analyte.
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                                                  <                  429-1
                            MSV(dscm)  =PQL x _I_
                                                O I W
            Where:
            PQL   =  The practical quantitation limit, ng/sample (Section 2.3.3)
            STC   =  The source target concentration, ng/dscm (Section 2.2.1)

2.5.3       Minimum Sampling Time (MST)

            This is the minimum  time required to collect the minimum sample volume at
            the expected average volumetric sampling rate (VSR). Use Equation 429-2
            to calculate the minimum sampling time (MST) required to collect the
            minimum sample volume calculated in Section 2.5.2. The tester must use an
            average volumetric sampling rate (VSR) appropriate for the source to be
            tested.
            Where:

            VSR   =  Expected average volumetric sampling rate, dscfm
             60    =  Factor to convert minutes to hours
         0.028317 =  Factor to convert dscf to dscm

            The end user must decide whether the MSTs are all practically feasible and
            whether they can be increased to allow for any deviation from the sampling
            and analytical conditions assumed by the test plan.  Based on this decision,
            the tester must use either Section 2.5.4 (a) or  2.5.4 (b) to calculate a
            planned sample volume (PSV).

2.5.4       Planned Sample Volume (PSV)

            This is the volume of emissions that must be sampled to provide the target
            analytes at levels between the PQL and the limit of linearity.  The planned
            sample volume is the primary sampling target whenever practically feasible.
            The PSV is calculated according to either 2.5.4 (a)  or 2.5.4 (b).

            (a)     If the end user has decided that the MSTs can be increased, the
                   tester must use Equation 429-3 to calculate the PSV  using the largest
                   of the  19 MSV values calculated in Section 2.5.2.  and the largest
                   value for F that will give a practically achievable sample volume that
                   provides the target analytes at levels between the PQL and the limit
                   of linearity.  Use this PSV to calculate the planned sampling time
                   (Section 2.5.5 a)  and Equation 429-6.

            (b)     If the MSTs are not all practically achievable, the tester and the end
                   user must agree on a maximum  practical sampling time
                   (Section 2.5.5b).  This value must then be used for the PST in
                   Equation 429-4 to calculate the PSV. The tester must identify in the

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                   source test protocol the target analytes for which the PSV is lower
                   than the MSV.  The primary reporting objective of the test cannot be
                   achieved for those analytes.  If the primary reporting objective cannot
                   be achieved for all of the target analytes, it must be discussed in the
                   protocol and the alternative reporting objective (Section 2.5.6) must
                   be approved by the end user of the results.

                   The volume of sample that is actually collected will be determined by
                   practical sampling limitations,  the intended use of the data and the
                   level of uncertainty that the end user can tolerate in the measurement
                   of the target concentrations. This uncertainty will decrease as the
                   value of F (Equation 429-5) increases.

                                                                  429-3
                               PSV(dscm) =MSV  x F
                                                                  429-4
                              PSV(dscm)  = PST x VSR
                                         PSV                     429"5
                                         "MSV
            Where:
             PST    =  Planned sampling time  from Section 2.5.5
             F       =  A safety factor (>1) that allows for deviation from ideal sampling
                       and analytical conditions
2.5.5       Planned Sampling Time (PST)

            Two options are available for calculating the planned sampling time
            depending on whether the primary objective can be achieved for all of the
            target analytes.

            (a)     The  planned sampling time (PST) shall be long enough to 1) collect
                   the planned sample volume with reportable levels of the target
                   analytes and 2) sample representative operating conditions of the
                   source.  If the average sampling rate (VSR) used to estimate the
                   planned sampling time cannot be achieved in the field
                   (Section 4.4.4.1), the sampling time must be recalculated using the
                   actual VSR and the target PSV in equation 429-6.

            (b)     The planned sampling time shall be a practical maximum approved by
                   the end user and it shall be long enough to sample representative
                   operating conditions of the source.

                                                1          1        429-6
                                            002131
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2.5.6        Preliminary Estimate of Source Reporting Limit (SRL)

             Before the test proceeds, the end user and the tester shall agree on a
             preliminary estimate of the source reporting limit for each target PAH.  The
             SRL shall be calculated using Equation 429-7. The planned sample volume
             will contain reportable levels of a given analyte if that analyte is present in
             the emissions at a concentration that is equal to or greater than the
             calculated SRL.

                                                                   429'7
                               SRL(ng/dscm)
            Where:

            SRL  =   Preliminary estimate of source reporting limit, ng/dscm
            PQL  =   Practical quantitation limit, ng
            PSV  =   Planned sample volume, dscm

2.5.7    Example Calculations

         Figure 9 B is an example of the minimum required calculations of sampling
         parameters for the source test protocol.

3.       INTERFERENCES

         Interferences may be caused by contaminants in solvents, reagents, sorbents,
         glassware, and other sample processing hardware that lead to discrete artifacts
         and/or elevated backgrounds at the ions monitored.  All of these materials must
         be routinely demonstrated to be free from interferences under the conditions of
         the analysis by running laboratory reagent blanks as described in Section 6.1.1.

         The use of high purity reagents and solvents helps to minimize interference
         problems.  Purification of solvents by distillation in all-glass systems may be
         required.

         Transformation of PAH and the formation of artifacts can occur in the sampling
         train.  PAH degradation and  transformation  on sampling train filters  have been
         demonstrated. Certain reactive PAH such as benzolalpyrene,
         benzo[a]anthracene, and fluoranthene  when trapped on filters can readily react
         with stack gases. These PAH are transformed by reaction with low levels of
         nitric acid and higher levels of  nitrogen oxides, ozone, and sulfur oxides.

         PAH degradation may be of  even greater concern when they are trapped in the
         impingers. When stack gases  such as sulfur oxides and nitrogen oxides come in
         contact with the impinger water they are converted into sulfuric acid and nitric
         acid respectively. There is evidence that under such conditions certain PAH will
         be degraded.  It is recommended that the PAH levels in the impingers be used as
         a qualitative tool to determine  if breakthrough has occurred in the resin.
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4.       SAMPLING APPARATUS, MATERIALS AND REAGENTS

4.1      SAMPLING APPARATUS

         The sampling train components listed below are required.  The tester may use an
         alternative to the required sampling apparatus only if, after review by the
         Executive Officer, it is deemed equivalent for the purposes of this test method.

         Mention of trade names or specific products does not constitute endorsement by
         the California Air Resources Board. In all cases, equivalent items from other
         suppliers may be used.

         A schematic of the sampling train is shown in Figure 2.  The train consists of
         nozzle, probe, heated particulate  filter, condenser, and sorbent module followed
         by three impingers and a silica gel drying cartridge.  An in-stack filter may not be
         used because at the  in-stack temperatures the filter material must be of a
         material other than the Teflon required by the method. A cyclone or similar
         device in the  heated  filter box may be used for sources emitting a large amount
         of particulate matter.

         For sources with a high moisture  content, a water trap may be placed between
         the heated filter and  the sorbent module.  Additional impingers may  also  be
         placed after the sorbent module.  If any of these options are used, details must
         be provided in the test  report.  The train may be constructed by adaptation of an
         ARB Method  5  train. Descriptions of the train components are contained in the
         following sections.

4.1.1       Probe Nozzle

            Quartz, or borosilicate glass with sharp, tapered leading edge. The angle of
            taper shall be 30° and the taper shall be on the outside to preserve a
            constant internal diameter. The probe nozzle shall be of the button-hook or
            elbow design, unless otherwise approved by the Executive Officer.

            A range of sizes suitable for isokinetic sampling  should be available, e.g.,
            0.32 to 1.27 cm (1/8 to 1/2 in.) - or larger if higher volume sampling trains
            are used - inside  diameter (ID) nozzles in increments of 0.16 cm  (1/16 in.).
            Each nozzle shall be calibrated according to the procedures outlined in
            Section 5.1  of ARB method 5.

4.1.2       Probe

            The probe should be lined or made of Teflon, quartz, or borosilicate glass.
            The liner or  probe is to provide an inert surface for the PAH in the stack gas.
            The liner or  probe extends past the retaining nut into the stack.  A
            temperature-controlled jacket provides protection of the liner or probe. The
            liner shall  be equipped with a  connecting fitting that is capable of forming a
            leak-free,  vacuum tight connection without the use of sealing greases.
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4.1.3        Preseparator
             A cyclone, a high capacity impactor or other device-may be used if
             necessary to remove the majority of the particles before the gas stream is
             filtered.  This catch must be used for any subsequent analysis. The  device
             shall be constructed of quartz or borosilicate glass. Other materials  may be
             used subject to approval by the Executive Officer.
4.1.4        Filter Holder
             The filter holder shall be constructed of borosilicate glass, with a Teflon frit
             or Teflon coated wire support and glass-to-glass seal or Teflon gasket.  The
             holder design shall provide a positive seal against leakage from the outside or
             around the filter. The holder shall be attached immediately at the outlet of
             the probe, cyclone, or nozzle depending on the configuration used.  Other
             holder and gasket materials may be used subject to approval  by the Executive
             Officer.
4.1.5        Sample Transfer Line
             The sample transfer line shall be Teflon (1/4 in. O.D. x 1/32 in. wall) with
             connecting fittings that are capable of forming leak-free, vacuum tight
             connections without using sealing greases. The line should be as short as
             possible.
4.1.6        Condenser
             The condenser shall be constructed of borosilicate glass and shall be
             designed to allow the cooling of the gas stream to at least 20°C before it
             enters the sorbent module.  Design for the normal range of stack gas
             conditions is shown in Figure 3.
4.1.7        Sorbent Module
            The sorbent module shall be made of glass with connecting fittings that are
            able to form leak-free, vacuum tight seals without the use of sealant greases
            (Figure 3). The vertical resin trap is preceded by a coil-type condenser, also
            oriented  vertically, with circulating cold water.  Gas entering the sorbent
            module must have been cooled to 20 °C  (68°F) or less.  The gas temperature
            shall be monitored by a  thermocouple placed either at the inlet or exit of the
            sorbent trap. The sorbent bed must be firmly packed and secured  in place to
            prevent settling or channeling during sample collection.  Ground glass caps
            (or equivalent) must be provided to seal the sorbent-filled trap both prior to
            and following sampling. All sorbent modules must be maintained in the
            vertical position during sampling.
4.1.8       Impinger Train
            Connect three or more impingers in series with ground glass fittings able to   •
            form leak-free, vacuum tight seals without sealant greases.  All impingers
            shall be of the Greenburg-Smith design modified by replacing the tip with a


August 9, 1996                                             Proposed M-429  Page 12

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             1.3 cm (1/2 in.) I.D. glass tube extending to 1.3 cm (1/2 in.Jfrom the bottom
             of the flask.

             The first impinger may be oversized for sampling high moisture streams.  The
             first and second impingers shall contain 100 ml of 3 mM sodium bicarbonate
             (NaHC03) and 2.4 mM sodium carbonate Na2C03) (Section 4.2.5). This is
             intended to neutralize any acids that might form in the impingers.  The third
             impinger shall be empty.  Silica gel shall be added to the fourth impinger.
             A thermometer which measures temperatures to within 1°C (2°F), shall be
             placed at the outlet of the third impinger.
4.1.9        Silica Gel Cartridge
             This may be used instead of a fourth impinger.  It shall be sized to hold 200
             to 300 gm of silica gel.

4.1.10       PitotTube

             Type S, as described in Section 2.1 of ARB Method 2 or other devices
             approved by the Executive Officer.  The pilot tube shall be attached to the
             probe extension to allow constant monitoring of the stack gas velocity as
             required  by Section 2.1.3 of ARB Method 5.  When the pitot tube occurs
             with other sampling components as part of an assembly, the arrangements
             must meet the  specifications required by Section 4.1.1 of ARB Method 2.
             Interference-free arrangements are illustrated in Figures 2-6 through 2-8 of
             ARB Method 2  for Type S pitot tubes having external tubing diameters
             between 0.48 and 0.95 cm (3/1 6 and 3/8 in.).

             Source-sampling assemblies that do not meet these  minimum spacing
             requirements (or the equivalent of these requirements) may be used only if
             the pitot tube coefficients of such assemblies have been determined by
             calibration procedures approved by the Executive Officer.

4.1.11       Differential Pressure Gauge

             Two inclined manometers or equivalent devices, as described in Section 2.2
             of ARB Method 2. One manometer shall be used for velocity head (AP)
             readings and the other for orifice differential pressure readings.

4.1.12       Metering System

             Vacuum  gauge, leak-free  pump, thermometers accurate to within 3°C
             (5.4°F), dry gas meter capable of measuring volume to within 2 percent, and
             related equipment, as shown in Figure 2. Other metering systems must meet
             the requirements stated in Section 2.1.8 of ARB Method 5.

4.1.13       Barometer

             Mercury, aneroid, or other barometer capable of measuring atmospheric
             pressure to within 2.5 mm Hg (0.1 in. Hg). In many cases, the barometric
             reading may be obtained from a nearby national weather service station, in
             which case the station value (which is the absolute  barometric pressure) shall

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             be requested and an adjustment for elevation differences between the
             weather station and sampling point shall be applied at a rate of minus 2.5
             mm  Hg (0.1 in. Hg) per 30 m (100 ft) elevation increase or vice versa for
             elevation decrease.

4.1.14       Gas Density Determination Equipment

             Temperature sensor and pressure gauge, as described in Section 2.3 and 2.4
             of Method  2, and gas analyzer, if necessary, as described in Method 3.  The
             preferred configuration and alternative  arrangements of the temperature
             sensor shall be the same as those described in Section 2.1.10 of ARE
             Method 5.

4.1.15       Filter Heating System

             The  heating system must be capable of maintaining a temperature around the
             filter holder during sampling of (120 ± 14°C) (248 ± 25°F). A temperature
             gauge capable of measuring temperature to within 3°C (5.4°F) shall be
             installed so that the temperature around the filter holder can be regulated and
             monitored during sampling.

4.1.16       Balance

             To weigh the impingers and silica gel cartridge to within 0.5 g.

4.2      SAMPLING MATERIALS AND REAGENTS

4.2.1        Filters

             The  filters shall be Teflon coated glass fiber filters without organic binders, or
             Teflon membrane filters, and shall exhibit at least 99.95 percent efficiency
             (0.05 percent penetration) on 0.3 micron dioctyl phthalate smoke particles.
             The  filter efficiency test shall be conducted in accordance with  ASTM
             standard Method D 2986-71. Test data from the supplier's quality control
             program are sufficient for this purpose.  Record the manufacturer's lot
             number.

4.2.1.1           Contamination Check of Filter

                 The tester must have the filters cleaned by the analyst and checked for
                 contamination prior to use in the field. The contamination check must
                 confirm that there are no PAH contaminants  present that will interfere
                 with the analysis of the  sample PAHs of interest at the target reporting
                 limits.  The analyst must record the date the filter was cleaned.

                 The filters shall be cleaned in batches  not to exceed 50 filters. To clean
                 the filters, shake for one hour in methylene chloride in a glass dish that
                 has been cleaned according to Section 6.2.  After extraction,  remove
                 the filters and dry them  under a clean  N2 stream.  Analyze  one filter
                 using the same extraction, clean-up and analysis procedures to be used
                 for the field samples (Sections 6.5.1.2, 6.6,  and 7.5).


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                       Blank value  _ Total mass (ng) of analyte      429-8
                        per filter        NO. filters extracted

                 The acceptance criteria for filter cleanliness depends on  1) the method
                 reporting limit, 2) the expected field sample volume  and  3) the desired
                 reporting limit for the sampled emissions stream.  Filters with PAH
                 levels equal to or greater than the target reporting limit for the analyte(s)
                 of concern shall be rejected for field use.

                 If the filter does not pass the contamination check, re-extract the batch
                 and analyze a clean filter from the re-extracted batch. Repeat the re-
                 extraction and analysis until an acceptably low background level is
                 achieved. Store the remainder tightly wrapped in clean hexane-rinsed
                 aluminum foil as described in Section 4.3.3.

                 Record the date of the last cleaning of the filters and the date of the
                 PAH analysis, and  prepare a laboratory report of the analytical results
                 that includes all of the information required by Section 10.2.

                 The tester shall obtain this laboratory report with the date of cleaning of
                 the filters, and the date of the filter contamination check from the
                 analyst, and report them  in the source test protocol  and  the test report
                 as required by Sections 10.1  and 10.3.

4.2.2        Amberlite XAD-2 Resin

             The XAD-2 resin must be purchased precleaned and  then cleaned again as
             described below before use in the sampling train.

4.2.2.1          Cleaning XAD-2 Resin

                 This procedure  must be carried out in a giant Soxhlet extractor which
                 will hold enough XAD-2 for several sorbent traps, method blanks and QC
                 samples.  Use an all glass thimble containing an extra coarse frit for
                 extraction of the XAD-2.  The frit is recessed  10 to  15 mm above a
                 crenelated ring  at the bottom of the thimble to facilitate  drainage.  The
                 resin must be carefully retained  in the extractor  cup  with a glass wool
                 plug and stainless steel screen to prevent floating on the methylene
                 chloride.

                 Clean the  resin  by two sequential 24 hour Soxhlet extractions with
                 methylene chloride.  Replace with fresh methylene chloride after the first
                 24 hour period.

4.2.2.2          Drying Cleaned XAD-2 Resin

                 The adsorbent must be dried with clean inert gas. Liquid nitrogen from a
                 standard commercial liquid nitrogen cylinder has proven to be a reliable
                 source of  large  volumes of gas free from organic contaminants.  A
                 10.2 cm ID Pyrex pipe 0.6 m long with suitable  retainers as shown in
                 Figure 4 will serve  as a satisfactory column.  Connect the liquid nitrogen

August 9, 1996                                             Proposed  M-429  Page 15

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                 cylinder to the column by a length of cleaned 0.95 cm ID copper tubing,
                 coiled to pass through a heat source.  A convenient heat source is a
                 water bath heated from a steam line.  The final nitrogen temperature
                 should only be warm to the touch and not over 40 °C.

                 Continue the flow of nitrogen through the adsorbent until all the residual
                 solvent is removed. The rate of flow should be high enough that the
                 particles are gently agitated but not so high as to cause  the particles to
                 break up.

4.2.2.3          Residual Methylene Chloride Check.

                 Extraction: Weigh a 1.0 g sample of dried resin into a small vial, add 3
                 rnL of hexane, cap the vial and shake it well.

                 Analysis:  Inject a 2 ^L sample of the extract into a gas chromatograph
                 operated under  the following conditions:

                 Column:          6 ft x 1/8 in stainless steel containing  10%  OV-101
                                 on 100/120 Supelcoport.

                 Carrier Gas:      Helium at a rate of 30 mL/min.

                 Detector:        Flame ionization detector operated at a sensitivity  of 4
                                 X 1Q-11 A/mV.

                 Injection Port
                 Temperature:     250 °C.

                 Detector
                 Temperature:     305 °C.

                 Oven
                 Temperature:     30 °C for 4 min; programmed to  rise at 40 °C per min
                                 until it reaches 250 °C; return to 30 °C after 1000
                                 seconds.

                 Compare the results of the analysis to the results from a  reference
                 solution prepared by adding 2.5 //L of methylene chloride into  100 mL of
                 hexane.  This corresponds to 100 ;/g of methylene  chloride per g of
                 adsorbent. The maximum acceptable concentration is 1000/yg/g of
                 adsorbent. If the methylene chloride in the adsorbent exceeds this level,
                 drying must be continued until the excess methylene chloride is
                 removed.

4.2.2.4          Contamination Check of XAD-2 Resin

                The cleaned, dried XAD-2 resin must be checked for PAH contamination.
                Analyze a sample  of the resin equivalent in size to the amount required
                to charge one sorbent cartridge for a sampling train. The extraction,
                concentration, cleanup and GC/MS analytical  procedures shall  be the


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                 same for this sample as for the field samples (Sections 6.5.1.2, 6.6, and
                 7.5).

                 The acceptance limit will depend on the PQL, the expected
                 concentration in the sampled gas stream, and the planned sample
                 volume.  The contamination level must be less than the PQL or no more
                 than 20 percent of the expected sample level.

                 If the cleaned resin yields a value for a target analyte which is not
                 acceptable for the end user's intended application of the test results,
                 repeat the extraction unless the analyst has historical data that
                 demonstrate that re-extraction cannot reasonably be expected to further
                 reduce the contamination levels.  The tester must obtain these data from
                 the analyst and include them in both the source test protocol and the
                 emissions test report.

                 The contamination check shall be repeated if the analyst does not have
                 such historical data.  The analyst shall reclean and dry the resin
                 (4.2.2.1, 4.2.2.2, and 4.2.2.3) and repeat the PAH analysis of the re-
                 cleaned resin.  If the repeat analysis yields a similar result to the first,
                 record the contamination level for both the initial cleaning and the re-
                 cleaning.

                 The analyst shall record the dates of the cleaning and extraction of the
                 resin, and prepare a laboratory report of the analytical results that
                 includes all of the information required by Section 10.2.

                 The tester shall obtain the dates of cleaning and the laboratory report of
                 the results of the contamination check from the analyst, and report them
                 in both the source test protocol and the emissions test report as required
                 by Sections 10.1 and 10.3.

                 The tester shall identify the analytes for which the PQLs wiil be based
                 on a blank contamination value, and calculate the PQLs as required by
                 Section 2.3.3.
4.2.2.5          Storage of XAD-2 Resin
                 After cleaning, the resin may be stored in a wide mouth amber glass
                 container with a Teflon-lined cap, or placed in one of the glass adsorbent
                 modules wrapped in aluminum foil and capped or tightly sealed with
                 Teflon film at each end. The containers and modules shall then be
                 stored away from light at temperatures 4 °C or lower until the resin is
                 used in the sampling train.

                 The adsorbent must be used within twenty one (21)  days of cleaning. If
                 the adsorbent is not used within 21 days, it must be re-checked for
                 contamination before use.
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4.2.3       Silica Gel
             Indicating type, 6 to  16 mesh. If previously used, dry at 175°C (350°F) for 2
             hours. New silica gel may be used as received.  Alternatively, other
             desiccants (equivalent or better) may be used, subject to approval by the
             Executive Officer.
4.2.4        Reagent Water
             Deionized, then glass-distilled, and stored in hexane- and methylene chloride-
             rinsed glass containers with TFE-lined screw caps.

4.2.5        Impinger Solution

             Sodium bicarbonate 3 mM, and sodium carbonate 2.4 mM.  Dissolve
             1.0081 g sodium bicarbonate (NaHC03) and 1.0176 g of sodium carbonate
             (Na2C03) in reagent water (4.2.4), and dilute to 4 liters.

4.2.6        Crushed Ice

             Place crushed ice in the water bath around the impingers.

4.2.7        Glass Wool

             Cleaned by sequential rinsing in three aliquots of hexane, dried in a 110 °C
             oven, and stored in a hexane-washed glass jar with TFE-lined screw cap.

4.2.8        Chromic Acid Cleaning Solution

             Dissolve 200 g of sodium dichromate in 15 ml of reagent water, and then
             carefully add 400 ml of concentrated sulfuric acid.

4.3      PRE-TEST PREPARATION

         The positive identification and quantitation  of PAH in an emissions test of
         stationary sources are strongly dependent on the integrity of the samples
        ' received and the precision and accuracy of all analytical procedures employed.
         The QA procedures described in Sections 4.3.7 and 8 are to be used to monitor
         the performance of the sampling methods, identify problems, and take corrective
         action.

4.3.1        Calibration

             All sampling train components shall be maintained and calibrated according to
             the procedure described in APTD-0576  (Section 11.7), unless otherwise
             specified herein. The tester shall maintain a record of all calibration data.

4.3.1.1       Probe Nozzle

             Probe nozzles shall be calibrated according to the procedure  described in
             ARB Method 5.
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4.3.1.2      PitotTube
             Calibrate the Type S pitot tube assembly according to the procedure
             described in Section 4 of ARB Method 2.
4.3.1.3      Metering System
             Calibrate the metering system before and after use according to the
             requirements of Section 5.3 of ARB Method 5.

4.3.1.4      Temperature Gauges

             Use the procedure in Section 4.3 of ARB Method 2 to calibrate in-stack
             temperature gauges.  Dial thermometers, such as those used for the dry gas
             meter and condenser outlet, shall be calibrated against mercury-in-glass
             thermometers.

4.3.1.5      Leak Check of Metering System Shown in Figure 1

             The tester shall use the procedure described in Section 5.6 of ARB Method 5

4.3.1.6      Barometer

             Calibrate against a mercury barometer.

4.3.2       Cleaning Glassware for Sampling and Recovery

             All glass parts  of the train upstream of and including the sorbent module and
             the first impingers shall be cleaned as described in Section 3A of the 1974
             issue of Manual of Analytical  Methods for Analysis of Pesticide Residues in
             Human and Environmental  Samples  (Reference 11.4).  Take special care to
             remove  residual silicone grease sealants on ground glass connections of used
             glassware.  These greasy residues shall be removed by soaking several hours
             in a chromic acid cleaning solution (4.2.8) prior to routine  cleaning as
             described above. Other cleaning procedures may be used as long as
             acceptable blanks are obtained.  Acceptance criteria for blanks are stated in
             Section  8.2.

             Rinse all glassware with acetone, hexane, and methylene  chloride prior to use
             in the PAH sampling train.

             Glassware used in sample recovery  procedures must be rinsed as soon as
             possible after use with the last solvent used in it.  This must be followed by
             detergent washing with hot water, and rinses with tap water, deionized
             water, acetone, hexane, and methylene chloride. Other cleaning procedures
             may be used as long as acceptable blanks are obtained. Acceptance criteria
             for blanks are stated in Section 8.2.

4.3.3        Preparation of Filter

             The clean dry filter (4.2.1)  must be kept tightly wrapped in hexane-rinsed
             aluminum foil and stored  at 0 to 4°C in a container away from light until

August 9, 1996                                             Proposed M-429  Page 19

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            sampling. Before inserting the filter in the sampling train, check visually
            against light for irregularities and flaws or pinhole leaks.

4.3.4       Preparation of Sorbent Cartridge, Method Blank, and
            Laboratory Control Samples

            Sorbent Cartridge

            Use a sufficient amount (at least 30 gms or 5 gms/m3 of stack gas to be
            sampled) of cleaned resin to completely fill the glass sorbent cartridge which
            has been thoroughly cleaned as prescribed  (4.2.2).

            Add the required surrogate standards (Table 7) to the sorbent cartridges for
            all of the sampling and blank trains for each series of test runs.  Follow the
            resin with hexane-rinsed glass wool, cap both ends, and wrap the cartridge in
            aluminum foil. Store the prepared cartridges as required by Section 4.3.5.

            The sorbent  cartridges must be loaded, and the surrogate standards must be
            added  to the resin in a clean area in the laboratory.  There must be no
            turnaround of a used cartridge in the field.

            The analyst shall record the date that the surrogate standards were added to
            the resin and the amount of each compound.  The tester shall obtain these
            data from the analyst and report them in the source test protocol and the
            test report.

            The appropriate levels for the surrogate standards are given in Table 7 which
            shows the spiking plan for surrogate standards, internal standards, alternate
            standards, and recovery standards.  All of these required compounds are
            generally available.  Additional labelled  PAH may also be used if available.
            The labelled  compounds used as surrogate  standards must be different from
            the internal standards used for quantitation, and from the alternate and
            recovery standards.  If the spiking scheme  (Table 7) is modified, the tester
            must demonstrate that the proposed modification will generate data of
            satisfactory quality.  Table 7A shows an approved modification that has been
            used in ARB's method development.  All  modifications must be approved by
            the Executive Officer before the emissions test is performed.

            Laboratory Method Blank

            Take a sample of XAD-2 resin from the same batch used to prepare the
            sampling cartridge.  This will serve as the laboratory method blank
            (Section 8.1.1).  The mass of this sample must be the same as that used  in
            the sampling train.  Spike with the same  surrogate standards at the same
            levels used in the sampling cartridges.

            Laboratory Control Sample

            Set aside two samples of XAD-2 resin from the same batch used to prepare
            the sampling cartridge.  These will serve  as the laboratory control samples.
            (Section 8.1.3).  The mass of each sample must be the same as that  used in
            the sampling train.

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4.3.5        Storage of Prepared Cartridges. Method Blank and Laboratory Control Sample

             Store the aluminum foil wrapped sorbent cartridges away from light at 4 °C
             or lower until they are fitted into the sampling trains.  Do not remove the
             caps before the setup of the sampling train.

             The maximum storage time from cleaning of the resin to sampling with the
             spiked resin cartridge must not exceed 21 days (4.2.2.5).

             Store the laboratory method blank and laboratory control samples in amber
             glass jars with Teflon lined lids at temperatures no higher than 4 °C.

4.4      SAMPLE COLLECTION

         Because of the complexity of  this method, testers must be experienced with the
         test procedures in order to ensure reliable results.

4.4.1        Preliminary Field Determinations

             Select the sampling site and the minimum number of sampling points
             according to ARB Method  1  or as specified by the Executive Officer.

             Determine the stack pressure, temperature, and the range of velocity heads
             using ARB Method 2. Conduct a  leak-check of the pitot lines according to
             ARB Method 2, Section 3.1.

             Determine the moisture content using ARB Method 4 or its alternatives for
             the  purpose of making isokinetic sampling rate settings.

             Determine the stack gas dry molecular weight, as described in ARB
             Method 2, Section 3.6.  If integrated sampling (ARB Method 3) is used for
             molecular weight determination, the integrated bag sample shall be taken
             simultaneously  with, and for the same total length of time as, the sample
             run.

             Select a nozzle  size based on the  range of velocity heads, such that it is not
             necessary to change the nozzle size in order to maintain isokinetic sampling
             rates.  Do not change the  nozzle size during the run. Ensure that the proper
             differential pressure gauge is chosen for the range of velocity heads
             encountered (see Section  2.2 of ARB Method 2).

             Select a probe extension length such that all traverse points can be sampled.
             For large stacks, consider  sampling from opposite sides  of the stack to
             reduce the length of probes.

             The target sample volume  and sampling time must already have been
             calculated for the source test protocol and approved by  the end user as
             required by Sections 2.2 and 2.5. The total sampling time must be such that
             (1) the sampling time per point is  not less than 2 minutes (or some greater
             time interval as specified by the Executive Officer), and  (2) the total gas
             sample volume  collected (corrected to standard conditions) will not be less
             than the target  value calculated for the source test protocol (Section  2.5.5).

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            To avoid timekeeping errors, the number of minutes sampled at each point
            should be an integer or an integer plus one-half minute.

4.4.2       Preparation of Collection Train

            Keep all openings where contamination can occur covered until just prior to
            assembly or until sampling is about to begin.

            Caution:  Do not use sealant greases in assembling the sampling train.

            Record the performance of the setup procedures for the sampling train.
            Figure 10 is an example of a form for recording the sampling train setup data.
            The  tester must record all of the routine information indicated on this form as
            well as any additional data which are necessary for documenting the quality
            of any reported results.

            Place 100 ml of the impinger solution (4.2.5) in the first impinger and weigh.
            Record the total weight.  Repeat the procedure for the second impinger.
            Leave the third impinger empty.  Weigh the empty third impinger and record
            the weight.

            Weigh 200 to 300 g of silica gel to the  nearest 0.5 g directly into a tared
            impinger or silica gel cartridge just prior to assembly of the sampling train.
            The  tester may optionally measure .and  record in advance of test time the
            weights of several portions of silica gel  in air-tight containers. One portion of
            the preweighed silica gel must then be transferred from its container to the
            silica gel cartridge  or fourth impinger. Place the container in a clean place for
            later use in the sample recovery.

            Using tweezers or  clean disposable surgical gloves, place a filter in the filter
            holder.  Be sure that the filter is properly centered and the gasket properly
            placed so as to prevent the sample gas  stream from circumventing the filter.
            Check the filter for tears after assembly of the filter holder is completed.

            Mark the probe extension with heat resistant tape or by some other method
            to denote the proper distance into the stack or duct for each sampling point.

            Assemble the train as in Figure 2. Place crushed ice around the impingers.

4.4.3       Leak Check Procedures

4.4.3.1           Pretest Leak Check

                 After the sampling train has been assembled, turn on and set the filter
                 and probe heating systems  at the desired operating temperatures.  Allow
                 time for the temperature to stabilize.  Leak-check the train at the
                 sampling site by plugging the nozzle with a TFE plug and pulling a
                 vacuum of at least 380 mm Hg (15 in.  Hg).

                 Note:     A lower vacuum may be used, provided that it is not
                           exceeded during the test.


August 9, 1996                                              Proposed M-429 Page 22

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                 The following leak-check instructions for the sampling train are
                 described in Section 4.1.4.1  of ARE Method 5. Start the pump with by-
                 pass valve fully open and coarse adjust valve completely closed.
                 Partially open the coarse adjust valve and slowly close the by-pass valve
                 until the desired vacuum is reached. Do  not reverse the direction of the
                 by-pass valve.  This will cause water to back up into the filter holder.  If
                 the desired vacuum is exceeded, either leak-check at this higher vacuum
                 or end the leak-check as described  below and start over.

                 Determine the leakage rate.  A leakage rate in excess of 4 percent of the
                 average sampling rate or 0.00057 m3 per min. (0.02 cfm), whichever is
                 less, is unacceptable. Repeat the leak check procedure until an
                 acceptable leakage rate is obtained. Record the leakage rate on the field
                 data sheet (Figure 5).

                 When the leak-check is completed, first slowly remove the plug from the
                 inlet to the probe nozzle and  immediately turn off the vacuum pump.
                 This prevents water from being forced backward and keeps silica gel
                 from being  entrained  backward.
4.4.3.2          Leak Checks During Sample Run
                 If, during the sampling run, it becomes necessary to change a
                 component (e.g., filter assembly or impinger), a leak check shall be
                 conducted  immediately before the change is made. The leak-check
                 shall be done according to the procedure described in Section 4.4.3.1
                 above, except that it shall be done at a vacuum equal to or greater than
                 the maximum value recorded up to that point in the test.  If the leakage
                 rate is found to be  no greater than 0.00057 m3/min (0.02 cfm) or 4
                 percent of the average sampling rate (whichever is less), the  results are
                 acceptable, and no correction will  need to be applied to the total volume
                 of dry gas metered. If, however, a higher leakage rate is obtained, the
                 tester shall either (1) record the leakage rate and correct the  volume of
                 gas sampled since the last leak check as shown in  Section 4.4.3.4
                 below, or (2) void the sampling run.  Record the leakage rate.

                 Immediately after component changes, leak-checks must be conducted
                 according to the procedure outlined in Section 4.4.3.1  above. Record
                 the leakage rate on the field data sheet (Figure 5).
4.4.3.3          Post Test Leak Check
                 A leak-check is mandatory at the conclusion of each sampling run. The
                 leak-check shall be done in accordance with the procedures outlined in
                 Section 4.4.3.1 except that it shall be conducted at a vacuum equal to
                 or greater than the maximum value recorded during the sampling run.
                 Record the leakage rate on the field data sheet (Figure 5).  If the leakage
                 rate is found to be no greater than 0.00057 m3/min (0.02 cfm) or 4
                 percent of the average sampling rate (whichever is less), the results are
                 acceptable, and no correction need be applied  to the total volume of dry
                 gas metered. If, however, a higher leakage rate is obtained, the tester
August 9, 1996                                             Proposed M-429  Page 23

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                shall either, (1) record the leakage rate and correct the sample volume as
                shown in Section 4.4.3.4 below, or (2) void the sampling run.

4.4.3.4         Correcting for Excessive Leakage Rates

                If the leakage rate observed during any leak-check after the start of a
                test exceeds  the maximum leakage rate La (see definition below).
                replace Vm in Equation 429-9 with the following expression.
                         Vm -(L, -La)6|  - (Lp -La}6
                                                                  429-9
               Where:

               Vm =   Volume of gas sampled as measured by the dry gas meter
                        (dscf).

               La  =   Maximum acceptable leakage rate equal to 0.00057 m3/min
                        (0.02 ft3/min) or 4% of the average sampling rate, whichever is
                        smaller.

               Lp  =   Leakage rate observed during the post-test leak-check, m3/m?n
                        (ft3/min).

               Lj  =   Leakage rate observed during the leak-check performed prior to
                        the "ith" leakcheck (i = 1,2,3...n), m3/min (ft3/min).

               9,  =   Sampling time interval between two successive leak-checks
                        beginning with the interval between the first and second leak-
                        checks, min.

               6p  =   Sampling time interval between the last (nth) leak-check and the
                        end of the test, min.

         Substitute only for those leakage rates (Lj or Lp) which exceed La.

4.4.4    Train Operation

4.4.4.1      Sampling Train

            During the sampling run maintain a sampling rate within 10 percent of true
            isokinetic, unless otherwise specified or approved by the Executive Officer.
            The actual sampling rate must be at or above the VSR (Equation 429-4) to
            collect the target sample mass in the estimated sampling time. If the target
            sampling  rate cannot be achieved, adjust the planned sampling time to
            achieve the target sample volume (PSV).

            For each run, record the data required on the sample data sheet shown in
            Figure 5.  The operator must record the dry gas meter reading at the
            beginning of the test, at the beginning and end of each sampling time


August 9, 1996                                            Proposed M-429 Page 24

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             increment, when changes in flow rates are made, before and after each leak
             check, and when sampling is halted.

             Record other readings required by Figure 5 at least once at each sample point
             during each time increment and additional readings when significant changes
             (20 percent variation in velocity head readings) necessitate additional
             adjustments in flow rate.

             Level and zero the manometer.  Because the manometer level and zero may
             drift due to vibrations and temperature changes, make periodic checks during
             the traverse.

             Clean the portholes prior to the test run to minimize the chance of sampling
             the deposited material.  To begin sampling, remove the nozzle cap and verify
             that the pitot tube and probe extension are properly positioned.  Position the
             nozzle at the first traverse point with the tip pointing directly into the gas
             stream.

             Immediately start the pump and adjust the flow to isokinetic conditions.
             Nomographs are available, which aid in the rapid adjustment of the isokinetic
             sampling rate without excessive computations. These nomographs are
             designed for use when the Type S pitot tube coefficient (Cp) is 0.85 ±0.02,
             and the stack gas equivalent density (dry molecular weight) (Md) is equal to
             29 ±4. APTD-0576 (Reference 11.7) details the procedure for using the
             nomographs.  If Cp and Md are outside the above stated ranges, do not use
             the nomographs unless appropriate steps (see Reference 11.8) are taken to
             compensate for the deviations.

             When the stack is under significant negative pressure (height of impinger
             stem), take care to close the coarse adjust valve before inserting the probe
             extension assembly into the stack to prevent water from being forced
             backward. If necessary, the  pump may be turned on with the coarse adjust
             valve closed.

             When the probe is in position, block off the openings around the  probe and
             porthole to prevent unrepresentative dilution of the gas stream.

             Turn on the recirculating pump for the adsorbent module and  the condenser,
             and begin monitoring the temperature of the gas entering the adsorbent trap.
             Ensure that the temperature of the gas is 20 °C or lower before sampling is
             started.

             Traverse the stack cross section, as required by ARB Method 1 or as
             specified by the Executive Officer, being careful not to bump  the probe
             nozzle into the stack walls when sampling near the walls or when removing
             or inserting the probe extension through the portholes. This minimizes the
             chance of extracting deposited material.

             During the test run, take appropriate steps (e.g., adding crushed  ice to the
             impinger ice bath) to maintain the temperature at the condenser outlet below
             20°C (68°F).  Also, periodically check the level and zero of the manometer.
August 9, 1996                                            Proposed M-429  Page 25

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             If the pressure drop across the filter becomes too high, making isokinetic
             sampling difficult to maintain, the filter may be replaced during a sample run.
             Another complete filter assembly must be used rather than changing the filter
             itself.  Before a new filter assembly is installed, conduct a leak-check as
             outlined-in Section 4.4.3.2. The total PAH analysis shall include the
             combined catches of all filter assemblies.

             A single train shall be used for the  entire sample run, except in cases where
             simultaneous sampling is required in two or more separate ducts or at two or
             more different locations within the same duct, or, in cases where equipment
             failure necessitates a change of trains.  In all other situations, the use of two
             or more trains will be subject to approval by the  Executive Officer.

             Note that when two or more trains are used, a separate analysis of each train
             shall be performed, unless identical nozzle sizes were used on all trains, in
             which case the catches from the individual trains may be combined and a
             single analysis performed.

             At the end of the sample run, turn  off the pump, remove the probe extension
             assembly from the stack, and record the final dry gas meter reading.  Perform
             a  leak-check, as outlined in Section 4.4.3.3. Also, leak-check the pitot lines
             as described  in ARB Method 2; the lines must pass this leak-check, in order
             to validate the velocity head data.  Record leakage rates.

             Record any unusual events during the  sampling period.

4.4.4.2      Blank Train

             There shall be at least  one blank train  for each series of three or fewer test
             runs. For those sources at which emissions are sampled at more than one
             sampling location, there shall be at least one blank train assembled at each
             location for each set of three or fewer runs.

             Prepare and set up the blank train in a manner identical to that described
             above for the sampling trains.  The blank train shall be taken through all of
             the sampling  train preparation steps including the leak check without actual
             sampling of the gas stream. Recover the blank train as described in
             Section 5.3.  Follow all subsequent steps specified for the sampling train
             including extraction, analysis, and data reporting.

4.4.5        Calculation of Percent Isokinetic

             Calculate percent isokinetic (Section 4.5.7) to determine whether the run
             should be repeated. If there was difficulty in maintaining isokinetic rates
             because of source conditions,, consult  with the Executive Officer for  possible
             variance on the isokinetic rates.

4.5      CALCULATIONS
                                                                                   «
         Carry out calculations retaining at least one extra decimal figure beyond  that of
         the acquired data. Round off figures after the final calculation.
August 9, 1996                                              Proposed M-429 Page 26

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4.5.1    Nomenclature

         A       =   Cross-sectional area of stack, ft2.

         An      =   Cross-sectional area of nozzle, ft2.

         BWS     =   Water vapor in the gas stream, proportion by volume.

         Cs      =   Concentration of PAH in stack gas, ng/dscm, corrected to standard
                     conditions of 20°C, 760 mm Hg (68°F. 29.92 in. Hg) on dry basis.

         Gs      =   Total mass of PAH in stack gas sample, ng.

         AH      =   Average pressure differential across the orifice meter, mm H20 (in.
                     H20).

         I        =   Percent isokinetic sampling.

         La      =   Maximum acceptable leakage rate for either  a pretest leak-check or
                     for a leak check following a component change; equal to 0.00057
                     m3/min (0.02 cfm) or 4 percent of the average sampling rate,
                     whichever is  less.

         Lj       =   Individual leakage rate  observed during the leak-check conducted
                     prior to the "ith" component change (i = 1,  2, 3, ...n), m^/min
                     (cfm).
                                                                         4*
         I.      =   Leakage rate observed  during the post-test leak check,  rrr/min
                     (cfm).

         Md      =   Molecular weight of stack gas, dry basis, Ib/lb-mole (g/g-mole).

         Mw     =   Molecular weight of water,  18.0 g/g-mole (18.0 Ib/lb-mole).

         Ms      =   Molecular weight of stack gas, wet basis, Ib/lb-mole (g/g-mole).

         Pbar     =   Barometric pressure at the sampling site, mm Hg (in. Hg).

         Ps      =   Absolute stack gas pressure, mm Hg (in Hg).

         Pstd     =   Standard absolute pressure, 760 mm  Hg (29.92 in. Hg).

         Qj^     =   Dry volumetric stack gas flow rate corrected to standard conditions,
                     dscf/min (dscm/min).

         pw      =   Density of water, 0.9982 g/mL (0.002201 Ib/mL).

         R       =   Ideal gas constant 0.06236 mm Hg-m3/°K-g-mole (21.85 in Hg-
                     ft3/R-lb-mole).
August 9, 1996                                             Proposed M-429 Page 27

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         Tm      =  Absolute average dry gas meter temperature. °K (°R).
         Ts      =  Absolute average stack gas temperature °K (°R).

         Tstd     =  Standard absolute temperature, 293°K (528°R).

         V1c     =  Total volume of liquid collected in impingers and silica gel, m!_.

         Vm      =  Volume of gas sample as measured by dry gas meter, dcm (dcf).

         vm(std)   =  Volume of gas sample measured by the dry gas meter, corrected to
                    standard conditions, dscm (dscf).

         vw(std)   =  Volume of water vapor in the gas sample, corrected to standard
                    conditions, dscm  {dscf).

         vs      =  Stack gas velocity, calculated by ARB Method 2, Equation 2-9,
                    ft/sec (m/sec).

         Y       =  Dry gas meter calibration factor.

         0       =  Total sampling time, min.

         61      =  Sampling time interval, from  the beginning of  a run until the first
                    component change, min.

         8j       =  Sampling time interval between two successive component
                    changes, beginning with the  interval between the first and second
                    changes, min.

         6p      =  Sampling time interval, from  the final (nth) component change until
                    the end of the sampling run,  min.

         cpw      =  Sampling time interval, from  the final (nth) component change until

         13.6    =  Specific gravity of mercury.

         60      =  Conversion factor, sec/min.

         100     =  Conversion to percent.

4.5.2       Average Dry Gas Meter Temperature and Average Orifice Pressure Drop

            See sampling run record (Figure 5).

4.5.3       Dry Gas Volume

            Use Equation 429-10 to correct the sample volume measured by the  dry gas
            meter to standard conditions (20°C, 760 mm Hg or 68°F,  29.92 in Hg).
August 9. 1996                                            Proposed M-429  Page 28

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                                      4.  AH ]              /p,  4.  Ah  1    429-10
                            T ^  I1 oar    i-a fi                bar   iQ c     ^zs IU
                    = x/  v  I std  \	13.b/   -  K  w   Y ]	13.r
               m(std)   vm Y  -^	5	   ~  N1 vm Y 	^	
                            1 m      'std                       ' m


             Where:
                        Tstd
                 K!  =  	      =  0.3858 °K/mm Hg for metric units

                                  =   17.65 °R/in  Hg for English units
Pstd
             NOTE:  Equation 429-10 may be used as written unless the leakage rate
             observed during any of the mandatory leak-checks (i.e., the post-test leak-
             check or leak-checks conducted prior to component changes) exceeds La.  If
             Lp or LJ exceeds La, Vm in Equation 429-10 must be modified as described in
             Section 4.4.3.4.

4.5.4        Average Stack Gas Velocity

             Calculate the average stack gas velocity, vs/ as specified in ARB Method 2,
             Section 5.2.

4.5.5        Volume of Water Vapor

             Calculate the volume of water vapor using  Equation 429-1 1 and the weight
             of the liquid collected during sampling (Sections  5.3.6 and 5.3.8).


                        v       _ w   Pw  RTstd _ K  v
                        Vw(std)  - Vlc  -  -_- - K2 Vlc

             Where:
                 K2  =   0.001333 m3/mL for metric units, or
                     =   0.04707 ft3/mL for English units.
4.5.6        Moisture Content
             Calculate the moisture content of the gas, Bws.

                                          Vw,std>                    429-12
                              B
                               ws
                                      vm(std) +Vw(std)
         NOTE:  In saturated or water-droplet laden streams, the procedure for
                 determining the moisture content is given in the note to Section 1.2 of
                 Method 4. For the purpose of this method, the average stack-gas
                 temperature from Figure 5 may be  used for this determination, provided
                 that the accuracy of the in-stack temperature sensor is  ± 1°C (2°F)
Augusts, 1996                                            Proposed M-429  Page 29

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4.5.7       Isokinetic Variation


4.5.7.1          Calculation from Raw Data
                         100TS[K3V1C  +       (Pbar + -*            429-13
                                    60 9 vs Ps An


            Where:


                K3   = 0.003454 mm Hg-m3/mL-°K for metric units


                     = 0.002669 in Hg-ft3/mL-°R for English units


4.5.7.2         Calculation from Intermediate Values
                                         Vm(std)
                              Tstd vs 6 An Ps 60 (1  - Bws)             429-14


                            = K4
Ts Vm(std)
                                 PSVS6 An(1 -Bws)


            Where:


                K4   =  4.320 for metric units.


                     =  0.09450 for English units.


4.5.8       Average stack gas dry volumetric flow rate


            Use Equation 429-1 5 to calculate the average dry volumetric flow rate of the
            gas.
                              =60K, (1 -B^)  vs
                                                                     429-15
            Where:

                        Tstd
                K!  =  	     =   0.3858 °K/mm Hg for metric units

                        pstd
                                 =   17.65 °R/in Hg for English units


4.6      ISOKIIMETIC CRITERIA


         If 90 percent  < I <  110 percent, the isokinetic results are acceptable. If there
         is a bias to the results because I  < 90 percent or I >  110 percent, then the
         results must be rejected and the test repeated, unless the test results are
         accepted  by the Executive Officer.
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5        SAMPLE RECOVERY

5.1      SAMPLE RECOVERY APPARATUS

5.1.1        Probe Nozzle Brush

             Inert bristle brush with stainless steel wire handle. The brush shall be
             properly sized and shaped to brush out the probe nozzle.

5.1.2        Wash  Bottles

             Teflon wash bottles are required; Teflon FEP*.

5.1.3        Glass Sample Storage Containers

             Precleaned narrow mouth amber glass bottles, 500 ml or 1000 mL.  Screw
             cap liners shall be Teflon.

5.1.4        Filter Storage Containers

             Sealed filter holder or precleaned, wide-mouth amber glass containers with
             Teflon lined screw caps.

5.1.5        Balance

             To measure condensed water to within 0.5 g.

5.1.6        Silica  Gel Storage Containers

             Air tight metal containers to store silica gel.

5.1.7        Funnel and Rubber Policeman

             To aid in transfer of silica gel to container; not necessary if silica gel is
             weighed in the field.

5.1.8        Funnel

             To aid in sample recovery.  Glass or Teflon* must be used.

5.1.9        Ground Glass Caps or Hexane Rinsed Aluminum Foil

             To cap off adsorbent tube and the other sample-exposed portions of the
             aluminum foil.

5.1.10       Aluminum Foil

             Heavy-duty, precleaned with methylene chloride.
Augusts, 1996                                            Proposed M-429  Page 31

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5.2      SAMPLE RECOVERY REAGENTS

5.2.1        Reagent Water

            Deionized (Dl), then glass distilled, and stored in hexane and methylene
            chloride-rinsed glass containers with TFE-lined screw caps.

5.2.2       Acetone

            Nanograde quality. "Distilled in Glass" or equivalent, stored in original
            containers. A blank must be screened by the analytical detection method.

5.2.3       Hexane

            Nanograde quality. "Distilled in Glass" or equivalent, stored in original
            containers. A blank must be screened by the analytical detection method.

5.2.4       Methylene Chloride

            Nanograde quality or equivalent.  A blank must be screened by the analytical
            detection method.

5.3      SAMPLE RECOVERY PROCEDURE

         Proper cleanup procedure begins as soon as the probe is removed from the stack
         at the end of the sampling period and a post test leak check has been performed
         (4.4.3.3).  Allow the probe to cool.

         When the probe can be safely handled, wipe off all  external participate matter
         near the tip of the probe nozzle.  Conduct the  post test leak check as described
         in Section 4.4.3.3. Remove the probe from the train and close off both ends of
         the probe with precleaned aluminum foil (5.1.10). Seal off the inlet to the train
         with a ground glass cup or precleaned aluminum foil.

         Transfer the probe and impinger assembly to the cleanup area. This area must
         be clean, and enclosed so that the chances of contaminating the sample will be
         minimized.

         No smoking is allowed.

         Inspect the train prior to and during disassembly and note any  abnormal
         conditions, broken filters, color of the impinger liquid, etc.  Figure 6 summarizes
         the recovery procedure described in Sections 5.3.1  to 5.3.8.

         Figure 11 is an example of a form for recording the  performance of the sample
         recovery procedure.  The tester must record all of the routine information
         indicated on  this form as well as any additional data which are necessary for
         documenting the quality of any reported results.
August 9, 1996                                             Proposed M-429 Page 32

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5.3.1        Sample Container No. 1 (front half rinses)

             Quantitatively recover materialdeposited in the nozzle, probe, the front half
             of the filter holder, and the cyclone, if used, first by brushing and then by
             sequentially rinsing with acetone, hexane, and methylene chloride three times
             each. Place all these rinses in Container No. 1. Mark the liquid level.

5.3.2        Cyclone Catch

             If the optional cyclone is used, quantitatively recover  the particulate matter
             by sequentially rinsing the cyclone with acetone, hexane, and methylene
             chloride. Store in a clean sample container and cap.

5.3.3        Sample Container No. 2 (filter)

             Carefully remove the filter from the filter holder and place it in its identified
             container.  Use a pair of precleaned tweezers  to handle the filter.  Do not
             wrap the filter in aluminum foil.  If it is necessary to fold  the filter, make sure
             that the particulate cake is inside the fold.  Carefully transfer to the container
             any particulate matter and/or  filter fibers which adhere to the filter holder
             gasket by using a dry inert bristle brush and/or a sharp-edged blade. Seal the
             container.

5.3.4        Sorbent Module

             Remove the sorbent module from the train and cap it.

5.3.5        Sample Container No. 3 (back half rinses)

             Rinse the back half of the filter holder, the transfer line between the filter and
             the condenser, and the condenser (if using the separate condenser-sorbent
             trap) three times each with acetone, hexane and  methylene chloride, and
             collect all rinses in Container Mo. 3.  If using the combined condenser/sorbent
             trap, the rinse of the condenser shall be performed in  the laboratory after
             removal of the XAD-2 portion. If the optional  water knockout trap has been
             employed, the contents and rinses shall be placed in Container No. 3. Rinse
             it three times each with acetone,  hexane, and methylene chloride.  Mark the
             liquid level.

             The back half rinses may also be combined in  a single container with the
             front half rinses (Section 5.3.1).

5.3.6        Sample Container No. 4 (Impinger contents)

             Wipe off the outside of each of the first three  impingers to remove excess
             water and other material.  Weigh the impingers and contents to the nearest
             ±0.5 g using a balance.  Record the weight.  Calculate and then record the
             weight of liquid collected during sampling.  Use this weight and the weight of
             liquid collected in the silica gel (Section 5.3.8) to calculate the moisture
             content of the effluent  gas (Sections 4.5.5 and 4.5.6).  Pour the impinger
             catch directly into Container No.  4.  Mark the  liquid level.
August 9, 1996                                              Proposed M-429 Page 33

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5.3.7       Sample Container No. 5 (Impinger rinses)

            Rinse each impinger sequentially three times with acetone, hexane, and
            methylene chloride and pour rinses into Container No. 5.  Mark the liquid
            level. These rinses may be combined with the previously weighed impinger
            contents in Container No. 4.

5.3.8       Weighing Silica Gel

            Weigh the spent silica gel to the nearest 0.5 g using a balance. Record the
            weight.  Calculate and then record the weight of liquid collected during
            sampling. Use this weight and the weight of liquid collected in the impingers
            (Section 5.3.6) to calculate the moisture content of the effluent gas
            (Sections 4.5.5 and 4.5.6). .

5.4      SAMPLE PRESERVATION AND HANDLING

         From the time of collection to extraction, maintain all samples (Sections 5.3.1 to
         5.3.7) at 4°C or lower and protect from  light.   All samples must be extracted as
         soon as practically feasible, but within 21  days of collection; and all extracts
         must be analyzed as soon as practically  feasible, but within 40 days of
         extraction.  Success in meeting the holding time requirement will depend on pre-
         test planning by the tester and the laboratory.

6        ANALYTICAL PREPARATION

         This method is restricted to use only by  or under the supervision of analysts
         experienced in the use of capillary column gas chromatography/mass
         spectrometry and skilled in the interpretation of mass spectra.  Each analyst
         must demonstrate the ability to generate acceptable results with this method
         using the procedures described in Sections 7.3, 8.2.6, and 8.3.1.

6.1      SAFETY

         The toxicity or carcinogenicity of each reagent used in this method has not been
         precisely defined.  Nevertheless, each chemical compound should be treated as a
         potential health hazard and exposure to these  chemicals must be reduced to the
         lowest possible level by whatever means available.  The laboratory is responsible
         for maintaining a current file of OSHA regulations regarding the safe handling of
         the chemicals specified  in this method.  A reference file of material data handling
         sheets should also be made available to  all personnel involved in the chemical
         analysis. Reference 11.9 describes procedures for handling hazardous chemicals
         in laboratories.

         The following method analytes have been classified as known or suspected
         human or mammalian carcinogens:  benzo(a)anthracene and dibenzo-
         (a,h,)anthracene. A guideline for the safe handling of carcinogens can be found
         in Section  5209 of Title 8 of the California Administrative Code.
August 9, 1996                                             Proposed M-429  Page 34

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6.2      CLEANING OF LABORATORY GLASSWARE

         Glassware used in the analytical procedures (including the Soxhlet apparatus and
         disposable bottles) must be cleaned as soon as possible after use by rinsing with
         the last solvent used in it.  This must be followed by detergent washing with hot
         water, and rinses with tap water, deionized water, acetone,  hexane, and
         methylene chloride.  Other cleaning procedures may be used as long as
         acceptable blanks are obtained.  Acceptance criteria for blanks are given in
         Section 8.2.

         Clean aluminum foil  with acetone followed by hexane and methylene chloride.

6.3      APPARATUS

6.3.1        Grab Sample Bottle

             Amber glass, 125-mL and 250-mL, fitted with screw caps lined with Teflon.
             The bottle and cap liner must be acid washed and solvent rinsed with
             acetone and methylene chloride, and dried before use.

6.3.2        Concentrator Tube, Kuderna-Danish

             10-mL, graduated (Kontes-K-570050-1025 or equivalent).  Calibration must
             be checked at the volumes employed in the test. A ground glass stopper
             must be used to prevent evaporation of extracts.

6.3.3        Evaporation Flask, Kuderna-Danish

             500-mL (Kontes K-570001-0500 or equivalent).  (Attached to concentrator
             tube with springs).

6.3.4        Snyder Column,  Kuderna-Danish

             Three-ball macro {Kontes K-569001-0121 or equivalent).

6.3.5        Snyder Column,  Kuderna-Danish

             Two-ball micro (Kontes K-569001-0219 or equivalent).

6.3.6        Minivials

             1.0 ml vials; cone-shaped to facilitate  removal of very small samples; heavy
             wall borosilicate  glass; with Teflon-faced  rubber septa and screw caps.

6.3.7        Soxhlet Apparatus

             1 liter  receiver, 1 heating mantle, condenser, Soxhlet extractor.

6.3.8        Rotary Evaporator

             Rotovap R (or equivalent), Brinkmann Instruments, Westbury, NY.


Augusts, 1996                                             Proposed M-429  Page  35

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6.3.9       Nitrogen Slowdown Apparatus

            N-Evap Analytical Evaporator Model 111 (or equivalent), Organomation
            Associates Inc., Northborough,  MA.

6.3.10      Analytical Balance

            Analytical. Capable of accurately weighing to the nearest 0.0001 g.

6.3.11      Disposable Pipet

            5 3/4 inch x  7.0 mm OD.,

6.4      SAMPLE PREPARATION REAGENTS

6.4.1       Reagent water

            Same as  5.2.1.

6.4.2       Acetone

            Same as  5.2.2.

6.4.3       Hexane

            Same as  5.2.3.

6.4.4       Methylene Chloride

            Same as  5.2.4.

6.4.5       Sulfuric Acid

            ACS.  Reagent grade. Concentrated, sp. gr. 1.84.

6.4.6       Sodium Sulfate

            ACS.  Reagent grade.  Granular, anhydrous. Purify prior to use by extracting
            with methylene chloride and oven drying for 4 or more hours in a shallow
            tray. Place the cleaned material in a glass container with a Teflon lined screw
            cap, and  store in a  desiccator.

6.4.7       Silica  Gel

            For column chromatography, type 60, EM reagent, 100-200 mesh, or
            equivalent. Soxhlet extract with methylene chloride, and activate by heating
            in a foil covered glass container for longer than 16 hours at 130 °C, then
            store in a desiccator.  The storage period shall not exceed two days.

            NOTE: The performance of silica gel in the column cleanup procedure varies
            with manufacturers and with the method of storage.  The analyst shall
            establish  a procedure that satisfies the performance criteria of Section 6.6.1.

August 9, 1996                                            Proposed M-429  Page 36

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6.4.8        Alumina: Acidic

             Soxhlet extract with methylene chloride, and activate in a foil covered glass
             container for 24 hours at 190 °C.

             NOTE:   The performance of alumina in the column cleanup procedure varies
             with manufacturers and with the method of storage. The analyst shall
             establish a procedure that meets the performance criteria of Section 6.6.1.

6.4.9        Nitrogen

             Obtained from bleed from liquid nitrogen tank.

6.5      SAMPLE EXTRACTION

         WARNING:  Stack sampling will yield both liquid and solid samples for PAH
         analysis. Samples must not be split prior to extraction even when they appear
         homogeneous as in the case of single liquid phase samples.  Solid samples such
         as the resin  are not homogeneous and particulate matter may not be uniformly
         distributed on the filter.  In addition, filter samples are generally so small that the
         desired detection limit might not be achieved if the sample were split.

         The recovered samples may be combined as follows:

         1)  Particulate filter and particulate matter collected on the filter (Section 5.3.3),
             cyclone catch (Section 5.3.2) and sample container No.  1  (Section 5.3.1).

         2)  Sample container No. 3 (Section 5.3.5), resin (Section 5.3.4) and rinse of
             resin cartridge.

         3)  Sample container No.4 (Section 5.3.6) and sample container No.5 (Section
             5.3.7)

         Two schemes for sample preparation are described in Sections 6.5.1 and 6.5.2
         below.  One of these must be used.

         Section 6.5.1 describes sample preparation procedures for separate GC/MS
         analyses of impingers and the remainder of the sampling train. Figure 7 is a
         flowchart of the extraction and cleanup procedures.

         Section 6.5.2 describes sample preparation procedures for GC/MS analysis of a
         single composite extract from each sampling train.  The recovered samples are
         combined as shown in Figure 8.

6.5.1        Separate Analysis of Impingers

             A separate analysis of the impingers can be used to determine whether there
             has been breakthrough of PAHs past the resin.
Augusts, 1996                                             Proposed M-429 Page 37

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6.5.1.1          Extraction of Liquid Samples

                 A.  Sample Container No. 1 (Front half rinses)

                    Concentrate the contents of sample container No. 1 (Section 5.3.1)
                    to a volume of about 1-5 mL using the nitrogen blowdown
                    apparatus. Rinse the sample container three times with small
                    amounts of methylene chloride and add these rinses to the
                    concentrated solution. Concentrate further to about 1-5 mL. This
                    residue  will likely contain particulate matter which was removed in
                    the rinses of the probe and nozzle. Transfer the residue (along  with
                    three  rinses of the final sample vessel) to the  Soxhlet apparatus with
                    the filter and particulate catch and proceed as described under
                    Section 6.5.1.2 below.

                 B.  Sample Container No. 3 (Back half rinses)

                    Concentrate the contents of sample container No. 3 (Section 5.3.5)
                    to a volume of about 1-5 mL using the nitrogen blowdown
                    apparatus. Rinse the sample container three times with small
                    amounts of methylene chloride and add these rinses to the
                    concentrated solution. Concentrate further to about 1-5 mL.
                    Combine this residue (along with three rinses  of the finaP sample
                    vessel) in the Soxhlet apparatus with the resin sample, and proceed
                    as described under Section 6.5.1.2 below.

                 C.  Containers No. 4 and No.  5 (Impinger contents and rinses)

                    Place  the contents of Sample Containers No. 4 and No. 5 (Sections
                    5.4.6 and 5.4.7) in a separatory funnel. Add  the appropriate
                    amount of 2H-labelled alternate standard solution (Section 7 and
                    Table 7 or 7A) to achieve the final extract concentrations indicated
                    in Table 8 or 8A. The amounts required by Section 7.2.4 are based
                    on a final volume of 500 //L for analysis (450 fjL of sample extract
                    and 50 jjL of recovery standard solution).  Extract the sample three
                    times with 60 mL aliquots of methylene chloride. Combine the
                    organic  fractions. Divide the  extract in two - one half to be
                    archived, and the other for cleanup and GC/MS analysis. Store the
                    archive sample at 4°C away from light.

                    Pour the remaining extract through Na2S04 'nto a round bottom
                    flask.  Add 60 to 100 mL hexane  and evaporate to about 10 mL.
                    Repeat three times or less if the methylene chloride can be removed
                    with less hexane. Add the appropriate amount of alternate standard
                    (Section 7.2.7) to achieve the final extract concentrations shown in
                    Table  6  or 6A. This standard must be used to monitor the efficiency
                    of the cleanup procedure.

                    Concentrate the remaining sample to 2 mL with a Kuderna-Danish
                    concentrator or rotary evaporator, then transfer the extract to a 8-
                    mL test  tube with hexane.  Proceed with sample cleanup procedures
                    below (Section 6.6).

August 9, 1996                                             Proposed M-429  Page 38

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6.5.1.2          Extraction of Solid Samples

                     Filter, Paniculate matter, and Resin
                     The Soxhlet apparatus must be large enough to allow extraction of
                     the sample in a single batch.  Clean the Soxhlet apparatus by a 4 to
                     8-hr Soxhlet  with methylene chloride at a cycling rate of 3 cycles
                     per hour. Discard the solvent.  Add 20 g Na2S04 to the thimble.
                     Combine the filter, resin, glass wool, and concentrated front and
                     back half rinses (6.5.1.1A and 6.5.1.1B) and place on top of the
                     Na2S04. Add the appropriate amount of internal  standard (Section
                     7.2.4 and Table 7) to achieve the final extract concentrations
                     indicated in Table 8.

                     Place the thimble in the Soxhlet apparatus, and add about 700 ml
                     of methylene chloride to the receiver. Assemble the Soxhlet, turn
                     on the heating controls and cooling water, and  allow to  reflux for 16
                     hours at a rate  of 3 cycles per hour.  After extraction, allow the
                     Soxhlet to cool. Divide the sample in two - one half to be archived,
                     and the  other for cleanup and GC/MS analysis.  Store the archive
                     sample at 4°C away from light.
                     Exchange the remaining extract to hexane.  Add 60 to 100 ml
                     hexane and evaporate to about 10 mL. Repeat three times or as
                     necessary to remove the methylene chloride.  Add the appropriate
                     amount of alternate standard (Section 7.2.7 and Table 7 or 7A) to
                     achieve the final extract concentrations shown in Table 8 or 8A.
                     This alternate standard must be used to monitor the  efficiency of
                     the cleanup procedure when the impingers are analyzed separately
                     from the remainder of the sampling train.

                     Concentrate the remaining sample to about 2  ml with a Kuderna-
                     Danish concentrator or rotoevaporator, then transfer the extract to a
                     8-mL test tube with hexane.  Proceed with sample cleanup
                     procedures below (Section 6.6).

6.5.2       Single Composite Extract For Analysis

6.5.2.1          Extraction of Aqueous Samples

                     Containers No. 4 and No. 5 (Impinger contents and rinses)

                     Pour the contents of Sample Containers No. 4 and No. 5 (Sections
                     5.3.6 and 5.3.7) into an appropriate size separatory funnel.  Do not
                     add internal standards.  Instead, add the appropriate amount of
                     alternate standard spiking solution (Section 7  and Table 7 or 7A) to
                     achieve the final extract concentrations indicated in Table 8 or 8A.

                     Extract the sample three times with 60 ml aliquots of methylene
                     chloride.  Combine the organic fractions with the solid samples and
                     concentrated rinses (6.5.2.2) in a Soxhlet extractor.

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6.5.2.2          Extraction of Solid Samples

                 Concentrate the front and back half rinses as described in Sections
                 6.5.1.1 A and 6.5.1.1B. Clean the Soxhlet apparatus as in Section
                 6.5.1.2.  Place the filter and resin in the Soxhlet apparatus along with
                 the concentrated front and back half rinses and the impinger extract.
                 Add the internal standards, extract the sample, and concentrate the
                 extract as described in  Section 6.5.1.2. Divide the extract into two
                 equal portions.  Store one of these, the archive sample, at 4 °C away
                 from light.  The remaining extract must be exchanged to hexane as
                 described in Section 6.5.1.2.  Do not add the alternate standard to this
                 composite extract. It has already been added to the impinger sample
                 (6.5.2.1).

                 Concentrate the extract to 2 ml with a Kuderna-Danish concentrator or
                 rotary evaporator, then transfer to a 8-mL test tube with hexane or
                 equivalent non-polar solvent such as isooctane. Proceed with sample
                 cleanup procedures below (Section 6.6)

6.6      COLUMN CLEANUP

         Several column chromatographic cleanup options are available.  Either of the two
         described below may be sufficient. Before using a procedure for the cleanup of
         sample extracts, the analyst must demonstrate that the requirements of Sections
         8.1.3.1  and 8.2.6 can be met using the cleanup procedure.  Acceptable
         alternative cleanup procedures may also be used provided that the analyst can
         demonstrate that the performance requirements of Sections 8.1.3.1 and 8.2.6
         can be met.  Compliance with the requirements of Sections 8.1.1.1 and 8.2.6
         must also be demonstrated whenever there is a change in the column cleanup
         procedure used for the initial demonstration.

         The sample extract obtained as described in Sections 6.5.1C and  6.5.1.2 or
         6.5.2.2 is concentrated to a volume of  about 1 ml using the nitrogen blowdown
         apparatus, and this is transferred quantitatively with hexane rinsings to at least
         one of the columns described  below.

6.6.1       Column Preparation

            A.   Silica Gel Column

                 Pack a glass gravity column (250 mm x 10 mm) in the following
                 manner:

                 Insert a clean glass wool plug (Section 4.2.7) into the bottom of the
                 column and add 10 grams of activated silica gel (Section 6.4.7) in
                 methylene chloride. Tap the column to settle the silica gel, and then add
                 a 1 cm layer of anhydrous sodium sulfate (Section 6.4.6)

                 Variations among  batches of silica gel may affect the elution volume of
                 the various PAH.  Therefore, the volume of solvent required to
                 completely elute all of the PAH must be verified by the  analyst. The
                 weight of the silica gel can then be adjusted accordingly.  Satisfactory

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                 recovery (as defined in Section 6.6) of each native PAH in the LCS
                 (8.1.3) must be demonstrated whenever there is a change in the method
                 of preparing the silica gel columns.

             B.   Acid Alumina Column

                 Pack a 250 mm x 10 mm glass gravity column as follows:

                 Insert a clean glass wool plug (Section 4.2.7) into the bottom of the
                 column. Add 6 g of acid alumina prepared as described in
                 Section 6.4.8. Tap the column gently to settle the alumina, and add 1
                 cm of anhydrous sodium sulfate to the top.

                 Satisfactory recovery (as defined in Section 6.6) of each native  PAH in
                 the LCS (8.1.3) must be demonstrated whenever there is a change in
                 the method of preparing the acid alumina columns.

6.6.2    Column Chromatography Procedure

             A.   Silica Gel Column

                 Elute the column with 40 mL of hexane. The rate for all elutions should
                 be about 2 mL/min.  Discard the eluate and just prior to exposure of the
                 sodium sulfate layer to the air, transfer the 1 ml sample extract onto the
                 column using two additional 2 mL rinses of hexane to complete  the
                 transfer. Just prior to exposure of  the sodium sulfate layer to the air,
                 begin elution of the column with 25 mL of  hexane followed by 25 mL of
                 methylene chloride/hexane (2:3)(v/v).  Collect the entire eluate.
                 Concentrate the collected fraction to about 5 mL using the K-D
                 apparatus  or a rotary evaporator. Do not allow the extract to  go to
                 dryness.

                 Transfer to a minivial using a hexane rinse  and concentrate to 450 /jL
                 using a gentle stream of nitrogen.  Store the extracts in a refrigerator at
                 4 °C or lower away from light until GC/MS analysis (Section 7).

             Bo   Alumina Column

                 Elute the column with 50 mL of hexane.  Let the solvent flow through
                 the column until the  head of the liquid in the column is just above the
                 sodium sulfate layer.  Close the stopcock to stop solvent flow.

                 Transfer 1  mL of the sample extract onto the column.  Rinse out extract
                 vial with two  1 mL rinses of hexane and add it to the top of the  column
                 immediately.  To avoid overloading  the column, it is suggested that no
                 more than  300 mg of extractable organics  be placed  on the column.

                 Just prior to exposure of the sodium sulfate to the air, elute the  column
                 with a total of 15 mL of hexane. If the extract is in 1 mL of hexane,
                 and if 2 mL of hexane was used as a rinse, then  12 mL of additional
                 hexane should be used. Collect the effluent and concentrate to  about 2
                 mL using the K-D apparatus or a rotary evaporator.

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                 Transfer to a minivial using a hexane rinse and concentrate to 450//L
                 using a gentle stream-of nitrogen.  Store the extracts at 4°C or lower
                 away from light until GC/MS analysis.

7        GC/MS ANALYSIS

7.1      APPARATUS

7.1.1        Gas Chromatograph

             An analytical system complete with a temperature programmable gas
             chromatograph and all required accessories'including syringes, analytical
             columns, and gases.  The GC injection port must be designed for capillary
             columns.  Splitless injection is recommended.

7.1.2        Column

             Fused silica columns are required.

             A.   30 M long x 0.32 mm ID  fused silica capillary column coated with a
                 crosslinked phenyl methyl silicone such as DB-5.

             B.   Any column equivalent to the DB-5 column may be used as long as it
                 has the same separation capabilities as the DB-5.

7.1.3        Mass Spectrometer

7.1.3.1          Low Resolution

                 A low resolution mass spectrometer (LRMS) equipped with a 70 eV
                 (nominal) ion source operated in the electron impact ionization mode,
                 and capable of monitoring all of the ions in each Selected Ion Monitoring
                 (SIM) group (Table 13) with a total cycle time of 1 second or less.

7.1.3.2          High Resolution

                 The high resolution mass  spectrometer (HRMS) must be capable of
                 operation in the SIM mode at a resolving power of 8,000. Electron
                 impact ionization must be used. The mass spectrometer must be
                 capable of monitoring all of the ions listed in each of the three SIM
                 descriptors (Table  14) with a total cycle time of 1 second or less.

7.1.4        GC/MS Interface

             Any gas chromatograph to mass spectrometer interface may be used as long
             as it gives acceptable calibration response for each analyte of interest at the
             desired concentration and achieves the required tuning performance criteria
             (Sections 7.3.5 and 7.3.6). All components of the interface must be glass
             or glass-lined materials. To achieve maximum sensitivity, the exit end of  the
             capillary column should be  placed in the mass spectrometer ion source
             without being exposed to the ionizing electron beam.
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7.1.5        Data Acquisition System

             A computer system must be interfaced to the mass spectrometer.  The
             system must allow the continuous acquisition and storage on machine-
             readable media of all data obtained throughout the duration of the
             chromatographic program.  The computer must have software that can
             search any GC/MS data file for ions of a specific mass and plot a Selected
             Ion Current Profile or SICP (a plot of the abundances of the selected ions
             versus time or scan number).  Software must also be able to integrate, in any
             SICP, the abundance between specified time or scan-number limits.

             The data system must provide hard copies of individual ion chromatograms
             for selected gas chromatographic time intervals.

             The data system must also be able to provide hard copies of a summary
             report of the results of the GC/MS runs.  Figures 14A to 14C show the
             minimum data that the system must be available to provide.

7.2      REAGENTS

7.2.1        Stock Standard Solution (1.00 //g///L)

             Standard solutions can be prepared from pure standard materials or
             purchased as certified solutions.

7.2.2        Preparation of Stock Solutions

             A.  Calibration standards.  Prepare stock calibration standard solutions of
                 each of the PAH analytes by accurately weighing the required amount of
                 pure material. Dissolve the material in isooctane and dilute to volume.
                 When compound purity is assayed to be 96% or'greater, the weight may
                 be used without correction to calculate the concentration of the stock
                 standard.

                 Commercially prepared stock standards may  be used at any
                 concentration if they are  certified  by the manufacturer or by an
                 independent source.

             B.   Internal standards. Prepare stock solutions in isooctane of the fourteen
                 internal standards listed in Table 4 or 4A at concentrations of 1000
                 ng//;L.

             C.   Recovery standards. Prepare stock solutions in isooctane of the three
                 recovery standards listed in Table 4 or 4XA at concentrations of
                 1000ng///L.

             D.   Alternate standard. Prepare a stock solution in isooctane of the
                 alternate standard listed in Table 4 or 4A at a concentration of
                 1000 ng///L.
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             E.   Surrogate standards.  Prepare stock solutions in isooctane of the
                 surrogate standards listed in Table 4 or 4A at a concentration of
                 1000 ng//;L.

             Store stock standard solutions in Teflon'-sealed screw-cap bottles at 4°C and
             protect from light. Stock standard solutions must be checked frequently for
             signs of degradation or evaporation, especially just before using them to
             prepare calibration standard solutions or spiking solutions.
                                                        *«•
             Replace stock standard solutions every 12 months or more frequently if
             comparison with quality control check samples according to Section 7.4.1
             indicates a problem.

7.2.3        Calibration Standards

             Prepare calibration standards at a minimum of five concentration  levels. One
             of the calibration standards should be at a concentration near, but above, the
             method detection limit. The others should include the range of
             concentrations found in real samples but should not exceed the linear range
             of the GC/MS system.

             Prepare calibration working standard solutions by combining appropriate
             volumes of individual or mixed calibration standards with internal  standard,
             recovery standards, and alternate standard spiking solution and making up to
             volume with hexane to obtain the solution concentrations given in Tables 5,
             6, and 6A.  The  suggested ranges are 0.25 ng//;L to 5.0 ng//y|_ for LRMS and
             10 pg//;L to 500 pg///L for HRMS.

             All standards must be stored at 4°C or lower and mustjDe freshly prepared if
             the check according to Section 7.4.1 indicates a problem.

7.2.4        Internal Standard (IS) Spiking Solution

             The concentration of internal standard in the IS spiking solution must be such
             that the amount  of solution added to the calibration standard solution and the
             sample is at least 2 ml.

             Prepare the  internal standard spiking solution by using appropriate volumes of
             stock solutions of Section  7.2.2B to give the concentrations shown in
             Table 4 or 4A. A volume of 2  ml of either the LRMS or HRMS spiking
             solution will provide the amount of the internal standards that must be
             added to the sample (Table 7 or 7A) before extraction to achieve, in a final
             volume of 500 ;/L, the sample extract concentrations shown in Table 8 for
             LRMS and Table 8 or 8A for HRMS analysis.  The target concentrations in
             Tables 8 and 8A are based on a final volume  of 500 //L  and 100 percent
             recovery of the internal standards added to the sample.

7.2.5        Recovery Standard Spiking Solution

             The concentration of recovery standard in this spiking solution must be such
             that the amount  of solution added to the concentrated sample extract is
             50 //L to give a final extract volume of  500 //L.

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             Use an appropriate volume of stock solution of Section 7.2.2C to prepare a
             recovery standard spiking solution with the concentrations shown in
             Table 4or 4A. Store at 4 °C or lower.

             A volume of 50 //L of the recovery standard spiking solution shown in
             Table 4 or 4A will provide the amount of each recovery standard required by
             Table 7 or 7A to achieve the target sample concentration of Table 8 or 8A.
             Final volumes, may be adjusted depending on the target detection limit.

7.2.6        Surrogate Standard Spiking Solution

             The concentration of surrogate standard in this spiking solution must be such
             that the amount of solution added to the calibration standard solution and the
             sorbent module is at least 2 ml.

             Prepare the surrogate standard spiking solution by using the appropriate
             volume of stock solution of Section 7.2.2E to give the concentration shown
             in Table 4 or 4A. A volume of 2 ml of either the LRMS or HRMS spiking
             solution will provide the amount  of the surrogate standards that must be
             added to the sample (Table 7 or 7A) before sampling to achieve the sample
             extract concentrations shown in Table 8 or 8A in a final sample volume of
             500 pL.

7.2.7        Alternate Standard Spiking Solution

             The concentration of alternate standard in this spiking solution must be such
             that the amount of solution added to the calibration standard solution and the
             sample extracts is at least 2 ml.

             Prepare the alternate standard spiking solution by using the appropriate
             volume of stock solution of Section 7.2.2D to give the concentration shown
             in Table 4 or 4A. A volume of 2 ml of either the LRMS or HRMS spiking
             solution will provide the amount  of the alternate standard that must be
             added to the sample (Table 7 or 7A) before extraction to achieve the sample
             extract concentrations shown in Table 8 or 8A in a final sample volume of
             500/yL.

7.2.8        Calibration Check Standard

             The calibration check standard shall be used for column performance checks,
             and  for continuing calibration checks.  Solution #3 from Table 5 shall be the
             calibration check standard for LRMS, while Solution #3 from Table 6 or 6A
             shall be the calibration check standard for HRMS.

7.3      INITIAL CALIBRATION

         An  acceptable initial calibration (7.3.8) is required before any samples are
         analyzed, and then intermittently throughout sample analyses as dictated by
         results of the continuing calibration procedures described  in Section 7.4. The
         GC/MS system must be properly calibrated and the performance documented
         during the initial calibration.
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7.3.1        Retention Time Windows
             Before sample analysis, determine the retention time windows during which
             the selected ions will be monitored.  Determine Relative Retention Time
             (RRTs) for each analyte by using the corresponding 2H - labelled standard.

 7.3.2        GC Operating Conditions

             The GC column performance (Section 7.3.5) must be documented during the
             initial calibration.  Table 10 summarizes GC operating conditions known to
             produce acceptable results with the column listed.  The GC conditions must
             be established by  each analyst for the particular instrumentation by injecting
             aliquots of the calibration check standard (7.2.8). It may be necessary to
             adjust the operating conditions slightly based on observations from analysis
             of these solutions. Other columns and/or conditions may be used as long as
             column performance criteria of Section 7.3.5 are satisfied.

             Thereafter the calibration check standard must be analyzed daily to verify the
             performance of the system (Section 7.4).

 7.3.3        GC/MS Tuning Criteria

             A.   Low Resolution Mass Spectrometry

                 Use a compound such perfluorotributylamine (PFTBA) to verify that the
                 intensity of the peaks is acceptable. If PFTBA  is used, mass spectral
                 peak profiles  for m/z  69, 219 and 264 must be recorded, plotted, and
                 reported.  The scan should include a minimum of +/- two peaks (i.e, m/z
                 67-71 for the m/z 69 profile).

             B.   High Resolution Mass Spectrometry

                 Tune the instrument to meet the minimum required resolving power of
                 8,000 at 192.9888 or any other PFK reference signal close to 128.0626
                 (naphthalene). Use peak matching and the chosen PFK reference peak
                 to verify that  the exact mass of m/z 242.9856 is within 5 ppm of the
                 required value. The selection of the low and high mass ions must be
                 such that they provide the largest voltage jump performed in any of the
                 three mass descriptors.

 7.3.4        MS Operating Conditions

             A.   Low Resolution Mass Spectrometry

                 Analyze standards and samples with the mass  spectrometer operating in
                 the Selected Ion Monitoring (SIM) mode with a total cycle time of 1
                 second or less.
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             B.   High Resolution Mass Spectrometry

                 Analyze standards and samples with the mass spectrometer operating in
                 the SIM mode with a total cycle time (including the voltage reset time)
                 of one second or less.

                 A reference compound such as Perfluorokerosene (PFK) must be used to
                 calibrate the SIM mass range.  One PFK ion per mass descriptor is used
                 as a lock-mass ion to correct for mass drifts that occur during the
                 analysis. In addition to the lock-mass ion, several ions  characteristic of
                 PFK are monitored as QC check ions (Table 13).

7.3.5        GC Column Performance Criteria

             A.   The height of the valley between anthracene and phenanthrene at m/z
                 178 or the 2H-analogs at m/z 188 shall not  exceed 50  percent of the
                 taller of the two peaks.

             B.   The height of the valley between benzo(b)fluoranthene  and
                 benzo(k)fluoranthene shall not  exceed 60 percent of the taller of the two
                 peaks.

             If these criteria are not met and normal column maintenance procedures are
             not successful, the column must be replaced and the initial calibration
             repeated.

7.3.6        Mass Spectrometer Performance

             A.   Low Resolution  Mass Spectrometry

                 Verify acceptable sensitivity during initial calibration. Demonstrate that
                 the instrument will achieve a minimum signal-to-noise ratio of 10:1 for
                 the quantitation and confirmation ions when the calibration standard
                 with the lowest concentration  is injected into the GC/MS system.

             B.   High Resolution Mass Spectrometry

                 Record the peak profile of the high mass reference signal (m/z
                 242.9856) obtained during peak matching by using the low-mass PFK
                 ion at m/z 192.9888 (or lower in mass) as a reference.  The minimum
                 resolving power of 8,000 must be demonstrated on the high-mass ion
                 while it is transmitted at a lower accelerating voltage than the low-mass
                 reference ion, which is transmitted at full  sensitivity.

                 The format of the peak profile  representation must allow manual
                 determination of the resolution, that is,  the horizontal axis must be a
                 calibrated mass scale (amu or ppm per division).

                 The peak width  of the high mass ion at 5  percent of the peak height
                 must not exceed 125 ppm in mass.
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7.3.7        Calibration Procedure

             Using stock standards, prepare at least five calibration standard solutions,
             using the same solvent that was used in the final sample extract. Keep the
             recovery standards and the internal standards at fixed concentrations.  Adjust
             the concentrations recommended in Tables 5 and 6, if necessary, to ensure
             that the sample analyte concentration falls within the  calibration range. The
             calibration curve must be described within the  linear range of the method.
             Calibrate the mass spectrometer response using a 2 /;L aliquot of each
             calibration solution. Analyze each solution once.

             Calculate:

             A.   the relative response factors (RRFs) for each analyte as described  in
                  Sections 7.7.1.1, 7.7.1.2, and 7.7.1.3.

             B.   the mean RRFs as required by Section 7.7.1.4.

             C.   the standard deviation (SD) and relative standard  deviation (RSD) as
                  required by Section 7.7.2.

             Report all results as required by Section 10.2.

7.3.8        Criteria for Acceptable Initial Calibration

             An acceptable initial calibration must satisfy the following performance
             criteria:

             A.   The requirements of Sections 7.3.5 and 7.4.6 must be met.

             B.   The signal to noise ratio (S/N) for the GC signals present in every
                  selected ion current profile (SICP) must be  > 10:1 for the labelled
                  standards and unlabelled analytes.

             C.   The percent relative standard deviation for the mean relative response
                  factors  must be no greater than 30 percent for both the unlabelled
                  analytes and internal standards (Section 7.7.2). Otherwise,  take
                  corrective action as required by Section 7.7.2.

7.4      CONTINUING CALIBRATION

         The continuing calibration consists of an analysis of the calibration check
         standard (Section 7.2.8) once during each 12-hour shift as described in  Section
         7.4.1.

         The criteria for acceptable continuing calibration are given  in Section 7.4.2.
         These must be satisfied or else corrective action must be taken as required by
         Section 7.4.2.
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7.4.1        Calibration Check

             The calibration check standard (Section 7.2.8) must be analyzed at the
             beginning and end of each analysis period, or at the beginning of every 1 2-
             hour shift if the laboratory operates during consecutive 12 hour shifts.

             Inject a 2-//L aliquot of the calibration check standard (Section  7.2.8) into the
             GC/MS. Use the same data acquisition parameters as those used during the
             initial calibration.

             Check the retention time windows for each of the compounds.  They must
             satisfy the criterion of Section 7.4.2C

             Check for GC resolution and peak shape. Document acceptable column
             performance as described in Section  7.3.5.  If these criteria are not met, and
             normal column maintenance procedures are unsuccessful, the column must
             be replaced and the calibration repeated.

             Calculate the continuing RRF and ARRF, the relative percent difference (RPD)
             between the daily RRF and the initial calibration mean  RRF as described in
             Section 7.7.1.5.

             Report the results as required by Section 10.2.

7.4.2        Continuing Calibration Performance Criteria

             An acceptable continuing  calibration  must satisfy the following performance
             criteria:

             A.  The signal to noise ratio (S/N) for the GC signals present in the selected
                 ion current profile (SICP) for all labelled and unlabelled standards must
                 be > 10:1.

             B.  The measured RRFs of all analytes (labelled and unlabelled} must be
                 within 30 percent of the mean values established  during the initial
                 calibration. If this criterion is not satisfied, a new initial calibration curve
                 must be established before sample extracts can be analyzed.

             C.  The retention time for any internal standard must not change by more
                 than 30 seconds from the most  recent calibration  check. Otherwise,
                 inspect the chromatographic system for malfunctions and make the
                 necessary corrections. Document acceptable performance with a new
                 initial calibration curve.

7.5      GC/MS ANALYSIS

         The laboratory may proceed with the analysis of samples and blanks only after
         demonstrating acceptable performance as specified in Sections 7.3 and 7.4.

         Analyze standards, field samples and QA samples (Section 8.1) with the gas
         chromatograph and mass spectrometer operating under the conditions
         recommended in Sections 7.3.2 and 7.3.4.

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          Approximately I hr before HRGC/LRMS or HRGC/HRMS analysis, adjust the
          sample extract volume to approximately 500 /;L  This is done by adding 50 fjL of
          the recovery standard spike solution (Section 7.2.5, and Table 4 or 4A) to the
          450 ^L final volume (Section 6.6.2) of the concentrated sample extract give the
          sample extract concentration required by Table 8  or 8A. If the sample volume
          must be changed  to achieve a desired detection limit, the recovery spike solution
          concentration must be adjusted accordingly to achieve the target concentrations
          of Table 8 or 8A.

          Inject a2fjl aliquot of the sample extract (Section 6.6.2) on to  the DB-5
          column. Use the  same volume as that used during calibration.  Recommended
          GC/MS operating  conditions are described in Section 7.3.

          The presence of a given  PAH is qualitatively confirmed if the criteria of Section
          7.6.1 are satisfied.

          The response for any quantitation or confirmation ion in the sample extract must
          not exceed the response of the highest concentration calibration standard.

          Collect, record, and store the data for the calculations required by Sections
          9.1.7, 9.1.8, 9.1.9, and 9.1.10.  Report the results as required by Section 10.2.

 7.6       QUALITATIVE ANALYSIS

 7.6.1        Identification Criteria

 7.6.1.1          Ion  Criteria

                 For  LRMS analysis, all quantitation and confirmation ions (Table  13)
                 must be present.

 7.6.1.2          Relative Retention Time (RRT) Criteria

                 The relative retention time (RRT) of the analyte compared to the RRT for
                 the  2H-standards must be within ±0.008 RRT units of the relative
                 retention  times obtained from the continuing calibration  (or initial
                 calibration if this applies).

 7.6.1.3          Signal to  Noise Ratio

                 The signal to mean noise ratio must be 10:1 for the internal standards.
                 This ratio for the unlabelled compounds must be greater than 2.5 to  1
                 for the quantitation ions for HRMS and for both quantitation and
                 confirmation ions for LRMS.

                 If broad background interference restricts the sensitivity of the GC/MS
                 analysis, the analyst must employ additional cleanup on  the archive
                 sample and reanalyze.
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7.7      QUANTITATIVE ANALYSIS

7.7.1        Relative Response Factors (RRFs)

7.7.1.1          RRF for Unlabelled PAH and Surrogate Standards
                 from Initial Calibration Data

                 Use the results of the calibration and Equation 429-13 to calculate the
                 relative response factors (RRFs) for each calibration compound and
                 surrogate standard in each calibration solution (Tables 5 or 5A).  Table
                 11  shows the assignments of the internal standards for calculation of
                 the RRFs for the calibration solution shown in Table 5. Table 11A
                 shows the assignments of the internal standards for calculation of the
                 RRFs for the calibration solution shown in Table 5A.  Report the results
                 as required by Section  10.2.

7.7.1.2          RRF for Determining Internal Standard Recovery

                 Use the results of the calibration in Equation 429-18 to calculate the
                 relative response factor for each internal standard relative to an
                 appropriate recovery standard. Table 11 shows the assignments of the
                 recovery standards for calculating internal standard recoveries for the
                 calibration solution shown in Table  5.  Table 11A shows the
                 assignments of the recovery standards for calculating internal standard
                 recoveries for the calibration solution shown in  Table 5A.  Report the
                 results as required by Section 10.2.

7.7.1.3          RRF for Determining Alternate Standard Recovery

                 Use the calibration results and Equation 429-19 to calculate the
                 response factor for the alternate standard relative to the appropriate
                 recovery standard. Table 11 shows the assignment of the recovery
                 standards for calculating alternate standard recovery for the calibration
                 solution shown in Table 5. for the calibration solution shown in Table 5.
                 Report the results as required by Section 10.2.

7.7.1.4          Mean Relative Response Factor

                 Use Equation 429-20 to calculate the mean RRF for each compound
                 (unlabelled calibration standards, surrogate standards, internal standards
                 and alternate standard). This is  the average of  the five RRFs calculated
                 for each compound (one RRF calculated for each calibration solution).
                 The mean  RRF may be used if the linearity criterion of Section 7.7.2 is
                 satisfied.
                 Report the results as required by Section 10.2.

7.7.1.5          RRF from Continuing Calibration Data

                 Analyze one or more calibration  standards (one  must be the medium
                 level standard) on each work shift of 12 hours or less. Use Equations
                 429-1 7, 429-18, and 429-19 to calculate the RRFs for each analyte.
                 Use Equation 429-22 to calculate ARRF, the relative percent difference

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                between the daily RRF and the mean RRF calculated during initial
                calibration. Check whether the performance criterion of Section 7.4.2B
                is satisfied. Report the results as required by Section 10.2.

7.7.2       Relative Standard Deviation of Relative Response Factors

            For each analyte, calculate the sample standard deviation (SD) of the RRFs
            used to  calculate the mean RRF. Use Equation 429-21 to calculate the
            percent  relative standard deviation (%RSD) for each analyte.  The analyst
            may use the mean RRF if the percent relative standard deviation of the RRFs
            is 30%  or less. If the RSD requirement is not satisfied, analyze additional
            aliquots of appropriate calibration solutions to obtain an acceptable RSD of
            RRFs  over the entire concentration range, or take action to improve GC/MS
            performance.  Otherwise, use the complete five point calibration curve for
            that compound.

8        QUALITY ASSURANCE/QUALITY CONTROL

         Each laboratory that uses this method is required to operate a formal quality
         control program.  The minimum quality control requirements of this program
         consists of an initial demonstration of laboratory capability (according to
         Sections 7.3 and 8.1.3.1), and periodic analysis of blanks and spiked samples as
         required in Sections 8.1.1 and 8.1.3.2 as a continuing check on performance.

         The laboratory must maintain performance records to document the quality of
         data that  are generated. The results of the data quality checks must be
         compared with the method performance criteria to determine if the analytical
         results meet the performance requirements of the method. The laboratory must.
         generate accuracy statements as described in  Section 8.4.1.

8.1      QA SAMPLES

8.1.1       Laboratory Method Blank

            The analyst must run a laboratory method bfank with each set  of 15 or fewer
            samples. The method blank must be a resin sample from the same batch
            used to  prepare the sampling cartridge and the laboratory control samples.
            The method blank must be prepared and stored as described in
            Sections 4.3.4 and 4.3.5.

            The analyst shall perform all of the same procedures on the method blank as
            are performed on the solid samples (Section 6.5.2.1) from the beginning of
            sample extraction through to the end of the GC/MS analytical procedures.

8.1.2       Performance Evaluation Samples

            The laboratory should analyze performance evaluation samples quarterly
            when  these samples become available.  These samples must be prepared and
            analyzed by the same methods used for the field samples.  Performance for
            the most recent quarter should be reported with the results of the sample
            analysis.
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8.1.3        Laboratory Control Sample (LCS)

8.1.3.1          Initial Demonstration of Laboratory Capability

                 Before  performing sample analyses for the first time, the analyst shall
                 demonstrate the ability to generate results of acceptable precision and
                 accuracy by using the following procedures.

                 Prepare spiking solutions from stock standards prepared independently
                 from those used for calibration.  Spike at least four resin samples
                 cleaned as described in Section  4.2.2 with each of the target unlabelled
                 analytes as indicated in Table 9. Blank resin contamination levels must
                 be no greater than 10 percent of the levels of  the spiked analytes.  Add
                 the amounts of internal standards required by Table 7 or 7A.  Add the
                 alternate standard to the extract to monitor the efficiency of the cleanup
                 procedure.

                 The LCS spikes shall undergo all of the same procedures as are
                 performed on the solid samples  (Section 6.5.1.2) from the beginning of
                 sample extraction through to the end of the GC/MS analytical
                 procedures.

                 Calculate:

                 (A) percent recoveries for the internal  standards and alternate standard,
                 (B) the mass of each target analyte in //g/sample or ng/sample,
                 (C) the average of the results for the four analyses in ^g/sample or
                     ng/sample,
                 (D) the average recovery (R) as a percentage of the amount added,  and
                 (E) the relative standard deviation SR.
                 Report the results as required by Section 10.2.4.

                 If all the acceptance criteria of Section 8.2.6 are satisfied for all of the
                 target PAH, the analyst may begin analysis of  blanks and samples.
                 Otherwise, corrective action must be taken as required by Section 8.2.6.
8.1.3.2          Ongoing Analysis of LCS

                 The analyst must run two laboratory control samples with each set of
                 15 or fewer samples.  The resin for the LCS must be taken from the
                 same batch used to prepare the sampling cartridge and the laboratory
                 method blank.  The LCS resin must be prepared and stored as described
                 in Sections 4.3.4 and 4.3.5.

                 Prepare spiking solutions from stock standards prepared independently
                 from those used for calibration.  Spike each resin sample with each of
                 the target unlabelled analytes as indicated in Table 9. Blank resin
                 contamination levels must be no greater than 10 percent of the levels of
                 the spiked analytes. Add the amounts of internal standards required  by
                 Table 7 or 7A.  Add the alternate standard to the extract to monitor the
                 efficiency of the cleanup procedure.

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                 The LCS spikes shall undergo all of the same procedures as are
                 performed on the solid samples (Section 6.5.1.2) from the beginning of
                 sample extraction through to the end of the GC/MS analytical
                 procedures.

             Calculate:

             (A)  percent recoveries for the internal standards and alternate standard.
             (B)  the mass of each target analyte in /;g/sample or ng/sample,
             (C)  the average of  the results for the two analyses in //g/sample or
                 ng/sample,
             (D)  the average recovery as a percentage of the amount added, and
             (E)  the relative percent difference  for the two analyses.

             Report the results as required by Section 10.2.

             Add the results which satisfy the performance requirements of Section 8.2.6
             to the results of the initial LCS analyses (8.1.3.1) and previous ongoing data
             for each compound  in the LCS sample.

             Update the charts as described in Section 8.4.1.

8.2      ACCEPTANCE CRITERIA

8.2.1        Blank Trains

             The levels of any unlabelled analyte quantified in the blank train must not
             exceed 20 percent of the level of that analyte in the sampling train.  If this
             criterion cannot be met, calculate a reporting limit that is five  times the
             blank value (Equations 429-32 and  429-33). Do not subtract the blank value
             from the sample value.

8.2.2        Surrogate Standard  Recovery

             Acceptable surrogate  (field spike) recoveries should range from 50 to 150
             percent.  If field spike recoveries are not within the acceptable range, this
             must be clearly indicated in the laboratory report. The affected sampling run
             must be identified in the report of the calculated emissions data.

8.2.3        Internal Standard Recovery

             Recoveries for each of the internal standards must be greater than 50
             percent and less than 150 percent of the known value.

             If internal standard recoveries are outside  of the acceptable limits, the signal
             to noise ratio of the internal standard must  be greater than 10.  Otherwise
             the analytical procedure must be repeated on the stored portion of the
             extract.
                                                                                   -*
             NOTE:  This criterion is used to assess method performance.  As this is  an
                    isotope dilution technique, it is, when properly applied, independent
                    of internal standard recovery. Lower recoveries do not necessarily

August 9, 1996                                             Proposed M-429  Page 54

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                     invalidate the analytical results for PAH, but they may result in
                     higher detection limits than are desired.

             If low internal standard recoveries result in detection limits that are
             unacceptable, the cleanup and GC/MS analysis must be repeated with the
             stored portion of the extract. If the analysis of the archive sample gives low
             recoveries and high detection limits, the results  of both analyses must be
             reported.

8.2.4        Laboratory Method Blank

             The laboratory method blank must not contain any of the  target analytes
             listed in Table 1  at levels exceeding the PQL or 5 percent of the analyte
             concentration in the field sample.

             If the method blank is contaminated, check solvents, reagents, standard
             solutions apparatus and glassware to locate and eliminate the source of
             contamination before any more samples are analyzed. Table 3 shows those
             compounds that commonly occur as contaminants in the method  blank, and
             the ranges of concentrations that have been reported.

             If field samples were  processed with a  laboratory method blank that showed
             PAH  levels greater than 5 percent of the field sample, they must be re-
             analyzed using the archived portion of the sample  extract.

             Recoveries of the internal standards must satisfy the requirements of 8.2.3.
             If the internal standard recoveries are less than 50%, the  S/N ratio must be
             greater than 10  for the internal standard.

8.2.5        Performance Evaluation Sample

             The following will be  a requirement when performance evaluation samples
             become available, and performance criteria have been established:

             Performance for the most recent quarter must be reported with the results of
             the sample analysis.  If the performance criteria  (to be established) are not
             achieved, corrective action must be taken and acceptable performance
             demonstrated before sample analysis can be resumed.

8.2.6        Laboratory Control Samples

8.2.6.1      Initial and Ongoing Analysis

             The signal of each analyte in the initial and ongoing laboratory control
             samples must be at least 10 times that of the background.

             Acceptable accuracy  is a percent recovery between 50 and 150 percent.
             Acceptable precision for the initial LCS  samples  is  a relative standard
             deviation (RSD) of 30 percent or less.
             Acceptable precision for the ongoing analysis of duplicate samples is a
             relative percent difference of 50 percent or less.
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             If the RSD for the initial demonstration exceeds the precision limit, or any
             calculated recovery falls outside the range for accuracy, the laboratory
             performance for that analyte is unacceptable.
             If the RPD for any ongoing duplicate analyses exceeds the precision limit, or
             any calculated recovery falls outside the range for accuracy, the laboratory
             performance for that analyte is unacceptable.

             Beginning with Section 8.1 .3.1 , repeat the test for those analytes that failed
             to meet the performance criteria.  Repeated  failure, however, will  confirm a
             general problem with the measurement system.  If this  occurs, locate and
             correct the source of the problem and repeat the test for all compounds of
             interest beginning with Section 8.1.3.1 for the initial analysis and
             Section 8.3.1.2 for the ongoing analysis.

8.3      ESTIMATION OF THE METHOD DETECTION LIMIT (MDL) AND PRACTICAL
         QUANTITATION LIMIT (POL)

8.3.1    Initial Estimate of MDL and PQL

         The analyst shall prepare a batch of XAD-2 resin as described in Sections
         4.2.2. 1 to 4.2.2.3, then check for contamination as required by Section 4.2.2.4.
         Identify those PAH analytes present at background levels that are too high for
         the MDL determination. Use the procedure of Appendix A to calculate MDLs for
         the remaining target PAH compounds.  A suggested  initial spike level for the
         MDL determination is 5 times a theoretical method quantitation limit (TMQL)
         estimated  according to Equation 429-16.
                          TMQL  = Cxx100x2                  429-16
         Where:
         C   =  the concentration of the PAH in the lowest concentration calibration
                standard used in the initial calibration, (ng///L)

         V   =  the final extract volume, (//L)

         P   =  the assumed percent recovery (50%) of the internal standard

         2   =  a factor to account for the fact that the final extract volume (V) contains
                one half of the analyte in the sample. The other half is archived.

8.3.2    Ongoing Estimation of MDL and PQL

         Once every quarter in which this method is used, the analytical laboratory must
         analyze one spiked resin sample as described in Appendix A. Include all initial
         and quarterly results in the calculation of the standard deviation and MDL for
         each analyte that has not been identified as a common contaminant of the
         XAD-2 resin.
August 9, 1996                                             Proposed M-429 Page 56

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         If the MDL for any analyte exceeds the MDL established during the initial
         determination, take corrective action as necessary, and repeat the monthly
         analysis.  If any MDL still exceeds the  initial MDL, then the initial standard
         deviation estimation procedure (Appendix A) must be repeated.

8.4      LABORATORY PERFORMANCE

         The analyst must have documented  standard operating procedures (SOPs) that
         contain specific stepwise instructions for carrying out this method.  The  SOPs
         must be readily available and followed  by all personnel conducting the work.  The
         SOP must be made available for review upon request by the Executive Officer,
         the tester or reviewer of the analytical  results. The analyst may impose
         restrictions on the dissemination of the information in the SOP.

         The analyst must have documented  precision and accuracy statements
         (Section 8.4.1) readily available.

         The analyst must have results of the initial and ongoing estimates of the  MDL
         (Sections  8.3.1 and 8.3.2) readily available.

8.4.1    Precision and Accuracy Statement

         The precision and accuracy statements for the analytical procedure shall, be
         based on the results of the initial and ongoing LCS analyses. The frequency of
         analysis is stated in Section 8.1.3.

         Prepare a  table of the recoveries and the relative percent difference for each
         ongoing analysis of the LCS and LCS duplicate. Figure 15A is an example of
         such  a table. This must be included in the analytical data package submitted for
         each  set of sample analyses.

         Prepare a  quality control chart for each target analyte that provides a  graphic
         representation of continued laboratory  performance for that target analyte.
         Figure 15B is an example QC chart for  benzo(a)pyrene.

9.       CALCULATIONS

         Carry out calculations retaining at least one extra decimal figure beyond that of
         the acquired data.  Round off figures after the final calculation.

9.1      ANALYST'S CALCULATIONS

         The analyst shall carry out the calculations described in Sections 9.1.1 to
         9.1.11.
August 9, 1996                                             Proposed M-429  Page 57

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9.1.1    Relative Response Factors (RRF) for Unlabelled PAH and Surrogate Standards

         Calculate the RRF for each target unlabelled PAH analyte and surrogate standard
         in each calibration solution .  Use Equation 429-17 and the data obtained during
         initial calibration (7.3.7) or continuing calibration (7.4.1).
                                RRF   .  *.«
            Where:

            As  =  Area of the response for characteristic ions of the unlabelled analyte
                   or surrogate standard (Tables 11 or 1 1A, 13, and 14).

            Ajs  =  Area of the response for characteristic ions of the appropriate internal
                   standard (Tables 1 1 or 1 1 A, 13, and  14).

            Qs  =  Amount of the unlabelled PAH calibration analyte or surrogate
                   standard injected on to GC column, ng.

            Qis  =  Amount of the appropriate internal standard injected on to GC column, ng.

9.1 .2    RRF for Determination of Internal Standard Recovery

         Calculate RRFJS according to Equation 429-18, using data obtained from the
         analysis of the calibration standards.

                               RRF,s    A   x  Q                429-18
                                         Ars  *  Qis
           Where:
           Ars  =  Area of the response for characteristic ions of the appropriate
                   recovery standard (Tables 11  or 11 A, 13, and 14).

           Qrs  =  Amount of the appropriate recovery standard injected on to GC
                   column, ng.

9.1.3    RRF for Determination of Alternate Standard Recovery

         Calculate RRFas according to Equation 429-19, using data obtained from the
         analysis of the calibration standards.

                                        A°*   X  Q"              429'19
                                         Ars  *  Qas
           Where:
           Aas  =  Area of tne response for characteristic ions of the alternate standard
                   (Tables 13 and 14).

           Qas  =  Amount of alternate standard injected on to the GC column, ng.

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9.1.4    Mean Relative Response Factors (RRF)

         Calculate the mean RRF for each target unlabelled PAH, surrogate standard,
         internal standard and alternate standard using Equation 429-20 and the RRFs
         calculated according to Sections 9.1.1, 9.1.2, and 9.1.3.

                                        1   n                       429-20
                                HKF  = 1  £ (RRF)j
                                        n  pf


            Where:

            RRFj    =  RRF calculated for calibration solution "i" using one of Equations
                       429-17,429-18 or 429-19.

               n    =  The number of data points derived from the calibration. The
                       minimum requirement is a five-point calibration (Section 7.2.3,
                       Tables 5 and 6 or 6A)

9.1.5    Percent Relative Standard  Deviation (%RSD) of Relative Response Factors

         Use Equation 429-21 to calculate the relative standard deviation of the Relative
         Response Factors for each analyte.

                             %RSD  =  -S-H  x  100%             429-21
         Where:

         RRF  =    Mean relative response factor of a given analyte as defined in
                    Sections 7.7.1 .4 and 9.1 .4.

         SD   =    The sample standard deviation of the relative response factors used
                    to calculate the mean RRF.

9.1.6    Continuing Calibration ARRF

         Use Equation 429-22 to calculate ARRF, the relative percent difference (RPD)
         between the daily RRF and the mean RRF calculated during initial calibration.


                                                 „  ,00%            «9-22
                                       HRF
         Where:

         RRFC   =  The RRF of a given analyte obtained from the continuing calibration
                   {Section 7.4).
August 9, 1996                                            Proposed M-429 Page 59

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 9.1.7    Percent Recovery of Internal Standard, Ris

         Calculate the percent recovery, Ris for each internal standard in the sample
         extract, using Equation 429-23.
                         js  .        *       " _ x  100%
                              Ars  x  FTFTF^  x  Qjs

         Where:

          RRTis =  Mean relative response factor for internal standard (Equations 429-18
                   and 429-20).
 9.1.8    Percent Recovery of Surrogate Standard, R
                                                S3
         Calculate the percent recovery, Rss for each surrogate standard in the sample
         extract, using Equation 429-24.
                       Rss  . _ *      i* _ x  100%
                              Ais  x  HRF;  x QSS
         Where:
         Ass    =  Area of the response for characteristic ions of the surrogate standard
                   (Tables 13 and 14).

         Qss    =  Amount of the surrogate standard added to resin cartridge before
                   sampling, ng.

          RRFS  =  Mean relative response factor for surrogate standard (Equations
                   429-17 and 429-20).

9.1 .9    Percent Recovery of Alternate Standard, R^

         Calculate the percent recovery, Ras for the alternate standard in the sample
         extract, using Equation 429-25.

                      Ras  -       Aas  X °" _ -  x  100%           429'25
                              Ars x  fTRF^  x  Qas

         Where:

          RRFas =  Mean relative response factor for alternate standard (Equations 429-
                   19 and 429-20).
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 9.1.10   Mass of the Target Analytes and Surrogate Standards in
          Emissions Sample or Blank Train

            Use Equation 429-26 to determine the total mass of  each PAH compound or
            surrogate standard in the sample:

            Report the PQL (9.1.11) for those analytes that were not present at levels
            higher than the PQL  provided to the tester prior to testing  (2.3.3).

                                 M   .   QJS x  As                  429-26
                                       AJS x  RRF

          Where:

          M      =  Mass (ng) of surrogate standard (Ms) or target analyte (Mt) detected
                    in the sample.

          Qjs     =  Amount of  internal standard or surrogate standard added to each
                    sample.

          As     =  Area of the response for characteristic ions  of the unlabelled analyte
                    or surrogate standard (Tables 13 and 14).

          Ais     =  Area of the response for characteristic ions  of the appropriate
                    internal standard (Tables 13, and 14).
          RRP    =  Mean relative response factor of a given analyte calculated as
                    required by Sections 7.7.1.4 and 9.1.4.

9.1.11    Analytical Reporting Limit

            The analyst shall report the PQL (Section 2.3.3) for those analytes that were
            not present in the emissions sample or blank train at levels higher than the
            pre-test estimate of the PQL.

9.2       TESTER'S CALCULATIONS

9.2.1     Sample/Blank Train PAH Mass Ratio

          Use Equation 429-27 to calculate the sample/blank train mass ratio for each PAH
          detected at levels above the MOL in both the field sample and the blank train.

                                  RAT,0 .   *                  429'27
                                            MBT

          Where:

          Mt      =  Mass of target PAH analyte detected in the sampling train
                    (Equation 429-26).

          MBT    =  Mass of the same PAH analyte detected in the blank train.


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         If the sample to blank train PAH mass ratio is less than five, calculate the
         reporting limit for the tested source as required by Section 9.2.4.2. Do not
         calculate Mc (Section 9.2.2} or Me (Section 9.2.3) for the emissions report.

9.2.2    PAH Concentration in Emissions

         Use Equation 429-28 to calculate the concentration in the emissions of 1) the
         PAH analytes detected in the sampling train but not in the blank train, and 2) the
         PAH analytes that satisfy the minimum sample to blank train mass ratio required
         by Section 9.2.1.
                                                                   429-28
9.2.3
                           M,
                           Mt
                                                 1
                                  V,
                                   m(std)
                                    0.028317
         Where:
         M
          m(std)
          =  Concentration of PAH in the gas, ng/dscm, corrected to standard
              conditions of 20°C, 760 mm Hg (68°F, 29.92 in. Hg) on dry
              basis.

          =  Mass of PAH compound in gas sample, ng (Equation 429-26)

          =  Volume of gas sample measured by the dry gas meter, corrected
              to standard conditions, dscf (Equation 429-10)
0.028317 =  Factor for converting dscf to dscm.

PAH Mass Emission Rate

Use Equation 429-29 to calculate the mass emission rate for each PAH
compound that satisfies the minimum sample/blank train PAH mass ratio
(Section 9.2.1).
                             Mf
                                    V,
                                      m(std)
                                       "std
                                       ~60~
                                                                429-29
         Where:
          'std
         60
         =  Mass emission rate for PAH analyte, ng/second

         =  Mass of PAH compound in the gas sample, ng (Equation 429-26)

         =  Average stack gas dry volumetric flow rate corrected to standard
            conditions, dscf/min.

         =  Factor for converting minutes to seconds
August 9, 1996
                                                 Proposed M-429  Page 62

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9.2.4    Source Reporting Limit

9.2.4.1  PAH Not Detected in Either Sampling or Blank Train

         Use Equation 429-30 or 429-31 to calculate the reporting limit for those analytes
         that were not detected at levels above the PQL in either the sampling or blank
         train.

                          RL    -   PQL    y      1                  429-30
                             CS  "             0.028317
         Where:
                             RL
                                        PQL
                                es
                                      V
                                        m(std)
                           Qstd
                          "60"
429-31
         RLCS       =  Reporting limit for the tested source, (ng/dscm), corrected to
                       standard conditions of 20°C, 760 mm Hg (68°F, 29-92 in. Hg) on
                       dry basis.

         RLes       =  Reporting limit for the tested source, (ng/sec.).

         0.028317  =  Factor for converting dscf to dscm.
         60        =  Factor for converting minutes to seconds.

9.2.4.2  PAH Detected in Blank Train and Sample/Blank Train Ratio < 5

         If the sample to blank train PAH mass ratio is less than five, then Equation
         429-32 or 429-33 shall be used to calculate the reporting limit for that PAH.
         Where:
         RL
           eb
         M
           BT
                                   5 x MBT
                                   vm(std)
                             1
                             RLeb
                                     5 x MBT
               V
                                       m(std)
                         0.028317
                                                  -60-
                                             429-32
                                             429-33
Reporting limit for the tested source, (ng/dscm), corrected to
standard conditions of 20°C, 760 mm Hg (68°F, 29-92 in. Hg) on
dry basis.

Reporting limit for the tested source, (ng/sec.).

The total mass of that PAH analyte in the field blank train.
August 9, 1996
                                    Proposed M-429 Page 63

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10.      REPORTING REQUIREMENTS

         The source test protocol must contain all the sampling and analytical data
         required by Sections 2.2 to 2.5, 4.2.1.1, and 4.2.2.4, as well as the information
         listed in Sections 10.1 and 10.2 that pertain to identification and quantitation of
         the samples.

         The emissions test report must contain all of the sampling and analytical data
         necessary to calculate emissions values for the target analytes or to demonstrate
         satisfactory performance of the method.

         The end user or reviewer should be able to obtain from the source test report all
         information necessary to recalculate all reported test method results or to verify
         that all required procedures were performed.

         Any deviations from the procedures described in this method must be
         documented in the analytical and sampling report.

10.1     SOURCE TEST PROTOCOL

         At a  minimum, the source test  protocol must include all of the data  required by
         Section 2.2 and the information listed in Sections 10.1.1 through 10.1.4.

10.1.1      Preparation  of Filters

            A.  Manufacturer's lot number for the batch of filters to be used in the test.

            B.  Contamination check of filter (Section 4.2.1.1)

                 (i)  Date of cleaning.
                 (ii) Date of PAH analysis.
                 (iii) Table of results of PAH analysis  required by Section 4.2.1.  The
                    analytical report must include all of the data listed in Section 10.2.

            C.       Storage conditions  prior to the test (4.3.3)

10.1.2      Preparation  of XAD-2 resin

            A.    ID for  the batch to be used in the test.  The same  batch must be used
                 for the sampling train and the laboratory QC samples.

            B.    Contamination check of resin  (Sections 4.2.2.1 to 4.2.2.4)

                 (i)  Date of cleaning.
                 (ii) Date of PAH analysis.
                 (iii) Table of results of PAH analysis  required by Secton  4.2.2.4. The
                    analytical report must include all of the data listed in Section 10.2.

            C.    Addition of surrogate standards to the resin cartridge.

                 (i)  Amount of each compound.
                 (ii)  Date of spiking.

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            D.   Storage conditions prior to the test (Section 4.3.3)

10.1.3     Method Detection Limits and Practical Quantitation Limits

            The MDL and PQL for each target analyte determined as required by Sections
            2.3.2 and 2.3.3.

10.1.4     Target Sampling Parameters

            A.   Source target concentration of each emitted PAH of interest.

            B.   Results of calculations required by Sections 2.5.2 to 2.5.5.

            Figure  9 shows the minimum required calculations of target sampling
            parameters.

10.2     LABORATORY REPORT

          The analyst must generate a laboratory report for each pre-test analysis of the
          sampling  media (Sections  2.3, 4.2.2.1, and 4.2.2.4) and  each post-test analysis
          of the sampling trains and laboratory QC samples.

          A minimum of 7 post-test analyses are required to determine the emissions from
          the source and to document the quality of the emissions data.  These are the
          analyses of three sampling runs, one blank train, one laboratory method blank
          and two laboratory control samples.

          At a minimum, any report (data  package) from the analyst to the tester shall
          contain the information listed in Sections 10.2.1 to 10.2.6 pertaining to
          identification and PAH quantitation of all samples.

10.2.1       Five-point Initial Calibration

             The report of the results of the initial five-point calibration must include the
             data listed in A, B, and C below:

             A.   Mass chromatograms for each initial calibration  solution that show at a
                  minimum:

             (i)   Instrument ID,
             (ii)   laboratory sample ID on each chromatogram.
             (iii)   date and time of GC/MS analysis,
             (iv)   mass of monitored ions for each compound in the calibration solution -
                  unlabelled PAH, internal standard, surrogate standard, alternate
                  standard and recovery standard,
             (v)   retention time for each compound in the calibration solution, and
             (vi)   either peak height or area of the signals observed for the monitored ion
                  masses.
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             B.   A summary table of the data obtained for each initial calibration
                  solution that shows at a minimum:

             (i)   Instrument ID,
             (ii)   laboratory sample ID,
             (iii)  date and time of GC/MS analysis,
             (iv)  retention time for each compound - unlabelled PAH, internal standard.
                  surrogate standard, alternate standard and recovery standard,
             (v)   relative retention time for each unlabelled PAH,
             (vi)  either peak height or area of the signals observed for the monitored ion
                  masses,
             (vii)  the relative response factors for each unlabelled PAH, internal standard,
                  surrogate standard, and alternate standard, and
             (viii) analyst's signature

             Figure 14A is an example of a summary table that contains the minimum
             required information for the analysis of a single calibration solution.

             C.   A summary table that shows at a minimum:

             (i)   Instrument ID,
             (ii)   the date and time of the GC/MS analysis,
             (iii)  the relative response factor (RRF) calculated for each unlabelled PAH,
                  internal standard, surrogate standard, and alternate standard in each
                  calibration solution,
             (iv)  the average relative response factor (RRF) calculated for the five point
                  calibration,
             (v)   the relative standard deviation of the relative response factors, and
             (vi)  the recovery of each internal standard in percent.

             Figure 14B is an example of a report that contains the minimum required
             information for a five point calibration summary.
10.2.2       Continuing Calibration
             The report of the results of a continuing calibration must include the data
             listed in 10.2.2 A,  B, and C below:

             A.   Mass chromatogram that shows at a minimum the information listed in
                  10.2.1  A.

             B.   A summary table of the raw data obtained for the continuing calibration
                  that shows at a minimum, the information listed in 10.2.1 B.

             C.    A summary table that shows at a minimum:

             (i)   the relative response  factor (RRF) for each unlabelled PAH, internal
                  standard, surrogate standard, and alternate standard in the continuing
                  calibration solution,
             (ii)   the average relative response factor (RFTF) for each compound
                  calculated for the five point calibration,
August 9, 1996                                             Proposed M-429  Page 66

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              (iii)   ARRF for each unlabelled PAH, internal standard, surrogate standard.
                  and alternate standard in the continuing calibration solution,
              (iv)  the recovery of each internal standard in percent.

              Figure 14C is an example of a summary report that contains the minimum
              information required by Section 10.2.2C for the analysis of the continuing
              calibration solution.

 10.2.3       Laboratory Method Blank

              The laboratory report of the results of the analysis of the method blank must
              include at a minimum the data listed  in 10.2.3 A, B, and C below:

              A.   Mass chromatograms that show at a minimum the information listed in
                  10.2.1 A.

              B.   A summary table of the data obtained for each method blank that
                  shows at a minimum, the information listed in 10.2.5 B.

              C.   A summary table that reports the same data as listed in 10.2.5 C
                  below.

 10.2.4       Laboratory Control Samples

              The report of  the results of the analysis of the LCS samples must include at
              a minimum the data listed in 10.2.4 A, B, and C below:

              A.   Mass chromatograms that show at a minimum the information listed in
                  10.2.1 A.

              B.   A summary table of the raw data for each sample that shows at a
                  minimum, the information listed in 10.2.1 B, and in addition:

              (i)   Client's sample ID
              (ii)   mass of  each analyte,
              (iii)  the recovery of each internal standard, and alternate standard.

              Figure  16A is  an example of a summary table that contains the minimum
              information required by 10.2.4 B.

              C.   A summary table that reports for the two LCS analyses:

              (i)   client's sample ID,
              (ii)   sample matrix description,
              {iii)  date of cleaning  of the XAD-2 resin,
              (iv)  lot number for the resin (resin for all field samples and QA samples
                  must come from the same lot),
             (v)   date of extraction of LCS samples,

             Figure  15A is  an example of a summary table that contains the minimum
             information required by 10.2.4 C.
Augusts, 1996                                             Proposed M-429 Page 67

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10.2.5       Emissions Samples
             The report of the results of the analyses of the three sampling trains and the
             blabk train must include the data listed in 10.2.5 A, B, and C below:

             A.   Mass chromatograms that show at a minimum the information listed in
                  10.2.1  A, and in addition,

             (i) client's sample ID

             B.   A summary table of the data for the analysis of each sample that
                  shows at a minimum, the information listed in 10.2.1 B, and in
                  addition,

             (i)   client's sample ID
             (ii)   Date of five point initial calibration (ICAL)
             (iii)   ICAL ID,
             (iv)   mass of each analyte,
             (v)   the recovery of each internal standard, alternate standard and surrogate
                  standards in percent.

             Figure 16A is an  example of a summary table that contains the minimum-
             information required by 10.2.5 B.

             C.   A summary table that reports:

             (i)   client's sample ID (from a chain of custody record submitted by the
                  tester),
             (ii)   sample  matrix description,
             (iii)   date of cleaning of the XAD-2 resin,
             (iv)   lot number for the resin (resin for all field samples and QA samples
                  must come from the same lot),
             (ii)   date of  submittal of the tester's samples
             (v)   date of  extraction of samples,
             (vi)   Initial calibration Run ID,
             (vii)  Continuing calibration ID

             Figure 16B is an example of a summary table that contains the minimum
             information required by 10.2.5C.
10.2.6       Data Flags
             The laboratory report must include an explanation of any qualifiers that are
             used to indicate specific qualities of the data.
10.3     EMISSIONS TEST REPORT
         The emissions test report should include narrative that describes how the test
         was done. The tester's report must also include all the appropriate sections used
         in a report from a Method 5 test such as a description of the plant process,
         sampling port locations, control equipment, fuel being used, general plant load


August 9, 1996                                             Proposed M-429  Page 68

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         conditions during the test (description of plant production equipment problems,
         etc.), and anything else necessary to characterize the condition being tested.

         The tester's report must also include all of the information listed in Sections
         10.3.1 to 10.3.4.

10.3.1        Tester's Summary of Analytical Results

              The tester must summarize the results of the minimum seven analyses
              required for each source test. At a minimum, the summary must contain the
              information listed in Figure 17A including all data flags.

              The tester must obtain the detailed analytical results (Section 10.2) from the
              laboratory and include them in the appendices as required below.

10.3.2        Field Data Summary

              The report from the tester to the end user must contain a field data
              summary.  This summary must include at a minimum a table of the results of
              the calculations required by Section 4.5. as well as the values which were
              used to calculate the reported results. Figure 17B is an example of a field
              data summary that contains the minimum required information.

10.3.3        PAH Emissions Results

              Figure 17C show the calculations of the  concentrations and mass emission
              rates of the target PAH. The reviewer should be able to use the data in
              Figures 17A and 17B to check the calculations in Figure 17C.  The reviewer
              should also be able to check the appendix to the report to determine the
              accuracy and the quality of the data summarized by the tester in Figures
              17Aand 17B.

10.3.4        Appendix to the Emissions Test Report

              At a minimum, the following raw data or signed copies must be included in
              an appendix to the emissions test report.

              A.   Record of data for sample site selection and minimum  number of
                  traverse points.

              B.   Moisture determination for isokinetic settings.

              C.   Velocity traverse data.

              D.   Gas analysis for determination of molecular weight.

              E.   Calibration records.

              F.   Method 429 sampling run sheets.

              G.   PAH laboratory reports listed in Section 10.2


August9, 1996                                             Proposed M-429  Page 69

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         The information listed above is to be considered as the minimum that should be
         included to characterize a given operating condition. The end user or the
         executive officer may require additional information for any given project.

 11.      BIBLIOGRAPHY

 11.1        U.S. Environmental Protection Agency/Office of Water Engineering and
            Analysis Division (4303), Washington D.C., Method 1613. Tetra-through
            Octa-Chlorinated Dioxins and Furans by Isotope Dilution HRGC/HRMS.
            EPA821-B-94-005. (1994).

 11.2        U.S. Environmental Protection Agency/Office of Solid Waste, Washington
            D.C., Method 3611 A. Alumina Column Cleanup and Separation of Petroleum
            Wastes. In "Test Methods for Evaluating Solid Waste-Physical/Chemical
            Methods" SW-846 (1986).

 11.3        U.S. Environmental Protection Agency/Office of Solid Waste, Washington
            D.C., Method 3630B.  Silica Gel Cleanup.  In "Test Methods for Evaluating
            Solid Waste-Physical/Chemical Methods" SW-846 (1986).

 11.4        Thomason, J.R., ed., Cleaning of Laboratory Glassware. Section 3, A, pp 1-7
            in "Analysis of Pesticide Residues in Human and Environmental Samples",
            Environmental Protection Agency, Research Triangle Park, N.C. (1974).

 11.5        ARB Method 428. Determination of Polychlorinated Dibenzo-p-dioxin (PCDD)
            and Polychlorinated Dibenzofuran (PCDF) Emissions From Stationary Sources.
            September,  1990.

 11.6        U. S. Environmental Protection Agency, Method 1625 Revision B -
            Semivolatile Organic Compounds by Isotope Dilution. 40 CFR Ch.1 (7-1-95
            Edition) Pt. 136, App. A.

 11.7        Rom, Jerome J., Maintenance, Calibration, and Operation of  Isokinetic Source
            Sampling Equipment. Environmental Protection Agency. Research Triangle
            Park,NC.  APTD-0576. March, 1972.

 11.8        Shigehara, R.T., Adjustments in the EPA Nomograph for Different Pitot Tube
            Coefficients and Dry Molecular Weights.  Stack Sampling News, 2: 4-11.
            October, 1974

 11.9        "Prudent Practices in the Laboratory.  Handling and Disposal  of Chemicals,"
            National Academy Press. Washington D.C.  1995.
August 9, 1996                                            Proposed M-429  Page 70

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                                     TABLE 1
                         METHOD 429 TARGET ANALYTES
                                 Naphthalene
                                 2-Methylnaphthalene
                                 Acenaphthene
                                 Acenaphthylene
                                 Fluorene
                                 Phenanthrene
                                 Anthracene
                                 Fluoranthene
                                 Pyrene
                                 Benzo(a)anthracene
                                 Chrysene
                                 Benzo(b)fluoranthene
                                 Ben2o(k)fluoranthene
                                 Benzo(e)pyrene
                                 Benzo(a)pyrene
                                 Perylene
                                 Indenod ,2,3-cd)pyrene
                                 Dibenz(a,h)anthracene
                                 Benzo(ghi)perylene
Augusts, 1996                                           Proposed M-429  Page 71

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                                TABLE 2




              PRACTICAL QUANTITATION LIMITS FOR TARGET PAHs
Naphthalene
2-MethylnaphthaIene
Acenaphthene
Acenaphthylene
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Benzo(a)anthracene
Chrysene
Benzo(b)fiuoranthene
Benzo(k)fluoranthene
Benzo(e)pyrene
Benzo(a)pyrene
Perylene
lndeno{ 1 ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
LRMS
(/yg/sample)
/. ao
244
1.25
0.210
0.104
0.207
0.85
0.146
0.346
0.191
0.167
0.272
1.119
0.738
0.146
0.191
0.143
0.798
0.465
0.305
HRMS
(ng/sample)
480
66
5.0
5.0
16.5
22
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
370
19
5.0
5.0
5.5
14
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
August 9, 1996
Proposed M-429  Page 72

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                                                  TABLE 3




                        PAH ANALYSIS BY HRMS OF DIFFERENT LOTS OF CLEANED RESIN

PAH ANALYTES
Naphthalene
CONCENTRATION (ng/sample)
SAMPLE
A,
480
2-Methylnaphthalene j 65
Acenaphthylene
Acenaphthene
< 5.0
< 5.0
Fluorene j 16.5
Phenanthrene
Anthracene
22
< 5.0
A2
220
32
A3
198
38
< 5.0 < 5.0
< 5.0
n 	 ».»«•*•*»•.
9.8
16
< 5.0
< 5.0
A4
120
15.6
< 5.0
< 5.0
A5
350
32
< 5.0
< 5.0
13 j < 5.0 | 5.7
A6
340
15.6
< 5.0
< 5.0
— •
32 j<12.5" I 14 j 14.8
i j : :
< 5.0 j < 5.0
Fluoranthene | < 5.0 j < 5.0 < 5.0
Pyrene j < 5.0 | < 5.0 j < 5.0
Benzo(a)anthracene ! < 5.0 ! < 5.0 < 5.0
i i
Chrysene
Benzo(b)fluoranthene
< 5.0
< 5.0
Benzo(k)fluoranthene j < 5.0
Benzo(e)pyrene j < 5.0
Benzo(a)pyrene
Pery'ene
lndeno{1.2,3-cd)pyrene
Dibenzo(a,h)anthracene
Benzo(g,h,i)perylene
< 5.0
:
j < 5.0
| < 5.0
| .
j < 5.0
:
| < 5.0
! < 5.0
< 5.0 | < 5.0
< 5.0 | < 5.0
! < 5.0
i . 	
<5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
! < 5.0
< 5.0
| < 5.0 j < 5.0
| < 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0 j < 5.0
:
IDENTIFICATION
A7 | A8 | A9
320
32
< 5.0
360 I 370
!
26 ! 19
A10 JA11 |A12 |A13
380 340 520 220
45 15 32 48
< 5.0 | < 5.0 I < 5.0 < 5.0 < 5.0 < 5.0
< 5.0 i < 5.0 | < 5.0
7.4
16
< 5.0 < 5.0 < 5.0 < 5.0
5.8 I 5.5 I 10 5.5 6.8 5.0
i :
12 | 14
24 13 <13.0' 14
< 5.0 ! < 5.0 ! < 5.0 < 5.0 j < 5.0 I < 5.0 < 5.0 < 5.0 < 5.0
! i i : i
< 5.6 < 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0

-------
                                      TABLE 4

                  COMPOSITION OF THE SAMPLE SPIKING SOLUTIONS
     Spiking
     Solutions
Analytes
                                                            Concentration
LRMS
HRMS
        1.       Surrogate Standards

                 d10-Fluorene
                 d14-Terphenvl

        2.       Internal Standards

                 d8-Naphthalene
                 d10-2-Methylnaphthalene
                 dg-Acenaphthylene
                 d10-Phenanthrene
                 d10-Fluoranthene
                 d 12-Benzo(a)anthracene
                 d12-Chrysene
                 d 12-Benzo(b)f luoranthene
                 d 12-Benzo(k)f luoranthene
                 d12-Benzo(a)pyrene
                 d12-Perylene
                 d12-lndeno(1,2,3,c-d)pyrene
                 d14-Dibenz(a,h)anthracene
                 d12-Benzo(ghi)perylene
                                      1.0
                                      1.0
                                      1.0
                                      1.0
                                      1.0
                                      1.0
                                      1.0
                                      1.0
                                      1.0
                                      1.0
                                      1.0
                                      1.0
                                      1.0
                                      1.0
                                      1.0
                                      1.0
              250
              250
              100
              100
              100
              100
              100
              100
              100
              200
              200
              200
              200
              200
              200
              200
        3.       Alternate Standard

                 d10-Anthracene

        4.       Recovery Standards

                 d10-Acenaphthene
                 d10-Pyrene
                 d 1 2-benzo(e)pyrene
                                      1.0
                                    20.0
                                    20.0
                                    20.0
              100
            2000
            2000
            2000
August 9, 1996
                                      Proposed M-429 Page 74

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                                      TABLE 4A

             COMPOSITION OF ALTERNATIVE SAMPLE SPIKING SOLUTIONS
       Spiking
       Solutions
   Analytes
                                                           Concentration
P9///I
HRMS
          1A.
          2A.
Surrogate Standards


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                                TABLE 5

      CONCENTRATIONS OF PAHs IN WORKING GC/MS CALIBRATION STANDARD
            SOLUTIONS FOR LOW RESOLUTION MASS SPECTROMETRY
CONCENTRATIONS (ng///L)
Solutions

Calibration Standards
Naphthalene
2-Methyl naphthalene
Acenaphthene
Acenaphthylene
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Benzo(a)anthracene
Chrysene
Benzo(b)fluoranthene
Benzo(k)fluoranthene
Benzo(e)pyrene
Benzo(a)pyrene
Perylene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
Internal Standards
d8-Naphthalene
d10-2-Methylnaphthalene
d8-Acenaphthylene
d10-Phenanthrene
d10-Fluoranthene
d12-Benzo(a)anthracene
d12-Chrysene
d T 2-Benzo(b)f luoranthene
d ! 2-Benzo{k)f luoranthene
d12-Benzo(a)pyrene
d12-Perylene
d12-lndeno(1 ,2,3,c-d)pyrene
d14-Dibenz(a,h)anthracene
d T 2-Benzo(ghi)perylene
1

0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25
0.25

1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
2

0.5
0.5
0.5
0.5
0.5
0.5
0.5
0.5
0.5
0.5
0.5
0.5
0.5
0.5
0.5
0.5
0.5
0.5
0.5

1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
3

1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0

1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
4

2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.5
2.5

1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
5

5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0
5.0

1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
August 9, 1996
Proposed M-429 Page 76

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                                TABLE 5 (CONT)

       CONCENTRATIONS OF PAHs IN WORKING GC/MS CALIBRATION STANDARD
              SOLUTIONS FOR LOW RESOLUTION MASS SPECTROMETRY
                                              CONCENTRATIONS (ng///L)

                                                      Solutions
Surrogate Standards
d10-Fluorene
dm-Terphenyl
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
        Alternate Standard

        d10-Anthracene

        Recovery Standards

        d10-Acenaphthene
        d10-Pyrene
        d12-benzo(e)pyrene
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
1.0
August 9, 1996
                                                     Proposed M-429  Page 77

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                                TABLE 6

      CONCENTRATIONS OF PAHs IN WORKING GC/MS CALIBRATION STANDARD
             SOLUTIONS FOR HIGH RESOLUTION MASS SPECTROMETRY
CONCENTRATIONS (pg/j/L)
Solutions

Calibration Standards
Naphthalene
2-Methylnaphthalene
Acenaphthylene
Acenaphthene
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Benzo(a)anthracene
Chrysene
Benzo(b)fluoranthene
Benzo(k)fluoranthene
Benzo(e)pyrene
Benzo(a)pyrene
Perylene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
Internal Standards
d8-Naphthalene
dgMethylnaphthalene
dg-Acenaphthylene
d ^-Phenanthrene
diQ-Fluoranthene
d12-Benzo(a)anthracene
d12-Chrysene
d ! 2-Benzo(b)f luoranthene
d12-Benzo(k)fluoranthene
d 1 2-Benzo(a)pyrene
d12-Perylene
d12-lndeno(1 ,2,3,c-d)pyrene
d14-Dibenz(a,h)anthracene
d 1 2-Benzo(ghi)perylene
1

10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10

100
100
100
100
100
100
100
200
200
200
200
200
200
:200
2

50
50
50
50
50
50
50
50
50
50
50
50
50
50
50
50
50
50
50

100
100
100
100
100
100
100
200
200
200
200
200
200
200
3

100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100

100
100
100
100
100
100
100
200
200
200
200
200
200
200
4

200
200
200
200
200
200
200
200
200
200
200
200
200
200
200
200
200
200
200

100
100
100
100
100
100
100
200
200
200
200
200
200
200
5

500
500
500
500
500
500
500
500
500
500
500
500
500
500
500
500
500
500
500

100
100
100
100
100
100
100
200
200
200
200
200
200
200
Augusts, 1996
Proposed M-429 Page 78

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                               TABLE 6 (CONT)

       CONCENTRATIONS OF PAHS IN WORKING GC/MS CALIBRATION STANDARD
             SOLUTIONS FOR HIGH RESOLUTION MASS SPECTROMETRY
                                            CONCENTRATIONS (pg/^L)

                                                    Solutions
Surrogate Standards
d10-Fluorene
du-Terphenyl

100
100

100
100

100
100

100
100

100
100
        Alternate Standard

        d10-Anthracene                100     100     100     100     100

        Recovery Standards

        d10-Acenaphthene             200     200     200     200     200
        d10-Pyrene                   200     200     200     200     200
        d12-benzo(e)pyrene             200     200     200     200     200
August 9, 1996                                       Proposed M-429  Page 79

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                               TABLE 6A

     CONCENTRATIONS OF PAHs IN ALTERNATIVE WORKING GC/MS CALIBRATION
        STANDARD SOLUTIONS FOR HIGH RESOLUTION MASS SPECTROMETRY
CONCENTRATIONS (pg/^L)
Solutions

Calibration Standards
Naphthalene
2-Methylnaphthalene
Acenaphthylene
Acenaphthene
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Benzo(a)anthracene
Chrysene
Benzo(b)fluoranthene
Benzo(k)fluoranthene
Benzo(e)pyrene
Benzo(a)pyrene
Perylene
Indenod ,2,3-cd)pyrene
Dibenz(a,h)anthracene
Benzo(ghi)perylene
Internal Standards
da-Naphthalene
d8-Acenaphthylene
d10-Acenaphthene
d10-Fluorene
d10-Phenanthrene
d10-Fluoranthene
d12-Benzo(a)anthracene
d12-Chrysene
d 1 2-Benzo(b)f luoranthene
d 1 2-Benzo(k)f luoranthene
d12-Benzo(a)pyrene
d12-lndeno(1 ,2,3,c-d)pyrene
d14-Dibenz(a,h)anthracene
d12-Benzo(ghi)perylene
1

10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10
10

100
100
100
100
100
100
100
100
200
200
200
200
200
200
2

50
50
50
50
50
50
50
50
50
50
50
50
50
50
50
50
50
50
50

100
100
100
100
100
100
100
100
200
200
200
200
200
200
3

100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100
100

100
100
100
100
100
100
100
100
200
200
200
200
200
200
4

200
200
200
200
200
200
200
200
200
200
200
200
200
200
200
200
200
200
200

100
100
100
100
100
100
100
100
200
200
200
200
200
200
5

500
500
500
500
500
500
500
500
500
500
500
500
500
500
500
500
500
500
500

100
100
100
100
100
100
100
100
200
200
200
200
200
200
August 9, 1996
Proposed M-429 Page 80

-------
                              TABLE 6A  (CONT)

     CONCENTRATIONS OF PAHs IN ALTERNATIVE WORKING GC/MS CALIBRATION
        STANDARD SOLUTIONS FOR HIGH RESOLUTION MASS SPECTROMETRY
                                            CONCENTRATIONS (pg//yL)

                                                    Solutions
       Surrogate Standards

       d12-benzo(e)pyrene             100    100     -100     100     100
       du-Terphenyl                 100    100     100     100     100

       Alternate Standard

       d10-Anthracene                100    100     100     100     100

       Recovery Standards

       d10-2-Methylnaphthalene        200    200     200     200     200
       d10-Pyrene                   200    200     200     200     200
       d12-Perylene                  200    200     200     200     200
August 9,1996                                       Proposed M-429  Page 81

-------
                                 TABLE 7




                    SPIKE LEVELS FOR LABELLED STANDARDS
Time of
Addition
Before
sampling


Before
extraction














Before
extraction

Before
GC/MS



Analyte
Surrogate Standards

d10-Fluorene
d14-Terphenyl
Internal Standards

dg-Naphthalene
d10-2-Methylnaphthalene
d8-Acenaphthylene
d10-Phenanthrene
d10-Fluoranthene
d12-Benzo(a)anthracene
d12-Chrysene
d i 2-Benzo(b)f luoranthene
d 1 2-Benzo(d)f luoranthene
d12-Benzo(a)pyrene
d12-Perylene
d12-lndeno(1 ,2,3,c-d)pyrene
d-,4-Dibenz(a,h)anthracene
d 1 2-Benzo(ghi)perylene
Alternate Standard

d10-Anthracene
Recovery Standards

d10-Acenaphthene
d10-Pyrene
d12-benzo(e)pyrene
LRMS
(pg/sample)


2.0
2.0


2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0


2.0


1.0
1.0
1.0
HRMS
(ng/sample)


500
500


200
200
200
200
200
200
200
400
400
400
400
400
400
400


200


100
100
100
August 9. 1996
Proposed M-429 Page 82

-------
                                   TABLE 7A

   SPIKE LEVELS FOR LABELLED STANDARDS FOR ALTERNATIVE HRMS SPIKING SCHEME
        Time of
        Addition
     Analyte
  HRMS
(ng/sample)
         Before
         sampling
         Before
         extraction
        Before
        extraction
        Before
        GC/MS
Surrogate Standards

d12-benzo(e)pyrene
d14-Terphenyl

Internal Standards

d8-Naphthalene
d8-Acenaphthylene
d10-Acenaphthene
d10-Fluorene
d10-Phenanthrene
d10-Fluoranthene
d12-Benzo(a)anthracene
d12-Chrysene
d 12-Benzo(b)f luoranthene
d 12-Benzo(d)f luoranthene
d! 2-Benzo(a)pyrene
d12-lndeno(1,2,3,c-d)pyrene
du-Dibenz(a,h)anthracene
d! 2-Benzo(ghi)perylene

Alternate Standard

d10-Anthracene

Recovery Standards

d 10-2-Methylnaphthalene
d10-Pyrene
d12-Perylene
                                                             500
                                                             500
                                                             200
                                                             200
                                                             200
                                                             200
                                                             200
                                                             200
                                                             200
                                                             200
                                                             400
                                                             400
                                                             400
                                                             400
                                                             400
                                                             400
                                                             200
                                                             100
                                                             100
                                                             100
Augusts, 1996
                                                         Proposed M-429 Page 83

-------
                                    TABLE 8

    TARGET CONCENTRATIONS FOR LABELLED STANDARDS IN SAMPLE EXTRACT1
                                               LRMS
              P9///I
              HRMS
        Surrogate Standards

        d10-Fluorene
        du-Terphenyl

        Internal Standards

        d8-Naphthalene
        d10-2-Methylnaphthalene
        d8-Acenaphthylene
        d10-Phenanthrene
        d10-Fluoranthene
        d -| 2-Benzo(a)anthracene
        d12-Chrysene
        d 12-Benzo(b)f luoranthene
        d 12-Benzo(k)f luoranthene
        d12-Benzo(a)pyrene
        d12-Perylene
        d ! 2-lndeno( 1,2,3,c-d)pyrene
        d 14-Dibenz(a,h)anthracene
        d T 2-Benzo(ghi)perylene

        Alternate Standard

        d10-Anthracene

        Recovery Standards

        d10-Acenaphthene
        d10-Pyrene
        d12-benzo(e)pyrene
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
1.0
1.0
1.0
1.0
500
500
200
200
200
200
200
200
200
400
400
400
400
400
400
400
200
200
200
200
   1 Assuming 100 percent recovery.
August 9, 1996
      Proposed M-429  Page 84

-------
                                   TABLE 8A
    TARGET CONCENTRATIONS FOR LABELLED STANDARDS IN SAMPLE EXTRACT
              OBTAINED WITH ALTERNATIVE HRMS SPIKING SCHEME1
                                                          P9///I
                                                         HRMS
           Surrogate Standards

           d12-benzo(e)pyrene                               500
           du-Terphenyl                                    500

           Internal Standards

           d8-Naphthalene                                  200
           d8-Acenaphthylene                               200
           d10-Acenaphthene                                200
           d10-Fluorene                                     200
           d10-Phenanthrene                                200
           d10-Fluoranthene                                 200
           d12-Benzo(a)anthracene                           200
           d12-Chrysene                                    200
           d12-Benzo(b)fluoranthene                          400
           d12-Benzo(k)fluoranthene                          400
           d12-Benzo(a)pyrene                               400
           d12-lndeno(1,2,3,c-d)pyrene                        400
           d14-Dibenz(a,h)anthracene                         400
           d12-Benzo(ghi)perylene                            400

           Alternate Standard

           d10-Anthracene                                  200

           Recovery Standards

           d10-2-Methylnaphthalene                          200
           d10-Pyrene                                      200
           d12-Perylene                                     200
   1 Assuming 100 percent recovery.
August 9. 1996                                        Proposed M-429 Page 85

-------
                                   TABLE 9

   CONCENTRATIONS OF COMPOUNDS IN LABORATORY CONTROL SPIKE SAMPLE
                                                    ng/sample
                                              LRMS
             HRMS
        Unlabelled Compounds

        Naphthalene
        2-Methylnaphthalene
        Acenaphthylene
        Acenaphthene
        Fluorene
        Phenanthrene
        Anthracene
        Fluoranthene
        Pyrene
        Benzo(a)anthracene
        Chrysene
        Benzo(b)fluoranthene
        Benzo(k)fluoranthene
        Benzo(e)pyrene
        Benzo{a)pyrene
        Perylene
        IndenoCI ,2,3,c-d)pyrene
        Dibenz(a,h)anthracene
        Benzo(ghi)perylene

        Alternate Standard

        d10-Anthracene
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
2.0
1000
 200
 200
 200
 200
 500
 200
 200
 200
 200
 200
 200
 200
 200
 200
 200
 200
 200
 200
2.0
 200
August 9, 1996
      Proposed M-429 Page 86

-------
                                   TABLE 10
               RECOMMENDED GAS CHROMATOGRAPHIC OPERATING
                        CONDITIONS FOR PAH ANALYSIS
          Column Type

          Length (m)

          ID (mm)

          Film Thickness (//m)

          Helium Linear Velocity (cm/sec)

          Injection mode

          Splitless Time (sec)

          Initial Temperature (°C)

          Initial Time (min)

          Program  Rate (°C/min)

          Final Temperature (°C)

          Final Hold Time


          Injector Temperature (°C)
DB-5

30

0.25

0.32

30

Splitless

30

45

4

8

300

until benzo(ghi)
perylene has eluted

320
August 9, 1996
                                                    Proposed M-429 Page 87

-------
                                    TABLE 11
        ASSIGNMENTS OF INTERNAL STANDARDS FOR CALCULATION OF RRFs
        AND QUANTITATION OF TARGET PAHs AND SURROGATE STANDARDS
            Analyte
Internal Standards
          Unlabeled PAH
          Naphthalene
          2-Methylnaphthalene
          Acenaphthylene
          Acenaphthene
          Fluorene
          Phenanthrene
          Anthracene
          Fluoranthene
          Pyrene
          Benzo(a)anthracene
          Chrysene
          Benzo(b)fluoranthene
          Benzo(k)fluoranthene
          Benzo(e)pyrene
          Benzo(a)pyrene
          Perylene
          Indenod ,2,3-cd)pyrene
          Dibenz(a,h)anthracene
          Benzo(ghi)perylene

          Surrogate  Standards
          d10-Fluorene
          d-|4-Terphenyl
d8-Naphthalene
d-iQ-2-Methylnaphthalene
dg-Acenaphthylene
da-Acenaphthylene
d10-Phenanthrene
d10-Phenanthrene
d10-Phenanthrene
d-iQ-Fluoranthene
d10-Fluoranthene
d } 2-Benzo(a)anthracene
d12-Chrysene
d T 2-Benzo(b)f luoranthene
di 2-Benzo(k)f luoranthene
d12-Benzo(a)pyrene
di 2-Benzo(a)pyrene
d12-Perylene
d12-lndeno(1,2,3,c-d)pyrene
d14-Dibenz(a,h)anthracene
d T 2-Benzo(ghi)perylene
d10-Phenanthrene
d10-Fluoranthene
August 9. 1996
     Proposed M-429  Page 88

-------
                                  TABLE 11A

        ASSIGNMENTS OF INTERNAL STANDARDS FOR CALCULATION OF RRFs
        AND QUANTITATION OF TARGET PAHs AND SURROGATE STANDARDS
                   USING ALTERNATIVE HRMS SPIKING SCHEME
          Analyte
    Internal Standards
        Unlabeled PAH
         Naphthalene
         2-Methylnaphthalene
         Acenaphthylene
         Acenaphthene
         Fluorene
         Phenanthrene
         Anthracene
         Fluoranthene
         Pyrene
         Benzo(a)anthracene
         Chrysene
         Benzo(b)fluoranthene
         Benzo(k)f luoranthene'
         Benzo(e)pyrene
         Benzo(a)pyrene
         Perylene
         IndenoCI ,2,3-cd)pyrene
         Dibenz(a,h)anthracene
         Benzo(ghi)perylene

         Surrogate Standards
         d14-Terphenyl
         d12-Benzo(e)pyrene
dg-Naphthalene
d10-Acenaphthene
dg-Acenaphthylene
d! g-Acenaphthene
d10-Fluorene
d10-Phenanthrene
d10-Phenanthrene
d10-Fluoranthene
d10-Fluoranthene
d12-Benzo(a)anthracene
d12-Chrysene
d12-Benzo(b)fluoranthene
d 12-Benzo(k)f luoranthene
d12-Benzo(a)pyrene
d12-Benzo(a)pyrene
d12-Benzo(a)pyrene
d12-lndeno(1,2,3,c-d)pyrene
d14-Dibenz(a,h)anthracene
d12-Benzo{ghi)perylene
d10-Fluoranthene
d 12-Benzo(a)pyrene
August9, 1996
         Proposed M-429 Page 89

-------
                                    TABLE 12
          ASSIGNMENTS OF RECOVERY STANDARDS FOR DETERMINATION
              OF PERCENT RECOVERIES OF INTERNAL STANDARDS AND
                           THE ALTERNATE STANDARD
                Analyte
Recovery Standard
             Internal Standards

             dg-Naphthalene

             d10 -2-Methylnaphthalene

             d8-Acenaphthylene

             d-|0-Phenanthrene

             d-jQ-Fluoranthene

             d12-Benzo(a)anthracene

             d12-Chrysene

             d ! 2-Benzo(b)f luoranthene

             d 12-Benzo(k)f luoranthene

             d12-Benzo(a)pyrene

             d12-Perylene

             d12-lndeno{1,2,3,c-d)pyrene

             d14-Dibenz(a,h)anthracene

             dj 2-Benzo(ghi) perylene


             Alternate Standard

             d10-Anthracene
d10-Acenaphthene

d-iQ-Acenaphthene

d10-Acenaphthene

d10-Pyrene

d10-Pyrene

d10-Pyrene

d10-Pyrene

di2-Benzo(e)pyrene

d 12-Benzo(e)pyrene

  d12-Benzo(e)pyrene

d 12-Benzo(e)pyrene

d12-Benzo(e)pyrene

d12-Benzo(e)pyrene

d12-Benzo(e)pyrene
d10-Pyrene
August 9, 1996
   Proposed M-429 Page 90

-------
                                  TABLE 12A

        ASSIGNMENTS OF RECOVERY STANDARDS FOR DETERMINATION OF
      PERCENT RECOVERIES OF INTERNAL STANDARDS AND THE ALTERNATE
             STANDARD USING ALTERNATIVE HRMS SPIKING SCHEME
            Analyte
Recovery Standard
         Internal Standards

         dg-Naphthalene

         d10 -2-Methylnaphthalene

         dg-Acenaphthylene

         d10-Phenanthrene

         djQ-Fluoranthene

         d 12-Benzo(a)anthracene

         d12-Chrysene

         d12-Benzo(b)fluoranthene

         d12-Benzo(k)fluoranthene

         d12-Benzo(a)pyrene

         d12-Perylene

         d12-lndeno(1,2,3,c-d)pyrene

         d14-Dibenz(a,h)anthracene

         d12-Benzo{ghi)perylene


         Alternate Standard

         d10-Anthracene
d, 0-2-Methylnaphthalene

d 10-2-Methylnaphthalene

d10-2-Methylnaphthalene

d10-Pyrene

d10-Pyrene

d10-Pyrene

d10-Pyrene

d12-Perylene

d12-Perylene

d12-Perylene

d12-Perylene

d12-Perylene

d12-Perylene

d12-Perylene
d10-Pyrene
August 9, 1996
    Proposed M-429 Page 91

-------
                                TABLE 13

             QUANTITATION AND CONFIRMATION IONS FOR SELECTED
                   ION MONITORING OF PAHs BY HRGC/LRMS
Analyte
Naphthalene
d8-Naphthalene
2-Methylnaphthalene
d10-2-Methylnaphthalene
Acenaphthylene
da-Acenaphthylene
Acenaphthene
d10-Acenaphthene
Fluorene
d10-Fluorene
Phenanthrene
d10-Phenanthrene
Anthracene
d10-Anthracene
Fluoranthene
d10-Fluoranthene
Pyrene
d^-Pyrene
Benzo(a)anthracene
d12-Benzo(a)anthracene
Chrysene
d12-Chrysene
d14-Terphenyl
Quant.
Ion
128
136
142
152
152
160
154
164
166
176
178
188
178
188
202
212
202
212
228
240
228
240
244
Confirm.
Ion
127
68
141
153
153
165
176
94
176
94
101
106 '
101
106
114
120
114
120
122
% Relative
Abundance of
Confirm. Ion
10
80
80
15
86
80
15
15
15
15
15
15
15
August 9, 1996
Proposed M-429  Page 92

-------
                             TABLE 13(CONT)

             QUANTITATION AND CONFIRMATION IONS FOR SELECTED
                   ION MONITORING OF PAHs BY HRGC/LRMS
Analyte
Benzo(b)fluoranthene
d12-Benzo(b)fluoranthene
Benzo(k)fluoranthene
d 1 2-Benzo(k)f luorantbene
Benzo(e)pyrene
d12-Benzo(e)pyrene
Benzo(a)pyrene
d12-Benzo(a)pyrene
Perylene
d12-Perylene
Indenod ,2,3-cd)pyrene
d12-lndeno{1 ,2,3-cd)pyrene
Dibenz(ah)anthracene
d 1 4-Di benz(ah)anthracene
Benzo(ghi)perylene
d T 2-Benzo(ghi) perylene
Quant.
Ion
252
264
252
264
252
264
252
264
252
264
276
288
278
292
276
288
Confirm.
Ion
126
132
126
132
126
132
126
132
126
132
138
139
138
% Relative
Abundance of
Confirm. Ion
25
25
25
25
26
28
24
37
August 9, 1996
                                                Proposed M-429  Page 93

-------
                                TABLE 14




     MASS DESCRIPTORS USED FOR SELECTED ION MONITORING FOR HRGC/HRMS
Descriptor Analyte
No.
1









2
















IS
SS
AS
RS
LOCK
QC

Naphthalene
PFK
da-Naphthalene
2-Methyl naphthalene
d ! g-2-Methylna phthalene
Acenaphthylene
d8-Acenaphthylene
Acenaphthene
d10-Acenaphthene
PFK
Fluorene
d10-Fluorene
Phenanthrene
d10-Phenanthrene
Anthracene
d10-Anthracene
Fluoranthene
d^-Fluoranthene
Pyrene
PFK
d10-Pyrene
Benzo(a)anthracene
d T 2-Benzo-a-Anthracene
Chrysene
d12-Chrysene
PFK
d14-Terphenyl
= Internal Standard
= Surrogate Standard
= Alternate Standard
= Recovery Standard
= Lock-Mass Ion
= Quality Control Check Ion
Ion
Type
M
LOCK
IS
M
IS
M
IS
M
RS
QC
M
SS
M
IS
M
AS
M
IS
M
QC
RS
M
IS
M
IS
LOCK
SS






Accurate
m/z
128.0626
130.9920
136.1128
142.0782
152.1410
152.0626
160.1128
154.0782
164.1410
169.9888
165.0782
176.1410
178.0782
188.1410
178.0782
188.1410
202.0782
212.1410
202.0782
2C4.9888
212.1410
228.0939
240.1692
228.0939
240.1692
230.9856
244.1974






August 9, 1996
Proposed M-429  Page 94

-------
                             TABLE 14(CONT)




     MASS DESCRIPTORS USED FOR SELECTED ION MONITORING FOR HRGC/HRMS
Descriptor Analyte
No.


















The
H «
IS
SS
AS
RS

3 Perylene
d12-Perylene
PFK
Benzo(b)fluoranthene
d T 2-Benzo(b)f luoranthene
Benzo(k)fiuoranthene
d 1 2-Benzo-k-f luoranthene
Benzo(e)pyrene
d12-Benzo(e)pyrene
Benzo(a)pyrene
d12-Benzo(a)pyrene
Benzo(ghi)perylene
d12-Benzo(ghi)perylene
Indenod ,2,3-cd)pyrene
d12-lndeno(1 ,2,3-cd)pyrene
Dibenzo(ah)anthracene
PFK
d14-Dibenzo(ah)anthracene
following nuclidic masses were used:
1.007825 2H = 2.014102
= Internal Standard
= Surrogate Standard
= Alternate Standard
= Recovery Standard
Ion
Type
M
IS
QC
M
IS
M
IS
M
RS
M
IS
M
IS
M
IS
M
LOCK
IS

C = 12.000000




Accurate
m/z
252.0939
264.1692
268.9824
252.0939
264.1692
252.0939
264.1692
252.0939
264.1692
252.0939
264.1692
276.0939
288.1692
276.0939
288.1692
278.1096
280.9824
292.1974






LOCK = Lock-Mass Ion
QC
= Quality Control Check Ion


August 9, 1996
                                                 Proposed M-429 Page 95

-------
                                                         FIGURE 1
                                                METHOD 429 FLOWCHART
                                                                     7
    §1.3.9   The end user is identified
    51.3.10  The tester is designated
            The end user chooses:
    §2.1.1   •  source target concentration
    §2.1.2  The tester selects analyst with documented
    §8.4    experience in satisfactory performance of analytical
    §8.4.1  procedures
            Tester and laboratory coordinate:
    §4.3.2  •  pre-test cleaning of glassware
    §4.2    •  pre-test cleaning, contamination checks, and
    §4.3.3    storage of sampling materials and reagents
    §4.3.4  •  preparation of filter, sorbent cartridges, method
              blanks,  and LCS
§10.1
§10.1
§10.1
Tester requests pre-test analytical results from
laboratory:
1 • contamination check of filters
.2 • contamination check of XAD-2 resin
.3 • Method detection limits (MDLs) and
Practical quantitation limits (PQLs)
6
§2.5
Tester calculates and plans:
• S3 sampling runs and £1 blank sarnpSing train
• sample volume
• sampling time
• source reporting limit
• chain of custody
S4.3.1
Tester performs:
• calibration of equipment
8
§2.2
Tester writes:
• pre-test protocol
9
§4.4.1
§4.4.2
§4.4.3
§4.4.4
§5
Tester performs:
• preliminary field sampling determinations
• sampling train preparation
• leak checks
• sampling procedure
• £3 sampling runs
• £1 blank sampling train
• recovery of all runs and blank sampling train
10
§5.3
§5.4
Tester delivers:
• recovered sampling runs and blank train(s)
• chain of custody record
77
§6
§7
§8
§9
§10.2
Laboratory performs:
• extraction of field samples
• analyses
• QA/QC procedures
• chain of custody
• reporting requirements
12
§4.3.1
§9.2
§10.3
Tester performs:
• post-test calibrations
• calculations
• data recording and chain of custody
• reporting requirements
August 9, 1996
Proposed M-429  Page 96

-------
            Heated Probe,
             S-type Pilot
            &Temp. Sensor
   Stack
   Wall
     Temp.         L
     Readout
                Pilot
              Manometer
                       Orifice
                  Orifice
                Manometer
                                 Thermocouple
                                        Dry Gas
                                        Meter
Oven


Cyclone (Optional)


Filter Assembly

 — Transfer Line
     Condenser
     (watercooled)
                                                           Sorbent Module
                                                           (watercooled)
                                                      ImpingersinlceBath:
                                                    Buffer Solution in/1 &12
                                                          /3 Empty
                                                        Silica Gel in #4
                                                          Bypass
                                                           Valve
                Main
                Valve
                                                           Pump
                       Check
                       Valve
                                  Figure 2

                          PAH Sampling  Train
August 9, 1996
   Proposed M-429 Page 97

-------
c
(O
c
 (O
 (O
 CD
 O)
                                          H To Suith
                              8 mm Glass
                              Cooling Coil
                1—Water Jacket—'
XAD-2
Glass Sintered
    Disk
                               Condenser
                                        Sorbent Trap
O
TJ
O
0)
(0
Q.
(D

TJ
Q)
(Q
O

(O
00
                  Figure 3

Condenser and Sorbent Trap for Collection
             of Gaseous PAHs

-------
            Liquid Take Off
       Liquid Nitrogen
          Cylinder
          (150L)
                               Loo.se Weave Nylon
                                  Fabric Cover
                                     10.2 cm (41)
                                     Pyrex Pipe
                               0.95 cm (3/8')
                               / Tubing
Heat Source
                                                          Rne Screen
                              Figure 4

             XAD-2 Fluidized Bed Drying Apparatus
August 9, 1996
                                                Proposed M-429 Page 99

-------
                                                       FIGURE 5
                                           METHOD 429 FIELD DATA RECORD
Run No.	
Location  	
Date 	
Operator	
Meter Box No.
Local Time
 Start/Stop _
AH@ 	
Pitot Tube Factor
Probe Tip Dia, in.
Probe Length  	
Sampling Train Leak Test
Before	in. Hg  _
After
in. Hg
Stack Diameter 	
Meter Box Calibration
Factor (Y) 	
Leak Check Volume  	
Pitot Tube Leak Check
Before	 After
 Leak Rate
	cu.ft/min
	cu.ft/min
     cu. ft.
                             Project No.	
                             Plant Name 	
                             Ambient Temp °F
                             Meter Temp °F _
                             Bar. Press, "Hg _
                             Stack Press,
            'H2O
Assumed Moisture, % _
Heater Box Setting, °F _
Probe Heater Setting, °F
Assumed M.W. (wet%)
Assumed M.W. (dry%)
Sampling
Point
Start












Clock
Time













Dry Gas
Meter, cu, ft.













Pitot AP
in. H2O













Orifice AH
"H20
Desired













Actual













Temperature (°F)
Impinger













Filter box













Stack













Pump
Vacuum
in. Hg













   August 9, 1996
                                                               Proposed M-429  Page 100

-------
            c
           CO
            c
            CD
            CO
            CO
            O)
                                                           Figure  6

                                   Recovery  of  PAH Sampling Train
                    Rinse with known volume:
                         1. acetone
                         2. methylene chloride
                         3.hexane

                           Container
           o
           •a
           o
           CO
           CD
           a
           ro
           CO
           0)
          ca
           (D

 Mark liquid level,
Store at 4v or lower
  away from lioht
                          Transfer
                                                  Filter
«                          Container  \\
                           No  2    ))
 Store at 4'C
or lower away
  from light
Rinse with known volume:
        1. acetone
    2. methylene chloride
        3. hexane
/
                                                                \
                                         Filter support,
                                          Back hall
                                         filter holder
                             Transfer   | Condenser |
 Mark liqu d level,
Store at 4 C or lower
  away from light
                                                        Cap
C
                                                        Resin
                                                      cartridge
                             Store at 4°C or lower
                               away from light
                                                                                                                        A. Tare weigh Container /4
                                                                                                                        B. Decant contents of
                                                                                                                          Impingers into tared
                                                                                                                          Container /4
                                                          I
                                                                                                                         C. Weigh Container /4
                                                                                                                         D. Mark liquid level.
                                                                                                                          Store at 4°C or lower
                                                                                                                          away from light
                                              Rinse with known volume:
                                                   1. acetone
                                                   2. methylene chloride
                                                   3. hexane
                                                                                                      Mark liquid level,
                                                                                                      Store at 4°C or lower
                                                                                                      away from light
                                                                            A. Tare weigh
                                                                              cartrtridge with
                                                                              silica gel
                                                                            B. Weigh after
                                                                              sampling
                                                                                                                                                       Recycle

-------
                             Figure 7
     Flow Chart for Sampling, Extraction and Cleanup for
            Determination of PAH in a Split Sample
                              Surrogate Standards
                             Added to XAD-2 Resin
                                 Sampling

              [G.C7 Mass Spec.]
                                                 G.C7 Mass Spec.)
                             11 Containers No. land No. 3
Augusts, 1996
Proposed M-429 Page 102

-------
                            Figure 8
     Flow Chart for Sampling, Extraction and Cleanup for
        Determination of PAH in a Composite Sample
                              Surrogate Standards
                             Added to XAO-2 Resin
               MeCI2
            Soxhlet Extraction
                              Recovery Standards
        Containers No. 1 and No. 3
G.C./ Mass Spec.
August 9, 1996
                                                Proposed M-429  Page 103

-------
                                        FIGURE 9

               EXAMPLE OF PRE-TEST CALCULATIONS FOR PAH EMISSIONS TEST


Naphthalene
2-Methylnaphthalene
PQL
(ng/sample)
STC
(ng/dscm)
2400 < 1 500
330
Acenaphthylene j 5.0
Acenaphthene
Fluorene1
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Benzo(a)anthracene
Chrysene
Benzo(b)fluoranthene
BenzoikTfluoranthene
Benzo(e)pyrene
Benzo(a)pyrene
Perylene
Indenod ,2,3-c,d)pyrene
Dibenzo(a,h)anthracene
Benzo(g,h,i)perylene
5.0
83
110
5.0
5.0
~""5To'""'
5.0
5.0
_._
5.6
. ... ^
5.0
5.0
5.0
5.6
5.0
5.0
NA
180
6
<6
120
<6
' 46
46
<6
42
„„
50
NA

MSV
(dscf)
>56.5
NA
0.98
29.4
>489
32.4
>29.4
3.8
3.8
... ^_._™....._
... 4_
"" 3.5
3.5
NA
<6 I >29.4
NA
<6
<6
<6" 	
NA
>29.4
>29.4
>29.4
MST
(hours)
>1.89
NA
0.03
0.98
>16.3
1.08
>0.98
0.13^
""6.13""
>_f
0.14
0.12
0.12
...__
>0.98
NA
......>0:9L
>0.98
>0.98
PST = 6 hours
PSV = 180 dscf
F
NA
NA
183
6
NA
6
NA
47
47
NA
43
51
51
NA
NA
NA
NA
NA
NA
SRL
(ng/dscm}
471
64.7
0.98
0.98
16.3
21.6
0.98
0.98
6798
0.98
0.98
0.98
"__~
0.98
0.98
0.98
0.98
0.98
0.98
Average Volumetric Sampling Rate (VSR) = 0.5 dscfm = 30 dscf/hr
 PQL  =   Practical quantitation limit for analyte (based on pre-test analysis of XAD-2 resin)
 STC  =   Source target concentration for analyte.  (From previous emissions test.  Samples
           were analyzed by HRGC/LRMS).
 MSV  =   Minimum sample volume required to collect detectable levels of target analyte.
           (MSV = PQL •»•  STC)                          Equation 429-1
 MST  =   Minimum sample time required to collect detectable levels of target analyte at VSR.
           (MST - MSV -f- VSR)                         Equation 429-2
 PST  =   Planned sampling time (6 hours chosen as the longest practical sampling
           time for the planned emissions test)
 PSV  =   Planned sample volume (PSV =  PST x VSR)     Equation 429-4
 F     =   Safety factor (> 1) that allows for deviation from ideal sampling and analytical
           conditions.  (F = PSV - MSV)                  Equation 429-5
 SRL  =   Source reporting limit if the target analyte cannot be detected with the planned test
           parameters. (SRL = PQL * PSV)               Equation 429-7
 NA       This calculation is not applicable either because there is no STC value available or the
           STC is a detection limit.

       1    PSV is lower than the  MSV. Therefore, the analyte is not expected to be detected if it
           is present at the target concentrations. It will only be detected if the actual
           concentration is lower than  the indicated SRL.
August 9, 1996
Proposed M-429  Page 104

-------
 RUN NO.
 PLANT NAME
 SET-UP DATE
 RECEIVED BY
                               FIGURE 10

         CARB METHOD 429 (PAHs) SAMPLING TRAIN SET-UP RECORD

        	      PROJECT NO.     	
        	      PLANT LOCATION  	
        	      SET-UP BY        	
        	      DATE/TIME       	
  1.
  2.
  3.
  4.
 COMPONENTS

       NOZZLE



        PROBE



FILTER HOLDER
  5.    TRANSFER LINE
      AND CONDENSER
  6.
       Fittings

  XAD-2 RESIN
   CARTRIDGE
  7. IMPINGERS:  No. 1
          U-Connector

                No. 2
          U-Connector

                No. 3
          U-Connector
  8.
    SILCA GEL
   CARTRIDGE
                       COMPONENT ID
        FILTER   Lot*
              OTHER INFORMATION
                 Material

                Diameter

            Liner material

                  Length

          Before set-up, all
      openings sealed with

        Filter support type

              Filter Type

                   Size

     Contamination check?


      Transfer line material
       Both ends sealed in
         lab prior to set-up

                 Fittings

     Contamination check?

                 Spiked?

      Charge with 100 mL
impinger solution and weigh

      Charge with 100 mL
impinger solution and weigh


            Weigh empty
            Tare weight
                                          Appearance
August 9, 1996
                                                            Proposed M-429  Page 105

-------
                                           FIGURE 11

                   CARB METHOD 429 (PAHs) SAMPLING TRAIN RECOVERY RECORD
RUN NO.	   PROJECT NO.
PLANT NAME    	   PLANT LOCATION
RECOVERY DATE 	   RECOVERED BY
1. CHECK whether openings were covered.          RINSE 3x each with Acetone. MeCI2, Hexane.
   MARK liquid level and STORE containers at temp. <4°C away from light.

                      Openings       	Rinse volume (mL)	       Storage
   Component         covered?        Acetone        MeCU	     Hexane      Container(s) IDs
   Nozzle             	,     	 	   	   	
   Probe liner          	     	 	   	   	
   Filter holder front    	     	 	      	   	
2.  STORE filterls) at temp. <4°C away from light.      RECORD ALL sample storage information.
                                                           Storage              Storage
    Component          Appearance after sampling         (Temperature & light)     Container(s) ID
    Filter             	       	  	
    Filter             	       	  	
    Filter             	       	  	

3.  CHECK whether openings were covered.          RINSE 3x each with Acetone, MeCI2, Hexane.
    MARK liquid level and STORE containers at temp. <4°C away from light.

                     Openings  	Rinse volume (mL)	      Storage      Storage
    Component        covered?  Acetone       MeCU     Hexane     Temp. & lisht  Container ID
    Filter support and
    filter holder back   	  	   		  	  	
    Transfer line       	  	   	   	,  	  	
    Condenser         	  	   	   	  	  	
4. STORE Resin cartridges at temp. <4°C away from light.    RECORD ALL storage information.

   	ID	        Appearance after sampling           Storage temperature & light conditions
5. WEIGH impinger contents and silica gel cartridge.
   MARK liquid level and STORE impinger contents at temp. <4°C away from light.
                                                             Additional impingers     Silica gel
      Weight           No. 1        No. 2       No. 3        No. 4        No. 5      cartridge
   Final (g)            		   .	    	_   	    	
   Before sampling (g)
   Gain (g)         (A)	 (B)	 (C)	 (D)	(E)	  (F).

   Total condensate (A) +  (B) + (C) +  (D) + (E) + (F)   _____	(g)

   STORAGE CONTAINER ID(s)      	   	    	      	
6. RINSE impingers 3x each with Acetone, MeCI2, Hexane.
   MARK liquid level and STORE impinger rinses at temp. <4°C away from light.
   Rinse volumes (mL) Acetone
                     MeCI2
                     Hexane

   STORAGE CONTAINER ID(s)
   August 9, 1996                                                   Proposed M-429  Page 106

-------
Project #
            FIGURE 12

CHAIN OF CUSTODY SAMPLE RECORD

        Date:	
Source name: 	
Sampling location:	
Chain of Custody Log Record # (s)

SAMPLE STORAGE INFORMATION
   Start:	
   Stop:	
   Sample/Run #
   Sample type: _
   Operator:	
SAMPLE PRESERVATION
Ice/Dry ice?

Comments


CHAIN OF CUSTODY
             ACTION
               DATE
TIME
GIVEN BY
TAKEN BY
RELATED
IDs
FR
F
BR
C
I
IR
DESCRIPTION/COMMENTS
Front rinse (nozzle, probe, filter holder front)
Filter in sealed storage container
Back rinse (filter support, filter holder, sample line &
condenser
Resin cartridge
Impinger contents
Impinger rinses
Log #s






August 9, 1996
                              Proposed M-429 Page 107

-------
                                     FIGURE 13

                          CHAIN OF CUSTODY LOG RECORD
PROJECT NO.
                                                    Page
                                                     of
 Log #
Sample

  ID
Date
Time
Comments
Given

 by
Taken by
 Sample Identifier

        FR
        F
        BR
        IR
                        Sample  Description

        Rinses of probe and front half of filter holder
        Filter in sealed storage container
        Rinses of filter support, back half of filter holder, sample transfer line and
        condenser
        Aluminum foil wrapped, capped resin cartridge
        Impinger contents
        Impinger rinses
August 9, 1996
                                                  Proposed M-429 Page 108

-------
                                   FIGURE 14A
     EXAMPLE GC/MS SUMMARY REPORT (HRMS) FOR INITIAL CALIBRATION SOLUTION #1
  CALIFORNIA AIR RESOURCES BOARD METHOD 429 POLYCYCLIC AROMATIC HYDROCARBONS

                                                          INSTRUMENT:  W
                                                          OPERATOR:    MPA

                                                    RRF

                                                     0.75
                                                     1.30
                                                     1.44
                                                     0.94
                                                     1.05
                                                     1.15
                                                     1.02
                                                     1.26
                                                     1.31
                                                     1.13
                                                     1.13
                                                     1.69
                                                     1.24
                                                     1.20
                                                     1.07
                                                     0.70
                                                     2.19
                                                     1.66
                                                     2.23

                                                     4.22
                                                     1.29
                                                     1.32
                                                     0.93
                                                     0.82
                                                     1.03
                                                     0.75
                                                     0.82
                                                     1.35
                                                     1.95
                                                     1.91
                                                     0.92
                                                     0.87
                                                     0.80

                                                     0.52
                                                     0.37

                                                    0.69
ICALID: ST1120A1
RUN #: PAHCS1

Naphthalene
2-Methylnaphthalene
Acenaphthylene
Acenaphthene
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Benzofalanthracene
Chrysene
Benzo(b)fluoranthene
Benzo(k)fluoranthene
Benzo(e)pyrene
Benzolalpyrene
Perylene
lndeno(1,2,3-c,d)pyrene
Dibenzo(a,h)anthracene
Benzo(g,h,i)perylene
dg-Naphthalene
dg-Acenaphthylene
d10- Acenaphthene
d10-Fluorene
d10-Phenanthrene
d10-Fluoranthene
d12-Benzo(a)anthracene
d12-Chrysene
d 1 2-Benzo(b) f luoranthene
d12-Benzo(k)fluoranthene
d12-Benzo(a)pyrene
d12-lndeno(1,2,3-c,d)pyrene
du-Dibenzo(a,h)anthracene
d 5 2-Benzo(g,h,i)perylene
d14-Terphenyl
d12-Benzo(e)pyrene
d10- Anthracene
d , 0-2-Methylnaphthalene
d10-Pyrene
d12-Perylene
ACQUIRED: 12/3/94 16:23::
PROCESSED: 12/3/94
RT
8:20
9:42
11:04
11:20
12:06
13:20
13:23
14:38
14:55
16:34
16:39
18:54
18:58
19:42
19:51
20:06
23:60
24:01
25:15
8:17
11:02
11:17
12:04
13:18
14:37
16:32
16:36
18:50
18:54
19:47
23:52
23:52
25:07
14:59
19:37
13:22
9:38
14:54
20:01
RRT
1.006
1.007
1.003
1.004
1.003
1.003
1.001
1.001
1.001
1.002
1.003
1.004
1.004
1.004
1.003
1.004
1.006
1.006
1.005
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000

1.000
1.000
1.000
1.000
1.000
Area
6.66 E + 07
1.44 E + 07
1.57 E + 07
1.05 E + 07
8.15 E + 06
1.99 E + 07
7.07 E + 06
3.18 E + 07
3.31 E + 07
2.08 E + 07
2.26 E + 07
2.35 E + 07
2.50 E + 07
2.41 E + 07
2.11 E + 07
1.38 E + 07
2.07 E + 07
1.49 E + 07
1.84 E + 07
3.54E + 08
1.09 E + 08
1.11 E + 08
7. 78 E + 07
6.92 E + 07
2.53 E + 08
1.83 E + 08
2.00 E + 08
2.77 E + 08
4.03 E + 08
3.93 E+08
1.89 E+08
1.80 E + 08
1.65 E+08
2.65 E + 08
1.44 E + 08
5.82 E + 07
8.40 E + 07
2.45 E + 08
1.03 E + 08
August 9, 1996
                                                         Proposed M-429 Page 109

-------
                                           FIGURE 148

                       EXAMPLE OF INITIAL CALIBRATION (ICAL) RRF SUMMARY
      CALIFORNIA AIR RESOURCES BOARD METHOD 429 POLYCYCLIC AROMATIC HYDROCARBONS
 ICAL ID:
 RUN #:
ST1120
NA
Naphthalene
2-Methylnaphthalene
Acenaphthylene
Acenaphthene
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Benzolalanthracene
Chrysene
Benzofbjfluoranthene
Benzo(k)fluoranthene
Benzolelpyrene
Benzo(a)pyrene
Perylene
Indenol 1,2,3-c,d)pyrene
Dibenzo(a,h)anthracene
Benzo(g,h,i)perylene

d8-Naphthalene
d8-Acenaphthylene
d10-Acenaphthene
d10-Fluorene
d10-Phenanthrene
d10-Fluoranthene
d12-Benzo(a)anthracene
d12-Chrysene
d T 2-Benzo(b)f luoranthene
d12-Benzo(k)fluoranthene
d12-Benzo(a)pyrene
dl2-lndeno(1,2,3-c,d)pyrene
d14-Dibenzo(a,h)anthracene
d12-Benzo(g,h,i)perylene

d14-Terphenyl
d12-Benzo(e)pyrene

d10-Anthracene

d, 0-2-Methylnaphthalene
d10-Pyrene
d12-Perylene
ACQUIRED: 3-DEC-94
PROCESSED: 3-DEC-94
RRF #1

0.75
1.30
1.44
0.94
1.05
1.15
1.02
.26
.31
.13
.13
.69
.24
.20
1.07
0.70
2.19
1.66
2.23
4.22
1.29
1.32
0.93
0.82
1.03
0.75
0.82
1.35
1.95
1.91
0.92
0.87
0.80
0.52
0.37
RRF #2

0.66
1.15
1.27
0.84
0.94
1.06
1.00
1.15
1.27
1.05
1.02
1.45
1.25
1.12
0.99
0.63
2.01
1.60
2.05
4.15
1.29
1.34
0.95
0.82
1.00
0.70
0.79
1.39
1.95
1.96
0.88
0.84
0.76
0.52
0.37
RRF #3

0.61
1.10
1.24
0.80
0.88
1.01
0.98
1.08
1.13
1.05
0.97
1.46
1.14
1.06
0.96
0.58
1.92
1.56
1.96
4.16
1.28
1.32
0.94
0.82
1.07
0.70
0.81
1.46
2.14
2.11
0.98
0.91
0.83
0.49
0.37
RRF #4

0.64
1.12
1.28
0.83
0.92
1.05
0.95
1.13
1.15
1.04
0.98
1.42
1.18
1.06
0.96
0.60
1.99
1.61
2.00
4.18
1.27
1.30
0.95
0.86
1.07
0.72
0.83
1.27
1.84
1.82
0.85
0.78
0.73
0.48
0.36
RRF #5

0.71
1.26
1.43
0.94
1.07
1.23
1.14
1.28
1.41
1.23
1.11
1.86
1.26
1.19
1.14
0.70
2.26
1.87
2.32
4.10
1.30
1.32
0.95
0.88
0.99
0.70
0.84
1.32
2.11
1.99
0.98
0.89
0.80
0.51
0.36
INSTRUMENT: W
OPERATOR: MPA
Mean
RRF
0.67
1.19
1.33
0.87
0.97
1.10
1.02
1.18
1.25
1.10
1.04
1.58
1.21
1.12
1.02
0.64
2.07
1.66
2.11
4.16
1.29
1.32
0.94
0.81
1.03
0.71
0.82
1.36 '
2.00
1.96
0.92
0.86
0.78
0.51
0.36
SD

0.056
0.089
0.096
0.067
0.082
0.088
0.074
0.085
0.115
0.082
0.073
0.194
0.052
0.066
0.080
0.059
0.143
0.122
0.154
0.044
0.012
0.013
0.011
0.026
0.038
0.022
0.021
0.072
0.124
0.107
0.059
0.049
0.042
0.018
0.005
%RSD

8.29%
7.47%
7.19%
7.72%
8.43%
8.00%
7.25%
7.21%
9.22%
7.43%
7.00%
12.33%
4.32%
5.89%
7.81%
9.12%
6.90%
7.35%
7.28%
1.05%
0.91%
1.00%
1.21%
3.09%
3.71%
3.09%
2.56%
5.32%
6.23%
5.46%
6.40%
5.71%
5.36%
3.59%
1.50%
                0.69
0.73
0.74
0.80
0.90
0.77
0.080    10.40%
 August 9, 1996
                                                          Proposed M-429  Page 110

-------
                                     FIGURE 14C

                 EXAMPLE OF CONTINUING CALIBRATION (CONCAL) SUMMARY
    CALIFORNIA AIR RESOURCES BOARD METHOD 429 POLYCYCLIC AROMATIC HYDROCARBONS
CONCAL ID:
CONCAL DATE:
CC1202            ICALID:    ST1120
12/3/94            ICALDATE: 3-DEC-94

             RRF    ICAL RRF   ARRF
                                                     RPD
                                INSTRUMENT:   W
                                OPERATOR:     MPA
Naphthalene
2-Methylnaphthalene
Acenaphthylene
Acenaphthene
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Benzo(a)anthracene
Chrysene
Benzo(b)fluoranthene
Benzo(k)fluoranthene
Benzolelpyrene
Benzolalpyrene
Perylene
Indenod ,2, 3-c,d)pyrene
Dibenzo(a,h)anthracene
Benzofg, h,i)perylene
dg-Naphthalene
d8-Acenaphthylene
d10- Acenaphthene
d10-Fluorene
d10-Phenanthrene
d10-Fluoranthene
d 1 2-Benzo(a)anthracene
d12-Chrysene
d12-Benzo(b)fluoranthene
d12-Benzo(k)fluoranthene
d12-Benzo(a)pyrene
d12-lndeno(1 ,2,3-c,d)pyrene
d14-Dibenzo(a,h)anthracene
d , 2-Benzo(o,h,i)perylene
d14-Terphenyl
d12-Benzo(e)pyrene
0.68
1.42
1.42
0.91
0.98
1.10
0.98
1.12
1.18
1.08
1.04
1.46
1.12
1.04
0.95
0.62
2.04
1.61
2.11
4.78
1.20
1.25
0.85
0.79
1,05
0.69
0.82
1.24
1.91
1.87
0.84
0.80
0.76
0.50
0.37
0.67
1.19
1.33
0.87
0.97
1.10
1.02
1.18
1.25
1.10
1.04
1.58
1.21
1.12
1.02
0.64
2.07
1.66
2.11
1.16
1.29
1.32
0.94
0.81
1.03
0.71
0.82
1.36
2.00
1.96
0.92
0.86
0.78
0.51
0.36
0.01
0.23
0.09
0.04
0.01
0.00
-0.04
-0.06
-0.07
•0.02
0.00
-0.12
-0.09
-0.08
-0.07
-0.02
-0.03
-0.05
0.00
0.68
-0.09
-0.07
-0.09
-0.02
0.02
-0.02
0.00
-0.12
-0.09
-0.09
-0.08
-0.06
-0.02
-0.01
0.01
1.5
17.6
6.6
4.5
1.0
0.0
4.0
5.2
5.8
1.8
0.0
7.9
7.7
7.4
7.1
3.2
1.5
3.1
0.0
15.3
7.2
5.5
10.1
2.5
1.9
2.9
0.0
9.2
4.6
4.7
9.1
7.2
2.6
2.0
2.7
 d10-Anthracene

 d10-2-Methylnaphthalene
 d10-Pyrene
 d12-Perylene
0.71
                     0.77
         1.000
         1.000
-0.06
                           8.1
August 9, 1996
                                                           Proposed M-429  Page 111

-------
                                           FIGURE 15A.
                          EXAMPLE OF SUMMARY REPORT OF LCS RESULTS
       CALIFORNIA AIR RESOURCES BOARD METHOD 429 POLYCYCLIC AROMATIC HYDROCARBONS
Client ID  CARB
Lab ID: 14129/LCS1/LCS2
Instrument: _W	
Operator: .
Reviewer:
MPA
JCM
           COMPOUND:
Sample Matrix: XAD-2
Date Received:   NA
Date Extracted: 11/30/94
Date Analyzed:
  Naphthalene
  2-Methylnaphthalene
  Acenaphthylene
  Acenaphthene
  Fluorene
  Phenanthrene
  Anthracene
  Fluoranthene
  Pyrene
  Benzo(a)anthracene
  Chrysene
  Benzo(b)fluoranthene
  Benzo(k)fluoranthene
  Benzo(e)pyrene
  Benzo(a)pyrene
  Perylene
  lndeno(1,2,3-c,d)pyrene
  Dibenzo(a,h)anthracene
  Benzolg,h,i)perylene
  Internal Standards (%R)
  d8-Naphthalene
  d8-Acenaphthylene
  d10-Acenaphthene
  d10-Fluorene
  di0'Phenanthrene
  d10-Fluoranthene
  d 12-Benzo(a)anthracene
  d12-Chrysene
  d 12-Benzo(b)f luoranthene
  d12-Benzo(k)fluoranthene
  d12-Benzo(a)pyrene
  d12-lndeno(1,2,3-c,d)pyrene
  d14-Dibenzo(a,h)anthracene
  d, 2-Benzo(g,h,i)perylene

  Alternate Standard (%R)
  d10-Anthracene
d: 12/3/94
nt: Sample
LCS1
%R
100
96
95
92
94
93
91
90
87
87
83
92
92
97
89
89
87
88
89
67
73
76
79
88
84
96
96
88
85
92
104
96
102
CONC
Units
LCS2
%R
103
95
97
94
96
94
89
92
89
86
89
93
95
99
92
89
90
90
91
64
70
75
81
93
80
98
91
85
84
90
105
96
103
ICALID:  ST1120
ICAL DATE:
CONCAL ID:	
CONCALDATE:   NA
         NA
                                                   12/3/94
                                                    NA
                                                     RPD
                                                       3.0
                                                       1.0
                                                       2.1
                                                       2.2
                                                       2.1
                                                       1.1
                                                       2.2
                                                       2.2
                                                       2.3
                                                       1.2
                                                       7.0
                                                       1.1
                                                       3.2
                                                       2.0
                                                       3.3
                                                       0.0
                                                       3.4
                                                       2.2
                                                       1.2
Resin Lot #: LC1130M
LCS IDs:  NA	
LCS DATE:  NA
                           83
                          85
 August 9, 1996
                                                      Proposed M-429  Page 112

-------

-------
                                          FIGURE 16A
                 EXAMPLE GC/MS SUMMARY REPORT (HRMS) FOR SAMPLE RUN #32
     CALIFORNIA AIR RESOURCES BOARD METHOD 429 POLYCYCLIC AROMATIC HYDROCARBONS
 Lab ID:  14129-02
 Acquired:  12/3/94  16:23:40
 Client ID: M429-32
 Naphthalene
 2-Methylnaphthalene
 Acenaphthylene
 Acenaphthene
 Fluorene
 Phenanthrene
 Anthracene
 Fluoranthene
 Pyrene
 Benzolalanthracene
 Chrysene
 Benzo(b)fluoranthene
 Benzo(k)fluoranthene
 Benzo(e)pyrene
 Benzofalpyrene
 Perylene
 Indenof 1,2,3-c,d)pyrene
 Dibenzo(a,h)anthracene
 Benzolg.h.ilperylene

 d8-Naphthalene
 de-AcenaphthyIene
 d10- Acenaphthene
 d10-Fluorene
 d10-Phenanthrene
 d10-Fluoranthene
 d T 2-Benzo{a)anthracene
 d12-Chrysene
 d12-Benzo(b)fluoranthene
 d 12-Benzo(k)fluoranthene
 d 12-Benzo(a)pyrene
 d12-lndeno(1,2,3-c,d)pyrene
 d14-Dibenzo(a,h)anthracene
 d12-Benzo(g,h,i)perylene

 du-Terphenyl
 d,2-Benzo(e)pyrene

 d10-Anthracene

 d10-2-Methylnaphthalene
 d10-Pyrene
 d,2-Perylene
ICALID: 12/3/94  16:23:40
ICALDATE:  12/3/94
                     Instrument: W
                     Operator:   MPA
                     Reviewer:   JCM
                               RT
   RRT
Area
RRF     Amt. (ng)
                                                                                       %REC
8:21
9:41
11:03
11:19
12:05
13:17
13:21
14:36
14:52
16:32
16:32
18:49
Not found
19:36
19:46
20:01
23:54
23:56
25:09
8:18
11:01
11:16
12:02
13:16
14:34
16:28
16:31
18:45
18:50
19:41
23:46
23:45
24:60
14:55
19:32
13:20
9:38
14:51
19:56



















1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000

1.000
1.000
1.000
1.000
1.000
1.053 E+10
1.790 E + 08
9.371 E + 08
7.649 E + 06
2.417 E + 07
8.402 E + 08
2.905 E + 07
5.932 E + 08
7.611 E + 08
3. 120 E + 06
9.620 E + 06
1.030 E + 06
0.0
1.646 E + 07
4.936 E + 06
1.823 E + 06
5.728 E + 06
5.875 E + 05
1.584 E + 07
4.794 E + 08
1.972 E+08
2.142 E + 08
1.658 E + 08
1.652 E + 07
3.955 E + 08
2.835 E + 08
2.987 E + 08
3.439 E + 08
4.304 E + 08
4.895 E + 08
2.529 E + 08
2.400 E + 08
2.006 E + 08
7.988 E + 08
3.011 E + 08
6.795 E + 07
1.844 E + 07
6.576 E + 08
3.057 E + 08
0.67
1.19
1.33
0.87
0.97
1.10
1.02
1.18
1.25
1.10
1.04
1.58
1.21
1.12
1.02
0.64
2.07
1.66
2.11
1.16
1.29
1.32
0.94
0.81
1.03
0.71
0.82
1.36
2.00
1.96
0.92
0.86
0.78
0.51
0.36
0.77
...
...
—
10,478.37
140.98
712.59
8.21
30.02
925.53
34.54
254.36
307.62
1.9
6.2
7.6

13.61
3.95
2.32
4.37
0.59
14.95
124.92
166.07
176.19
190.71
213.39
116.22
121.18
1 1 1 .08
165.79
141.02
163.67
179.71
182.65
167.24
523
676.33
95.29
100
100
100



















62.5
83.0
88.1
95.4
106.7
58.1
60.6
55.5
41.4
35.3
40.9
44.9
45.7
41.8
105
135.3
47.6



August 9, 1996
                            Proposed M-429  Page 114

-------
                                          FIGURE 16B

               EXAMPLE LABORATORY REPORT OF PAH RESULTS FOR SAMPLE RUN #32
      CALIFORNIA AIR RESOURCES BOARD METHOD 429 POLYCYCLIC AROMATIC HYDROCARBONS
Client ID  M429-32
Lab ID:  14129-02
Instrument:  W
Operator:   MPA
Reviewer:   JCM
         COMPOUND:
Sample Matrix: M429
Date Received:  11/18/94
Date Extracted:  11 /30/94
Date Analyzed: 12/3/94
Sample amount:  Sample
 Naphthalene
 2-Methylnaphthalene
 Acenaphthylene
 Acenaphthene
 Fluorene
 Phenanthrene
 Anthracene
 Fluoranthene
 Pyrene
 Benzo (a)anthracene
 Chrysene
 Benzolblfluoranthene
 Benzo(k) f luoranthene
 Benzo(e)pyrene
 Benzolalpyrene
 Perylene
 Indenod ,2,3-c,d)pyrene
 Dibenzo(a,h)anthracene
 Benzo(g,h,i)perylene
 Internal  Standards (%R)
 d8-Naphthalene
 d8-Acenaphthylene
 d10-Acenaphthene
 d10-Fluorene
 d10-Phenanthrene
 d10-Fluoranthene
 d12-Benzo(a)anthracene
 d12-Chrysene
 d! 2-Benzo(b)f luoranthene
 d 12-Benzo(k)fluoranthene
 d 12-Benzo!a)pyrene
 d12-lndeno(1,2,3-c,d)pyrene
 du-Dibenzo(a,h)anthracene
 d12-Benzo(g,h,i)perylene

 Alternate Standard (%R)
 d10-Anthracene
 Surrogate Standard (%R)
d14-Terphenyl
d12-Benzo(e)pyrene
            Cone.

              10478
                141
                712
                  8.2
                 30
                930
                 35
                254
                307
                 ND
                  6.2
                  7.6
                 ND
                 14
                 ND
                 ND
                 ND
                 ND
                 15

                 62
                 83
                 88
                 95
                107
                 58
                 61
                 56
                 41
                 35
                 41
                 45
                 46
                 42
                48
                105
                135
ICAL ID:  ST1120
ICAL DATE:
CONCAL ID:
CONCALDATE:   N>
Units:   no/sample
12/3/94
 NA
        R.L

        1600
          94
           5.0
           5.0
          27
          80
           5.0
           5.0
           5.0
           5.0
           5.0
           5.0
           5.0
           5.0
           5.0
           5.0
           5.0
           5.0
           5.0
Resin Lot #:  LC1130M
LCS IDs:  14129-LCS1/LCS2
LCS DATE:   12/3/94
                        Flags
                                   H
                                   H
                                   H
                                   H
                                   H
                                   H
 Augusts, 1996
                                                                   Proposed M-429  Page 115

-------
                                            FIGURE 17A
                    EXAMPLE OF TESTER'S SUMMARY OF LABORATORY REPORTS
Run »:

Naphthalene
2-Methylnaphthalene
Acenaphthylene
Acenaphthene
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Benzo(a)anthracene
Chrysene
Benzo(b)fluoranthene
Benzo(k)fluoranthene
Benzo(e)pyrene
Benzo(a)pyrene
Perylene
Indenol 1 ,2,3-c,d)pyrene
Dibenzo(a,h)anthracene
Benzo(g,h,i)perylene
Internal Standards (%R)
d8-Naphthalene
d8-Acenaphthylene
d 10-Acenaphthene
d10-Fluorene
d10-Phenanthrene
d10-Fluoranthene
d12-Benzo(a)anthracene
d12-Chrysene
d12-Benzo(b)fiuoranthene
31
32
33
Field
Blank
Method
Blank
ng/sampla
4300
< 94
140
9.2
27
310
26
83
iio
< 5.0
< 5.6
< 5.0
< 5.6
35
< 5.0
< 5.0
< 5.6
< 5.0
< 85

66
82
85
91
106
79
100
91
69
d12-Benzo(k)fiuoranthene j 62
d12-Benzo(a)pyrene j 70
d12-indeno(i,2,3-c,d)pyrene 82
d14-bibenzo(a,h)anthracene 72
d12-Benzo(g,n,i)perylene 84
Surrooate Standards (%R)
d14-Terphenyl
d12-Benzo(e)pyrene
Alternate Standard (%R)
d,0-Anthracene
Test Date

125
72

67
11/15/94 .
10000 J460000 *
140
710
8.2
30
930
35
250
310
< 5.0
6.2
7.6
< 5.0
< 35
< 5.0
< 5.0
< 5.0
< 5.0
< 85

62
83
6400 •
8 5666 •
500
180
43666" •
24o6
1606"6 •
26666 *
170
300
340
89
530
240
110
ib'o
6.4
440

57 •
85 •
88 80 *
95 102
107 79 *
58 75 •
61 108
56 99
41 H 60
35"H 50
41 H 58
45 H 58
42 H 58
46 H 58
'.';•; ': .
105
135

48 H

90
112 1

115
11/16/94 J11/17/94
<1600
< 94
9.1
< 5.6
< 27
< 80
5.3
16
19
< 5.0
< 5.0
< 5.0
< 5.0
6.9
< 5.0
< 5.0
< 5.0
< 5.0
. ..„.._.

53
73
81
90
107
83
114
__ -.

85
78
86
<1700
<78
< 5.0
< 5.0
< 27
< 74
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0
< 5.0

55
69
75
82
93
80~
93
88
84
84
89
106' 106
92 92
107

123
103

116
11/16/94
LCS #1
LCS tt2
percent recovery
100
96
95
92
94
93
91
90
87
87
83
92
92
97
89
89
87
103
95
97
94
96
94
89
92
89
86
89
93
95
99
92
89
90
88 j 90
89

67
73
76
79
88
84
96
96
88
85
92
104
96
104 j 102

130
112

101



83
91
" ' .... 'H. *!s
- i '• i '. | -. -,
64
70
75
81
93
80
98
91
85
84
90
105
""""96
103
' ••ri'iv.V"



85
NA ;NA |NA
Date received by lab. 11/18/94" i'l/18/94 |TT/ 18/94 11/18/94 ;NA jNA jNA
Date extracted 11/3"6794 |li730"/94 11/30/94 11/30/94 j 11/30/94 |11/30/94|1 1/30/94
Date analyzed 12/3/94 J12/3/94 12/3/94 12/3/94 1 1273/94 j 12/3/94 112/3/94
• < • denotes that the compound was not detected at levels above the indicated reporting limit.
•H" indicates internal Standard Recovery Results below 50%, but signal-to-noise greater than 10:1.
••• indicates compounds reanalyzed at 1:50 dilution due to saturation.
  August 9,  1996
Proposed M-429  Page  116

-------
                                  FIGURE 17B
                    FIELD DATA SUMMARY FOR PAH EMISSIONS TEST
RUN ID
DATE
START/STOP TIME
LOCATION
STACK DIAMETER
NOZZLE DIAMETER
METER BOX ID
STANDARD DRY GAS VOLUME Vm(.tdl
m
P.,.,

Tm
K,
Y
PERCENT MOISTURE Bw,
Impinger + tare
Final wt.
Net imp. catch
Silica gel tare
Post sampling wt.
Moisture gain
Total moisture (V1
^w(itd)
Vm|ttd|
K2
MOLECULAR WEIGHT Md
M.
°2
CO
C02
N2
"wi
GAS VELOCITY v.
Ap
T.
P.
P.
M.
K.
CP
VOLUMETRIC FLOW RATE Q,1d
BW«
v.
A
sec/min
Ki
ISOKINETIC RATIO 1
T,
''mlitd)
P.
e"
R
WI
K4
31
11-15-95
1015/1435
STACK
35.5 in.
0.3106
6419
146.19
132.65
29.78
1.15
60.0
17.64
1.08
12.9
2183.3
2609.8
426.5
1561.8
1 590.0
28.2
c) 464.7
21.43
145.19
O.O471
29.93
28.40
11.25
0.00
9.25
79.50
12.86
38.4
0.530
420
-0.27
29.76
28.40
86.49
0.83
8241
12.86
38.38
6.8736
60
17.64
96
420
145.19
29.76
38.38
240
12.86
0.00063
0.09460
32
11-16-95
1020/1645
STACK
35.6 in.
0.31 3 in.
6419
235.67
213.67
29.98
1.36
60.0
17.64
1.08
16.0
2092.3
2934.9
842.6
1788.8
1826.9
38.1
880.7
41.50
235.57
0.0471
29.95
28.16
10.76
0.00
9.50
79.75
14.98
40.88
0.66
428
-6.27
29.96
28.16
85.49
0.83
8631
14.98
40.88
6.8736
60
17.64
99
428
236.57
29.96
40.88
360
14.98
0.00063
0.09450
33
11-17-95
0855/1525
STACK
36.5 in.
0.3125 in.
5419
250.76 DSCF(68° F)
228.10 cubic ft
29.88 inches Hg
1.56 inches H2O
60.0 e F
17.64
1.08
18.4 percent
2063 grams
3210.2 grams
1 147.2 grams
1585.7 grams
1 536.2 grams
49.5 grams
1196.7 grams
66.39 DSCF(68° F)
250.76 DSCF(68° F)
0.0471
30.08 Ib/lbmole
27.86 Ib/lbmole
1 0.00 percent
0.00 percent
10.50 percent
79.50 percent
18.36 percent
43.2 feet/second
0.59 inches H,O
427 °F
-0.27 inches H2O
29.86 inches Hg
27.86 Ib/lbmole
85.49
0.83
8641 DSCF(68° F)
1 8.36 percent
43.23 feet/second
6.8736 sq. feet
60
17.64
1 04 percent
427 e F
250.76 DSCFM(68° F)
29.86 inches Hg
43.23 feet/second
360 minutes
18.36 percent
0.00053 sq. feet
0.09450
August 9, 1996
                                                       Proposed M-429 Page 117

-------
                                      FIGURE 17C

                          EXAMPLE OF EMISSIONS TEST REPORT

(ng/dscm)
Naphthalene
2-MetnyinapFthalene
Acenaphthylene
Acenaphthene
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Benzo(a)anthracene
Chrysene
Benzo(b)fluoranthene
Benzo(k)fluoranthene
Benzo(e)pyrene
Benzo(a)pyrene
Perylene
Indenod ,2,3-c,d)pyrene
Dibenzo(a,h)anthracene
Benzo(g,h,i)perylene

/ r (ng/sec)
Naphthalene
2-Methylnaphthalene
Acenaphthylene
Acenaphthene
Fluorene
Phenanthrene
Anthracene
Fluoranthene
Pyrene
Benzo(a)anthracene
Chrysene
Benzo{b7fTuoranfhene
Benzolkifiuoranthene
Benzolejpyrene
Benzo(a]pyrene
Perylene
]ndeno(1 .i.S-c.dTpyrene
Dibenzofa,h)anthracene
Benzolg.hjlperyiene
Run #31

1046
<23
34
2.2
6.6
75
<6.3
20
27
<1.2
<1.2
<1.2
<1.2
..„.„<*•*
<1.2
<1.2
<1.2
<1.2
<21


4068
<89
132
8.7
26
293
<25
79
104
<4.7
<4.7
<4.7
<4.7
<33
<4.7
<4.7
<4.7
<4.7
<80
Run #32

1499
21.6
106
1.2
4.5
139
	 o 	
::"38 	
47
<0.75
6.92
1.1
<0.75
<5.3
<0.75
<0.75
<0.75
<0.75
"~"
-------
                             METHOD 429 - APPENDIX A

                 DETERMINATION OF THE METHOD DETECTION LIMIT

This procedure is based on the approach adopted by the EPA and included as Appendix B
to Title 40, Part 136 of the Code of Federal Regulations (40 CFR 136).  The samples shall
be subjected to the same extraction, concentration, cleanup, and analytical procedures as
those required for the field samples.

A1       Procedure

         A1.1    Make an estimate of the detection limit (MDL) of each target compound
                 using one of the following:

                 (a)  The concentration value that corresponds to an instrument
                     signal/noise ratio in the range of 2.5 to 5.

                 (b)  The concentration equivalent of three times the standard deviation
                     of replicate instrumental measurements of the analyte in reagent
                     methylene chloride.

                 (c)  That region of the standard curve where there is a significant
                     change in sensitivity, i.e., a break in the slope of the standard curve.

                 (d)  Instrumental limitations.

                 (e)  The concentration equivalent to five times the theoretical
                     quantitation limit (Section 8.3.1 of the test method)

             The experience of the analyst is important to this process, but one of the
             above considerations must be included in the initial estimate of the detection
             limit.

         A1.2   Prepare according to the procedures described in Sections 4.2.2.1 to
                4.2.2.4 enough XAD-2 resin to provide, at a minimum, eight aliquots
                each with mass equal to that required to pack a Method 429 sorbent
                cartridge.  A contamination check must be conducted to identify those
                PAH for which a MDL cannot be determined by this method.

         A1.3   To each of seven (7) aliquots of the clean  resin, add an amount of each
                target analyte equal to the estimated detection limit.  The mass of each
                resin aliquot must be known, and should be approximately 40 grams, the
                amount required to pack a Method 429 sorbent cartridge. The eighth
                aliquot shall be a blank.

         A1.4   Process each  of the eight samples through the entire PAH analytical
                method.  All quality criteria requirements of the analytical method must
                be satisfied.
August 9, 1996                                            Proposed M-429  Page 119

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         A1 .5   Report the analytical results.  The laboratory report must satisfy all of the
                 reporting requirements of Section 10 of the test method.

         A1 .6   It may be economically and technically desirable to evaluate the
                 estimated method detection limit before proceeding with step A1.3.  This
                 will: (1) prevent repeating this entire procedure and (2) insure that the
                 procedure is being conducted at the correct concentration. It is quite
                 possible that an inflated MDL will be calculated from data obtained at
                 many times the real MDL even though the level of analyte is less than
              •   five times the calculated method detection limit.  To insure a good
                 estimate of the method detection, it is necessary to determine that a
                 lower concentration of analyte will not result in a significantly lower
                 method detection limit.  Take two aliquots of the sample to be used to
                 calculate the method detection limit and process each through the entire
                 method, including blank measurements as described above in step A1.3.
                 Evaluate these data:

                 (1 )   If the sample levels are in a desirable range for determination of the
                     MDL, take five additional aliquots and proceed. Use all seven
                     measurements for calculation of the MDL according to Section A2.

                 (2)   If these measurements indicate the selected analyte level is not  in
                     correct range, reestimate the MDL with a new sample as in A1 .2
                     and repeat steps A1 .3 to A1 .5.
A2      Calculation
         A2.1   Calculate the variance (S2) and standard deviation (S) of the replicate
                measurements, as follows:
S2 =J_
                                 n-1  LR
                                                             429-(A)-(34)
            Where:
                i = 1 to n, are the analytical results in the final method reporting units
                obtained from the n sample aliqouts and I refers to the sum of the X
                values from i = 1 to n.
Au9USt9'1"6                                            Proposed M-429  Page 120

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         A2.2   (a)  Compute the MDL as follows:


                           MDL  =  t(n.1( ,_. .o.99) x  (S)          429(A)-(35)

                 Where:

                     MDL = the method detection limit

                     t(n-i, 1-a = 0.99)  =  Students' t-value appropriate for a 99%
                     confidence level and a standard deviation estimate with n-1 degrees
                     of freedom. See Table 429(A)-1.

                     S = standard deviation of the replicate analyses.

                 (b)  The 95% confidence interval estimates for the MDL derived in
                     A2.2(a) are computed according to the following  equations derived
                     from percentiles of the chi square over degrees of freedom
                     distribution (x2/df).

                                  LCL = 0.64 MDL
                                  UCL = 2.20 MDL

                     where:       LCL and UCL are the lower and upper 95% confidence
                                  limits respectively based on seven aliquots.

A3      Optional Iterative Procedure

         A3.1   This is to verify the reasonableness of the estimate of the MDL and.
                subsequent MDL determinations.

                (a)  If this is the initial  attempt to compute MDL based on the estimate
                     of MDL formulated in Step A1.1, take the MDL as calculated in  Step
                     A2.2, spike the matrix at this calculated MDL and repeat the
                     procedure starting with Step A1.3.

                (b)  If this is the second or later iteration of the MDL calculation, use S2
                     from the current MDL calculation and S2 from the previous MDL
                     calculation to compute the F-ratio.  The F-ratio is  calculated by
                     substituting the larger S2 into the numerator S2A  and the other into
                     the denominator S B. The computed F-ratio is then compared with
                     the F-ratio found in the table which is 3.05 as follows:  if
                     S2A/S2B<3.05, then compute the pooled standard deviation by  the
                     following  equation:


                                                             429(A)-(36)
                                         oa » -t- oar.
                               Spooled =
                                             12
August 9, 1996                                            Proposed M-429 Page 121

-------
               if S2A/S2B>3.05, respika at the most recent calculated MDL and process
               the samples through the procedure starting with Step A1.3.  If the most
               recent calculated MDL does not permit qualitative identification when
               samples are spiked at that level, report the MDL as a concentration
               between the current and previous MDL which permits qualitative
               identification.

               (c)  Use the Spooled as calculated in Equation 429(A)-3 to compute the
                   final MDL according to the following equation:

                              MDL  = 2.681 (Spooled)              4291AM37).


               Where:  2.681 is equal to t(12( ^ = .99)-

               (d)  The 95% confidence limits for MDL calculated using Equation
                   429(A)-4 are computed according to the following equations derived
                   from percentiles of the chi squared over degrees of freedom
                   distribution.

                               LCL = 0.72 MDL
                               UCL = 1.65 MDL

               where LCL and UCL are the lower and upper 95% confidence limits
               respectively based on  14 aliquots.
                                TABLE 429(A)-1

      SELECTED STUDENT'S t VALUES AT THE 99 PERCENT CONFIDENCE LEVEL
                                                          v
Number of
Replicates

7
8
9
10
11
16
21
26
31
61
Degrees
of Freedom
(n-1)
6
7
8
9
10
15
20
25
30
60


Vl, .99}
3.143
2.998
2.896
2.821
2.764
2.602
2.528
2.485
2.457
2.390
August 9, 1996                                          Proposed M-429  Page 122

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FORMULA:  Table 1

M.W.: Table 1
  POLYNUCLEAR AROMATIC HYDROCARBONS
 ~~~~METHOD:  5506
                                    ISSUED:  5/15/85
OSHA: proposed for B[a]P:  0.2  vg/m3
ACGIH: suspect carcinogen  (B[a]P)
 PROPERTIES:  Table 1
COMPOUNDS:   acenaphthene
            acenaphthylene
            anthracene
            benz[a]anthracene
            benzo[b]fluoranthene
	benzoCk]f1uoranthene
benzo[ghi]perylene
benzo[a]pyrene
benzo[e]pyrene
chrysene
dibenz[a,h]anthracene
fluoranthene
fluorene
i ndenoC1,2,3-cd]pyrene
naphthalene
phenanthrene
pyrene
SYNONYMS:  PAH:  PNA:  also see Table 2.
                    SAMPLING
                       MEASUREMENT

SAMPLER: FILTER + SORBENT
(2->im, 37-ron PTFE + washed XAD-2,
100 mg/50 mg)

FLOW RATE: 2 L/min

VOL-MIN: 200 L
-MAX: 1000 L

SHIPMENT: transfer filters to culture tubes;
wrap sorbent and culture tubes in
Al foil; ship @ 0 °C

SAMPLE STABILITY: unknown; protect from
heat and UV radiation

FIELD BLANKS: 101 (>3) of samples
MEDIA BLANKS: 6 to 10

AREA SAMPLES: 8 replicates on preweighed
filters for solvent selection


ACCURACY

RANGE STUDIED, BIAS, AND OVERALL
PRECISION (sr) : not measured

i
1METHOO: HPLC, FLUORESCENCE/UV DETECTION
i
IANALYTE: compounds above
i
'.EXTRACTION: 5 mL organic solvent appropriate to
! sample matrix (step 7)
i
! COLUMN: 15 cm x 4,6 mm, reverse phase, 5-iirn CJQ
i
! INJECTION VOLUME: 10 to 50 )iL
i
1MOBILE PHASE: HgO/C^CN gradient 9 ambient
! temperature
t
!FLOW RATE: 1.0 mL/min
i
! DETECTORS: UV @ 254 nm; fluorescence @ 340 nm
! (excitation), 425 nm (emission)
i
JCALIBRATION: external standards in O^CN
i
iRANGE, LOD AND PRECISION (sr) : EVALUATION OF
! METHOD
i
i
i
i
i
APPLICABILITY:  The working range for B[a]P is 1 to 50 vg/m3 for a 400-L air sample.
Specific sample sets may require modification in filter extraction  solvent, choice of
measurement method, and measurement conditions (see EVALUATION  OF METHOD).	
INTERFERENCES:  Any compound which elutes at the same HPLC retention  time may interfere.   Heat,
ozone, N02, or UV light may cause sample degradation.

OTHER METHODS:  This revises P&CAH 206 and 251 [1].  The spectrophotometric methods,  P&CAM 184
*nr± 186 [13. have not been revised.  Also see Method 5515 (GC).	

5/15/85                                    5506-1

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POLYNUCLEAR AROHATIC HYDROCARBONS
                                                                                   METHOD;  5506
REAGENTS:
1. Filter extraction solvent:
   benzene,* cyclohexane, methylene
   chloride, or other appropriate
   solvents, pesticide grade
   grade (step 7).
2. Water, distilled, deionized,
   degassed.
3. Acetonitrile, HPLC grade, degassed.
4. PAH reference standards,*
   appropriate to the PAH-containing
   matrix sampled.
5. Calibration stock solution,
   0.25 mg/ml.*  Check purity of each
   PAH reference standard by GC/FID,
   HPLC/fluorescence and/or melting
   point.  Purify, if necessary, by
   recrystallization.  Weigh 25 mg
   of each PAH into a 100-ml volumetric
   flask; dilute to volume with
   acetonitrile.  Stable six months
   if refrigerated and protected
   from  light.
   *See  SPECIAL  PRECAUTIONS.
EQUIPMENT:
 1. Sampler:
    a. Filter.  PTFE-laminated membrane filter, 2-ym
       pore size, 37-mn diameter (ZEFLOUR, Hembrana,
       Pleasanton, CA or equivalent), backed by a
       gasket (37-mn 00, 32-flro ID) cut from a cellulose
       support pad, in cassette filter holder.
       NOTE 1: If sampling is to be done in bright
               sunlight, use opaque or foil-wrapped
               cassettes to prevent sample degradation.
       NOTE 2: Take filters to be preweighed from the
               filter package and allow to equilibrate
               24 hrs with laboratory atmosphere before
               taring.
    b. Sorbent tube, connected to filter with minimum
       length PVC tubing.  Plastic caps are required
       after sampling.  Washed XAD-2 resin (front =
       100 mg; back = 50 mg) (Supelco ORBO 43 or
       equivalent).  Pressure drop at 2 L/min airflow
       1.6 to 2 kPa (15 to 20 cm H^).
 2. Personal sampling pump capable of operating for
    8 hrs at 2 L/min, with flexible connecting tubing.
 3. Aluminum foil.
 4. Vial, scintillation, 20-mL, glass, PTFE-lined cap.
 5. Refrigerant, bagged.
 6. Culture tubes, PTFE-lined screw cap, 13-mm x
    100-mn.
 7. Forceps.
 8. Filters, 0.45-pm, PTFE or nylon  (for filtering
    sample solutions).
 9. Pipet, 5-mL.
 10. Syringe or micropipets, 1- to 100-yL.
 11. Ultrasonic bath.
 12. HPLC, with gradient capability, fluorescence
    (excitation 9 240 nm, emission 9 425 nm) and UV
    (254 nm) detectors in series, electronic
    integrator, and column [HC-OOS-SILX (Perkin-Elmer
    Corp.), Vydac 201TP (The Separations Group) or
    equivalent; see page 5506-1].
 13. Volumetric flasks, 10- and 100-mL.
 14. Lighting in laboratory:  incandescent or
    UV-shielded fluorescent.
 15. Kuderna-Danish extractor.
 SPECIAL PRECAUTIONS:  Treat benzene and all polynuclear aromatic hydrocarbons as carcinogens
 Neat  compounds  should be weighed in a glove box.  Spent samples and unused standards aretoxic
 waste.  Regularly check counter tops and equipment with "black light" for fluorescence as an
 indicator of  contamination by PAH.
5/15/85
   5506-2

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METHOD;  5506	POLYNUCLEAR AROMATIC HYDROCARBONS

SAMPLING:
 1. Calibrate each personal sampling pump with a representative sampler in line.
 2. Take personal samples at 2 L/min for a total sample size of 200 to 1000 L.  Take a
    concurrent set of eight replicate area samples at 2 to 4 L/min on preweighed,  2-um PTFE
    filters in an area of highest expected PAH concentration.
    NOTE: The area samples are needed for solvent selection  (step 7).
 3. Immediately after sampling, transfer the filter carefully with forceps to a scintillation
    vial.  Hold filter at edge to avoid disturbing the deposit.  Cap the scintillation  vial  and
    wrap it in aluminum foil.
    NOTE: This step is necessary to avoid loss of analytes due to sublimation and degradation
          by light.
 4. Cap the sorbent tube and wrap it in aluminum foil.
 5. Ship to laboratory in insulated container with bagged refrigerant.

SAMPLE PREPARATION:
NOTE: UV light may degrade PAH.  Use yellow, UV-absorbing shields for fluorescent lights or use
       incandescent lighting,
 6. Refrigerate samples upon receipt at  laboratory.
 7. Determine optimum extraction solvent.
    a. Allow the preweighed area filter  samples to equilibrate 24 hrs with the laboratory
       atmosphere.
    b. Weigh the area filters.  Determine total weight collected on each.
    c. Extract the first pair of area  filters with acetonitrile, the  second with benzene, the
       third with cyclohexane, and  the fourth with methylene chloride,  according to step 8.
       NOTE: Use alternate solvents,  if  appropriate.  PAH of interest may be entrained within,
             and adsorbed by, particulate matter collected  on the  filter.  It  is necessary  to
             determine the solvent  which maximizes recovery of  the PAH  from each sample
             matrix.  For example,  methylene chloride [2,3] and  benzene:ethanol  (4:1 v/v) [4]
             have been recommended  for extraction of  PAH from diesel  exhaust particulate.
    d. Analyze the extracts for the PAH  of  interest  (steps  10 through 18).  Normalize  the total
       mass of PAH found to the mass of  sample  collected.
    e. Choose the solvent which gives  the highest recovery  of PAH  of interest.  Use the solvent
       chosen to extract the personal  filter samples.
 8. Extract filters.
    a. Add 5.0 mL of the solvent chosen  in  step 7 to  each scintillation vial  containing a
       filter.  Start media and reagent  blanks  at this step.
    b. Cap and let sit  15 to 20 min in an ultrasonic  bath.
       NOTE 1: Soxhlet extraction may  be required when large amounts of highly adsorptive
               particulate matter  (e.g.,  fly ash or diesel  soot) are present.
       NOTE 2: The sample must be dissolved in  acetonitrile for  chromatography.   If needed,
               perform solvent exchange  as  follows:
               CAUTION: To avoid  loss  of volatile components, do not allow the sample  to go to
                        dryness at  any time.
                (1) After filtration (step  10),  take the  sample to  near dryness in a
                   Kuderna-Danish extractor.
                (2) Add ca.  1 mL acetonitrile,  take to near  dryness, and adjust final volume to
                    1.0 mL with acetonitrile and filter again.
  9.  Desorb  PAH  from  sorbent.
     a. Score  each  sorbent  tube with a  file  in  front of the  front (larger) sorbent section.
        Break  tube  at  score  line.
 5/15/85                                     5506-3

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POLYNUCLEAR AROHATIC HYDROCARBONS		METHOD:  5506

    b. Transfer glass wool plug and front sorbent section to a culture tube.  Discard the foam
       plug.  Transfer back sorbent section to a second culture tube.
    c. Add 5.0 mL acetonitrile to each culture tube.  Cap the culture tubes.
    d. Allow samples to sit for 30 min.  Swirl occasionally.
10. Filter all sample extracts through an 0.45-ym membrane  filter.

CALIBRATION AND QUALITY CONTROL:
11. Calibrate daily with at least five working standards.
    a. Dilute aliquots of calibration stock solution with acetonitrile in 10-mL volumetric
       flasks (e.g., to 2.5, 0.5, 0.1, 0.02, and 0.002 ug/mL).
    b. Intersperse working standards and samples in the measurements.
    c. Prepare calibration graphs (peak area vs. ug of each PAH per sample).
12. Recovery and desorption efficiency.
    a. Determine recovery  (R) from filters and desorption efficiency (DE) from sorbent tubes at
       least once for each lot of filters and sorbent tubes used in the range of interest.
       (1) Filters.  Using a microliter syringe or micropipette, spike four filters at each of
           five concentration levels with a mixture of the analytes.  Allow the filters to dry
            in the dark overnight.  Analyze the filters (steps 8, 10, and 14 through 16.
           Prepare graphs of R vs. amounts found.
           NOTE: This step may not be used for some highly adsorptive particulate matrices for
                 which calibration by the method of standard additions may be more accurate.
       (2) Sorbent tubes.  Transfer an unused front sorbent section to a culture tube.  Prepare
           a  total of 24  culture tubes in order to measure  DE at five concentration levels plus
           blanks  in quadruplicate.  Using a microliter syringe or micropipette, add
            calibration stock solution directly to sorbent.  Cap culture tubes and allow to
           stand overnight.  Analyze  (steps 9, 10, and 14 through 16).  Prepare graphs of DE
            vs. amounts found.
    b. Check R and DE at  two levels for each sample set, in duplicate.  Repeat determination of
       R and  DE graphs if checks do not agree to within +51 of DE graph.
 13. Analyze at least three field blanks for each sample medium.

MEASUREMENT:
 14. Set  HPLC  according to manufacturer's recommendations and  to conditions on page 5506-1.
    Equilibrate column at 601 CH3CN/401 H20 at 1.0 mL/min for 15 min before injecting first
    sample.
 15. Inject  sample aliquot.  Start mobile phase gradient:
    a. Linear gradient 601 CHsCN to 1001 O^CN, 20 min.
    b. Hold at  1001 CH^CH  for 20 min.
       NOTE:  Hold  longer  if necessary to prevent carryover  of background, e.g., from coal dust.
    c. Linear gradient to initial condition, 5 min.
 16. Measure peak areas.
    NOTE 1: Approximate retention times appear in Table 3.
    NOTE 2: If peak area  is above the calibration range, dilute with appropriate solvent,
            reanalyze, and apply dilution factor in calculations.
    NOTE 3: If sample has many  interferences, additional sample cleanup may be necessary.  Many
            cleanup procedures have been published.   Liquid-liquid partitioning between
            cyclohexane and nitrcmethane [5,6] is widely used, but other techniques may be more
            appropriate for specific  samples.
 5/15/85                                      5506-4

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METHOD:  5506	POLYNUCLEAR AROHATIC HYDROCARBONS

CALCULATIONS:
17. Read the mass,  pg (corrected for R  or  DE) of  each  analyte found on the filter  (W) and
    front sorbent  (Wf) and back  sorbent  (HO) sections, and on the average media blank
    filter (B) and  front sorbent (Bf) and  back sorbent (65) sections from the calibration
    graphs.
18. Calculate concentration, C  (yg/m3), in air as the sum of the particulate concentration
    and the vapor concentration  using the  actual  air volume sampled, V (L).

                          C =  (W-B.Wf.Wb-Bf-Bb).lQ3i
                                             V

    NOTE: Uf and W^ include analyte  originally collected on the  filter as particulate, then
          volatilized during sampling.   This can  be a  significant fraction for many PAH (e.g.,
          fluoranthane, naphthalene, fluorene, anthracene, phenanthrene).

EVALUATION OF METHOD:
The fluorescence detector used  in this  method  is  both  sensitive  and selective.  The detector
can "see" as little as 50 pg of  many PAH injected on the column.  LODs for the 17 analytes
range from 50 to 350 ng per sample.   It does not  respond to non-fluorescent molecules such as
aliphatics.  The method is, therefore,  most amenable to determination of trace amounts of PAH
in mixtures of aliphatic compounds.   Successful applications include:  aluminum reduction
facilities, asphalt fume, coal  gasification plants, coal liquefaction plants, coal tar pitch,
coke oven emissions, creosote  treatment facilities, diesel exhaust, graphite electrode
manufacturing, petroleum pitch,  and  roofing tearoff operations.

This method has been evaluated by analyzing spiked filters, spiked sorbent tubes, and complete
spiked sampling trains through which were  drawn 500 L  of air [7].  Each of the three groups was
spiked with each analyte at two concentration  levels in sextuplicate.  Particular note should
be made that the effect of particulate  matter  has not  been evaluated, and every sampling matrix
is unique.  The data on the following page were obtained on spiked samplers stored refrigerated
in the dark for three months followed by measurement with HPLC.
 5/15/85                                     5506-5

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CALIBRATION RANGE (

1.
2.
3.
4.
5.
6.
7.
8.
9.
10.
11.
12.
13.
14.
15.
16.
17.
COMPOUND
ACENAPHTHENE
ACENAPHTHYLENE
ANTHRACENE
BENZ[a]ANTHRACENE
BENZO[b]FLUORANTHENE
BENZO[k IFLUORANTHENE
BENZO[ghi]PERYLENE
BENZO[a]PYRENE
BENZO[e]PYRENE
CHRYSENE
DIBENZta , h ]ANTHRACENE
FLUORANTHENE
FLUORENE
INDENO[ 1 ,2 ,3-cd]PYRENE
NAPHTHALENE
PHENANTHRENE
PYRENE
(ug per sample)
2.
1.
0.
0.
0.
0.
0.
0.
0.
0.
0 -
0 -
4 -
4 -
4 -
4 -
5 -
4 -
5 -
4 -
0.5 -
0.
0.
0.
0.
4 -
7 -
5 -
6 -
0.4 -
0.5 -
13
100
13
13
12
13
25
14
13
12
25
13
13
12
13
13
13
LOO
ug per
sample)
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
.8
.35
.05
.15
.1
.15
.2
.2
.2
.15
.2
.15
.25
.2
.25
.1
.2
MEASUREMENT PRECISION
SPIKED +
t_
SPIKED9
.058
.032
.039
.032
.027
.025
.031
.027
(O
.039
.026
.026
.031
.044
.041
.036
(C)
S
S
S
F
F
F
F
F
AIR°
.093
.075
.037
.064
.028
.027
.029
.029
(50)
(100)
(5)
(5)
(10)
(1)
(10)
(5)
(0
F
F
S
S
F
S
S
.024
.029
.050
.090
.032
.125
.070
(5)
(10)
(10)
(10)
(10)
(50)
(2)
(C)
aRSD for filter (F) where volatilization is nil  or for sorbent (S) where substantial
 volatilization may occur during sampling.
bRSD determined at the pg level shown in parenthesis for a spiked filter followed by a
 sorbent tube.  After spiking,  laboratory air was drawn through the sampling train at 2 L/min
 for 4 hrs.
cNot determined.

REFERENCES:
 [1] NIOSH Manual of Analytical Methods, 2nd ed., Vol. 1, U.S. Department of Health, Education.
     and Welfare, Publ.  (NIOSH) 77-157-A (1977).
 [2] Breuer, G. M.  Anal. Lett.. V7(A11). 1293-1306 (1984).
 [3] Zweidinger, R. B.,  S. B.  Tejada, D. Dropkins, 0.  Huisingh, and L. Claxton.  "Characteriza-
     tion of Extractable Organics in Diesel Exhaust Particulate," paper presented at Symposium
     on Diesel Particulate Emissions Measurement Characterization, Ann Arbor, MI (1978).
 [4] Swarin, S. J. and R. L. Williams.  "Liquid Chromatographic Determination of Benzo[a]pyrene
     in Diesel Exhaust Particulate:   Verification of the Collection and Analytical Methods,"
     Polynuclear Aromatic Hydrocarbons:   Physical and Biological Effects. Bjorseth, A. and
     Dennis, Eds., Battelle Press,  771-790 (1980).
 [5] Wise, S. A., et al_.  "Analytical Methods for the Determination of Polycyclic Aromatic
     Hydrocarbons on Air Particulate Matter," Polynuclear Aromatic Hydrocarbons:  Physical and
     Biological Chemistry. Cooke, Dennis and Fisher, Eds., Battelle Press, 919-929 (1982).
 [6] Novotny, M., H. L.  Lee and K.  D. Bartle.  0. Chroma tog.  Sci.. J2, 606-612 (1974).
 [7] Backup Data Report for Method 5506, Analytical Report for NIOSH Sequence 4170 (NIOSH
     unpublished, March 16, 1984).                                                        '
 [8] Studt., P., Liebigs Ann.  Chem.. 528 (1978).
 [9] Clar, E.  Polycyclic Hydrocarbons.  Academic Press (1964).
[10] Handbook of Chemistry and Physics,  62nd ed., CRC Press (1982).

METHOD REVISED BY:  B. R. Bel inky and E. J. Slick, NIOSH/DPSE.


5/15/85                                     5506-6

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HETHOO:  5506
Table 1. Formulae and physical properties.

COMPOUND (bv H.W.)
1. NAPHTHALENE
2. ACENAPHTHYLENE
3. ACENAPHTHENE
4. FLUORENE
5. ANTHRACENE
6. PHENANTHRENE
7. FLUORANTHENE
8. PYRENE
9. BENZ[a]ANTHRACENE
10. CHRYSENE
11. BENZO[b]FLUORANTHENE
12. BENZO[k]FLUORANTH£NE
13. BENZO[a]PYRENE
14. BENZO[e]PYRENE
15. BENZO[ghi]P£RYLENE
16. INDENO[l,2,3-cd]PYRENE
17. DIBENZ[a,h]ANTHRACENE
EMPIRICAL
FORMULA
ClQHs
C12H8
C12H10
Cl3"lO
C14H10
C14H10
Cl6»10
C16H10
C18H12
C18H12
C20H12
C20H12
C20H12
C20H12
C22H12
C22H12
C22H14
MOLECULAR
WEIGHT
128.17
152.20
154.21
166.22
178.23
178.23
202.26
202.26
228.29
228.29
252.32
252.32
252.32
252.32
276.34
276.34
278.35

DETECTOR
UV
UV
UV
UV
UV
UV
FL
FL
FL
UV
FL
FL
FL
FL
FL
FL
FL
MELTING
POINT
(OQ)
80
92-93
96.2
116
218
100
110
156
158-159
255-256
168
217
177
178-179
273
161.5-163
262
BOILING
POINT
(°Q*
218
265-275
279
293-295
340
340
—
399
—
—
—
480
—
—
—
—
—


REF.
[9]
[10]
[10]
[9]
[9]
[9]
[9]
[9]
[9]
[9]
[9]
[10]
[9]
[9]
[9]
[8]
[9]
 *Many of these compounds will sublime.
 Table 2.   Synonyms.

  COMPOUND (alphabetically)

  1.  ACENAPHTHENE
  2.  ACENAPHTHYLENE
  3.  ANTHRACENE
  4.  BENZ[a]ANTHRACENE

  5.  BENZO[b]FLUORANTHENE

  6.  BENZO[k]FLUORANTHENE
  7.  BENZO[ghi]PERYLENE
  8.  BENZO[a]PYRENE
  9.  BENZO[e]PYRENE
 10.  CHRYSENE
 11.  OIBENZ[a,h]ANTHRACENE
 12.  FLUORANTHENE
 13.  FLUORENE
 14.  INDEMOn.2.3-cd]PYRENE
 15  NAPHTHALENE
 16. PHENANTHRENE
 17. PYRENE
                            SYNONYMS
CAS* 83-32-9
CAS* 208-96-8
CAS* 120-12-7
1,2-benzanthracene; benzo[b]phenanthrene; 2B3-benzophenanthrene;
tetraphene; CAS* 56-55-3
3,4-benzofluoranthene; 2,3-benzofluoranthene;
benz[e]acephenanthrylene; B[b]F; CAS* 205-99-2
11,12-benzofluoranthene; CAS* 207-08-9
1,12-benzoperylene; CAS* 191-24-2
3,4-benzopyrene; 6,7-benzopyrene;'B[a]P; BP; CAS* 50-32-8
1,2-benzopyrene; 4.5-benzopyrene; B[e]P; CAS* 192-97-2
1,2-benzophenanthrene; benzo[a]phenanthrene; CAS* 218-01-9
1,2,5,6-dibenzanthracene; CAS* 53-70-3
benzo[jk]fluorene; CAS* 206-44-0
CAS* 86-73-7
2,3-phenylenepyrene; CAS* 193-39-5
naphthene; CAS* 91-20-3
CAS* 85-01-8
benzo[def]phenanthrene; CAS*129-00-0
 5715/85
             5506-7

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POLYNUCLEAR AROHATIC HYDROCARBONS
                                                                                    METHOD:   5506
Table 3.  Approximate PAH retention times.

                    COMPOUND	

              1. NAPHTHALENE

              2. ACENAPHTHAIENE

              3. ACENAPHTHENE

              4. FLUORENE

              5. PHENANTHRENE

              6. ANTHRACENE

              7. FLUORANTHENE

              8. PYRENE

              9. BENZ[a]ANTHRACENE

              10. CHRYSENE

              11. BENZO[e]PYRENE

              12. BENZO[b]FLUORANTHENE

              13. BENZO[k]FLUORANTHENE

              14. BENZO[a]PYRENE

              15. OIBENZ[a,h]ANTHRACENE

              16. BENZO[ghi]PERYLENE

              17. INOENO[l,2,3-cd]PYRENE
                RETENTION TIME (min)*

                         2.4

                         2.8

                         3.6

                         3.9

                         4.7

                         5.8

                         6.8

                         7.7

                        11.2

                        12.1

                        14.0

                        14.8

                        16.5

                        17.3

                        20.0

                        20.0

                        21.2
*NOTE: Determined with a Perkin-Elmer HC-ODS-SILX  column.  Actual  retention times will  vary
       with  individual columns and column age.
5/15/85
5506-8

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METHOD:  5506
                   POLYNUCLEAR AROMATIC HYDROCARBONS
 ACENAPHTHENE
   ACENAPHTHYLENE
ANTHRACENE
 BENZQcOANTHRACENE   BENZOCWFLUORANTHENE BENZOOQFLUORANTHENE
  BENZOC9 h HPERYLENE    BENZOCeOPYRENE
    CHRYSENE
DIBENZCa.h} ANTHRACENE
                     INDENOCl,2,3-c d^PYRENE
    PHENANTHRENE            PYRENE
                      Figure 1. Structures of PAH.
                           BENZOQOPYRENE
 FLUORANTHENE
                              NAPHTHALENE
 5/15/85
        5506-9

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TECHNICAL REPORT DATA
Please read instructions on the reverse before completing
1. REPORT NO.
EPA^t54/R-99-002c
2.
4. TITLE AND SUBTITLE
Final Report - Emissions Testing of Combustion Stack and Pushing Operations at Coke
Battery No. 5/6 at ABC Coke in Birmingham, Alabama
Volume III of III
7. AUTHOR(S)
Franklin Meadows
Daniel F. Scheffel
9. PERFORMING ORGANIZATION NAME AND ADDRESS
Pacific Environmental Services, Inc.
Post Office Box 12077
Research Triangle Park, North Carolina 27709-2077
12. SPONSORING AGENCY NAME AND ADDRESS
U.S. Environmental Protection Agency
Office of Air Quality Planning and Standards
Emissions, Monitoring and Analysis Division
Research Triangle Park, North Carolina 2771 1
3. RECIPIENT'S ACCESSION NO.
5. REPORT DATE
February 1999
6. PERFORMING ORGANIZATION CODE
8. PERFORMING ORGANIZATION REPORT NO.
10. PROGRAM ELEMENT NO.
11. CONTRACT/GRANT NO.
68-D-98-004
13. TYPE OF REPORT AND PERIOD COVERED
Final
14. SPONSORING AGENCY CODE
15. SUPPLEMENTARY NOTES
16. ABSTRACT
The United States Environmental Protection Agency (EPA) is investigating the coke making industry to characterize hazardous air pollutants (HAPs)
emitted from coke pushing operations and combustion (underfire) stacks. This test report addresses pushing emissions from a coke oven, and emissions
from the combustion (underfire) stack that serves Coke Battery No. 5/6 at ABC Coke in Birmingham, Alabama. The purpose of this test program was to
quantify emissions from the inlet and outlet of the baghouse controlling emissions from the coke pushing operation and to quantify emissions from the
combustion outlet stack. The data may be used by the EPA in the future to support a residual risk assessment for coke oven facilities.
The testing was performed to quantify uncontrolled and controlled air emissions of filterable particulate matter (PM), methylene chloride extractable
matter (MCEM) and 19 polycyclic aromatic hydrocarbons (PAHs) including acenaphthene, acenaphthylene, anthracene, benzo(a)anthracene,
benzo(a)pyrene, benzo(b)fluoranthene, benzo(e)pyrene, benzo(k)fluoranthene, benzo(ghi)perylene, chrysene, dibenzo(a,h)anthracene, fluoranthene,
fluorene, indeno(l,2,3-cd)pyrene, 2-methylnapthalene, napthalene, perylene, phenanthrene, and pyrene. In addition, following the PM and MCEM
analyses, the samples were analyzed to screen for the presence of 17 trace metals. Baghouse dust samples were also collected and analyzed for 16 trace
metals. Simultaneous testing was performed at the inlet and outlet of the baghouse controlling emissions from the coke pushing operation. Sampling
was also performed on the combustion outlet stack. In addition to pollutant testing, oxygen (O2) and carbon dioxide (COJ were measured at each
location. During the sampling program, Research Triangle Institute (RTI), another EPA contractor, monitored and recorded process and emission
control system operating parameters.
This volume (Volume HI) is comprised of 379 pages and consists of Appendices: E (Calculations), F (QA/QC Data), G (Participants), and
H (Sampling and Analytical Procedures).
17. KEY WORDS AND DOCUMENT ANALYSIS
a. DESCRIPTIONS
Baghouse
Coke Ovens
Emission Measurements
Hazardous Air Pollutants
Metals
Methylene Chloride Extractable
Matter
Particulate Matter
Polycyclic Aromatic Hydrocarbons
18. DISTRIBUTION STATEMENT
Unlimited
b. IDENTIFIERS/OPEN ENDED TERMS

19. SECURITY CLASS (This Report)
Unclassified
20. SECURITY CLASS (This page)
Unclassified
c. COASTI Field/Group

21. NO. OF PAGES
1647
22. PRICE
EPA Form 2220-1 (Rev. 4-77)  PREVIOUS EDITION IS OBSOLETE
F:\U\FMeadows\TRD.Frm\WP 6.1

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