United States
Environmental Protection
Agency
Office of Air Quality
Planning and Standards
Research Triangle Park, NC 27711
EPA-454/R-00-040d
September 2000
Air
EVALUATION OF PARTICULATE MATTER
E PA (PM) CONTINUOUS EMISSION
MONITORING SYSTEMS (CEMS)
Final Report
Volume 4 — Appendices for RCA No. 2
-------
Volume 4—Appendices for RCA No. 2
Table of Contents
RCA #2 Appendix A—Process Operating Conditions
RCA #2 Appendix B—Computer Results for M17 Tests
RCA #2 Appendix C—M17 Field Sampling Data Sheets
RCA #2 Appendix D—M17 Field Laboratory Particulate Weight Data
RCA #2 Appendix E—M17 Post-Test Calibration Sheets
RCA #2 Appendix F—PM CEMS Data for Each Run
RCA #2 Appendix G—Statistical Analysis Data and Graphs from Initial Correlation
and RCA Data
-
*
U S Environmental Protection Agency
Region 5, Library (PL-12J)
77 West Jackson Boulevard, 12tn Floor
Chicago, 11 60604-3590
-------
RCA #2 Appendix A
Process Operating Conditions
MRJ-OPPT\R4703-02-07 Appendices Covers WPD
-------
Time
Parameters
Steam Flow (klb/hr)
Steam Temp (deg F)
Coal Row (Ib/hr)
Boiler O2s (Avg)
west
central
east
East Undergrate Air Flow (Ib/hr)
West Undergrate Air Flow (Ib/hr)
Baghouse Inlet Temp (deg F)
Baghouse Outlet Temp (deg F)
Baghouse DP (in H20)
ID Fan Suet. Press, (in H2O)
2A SDA Outlet Temp (deg F)
2A Atomizer KW (KW)
U2 % Solids (%)
2A Lime Flow (gpm)
Opacity
Time
Parameters
Steam Flow (klb/hr)
Steam Temp (deg F)
Coal Flow (Ib/hr)
Boiler O2s (Avg)
west
central
east
East Undergrate Air Flow (Ib/hr)
West Undergrate Air Flow (Ib/hr)
Baghouse Inlet Temp (deg F)
Baghouse Outlet Temp (deg F)
Baghouse DP (in H2O)
ID Fan Suet. Press, (in H2O)
2A SDA Outlet Temp (deg F)
2A Atomizer KW (KW)
U2 % Solids (%)
2A Lime Row (gpm)
Opacity
Run #30
12:15
I
275.9
963
30857
2.7
: 3.6
3
: 1.5
133341
130948
185.9
171.5
10
-25.5
185.6
66
35.6
2.6
8.40
Run #31
12:30
276.2
961
36000
2.8
3.7
2.8
1.8
130438
133543
186.3
172.9
9.7
-24.9
185.9
66
35.6
2.3
15:45
271.7
945
27000
2.9
4.8
2.8
1.2
131457
132528
185.2
174.1
10.3
-25.5
185
66
33.8
5
12:45
275.3
963
28421
2.6
3.6
2.5
1.7
130182
130029
184.7
173.6
10
-25.4
183.4
67
35.3
5.3
16:00
266.1
945
26341
3.1
5.5
2.4
1.5
129271
128296
185.4
174.3
9.8
-25.4
182.4
68
35.7
5.2
13:00
279.6
959
15652
2.4
3.4
2.3
1.4
130598
130059
186.3
173.7
10
-19.6
186.3
65
35.4
3.9
16:15
267.4
942
28421
2.9
5.3
2.6
0.8
128952
131384
184.9
173.7
10
-25.5
190
65
35
2.1
13:15
277.5
960
27000
2.4
3.6
2.5
1.1
127862
132575
183.8
176.6
9.8
-25.3
186.5
65
35.2
3.3
16:30
269.2
948
30000
3.2
5.6
3.4
0.5
127955
132474
183.7
173.7
9.7
-25.4
190
63
35.3
4.7
13:30
273.8
952
27692
2.5
3.5
2.5
1.5
130396
129388
185.4
175
10.3
-25.5
184
66
34.8
4.3
16:45
271.3
947
26341
3.1
5.4
3.4
0.4
131841
130199
186.4
174.8
11
-25.8
197
58
35
5.4
13:45
276.4
961
27692
2.4
3.2
2.4
1.6
130294
129878
187.3
175.5
10.1
-25.2
181.1
70
35
3.6
14:00
273.9
967
28421
2.5
3.6
2.4
1.5
129859
129698
187.2
175.6
10.4
-25.6
187.1
67
37.2
3.1
Run #30 Avg
276.1
961
27717
2.5
3.5
2.6
1.5
130371.3
130764.8
185.9
174.3
10.0
-24.6
185.0
66.5
35.5
3.6
Run #31 Avg
269.1
945.4
27620.6
3.0
5.3
2.9
0.9
129895.2
130976.2
185.1
174.1
10.2
-25.5
188.9
64.0
35.0
4.5
8.67
RCA#2 APPENDIX A
-------
Run #32
Time 9:00 9:15
Parameters
Steam Flow (klb/hr)
Steam Temp (deg F)
Coal Flow (Ib/hr)
Boiler 02s (Avg)
west
central
east
East Undergrate Air Flow (Ib/hr)
West Undergrate Air Flow (Ib/hr)
Baghouse Inlet Temp (deg F)
Baghouse Outlet Temp (deg F)
Baghouse DP (in H2O)
ID Fan Suet. Press, (in H2O)
2A SDA Outlet Temp (deg F)
2A Atomizer KW (KW)
U2 % Solids (%)
2A Lime Flow (gpm)
Opacity
9:30
9:45 10:00 10:15
Time
Parameters
Steam Flow (klb/hr)
Steam Temp (deg F)
Coal Flow (Ib/hr)
Boiler O2s (Avg)
west
central
east
East Undergrate Air Flow (Ib/hr)
West Undergrate Air Flow (Ib/hr)
Baghouse Inlet Temp (deg F)
Baghouse Outlet Temp (deg F)
Baghouse DP (in H2O)
ID Fan Suet. Press, (in H2O)
2A SDA Outlet Temp (deg F)
2A Atomizer KW (KW)
U2 % Solids (%)
2A Lime Flow (gpm)
Opacity 9.74
277.3
956
29189
3.6
4.2
3
125148
128462
185.7
174
11
-26.2
185.5
66
35.2
5.5
9.53
Run #33
I
I
I
\
\
274.8
951
27692
3.8
4.7
2.8
126806
129713
184.4
173.5
12.9
-26.3
186.6
67
34.7
4.4
12:00
282.7
954
28421
2.7
2.8
2.5
121658
119808
183.9
173.3
11.6
-26.6
182.5
72
34.1
4.3
275.4
950
27000
4.1
4.7
3.4
125666
128341
NA
174.1
10.8
-26.1
186.5
66
33.1
2.4
12:15
278.3
950
30000
2.8
3
2.6
122456
120456
183.9
174.2
10.4
-15.3
187.1
71
36.6
2.3
270.5
948
27000
4.3
4.7
3.9
124467
127020
NA
173.5
11.4
-26.4
185.6
67
35.7
3.5
12:30
276.4
959
26341
2.7
3.2
2.2
124716
127160
185.5
171.7
10.9
-26.3
186.3
67
34.2
4.8
276.3
947
27692
4.2
4.4
4
124832
127069
185.6
172.2
11.4
-26.3
183
65
35
4.1
12:45
277.8
958
27692
2.8
3.3
2.2
122954
125325
183.1
171.8
9.9
-25.9
182.2
70
33.2
4.7
273.5
953
30000
4.0
4.5
3.4
126596
126943
184.2
174.2
11.5
-26.5
183
66
32.7
2.9
13:00
274.6
961
34839
2.5
2.9
2.1
123898
125193
187.4
174.5
11
-19.2
184.2
71
36.2
2.7
13:15
274.4
950
28421
2.8
3.5
2
124570
127786
185.2
177.7
10.2
-25.4
186.2
66
34.9
6.8
Run #32 Avg
274.6
950.8
28095.5
4.0
4.5
3.4
#DIV/0!
125585.8
127924.7
185.0
173.6
11.5
-26.3
185.0
66.0
34.4
3.8
Run #33 Avg
277.4
955.3
29285.7
2.7
3.1
2.3
#DIV/0!
123375.3
124288.0
184.8
173.9
10.7
-23.1
184.8
69.5
34.9
4.3
RCA#2 APPENDIX A
-------
Time
Parameters
Steam Flow (klb/hr)
Steam Temp (deg F)
Coal Flow (Ib/hr)
Boiler O2s (Avg)
west
central
east
East Undergrate Air Flow (Ib/hr)
West Undergrate Air Flow (Ib/hr)
Baghouse Inlet Temp (deg F)
Baghouse Outlet Temp (deg F)
Baghouse DP (in H20)
ID Fan Suet. Press, (in H2O)
2A SDA Outlet Temp (deg F)
2A Atomizer KW (KW)
U2 % Solids (%)
2A Lime Flow (gpm)
Opacity
Time
Parameters
Steam Row (klb/hr)
Steam Temp (deg F)
Coal Flow (Ib/hr)
Boiler O2s (Avg)
west
central
east
East Undergrate Air Flow (Ib/hr)
West Undergrate Air Flow (Ib/hr)
Baghouse Inlet Temp (deg F)
Baghouse Outlet Temp (deg F)
Baghouse DP (in H2O)
ID Fan Suet. Press, (in H2O)
2A SDA Outlet Temp (deg F)
2A Atomizer KW (KW)
U2 % Solids (%)
2A Lime Row (gpm)
Opacity
Run #34
15:00
275.8
964
29189
2.8
: 3.1
2.5
123531
124870
184.5
175.5
10.9
-26.1
184.6
68
35.5
4.5
9.38
Run #35
9:00
276.8
948
28421
3.7
: 3.3
4.1
119739
122163
187.1
174.2
10.2
-25.1
185.1
62
35.4
5.6
8.52
15:15
275.5
956
30000
3.4
4.2
2.6
121363
120375
184.9
175.8
10.8
-26.1
185.4
69
36.1
6.1
9:15
275.6
954
30000
3.5
3.3
3.7
120992
121981
185
175.7
10.6
-25
184.6
64
33.4
5.5
15:30
276.9
952
29189
3.5
4.1
2.9
121472
119250
184.7
175.9
11.1
-26.1
184.2
70
35.3
4.7
9:30
276.7
947
27692
3.6
3.4
3.7
119364
120746
182.7
175.6
10.7
-24.9
184
65
33.5
4.6
15:45
275.9
950
27000
3.5
4.2
2.8
121199
118819
184.5
174.8
10.7
-25.9
181.2
70
35.7
6.9
9:45
276.7
953
29189
3.3
3.1
3.6
3.1
120487
120213
183.4
176.1
10.4
-25.7
184.8
65
34.6
5.6
16:00
276.4
952
27692
3.5
3.9
3
121308
119044
186.1
175.5
10.1
-25.4
186
69
35.1
6.2
10:00
274.3
951
28421
3.0
3.4
3.6
2
118951
119794
185.9
176.1
12
-26.1
185.8
63
35.3
6.1
16:15
277.8
952
27692
3.6
4.3
2.9
120323
119393
184.8
174.7
10.3
-26
186.8
67
34.5
4.7
10:15
272.1
955
29189
3.6
3.4
3.8
119813
118767
184
175.9
11.4
-25.8
186
64
36.2
5.9
Run #34 Avg
276.4
954.3
28460.3
3.4
4.0
2.8
#DIV/0!
121532.7
120291.8
184.9
175.4
10.7
-25.9
184.7
68.8
35.4
5.5
Run #35 Avg
275.4
951.3
28818.7
3.4
3.3
3.8
2.6
119891.0
120610.7
184.7
175.6
10.9
-25.4
185.1
63.8
34.7
5.6
RCA#2 APPENDIX A
-------
Run #36
Time 11:15
Parameters
Steam Flow (klb/hr)
Steam Temp (deg F)
Coal Flow (Ib/hr)
Boiler O2s (Avg)
west
central
east
East Undergrate Air Flow (Ib/hr) 119001
West Undergrate Air Flow (Ib/hr)
Baghouse Inlet Temp (deg F)
Baghouse Outlet Temp (deg F)
Baghouse DP (in H2O)
ID Fan Suet. Press, (in H2O)
2A SDA Outlet Temp (deg F)
2A Atomizer KW (KW)
U2 % Solids (%)
2A Lime Row (gpm)
Opacity
Time
Parameters
Steam Row (klb/hr)
Steam Temp (deg F)
Coal Flow (Ib/hr)
Boiler O2s (Avg)
west
central
east
East Undergrate Air Flow (Ib/hr)
West Undergrate Air Flow (Ib/hr)
Baghouse Inlet Temp (deg F)
Baghouse Outlet Temp (deg F)
Baghouse DP (in H2O)
ID Fan Suet. Press, (in H2O)
2A SDA Outlet Temp (deg F)
2A Atomizer KW (KW)
U2 % Solids (%)
2A Lime Flow (gpm)
Opacity
11:30 11:45 12:00 12:15
274.3
957
29189
3.3
2.8
3.7
119001
122334
186.6
175.4
11.8
-26.4
185.4
64
33.5
6.1
10.49
ton #37
23:30
202.3
952
19286
5.4
5.6
5.2
99793
98370
184.4
172.6
5.9
-16.5
185.3
50
33.2
6.6
9.65
273.7
943
26341
3.4
3.1
3.6
119355
120291
182.5
176.6
15.2
-26
183.9
64
33.4
4.8
23:45
203.4
948
19286
5.3
5.2
5.3
100394
99762
184.5
173.7
7.7
•16.3
180.4
57
35.8
5.6
269.1
952
28421
3.7
3.4
4
118559
120378
186.4
176.5
11.4
-25.7
184.5
68
32.7
5.1
0:15
208.5
952
19636
4.5
5.2
5.2
3.2
101188
99446
185.9
173.7
6.3
-17.2
185.2
50
33.5
3.2
270.6
952
29189
3.9
3.3
4.4
120340
118642
183.7
174.9
10.7
-25
184.5
69
36.5
6
0:30
206.6
952
20000
4.8
5
5.5
3.8
102053
100128
184
173
6.1
-17
184
47
34.8
6.6
275.8
951
27000
3.4
2.7
4.1
120414
121709
185.5
173.3
11.2
-25.6
182.6
70
35.3
5.6
0:45
204
952
20000
4.9
5.2
5.4
4
100947
98108
186.9
173.1
5.3
-16
187
44
36.9
5.9
Run #36 Avg
272.7
951.0
28028.0
3.5
3.1
4.0
#DIV/0!
119533.8
120670.8
184.9
175.3
12.1
-25.7
184.2
67.0
34.3
5.5
Run #37 Avg
205.0
951.2
19641.6
5.0
5.2
5.3
3.7
100875.0
99162.8
185.1
173.2
6.3
-16.6
184.4
49.6
34.8
5.6
RCA#2 APPENDIX A
-------
Run #38
Time 1:45
Parameters
Steam Flow (klb/hr)
Steam Temp (deg F)
Coal Flow (Ib/hr)
Boiler 02s (Avg)
west
central
east
East Undergrate Air Flow (Ib/hr)
West Undergrate Air Flow (Ib/hr)
Baghouse Inlet Temp (deg F)
Baghouse Outlet Temp (deg F)
Baghouse DP (in H2O)
ID Fan Suet. Press, (in H2O)
2A SDA Outlet Temp (deg F)
2A Atomizer KW (KW)
U2 % Solids (%)
2A Lime Flow (gpm)
Opacity
Time
Parameters
Steam Flow (klb/hr)
Steam Temp (deg F)
Coal Flow (Ib/hr)
Boiler O2s (Avg)
west
central
east
East Undergrate Air Flow (Ib/hr)
West Undergrate Air Flow (Ib/hr)
Baghouse Inlet Temp (deg F)
Baghouse Outlet Temp (deg F)
Baghouse DP (in H2O)
ID Fan Suet. Press, (in H2O)
2A SDA Outlet Temp (deg F)
2A Atomizer KW (KW)
U2 % Solids (%)
2A Lime Flow (gpm)
Opacity
2:00
2:15
2:30 2:45
3:00
207.3
947
20000
4.8
5
5.4
4.1
101488
98470
185.7
173.4
5.2
-15.9
182.2
52
33.2
4.6
7.84
lun #39
3:45
203.3
951
19636
5.1
5.1
5.3
5
101257
100145
186.7
173
5.6
-16.1
186.1
51
34.3
7.1
7.76
200.6
951
19286
4.8
4.9
5.2
4.2
100871
98661
186.1
173.5
5.6
-16.2
188.1
49
35.4
5.4
4:00
202.4
949
20377
5.1
4.7
5.1
5.5
101339
100764
184.3
173.9
5.7
-16.4
185.6
50
35.4
5.3
202.4
949
19636
5.0
5.2
5.3
4.4
100400
98714
184.8
174.5
5.9
-16.5
190.8
48
35.6
5.5
4:15
206.4
952
20769
4.9
4
5.2
5.6
101440
101029
183.4
173.4
5.2
-15.8
186
49
36.1
5.4
203.8
954
19636
5.0
5
5.5
4.4
100204
97735
184.7
173.4
5.4
-16
185.2
49
35.9
5.3
4:30
208.3
952
20377
4.9
3.7
5
5.9
101983
100248
183.1
173.4
6.1
-16.7
184.2
50
33.6
3.1
203.2
951
20000
5.0
5.2
5.4
4.3
101418
98900
185.8
173.4
5.9
-10.5
184
50
33.1
4.4
4:45
205.9
951
19636
5.0
4.2
5.1
5.7
102443
99858
183.4
173.3
5.1
-15.9
189.5
48
33.4
5.1
208.5
949
19286
4.9
4.9
5.3
4.6
100175
98167
185.9
174.5
5.2
-15.8
183.1
51
35.7
3.7
5:00
209.3
951
20769
4.9
4.3
5
5.3
101803
99948
186.6
172.8
6.2
-17.3
187.4
47
34.1
4.9
Run #38 Avg
204.3
950.2
19640.7
4.9
5.0
5.4
4.3
100759.3
98441.2
185.5
173.8
5.5
-15.2
185.6
49.8
34.8
4.8
Run #39 Avg
205.9
951.0
20260.7
5.0
4.3
5.1
5.5
101710.8
100332.0
184.6
173.3
5.7
-16.4
186.5
49.2
34.5
5.2
RCA#2 APPENDIX A
-------
Time
Parameters
Steam Flow (klb/hr)
Steam Temp (deg F)
Coal Flow (Ib/hr)
Boiler 02s (Avg)
west
central
east
East Undergrate Air Flow (Ib/hr)
West Undergrate Air Flow (Ib/hr)
Baghouse Inlet Temp (deg F)
Baghouse Outlet Temp (deg F)
Baghouse DP (in H2O)
ID Fan Suet. Press, (in H2O)
2A SDA Outlet Temp (deg F)
2A Atomizer KW (KW)
U2 % Solids (%)
2A Lime Flow (gpm)
Opacity
Time
Parameters
Steam Flow (klb/hr)
Steam Temp (deg F)
Coal Row (Ib/hr)
Boiler O2s (Avg)
west
central
east
East Undergrate Air Flow (Ib/hr)
West Undergrate Air Flow (Ib/hr)
Baghouse Inlet Temp (deg F)
Baghouse Outlet Temp (deg F)
Baghouse DP (in H2O)
ID Fan Suet. Press, (in H2O)
2A SDA Outlet Temp (deg F)
2A Atomizer KW (KW)
U2 % Solids (%)
2A Lime Flow (gpm)
Opacity
Run #40
9:00
218.2
959
24000
4.5
: 4
7.8
1.8
103534
99769
185.1
176
5.4
-16.2
186.7
50
35.4
1.1
Run #41
11:15
1
199.8
950
20000
5.0
: 6.3
6
: 2.7
i 98426
96231
I 187.7
I 176.6
I 7.3
-16.9
190.6
52
I 35.7
1.9
9:15
177.9
964
18305
5.6
6.4
5.2
5.3
97013
94466
186.5
174.9
4.9
-14.7
' 185.7
46
34.8
9.7
11:30
204.9
949
19636
4.9
6.4
5.7
2.5
98034
97526
176.4
5.4
-16.4
182.6
53
34.9
6.8
9:30
128.4
942
12857
8.2
8.8
7.3
8.5
86327
83607
183.8
175.6
4.4
-12.7
183.9
43
35.4
9.7
11:45
208.4
947
19636
4.8
6.5
5.5
2.4
99368
96381
183
176.3
6
-17.2
183.9
54
34.3
3.7
9:45
205
944
20769
5.6
5.1
8.3
3.4
101109
96746
184.8
176
5.2
-15
187.1
45
35
9.7
12:00
211.6
947
19286
4.5
6.4
5.3
1.9
100741
98661
175
175.3
5,5
-16.3
179.7
59
35.5
0.9
10:00
214.5
950
20769
4.2
4.3
5.6
2.7
102241
100094
183.2
175.5
6
-16.8
188.4
47
34.6
9.7
12:15
239
967
28421
4.8
3.9
5.6
107541
107168
184.2
175.6
7.1
-18.5
186.2
58
35.6
7.9
10:15
252.3
956
33750
4.6
4.6
119823
120164
185
178.2
8.7
-20.8
184.8
56
34.6
0.6
12:30
243.8
935
24545
4.0
4.3
3.7
106003
105497
183
174.9
9.4
-21.1
185.7
56
35.7
6.1
Run #40 Avg
199.4
952.5
21741.7
5.5
5.7
6.5
4.3
101674.5
99141.0
184.7
176.0
5.8
-16.0
186.1
47.8
35.0
6.8
Run #41 Avg
217.9
949.2
21920.7
4.7
5.6
5.3
2.4
101685.5
100244.0
182.6
175.9
6.8
-17.7
184.8
55.3
35.3
4.6
RCA#2 APPENDIX A
-------
Time
Parameters
Steam Flow (klb/hr)
Steam Temp (deg F)
Coal Row (Ib/hr)
Boiler O2s (Avg)
west
central
east
East Undergrate Air Flow (Ib/hr)
West Undergrate Air Flow (Ib/hr)
Baghouse Inlet Temp (deg F)
Baghouse Outlet Temp (deg F)
Baghouse DP (in H20)
ID Fan Suet. Press, (in H2O)
2A SDA Outlet Temp (deg F)
2A Atomizer KW (KW)
U2 % Solids (%)
2A Lime Flow (gpm)
Opacity
Run #42
14:00
243.5
956
28421
4.1
4
4.2
111401
1 12460
182.8
179
9
-20.1
183.6
57
36.5
6.9
14:15
208.2
928
18947
4.3
6.2
2.3
104184
103783
185.1
177.2
9.3
-12.2
183.8
56
35.7
3.9
14:30
212.7
942
20000
4.9
5.8
3.9
99591
98088
184.5
177.4
6.8
-17.2
184.5
55
33.6
0.9
14:45
216.1
950
21176
4.9
5.6
4.1
100395
99436
185.2
177.8
72,
-18.1
190.9
52
35
8.6
15:00
204.7
955
21600
4.9
5.2
4.5
99218
98256
185.2
177.2
6.6
-16.3
193.5
53
35.1
5.7
Run #42 Avg
217.0
946.2
22028.8
4.6
5.4
3.8
#DIV/0!
102957.8
102404.6
184.6
177.7
7.8
-16.8
187.3
54.6
35.2
5.2
RCA#2 APPENDIX A
-------
RCA #2 Appendix B
Computer Results for M17 Tests
MRJ-OPPT\R4703-02-07 Appendices Covers WPD
-------
FILE NAME - 30A
RUN # - 30 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/16/99 Time: 1215-1405
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Feet)= 203.524
Final Meter Volume (Cubic Feet)= 238.517
Meter Factor= 0.996
Final Leak Rate (cu ft/min)= 0.004
Net Meter Volume (Cubic Feet)= 34.853
Gas Volume (Dry Standard Cubic Feet)= 35.365
Barometric Pressure (in Hg)= 29.65
Static Pressure (Inches H20) = -25.90
Percent Oxygen= 4 . 2
Percent Carbon Dioxide= 15.1
Moisture Collected (ml)= 93.7
Percent Water= 11.1
Average Meter Temperature (F)= 56
Average Delta H (in H20)= 0.49
Average Delta P (in H20)= 1.567
Average Stack Temperature (F)= 178
Dry Molecular Weight= 30.58
Wet Molecular Weight= 29.19
Average Square Root of Delta P (in H20)= 1.1623
% Isokinetic= 100.3
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 100.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 4,444
Flow Rate (Actual, Cubic ft/min)= 116,110
Flow rate (Standard, Wet, Cubic ft/min)= 89,113
Flow Rate (Standard, Dry, Cubic ft/min)= 79,227
Particulate Loading - Front Half
Particulate Weight (g)= 0.0409
Particulate Loading, Dry Std. (gr/scf)= 0.0178
Particulate Loading, Actual (gr/cu ft)= 0.0121
Emission Rate (lb/hr)= 12.09
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 08:57:18
Corr. to 7% 02 & 12% C02
0.0148 0.0142
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 30A
RUN # - 30 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/16/99 Time: 1215-1405
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Meters)=
Final Meter Volume (Cubic Meters)=
Meter Factor=
Final Leak Rate (cu m/min)=
Net Meter Volume (Cubic Meters)=
Gas Volume (Dry Standard Cubic Meters)=
Barometric Pressure (mm Hg)=
Static Pressure (mm H20)=
Percent Oxygen=
Percent Carbon Dioxide=
Moisture Collected (ml)=
Percent Water=
Average Meter Temperature (C)=
Average Delta H (mm H20) =
Average Delta P (mm H20)=
Average Stack Temperature (C) =
Dry Molecular Weight=
Wet Molecular Weight=
Average Square Root of Delta P (mm H20)=
% Isokinetic=
Pitot Coefficient=
Sampling Time (Minutes)=
Nozzle Diameter (mm)=
Stack Axis #1 (Meters)=
Stack Axis #2 (Meters)=
Rectangular Stack
Stack Area (Square Meters)=
Stack Velocity (Actual, m/min)=
'Flow rate (Actual, Cubic m/min) =
Flow rate (Standard, Wet, Cubic m/min)=
Flow rate (Standard, Dry, Cubic m/min)=
Particulate Loading - Front Half
Particulate Weight (g)=
Particulate Loading, Dry Std. (mg/cu m)=
Particulate Loading, Actual (mg/cu m)=
Emission Rate (kg/hr)=
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 08:57:18
5.763
6.754
0.996
0.0001
0.987
1.001
753
-658
4.2
15.1
93.7
11.1
13
12.5
39.8
81
30.58
29.19
5.8578
100.3
0.84
100.0
3.71
1.448
1.676
2.427
1,355
3,288
2,523
2,243
0.0409
40.8
27.9
5.49
Corr. to 7% 02 & 12% C02
34.0 32.5
RCA#2 APPENDIX B
-------
FILE NAME - 30A
RUN # - 30 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/16/99 Time: 1215-1405
PROJECT # - 104703.1.002.05.01
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 08:57:18
Delta P
in. H20)
2.300
2.200
1.700
0.650
0.050
2.500
2.400
2.100
0.770
0.100
2.500
2.500
2.400
1.500
0.230
2.400
2.300
2.200
1.200
0.170
2.300
2.100
1.800
0.680
0. 120
Delta H
(in. H20)
0.72
0.69
0.53
0.20
0.01
0 .78
0.75
0.66
0.24
0.03
0.79
0.79
0.76
0.47
0.07
0.76
0.72
0.69
0.38
0.05
0.73
0.67
0.57
0.21
0.03
Stack
(F)
174
177
177
177
175
178
178
178
176
175
178
179
179
180
180
180
180
180
179
178
180
178
177
178
178
T
In(F)
51
52
53
53
54
53
54
55
57
57
55
57
58
59
59
58
58
60
60
60
59
61
61
62
61
Meter T
Out (F)
51
52
53
52
53
53
53
54
54
54
54
55
55
55
56
56
56
57
57
57
58
58
58
58
58
Fraction
DRY CATCH
FILTER
Fraction
PROBE RINSE
IMPINGERS
Final Wt. Tare Wt. Blank Wt. Net Wt,
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3508 3.3137 0.0000 0.0371
Final Wt
(g)
3 .6645
0.0000
Tare Wt.
Probe Rinse Blank (mg/ml)=
Impinger Blank (mg/ml)= 0.0000
(g)
3.6607
0.0000
0.0000
Vol.
(ml)
31.6
0.0
Net Wt
(g)
0.0038
0.0000
RCA#2 APPENDIX B
-------
FILE NAME - SOB
RUN # - 30 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/16/99 Time: 1217-1407
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Feet)= 823.925
Final Meter Volume (Cubic Feet)= 859.009
Meter Factor= 1.010
Final Leak Rate (cu ft/min)= 0.005
Net Meter Volume (Cubic Feet)= 35.435
Gas Volume (Dry Standard Cubic Feet)= 35.886
Barometric Pressure (in Hg)= 29.65
Static Pressure (Inches H20)= -25.90
Percent Oxygen= 4 . 2
Percent Carbon Dioxide= 15.1
Moisture Collected (ml)= 94.5
Percent Water= 11.0
Average Meter Temperature (F)= 57
Average Delta H (in H20)= 0.51
Average Delta P (in H20)= 1.584
Average Stack Temperature (F)= 180
Dry Molecular Weight= 30.58
Wet Molecular Weight= 29.20
Average Square Root of Delta P (in H20)= 1.1713
% Isokinetic= 101.1
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 100.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 4,486
Flow Rate (Actual, Cubic ft/min)= 117,207
•Flow rate (Standard, Wet, Cubic ft/min)= 89,629
Flow Rate (Standard, Dry, Cubic ft/min)= 79,739
Particulate Loading - Front Half
Particulate Weight (g)= 0.0335
Particulate Loading, Dry Std. (gr/scf)= 0.0144
Particulate Loading, Actual (gr/cu ft)= 0.0098
Emission Rate (lb/hr)= 9.82
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 08:57:32
Corr. to 7% 02 & 12% C02
0.0120 0.0114
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 3 OB
RUN # - 30 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/16/99 Time: 1217-1407
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Meters)=
Final Meter Volume (Cubic Meters)=
Meter Factor=
Final Leak Rate (cu m/min)=
Net Meter Volume (Cubic Meters)=
Gas Volume (Dry Standard Cubic Meters)=
Barometric Pressure (mm Hg)=
Static Pressure (mm H20)=
Percent Oxygen=
Percent Carbon Dioxide=
Moisture Collected (ml)=
Percent Water=
PROG.=VER 06/27/89
11-23-1999 08:57:32
Average Meter Temperature (C)=
Average Delta H (mm H20)=
Average Delta P (mm H20)=
Average Stack Temperature (C)=
Dry Molecular Weight=
Wet Molecular Weight=
Average Square Root of Delta P (mm H20);
% Isokinetic=
Pitot Coefficient=
Sampling Time (Minutes)=
Nozzle Diameter (mm)=
Stack Axis #1 (Meters)=
Stack Axis #2 (Meters)=
Rectangular Stack
Stack Area (Square Meters)=
Stack Velocity (Actual, m/min)=
Flow rate (Actual, Cubic m/min)=
Flow rate (Standard, Wet, Cubic m/min)=
Flow rate (Standard, Dry, Cubic m/min)=
Particulate Loading - Front Half
Particulate Weight (g)=
Particulate Loading, Dry Std. (mg/cu m)
Particulate Loading, Actual (mg/cu m)=
Emission Rate (kg/hr)=
No Back Half Analysis
23.330
24.324
1.010
0.0001
1.003
1.016
753
-658
4.2
15.1
94.5
11.0
14
13.0
40.2
82
30.58
29.20
5.9032
101.1
0.84
100.0
3.71
1.448
1.676
2.427
1,367
3,319
2,538
2,258
0.0335
33.0
22.4
4.46
Corr. to 7% 02
27.5
& 12% C02
26.2
RCA#2 APPENDIX B
-------
FILE NAME - 3 OB
RUN # - 30 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/16/99 Time: 1217-1407
PROJECT # - 104703.1.002.05.02
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 08:57:32
Delta P
(in. H20)
2.600
2.500
2.100
1.100
0.160
2.400
2.000
1.800
0.730
0.120
2.300
2.100
1.800
0.680
0.100
2.300
2.200
2.100
0.930
0.130
2.700
2.600
2.300
1.700
0.150
Delta H
(in. H20)
0.85
0.81
0.68
0.35
0.05
0.78
0.65
0.58
0.23
0.03
0.75
0.68
0.58
0.22
0.03
0.75
0.71
0.68
0.30
0 . 04
0.88
0.85
0.75
0.55
0.04
Stack
(F)
177
179
180
179
178
178
181
179
178
178
179
182
182
182
182
182
182
182
181
180
182
180
181
182
181
T Meter T
In(F)
54
54
55
55
55
55
55
56
57
57
57
58
57
58
58
58
58
59
59
60
59
59
61
62
62
Out (F)
53
54
54
55
55
55
55
55
56
56
56
57
56
57
57
57
57
58
58
58
59
59
60
60
60
Fraction
DRY CATCH
FILTER
•Fraction
PROBE RINSE
IMPINGERS
Final Wt. Tare Wt. Blank Wt. Net Wt,
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3408 3.3087 0.0000 0.0321
Final Wt. Tare Wt.
(g)
3.5871
0.0000
Probe Rinse Blank (mg/ml)=
Impinger Blank (mg/ml)= 0.0000
(g)
3.5857
0.0000
0.0000
Vol.
(ml)
31.5
0.0
Net Wt
(g)
0.0014
0.0000
RCA#2 APPENDIX B
-------
FILE NAME - 31A
RUN # - 31 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/16/99 Time: 1520-1645
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Feet)= 238.859
Final Meter Volume (Cubic Feet)= 266.079
Meter Factor= 0.996
Final Leak Rate (cu ft/min)= 0.002
Net Meter Volume (Cubic Feet)= 27.111
Gas Volume (Dry Standard Cubic Feet)= 27.394
Barometric Pressure (in Hg)= 29.60
Static Pressure (Inches H20)= -26.00
Percent Oxygen= 4 . 5
Percent Carbon Dioxide= 14.6
Moisture Collected (ml)= 81.1
Percent Water= 12 . 2
Average Meter Temperature (F)= 57
Average Delta H (in H20)= 0.52
Average Delta P (in H20)= 1.640
Average Stack Temperature (F) = 177
Dry Molecular Weight= 30.52
Wet Molecular Weight= 28.98
Average Square Root of Delta P (in H20)= 1.1986
% Isokinetic= 101.5
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 4,601
Flow Rate (Actual, Cubic ft/min)= 120,207
Flow rate (Standard, Wet, Cubic ft/min)= 92,182
Flow Rate (Standard, Dry, Cubic ft/min)= 80,901
Particulate Loading - Front Half
Particulate Weight (g)= 0.0293
Particulate Loading, Dry Std. (gr/scf)= 0.0165
Particulate Loading, Actual (gr/cu ft) = 0.0111
Emission Rate (lb/hr)= 11.42
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 08:57:46
Corr. to 7% 02 & 12% C02
0.0140 0.0135
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 31A
RUN # - 31 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/16/99 Time: 1520-1645
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Meters)= 6.764
Final Meter Volume (Cubic Meters)= 7.534
Meter Factor= 0.996
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.768
Gas Volume (Dry Standard Cubic Meters)= 0.776
Barometric Pressure (mm Hg)= 752
Static Pressure (mm H20) = -660
Percent Oxygen= 4.5
Percent Carbon Dioxide= 14.6
Moisture Collected (ml)= 81.1
Percent Water= 12.2
Average Meter Temperature (C)= 14
Average Delta H (mm H20)= 13.1
Average Delta P (mm H20)= 41.6
Average Stack Temperature (C) = 81
Dry Molecular Weight= 30.52
Wet Molecular Weight= 28.98
Average Square Root of Delta P (mm H20) = 6.0409
% Isokinetic= 101.5
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,402
•Flow rate (Actual, Cubic m/min) = 3,404
Flow rate (Standard, Wet, Cubic m/min)= 2,610
Flow rate (Standard, Dry, Cubic m/min)= 2,291
Particulate Loading - Front Half
Particulate Weight (g)= 0.0293
Particulate Loading, Dry Std. (mg/cu m)= 37.8
Particulate Loading, Actual (mg/cu m)= 25.4
Emission Rate (kg/hr)= 5.18
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 08:57:46
Corr. to 7% 02 & 12% C02
32.1 31.0
RCA#2 APPENDIX B
-------
FILE NAME - 31A
RUN # - 31 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/16/99 Time: 1520-1645
PROJECT # - 104703.1.002.05.01
PROG.=VER 06/27/89
11-23-1999 08:57:46
'oint #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
Delta P
(in
2.
2.
2.
1.
0.
2.
2.
2.
0.
0.
2.
1.
2.
0.
0.
2.
2.
2.
1.
0.
2.
2.
2.
1.
0.
. H20)
500
400
100
700
220
500
100
100
840
090
300
900
000
650
040
400
100
200
000
190
500
600
400
800
360
Delta H
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
79
75
66
54
06
79
66
66
26
02
73
60
63
20
01
76
66
70
31
06
79
82
76
57
11
Stack
(F)
178
179
178
177
177
178
178
177
177
178
178
177
178
176
177
177
177
178
179
178
177
177
177
177
169
T Meter T
In(F)
55
56
57
58
57
57
58
58
58
58
57
58
59
60
60
58
58
59
59
59
58
58
59
61
61
Out (F)
55
55
55
56
56
56
56
56
56
57
56
57
57
57
57
57
57
57
57
57
57
57
58
58
58
Fraction
DRY CATCH
FILTER
Fraction
PROBE RINSE
IMPINGERS
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.4017 3.3752 0.0000 0.0265
Final Wt.
(g)
3.6595
0.0000
0
Probe Rinse Blank (mg/ml)=
Impinger Blank (trig/ml) = 0.0000
Tare Wt,
(g)
3.6567
0.0000
0000
Vol.
(ml)
22.2
0.0
Net Wt,
(g)
0.0028
0.0000
RCA#2 APPENDIX B
-------
FILE NAME - 3 IB
RUN # - 31 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/16/99 Time: 1521-1646
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Feet)= 859.315
Final Meter Volume (Cubic Feet)= 886.812
Meter Factor= 1.010
Final Leak Rate (cu ft/min)= 0.004
Net Meter Volume (Cubic Feet)= 27.772
Gas Volume (Dry Standard Cubic Feet)= 28.037
Barometric Pressure (in Hg)= 29.60
Static Pressure (Inches H20)= -26.00
Percent Oxygen= 4.5
Percent Carbon Dioxide= 14.6
Moisture Collected (ml)= 73.7
Percent Water= 11.0
Average Meter Temperature (F)= 58
Average Delta H (in H20)= 0.49
Average Delta P(inH20)= 1.500
Average Stack Temperature (F)= 180
Dry Molecular Weight= 30.52
Wet Molecular Weight= 29.14
Average Square Root of Delta P (in H20) = 1.2232
% Isokinetic= 100.8
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 4,693
Flow Rate (Actual, Cubic ft/min)= 122,606
Flow rate (Standard, Wet, Cubic ft/min)= 93,634
Flow Rate (Standard, Dry, Cubic ft/min)= 83,318
Particulate Loading - Front Half
Particulate Weight (g)= 0.0188
Particulate Loading, Dry Std. (gr/scf)= 0.0103
Particulate Loading, Actual (gr/cu ft)= 0.0070
Emission Rate (lb/hr)= 7.37
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 08:58:00
Corr. to 7% 02 & 12% C02
0.0088 0.0085
10
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 3 IB
RUN # - 31 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/16/99 Time: 1521-1646
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Meters)=
Final Meter Volume (Cubic Meters)=
Meter Factor=
Final Leak Rate (cu m/min)=
Net Meter Volume (Cubic Meters)=
Gas Volume (Dry Standard Cubic Meters)=
Barometric Pressure (mm Hg)=
Static Pressure (mm H20)=
Percent Oxygen=
Percent Carbon Dioxide=
Moisture Collected (ml)=
Percent Water=
PROG.=VER 06/27/89
11-23-1999 08:58:00
Average Meter Temperature (C)=
Average Delta H (mm H20)=
Average Delta P (mm H20)=
Average Stack Temperature (C) =
Dry Molecular Weight=
Wet Molecular Weight=
Average Square Root of Delta P (mm H20)=
% Isokinetic=
Pitot Coefficient=
Sampling Time (Minutes)=
Nozzle Diameter (mm)=
Stack Axis #1 (Meters)=
Stack Axis #2 (Meters)=
Rectangular Stack
Stack Area (Square Meters)=
Stack Velocity (Actual, m/min)=
Flow rate (Actual, Cubic m/min)=
Flow rate (Standard, Wet, Cubic m/min)=
Flow rate (Standard, Dry, Cubic m/min)=
Particulate Loading - Front Half
Particulate Weight (g)=
Particulate Loading, Dry Std. (mg/cu m)=
Particulate Loading, Actual (mg/cu m)=
Emission Rate (kg/hr)=
No Back Half Analysis
24.332
25.111
1.010
0.0001
0.786
0.794
752
-660
4.5
14.6
73 .7
11.0
14
12.4
38.1
82
30.52
29.14
6.1649
100.8
0.84
75.0
3 .71
1.448
1.676
2.427
1,430
3,472
2,651
2,359
0.0188
23 .7
16.1
3.35
Corr. to 7% 02 & 12% C02'
20.1 19.5
RCA#2 APPENDIX B
11
-------
FILE NAME - 3IB
RUN # - 31 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/16/99 Time: 1521-1646
PROJECT # - 104703.1.002.05.02
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
PROG.=VER 06/27/89
11-23-1999 08:58:00
Delta P
(in. H20)
1.500
1.600
1.600
1.500
1.200
1.500
1.600
1.300
1.300
1.600
1.600
1.300
1.700
1.600
1.600
Delta H
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
49
52
52
49
39
49
52
42
42
52
52
42
55
52
52
Stack
(F)
180
180
180
180
179
181
181
180
179
180
179
179
181
179
179
T Meter T
In(F)
56
57
57
58
58
58
58
58
59
59
58
58
58
58
59
Out (F)
56
57
57
58
57
58
58
58
58
59
58
58
58
58
58
Fraction
DRY CATCH
FILTER
Fraction
PROBE RINSE
IMPINGERS
Final Wt. Tare Wt. Blank Wt. Net Wt,
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3642 3.3461 0.0000 0.0181
Final Wt
(g) (g)
3.6010 3.6003
0.0000
Tare Wt. Vol.
(ml)
24.7
0.0
Probe Rinse Blank (mg/ml)=
Impinger Blank (mg/ml)= 0.0000
0.0000
0.0000
Net Wt,
(g)
0.0007
0.0000
12
RCA#2 APPENDIX B
-------
FILE NAME - 32A
RUN # - 32 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 0854-1013
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Feet)= 266.519
Final Meter Volume (Cubic Feet)= 291.908
Meter Factor= 0.996
Final Leak Rate (cu ft/min)= 0.007
Net Meter Volume (Cubic Feet)= 25.287
Gas Volume (Dry Standard Cubic Feet)= 26.412
Barometric Pressure (in Hg)= 29.97
Static Pressure (Inches H20)= -27.12
Percent Oxygen= 4.8
Percent Carbon Dioxide= 14.7
Moisture Collected (ml)= 71.4
Percent Water= 11.3
Average Meter Temperature (F)= 47
Average Delta H (in H20)= 0.46
Average Delta P (in H20)= 1.533
Average Stack Temperature (F)= 177
Dry Molecular Weight= 30.54
Wet Molecular Weight= 29.13
Average Square Root of Delta P (in H20)= 1.1571
% Isokinetic= 100.0
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 4,407
Flow Rate (Actual, Cubic ft/min)= 115,139
Flow rate (Standard, Wet, Cubic ft/min)= 89,242
Flow Rate (Standard, Dry, Cubic ft/min)= 79,162
Particulate Loading - Front Half
Particulate Weight (g)= 0.0208
Particulate Loading, Dry Std. (gr/scf)= 0.0121
Particulate Loading, Actual (gr/cu ft)= 0.0083
Emission Rate (Ib/hr)= 8.23
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 08:58:20
Corr. to 7% 02 & 12% CO2
0.0105 0.0099
RCA#2 APPENDIX B
13
-------
* * METRIC UNITS * *
FILE NAME - 32A
RUN # - 32 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 0854-1013
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Meters)= 7.547
Final Meter Volume (Cubic Meters)= 8.266
Meter Factor= 0.996
Final Leak Rate (cu m/min)= 0.0002
Net Meter Volume (Cubic Meters)= 0.716
Gas Volume (Dry Standard Cubic Meters)= 0.748
Barometric Pressure (mm Hg)= 761
Static Pressure (mm H20)= -689
Percent Oxygen= 4.8
Percent Carbon Dioxide= 14.7
Moisture Collected (ml)= 71.4
Percent Water= 11.3
Average Meter Temperature (C)= 8
Average Delta H (mm H20) = 11.8
Average Delta P (mm H20)= 38.9
Average Stack Temperature (C) = 81
Dry Molecular Weight= 30.54
Wet Molecular Weight= 29.13
Average Square Root of Delta P (mm H20)= 5.8314
% Isokinetic= 100.0
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,343
.Flow rate (Actual, Cubic m/min) = 3,260
Flow rate (Standard, Wet, Cubic m/min)= 2,527
Flow rate (Standard, Dry, Cubic m/min)= 2,242
Particulate Loading - Front Half
Particulate Weight (g)= 0.0208
Particulate Loading, Dry Std. (mg/cu m)= 27.8
Particulate Loading, Actual (mg/cu m)= 19.1
Emission Rate (kg/hr)= 3.74
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 08:58:20
Corr. to 7% O2 & 12% C02
24.0 22.7
14
RCA#2 APPENDIX B
-------
FILE NAME - 32A
RUN # - 32 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 0854-1013
PROJECT # - 104703.1.002.05.01
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 08:58:20
Delta P
in. H20)
2.500
2.300
2.000
1.050
0.270
2.300
2.000
2.100
0.780
0.140
2.200
1.900
1.800
0.700
0. 060
2.400
2.100
2.100
0. 870
0.080
2.300
2.400
2.300
1.400
0.270
Delta H
(in. H20)
0.75
0.69
0.60
0.31
0.08
0.70
0 .61
0 .64
0.23
0.04
0.67
0.58
0.55
0.21
0.01
0.73
0 .64
0.64
0.26
0.02
0.70
0.74
0.71
0.43
0 .08
Stack
(F)
177
178
178
178
174
177
175
178
177
178
176
178
178
177
176
177
177
177
177
177
177
177
175
177
178
T
In(F)
40
41
42
43
43
44
44
47
47
48
47
48
50
50
50
49
50
51
53
53
51
53
54
56
56
Meter T
Out (F)
40
41
41
41
42
43
42
43
43
44
44
45
45
45
46
46
46
47
48
48
49
49
49
50
50
Fraction
DRY CATCH
FILTER
Fraction
Final Wt. Tare Wt. Blank Wt. Net Wt,
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3131 3.2944 0.0000 0.0187
Final Wt. Tare Wt.
(g) (g)
PROBE RINSE 3.7253 3.7232
IMPINGERS 0.0000 0.0000
Probe Rinse Blank (mg/ml)= 0.0000
Impinger Blank (mg/ml)= 0.0000
Vol
(ml)
26.7
0.0
Net Wt
(g)
0.0021
0.0000
RCA#2 APPENDIX B
15
-------
FILE NAME - 32B
RUN # - 32 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 0854-1014
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Feet)= 897.879
Final Meter Volume (Cubic Feet)= 925.209
Meter Factor= 1.010
Final Leak Rate (cu ft/min)= 0.004
Net Meter Volume (Cubic Feet)= 27.603
Gas Volume (Dry Standard Cubic Feet)= 28.660
Barometric Pressure (in Hg)= 29.97
Static Pressure (Inches H20)= -27.12
Percent Oxygen= 4 . 8
Percent Carbon Dioxide= 14.7
Moisture Collected (ml}= 82.3
Percent Water= 11.9
Average Meter Temperature (F)= 50
Average Delta H (in H20)= 0.44
Average Delta P (in H20)= 1.394
Average Stack Temperature (F)= 180
Dry Molecular Weight= 30.54
Wet Molecular Weight= 29.05
Average Square Root of Delta P (in H20)= 1.1780
% Isokinetic= 100.7
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 4,502
Flow Rate (Actual, Cubic ft/min)= 117,627
.Flow rate (Standard, Wet, Cubic ft/min)= 90,790
Flow Rate (Standard, Dry, Cubic ft/min)= 79,974
Particulate Loading - Front Half
Particulate Weight (g) = 0.0142
Particulate Loading, Dry Std. (gr/scf)= 0.0076
Particulate Loading, Actual (gr/cu ft)= 0.0052
Emission Rate (lb/hr)= 5.23
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 08:58:30
Corr. to 7% 02 & 12% C02
0.0066 0.0062
16
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 32B
RUN ft - 32 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 0854-1014
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Meters)= 25.424
Final Meter Volume (Cubic Meters)= 26.198
Meter Factor= 1.010
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.782
Gas Volume (Dry Standard Cubic Meters)= 0.812
Barometric Pressure (mm Hg)= 761
Static Pressure (mm H20)= -689
Percent Oxygen= 4.8
Percent Carbon Dioxide= 14.7
Moisture Collected (ml}= 82.3
Percent Water= 11.9
Average Meter Temperature (C)= 10
Average Delta H (mm H20)= 11.1
Average Delta P (mm H20) = 35.4
Average Stack Temperature (C) = 82
Dry Molecular Weight= 30.54
Wet Molecular Weight= 29.05
Average Square Root of Delta P (mm H20)= 5.9371
% Isokinetic= 100.7
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,372
Flow rate (Actual, Cubic m/min)= 3,331
Flow rate (Standard, Wet, Cubic m/min)= 2,571
Flow rate (Standard, Dry, Cubic m/min)= 2,265
Particulate Loading - Front Half
Particulate Weight (g)= 0.0142
Particulate Loading, Dry Std. (mg/cu m)= 17.5
Particulate Loading, Actual (mg/cu m)= 11.9
Emission Rate (kg/hr)= 2.37
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 08:58:30
Corr. to 7% 02
15.1
& 12% C02
14.3
RCA#2 APPENDIX B
17
-------
FILE NAME - 32B
RUN # - 32 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 0854-1014
PROJECT # - 104703.1.002.05.02
'oint #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
Delta P
(in. H20)
1.300
1.600
1.500
1.200
1.200
1.500
1.400
1.200
1.400
1.700
1.400
1.400
1.300
1.800
1.300
1.100
Delta H
(in. H20)
0.40
0.50
0.47
0.37
0.37
0.47
0.44
0.36
0.44
0.54
0.44
0.44
0.41
0.58
0.41
0.35
Stack
(F)
178
182
179
178
179
179
179
180
181
179
180
180
181
180
178
181
T Meter T
In(F)
43
44
44
45
47
48
50
51
52
54
55
56
51
57
58
60
Out (F)
43
43
43
44
45
46
47
48
48
50
51
52
53
53
54
56
PROG.=VER 06/27/89
11-23-1999 08:58:30
Fraction
DRY CATCH
FILTER
Fraction
PROBE RINSE
IMPINGERS
Probe Rinse Blank (mg/ml)=
Impinger Blank (mg/ml)= 0.0000
Final Wt. Tare Wt. Blank Wt. Net Wt,
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3168 3.3034 0.0000 0.0134
Final
(g)
.5713
.0000
•/ml) =
Wt
0
. Tare Wt .
(g)
3.5705
0.0000
.0000
Vol.
(ml)
23.9
0.0
0
0
Net Wt
(g)
.0008
.0000
18
RCA#2 APPENDIX B
-------
FILE NAME - 33A
RUN # - 33 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 1133-1322
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Feet)= 307.184
Final Meter Volume (Cubic Feet)= 341.362
Meter Factor= . 0.996
Final Leak Rate (cu ft/min)= 0.001
Net Meter Volume (Cubic Feet)= 34.041
Gas Volume (Dry Standard Cubic Feet)= 34.856
Barometric Pressure (in Hg) = 30.00
Static Pressure (Inches H20)= -26.85
Percent Oxygen= 3 . 3
Percent Carbon Dioxide= 15.4
Moisture Collected (ml)= 103.9
Percent Water= 12.3
Average Meter Temperature (F) = 57
Average Delta H (in H20)= 0.47
Average Delta P (in H20)= 1.504
Average Stack Temperature (F)= 178
Dry Molecular Weight= 30.60
Wet Molecular Weight= 29.05
Average Square Root of Delta P (in H20)= 1.1403
% Isokinetic= 101.4
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 100.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 4,348
Flow Rate (Actual, Cubic ft/min)= 113,603
Flow rate (Standard, Wet, Cubic ft/min)= 88,092
Flow Rate (Standard, Dry, Cubic ft/min)= 77,247
Particulate Loading - Front Half
Particulate Weight (g)= 0.0279
Particulate Loading, Dry Std. (gr/scf)= 0.0123
Particulate Loading, Actual (gr/cu ft)= 0.0084
Emission Rate (lb/hr)= 8.16
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:05:16
Corr. to 7% 02
0.0097
& 12% C02
0.0096
RCA#2 APPENDIX B
19
-------
* * METRIC UNITS * *
FILE NAME - 33A
RUN # - 33 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 1133-1322
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Meters)= 8.698
Final Meter Volume (Cubic Meters)= 9.666
Meter Factor= 0.996
Final Leak Rate (cu m/min)= 0.0000
Net Meter Volume (Cubic Meters)= 0.964
Gas Volume (Dry Standard Cubic Meters)= 0.987
Barometric Pressure (mm Hg)= 762
Static Pressure (mm H20)= -682
Percent Oxygen= 3 . 3
Percent Carbon Dioxide= 15.4
Moisture Collected (ml)= 103.9
Percent Water= 12.3
Average Meter Temperature (C)= 14
Average Delta H (mm H20)= .11.8
Average Delta P (mm H20)= 38.2
Average Stack Temperature (C)= 81
Dry Molecular Weight= 30.60
Wet Molecular Weight= 29.05
Average Square Root of Delta P (mm H20)= 5.7468
% Isokinetic= 101.4
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 100.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,325
.Flow rate (Actual, Cubic m/min) = 3,217
Flow rate (Standard, Wet, Cubic m/min)= 2,494
Flow rate (Standard, Dry, Cubic m/min)= 2,187
Particulate Loading - Front Half
Particulate Weight (g)= 0.0279
Particulate Loading, Dry Std. (mg/cu m)= 28.3
Particulate Loading, Actual (mg/cu m)= 19.2
Emission Rate (kg/hr)= 3.70
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:05:16
Corr. to 7% 02 & 12% C02
22.4 22.0
20
RCA#2 APPENDIX B
-------
FILE NAME - 33A
RUN # - 33 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 1133-1322
PROJECT # - 104703.1.002.05.01
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 09:05:16
Delta P
in
2.
2.
1.
0.
0.
2.
1.
2.
0.
0.
2.
2.
2.
1.
0.
2.
2.
2.
1.
0.
2.
2.
1.
0.
0.
. H20)
200
000
800
620
050
400
800
000
620
120
500
400
400
500
210
300
200
500
050
190
200
100
600
710
140
Delta H
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
67
61
55
19
01
74
56
62
19
03
78
74
75
47
06
72
68
78
33
05
69
65
50
22
04
Stack
(F)
180
181
180
180
180
180
178
177
177
175
174
178
177
175
175
174
180
177
176
177
176
179
179
180
180
T Meter T
In(F)
53
53
55
55
56
55
56
58
59
57
57
58
60
61
62
60
60
62
63
64
61
60
63
64
63
Out (F)
52
52
53
53
53
54
54
54
55
55
55
55
56
56
57
57
57
58
58
58
58
59
59
59
59
Fraction
DRY CATCH
FILTER
Fraction
Final Wt. Tare Wt. Blank Wt. Net Wt,
(g) (g) (g) (g)
o.oooo o.oooo o.oooo o.oooo
3.3271 3.3016 0.0000 0.0255
Final Wt
(g) (g)
3.6527 3.6503
PROBE RINSE
IMPINGERS 0.0000 0.0000
Probe Rinse Blank (mg/ml)= 0.0000
Impinger Blank (mg/ml)= 0.0000
Tare Wt. Vol.
(ml)
23.0
0.0
Net Wt,
(g)
0.0024
0.0000
RCA#2 APPENDIX B
21
-------
FILE NAME - 33B
RUN # - 33 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 1135-1324
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Feet)= 940.321
Final Meter Volume (Cubic Feet)= 974.999
Meter Factor= 1.010
Final Leak Rate (cu ft/min)= 0.003
Net Meter Volume (Cubic Feet)= 35.025
Gas Volume (Dry Standard Cubic Feet)= 35.334
Barometric Pressure (in Hg)= 30.00
Static Pressure (Inches H20)= -26.85
Percent Oxygen= 3 . 3
Percent Carbon Dioxide= 15.4
Moisture Collected (ml) = 98.2
Percent Water= 11.6
Average Meter Temperature (F)= 65
Average Delta H (in H20}= 0.50
Average Delta P (in H20)= 1.553
Average Stack Temperature (F)= 180
Dry Molecular Weight= 30.60
Wet Molecular Weight= 29.14
Average Square Root of Delta P (in H20)= 1.1605
% Isokinetic= 100.5
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 100.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 4,428
Flow Rate (Actual, Cubic ft/min)= 115,672
Flow rate (Standard, Wet, Cubic ft/min)= 89,326
Flow Rate (Standard, Dry, Cubic ft/min)= 78,987
Particulate Loading - Front Half
Particulate Weight (g)= 0.0260
Particulate Loading, Dry Std. (gr/scf)= 0.0113
Particulate Loading, Actual (gr/cu ft)= 0.0077
Emission Rate (lb/hr)= 7.67
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:05:34
Corr. to 7% O2 & 12% C02
0.0090 0.0088
22
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 33B
RUN # - 33 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 1135-1324
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Meters)= 26.626
Final Meter Volume (Cubic Meters)= 27.608
Meter Factor= 1.010
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.992
Gas Volume (Dry Standard Cubic Meters)= 1.001
Barometric Pressure (mm Hg)= 762
Static Pressure (mm H20)= -682
PROG.=VER 06/27/89
11-23-1999 09:05:34
Percent Oxygen= 3.3
Percent Carbon Dioxide= 15.4
Moisture Collected (ml)= 98.2
Percent Water= 11.6
Average Meter Temperature (C)= 18
Average Delta H (mm H20)= 12.8
Average Delta P (mm H20) = 39.4
Average Stack Temperature (C)= 82
Dry Molecular Weight= 30.60
Wet Molecular Weight= 29.14
Average Square Root of Delta P (mm H20)= 5.8487
% Isokinetic= 100.5
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 100.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,350
Flow rate (Actual, Cubic m/min)= 3,275
Flow rate (Standard, Wet, Cubic m/min)= 2,529
Flow rate (Standard, Dry, Cubic m/min)= 2,237
Particulate Loading - Front Half
Particulate Weight (g)= 0.0260
Particulate Loading, Dry Std. (mg/cu m)= 26.0
Particulate Loading, Actual (mg/cu m)= 17.7
Emission Rate (kg/hr)= 3.48
No Back Half Analysis
Corr. to 7% O2
20.6
& 12% C02
20.2
RCA#2 APPENDIX B
23
-------
FILE NAME - 33B
RUN # - 33 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 1135-1324
PROJECT # - 104703.1.002.05.02
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 09:05:34
Delta P
(in. H20)
2.400
2.300
1.900
1.700
0.230
2.300
2.000
1.800
0.830
0.070
2.200
2 .000
1.600
0.640
0 .040
2.200
2.200
2.100
0.760
0.170
2.400
2.700
2.300
1. 800
0.180
Delta H
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
77
74
61
55
07
74
65
58
27
02
72
65
52
21
01
72
72
69
24
05
79
88
75
59
05
Stack
(F)
182
184
183
182
182
181
181
179
178
178
177
180
178
177
179
179
180
179
181
180
180
181
181
184
185
T Meter T
In(F)
61
61
61
62
63
64
64
64
65
66
66
66
66
67
68
68
68
68
69
70
70
69
70
71
72
Out (F)
60
60
60
60
61
62
62
62
63
63
63
64
64
65
65
65
66
66
66
67
67
67
68
68
68
Fraction
DRY CATCH
FILTER
Fraction
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3350 3.3097 0.0000 0.0253
PROBE RINSE
IMPINGERS
Probe Rinse Blank (mg/ml)=
Final Wt. Tare Wt. Vol. Net Wt
(g) (g) (ml) (g)
3.9072 3.9065 23.3 0.0007
0.0000 0.0000 0.0 0.0000
0.0000
Impinger Blank (mg/ml)= 0.0000
24
RCA#2 APPENDK B
-------
FILE NAME - 34A
RUN # - 34 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 1450-1614
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Feet)= 341.752
Final Meter Volume (Cubic Feet)= 368.235
Meter Factor= 0.996
Final Leak Rate (cu ft/min)= 0.003
Net Meter Volume (Cubic Feet)= 26.377
Gas Volume (Dry Standard Cubic Feet)= 26.738
Barometric Pressure (in Hg)= 29.96
Static Pressure (Inches H20)= -27.39
Percent Oxygen= 4 . 2
Percent Carbon Dioxide= 14.6
Moisture Collected (ml)= 84.5
Percent Water= 13.0
Average Meter Temperature (F)= 62
Average Delta H (in H20)= 0.49
Average Delta P (in H20) = 1.577
Average Stack Temperature (F)= 179
Dry Molecular Weight= 30.50
Wet Molecular Weight= 28.88
Average Square Root of Delta P (in H20)= 1.1705
% Isokinetic= 101.7
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 4,487
Flow Rate (Actual, Cubic ft/min)= 117,221
Flow rate (Standard, Wet, Cubic ft/min)= 90,463
Flow Rate (Standard, Dry, Cubic ft/min)= 78,742
Particulate Loading - Front Half
Particulate Weight (g)= 0.0116
Particulate Loading, Dry Std. (gr/scf)= 0.0067
Particulate Loading, Actual (gr/cu ft)= 0.0045
Emission Rate (lb/hr)= 4.51
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:05:48
Corr. to 7% 02 & 12% C02
0.0056 0.0055
RCA#2 APPENDIX B
25
-------
* * METRIC UNITS * *
FILE NAME - 34A
RUN # - 34 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 1450-1614
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Meters)= 9.677
Final Meter Volume (Cubic Meters)= 10.427
Meter Factor= 0.996
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.747
Gas Volume (Dry Standard Cubic Meters)= 0.757
Barometric Pressure (mm Hg)= 761
Static Pressure (mm H20)= -696
Percent Oxygen= 4.2
Percent Carbon Dioxide= 14.6
Moisture Collected (ml)= 84.5
Percent Water= 13.0
Average Meter Temperature (C) = 17
Average Delta H (mm H20)= 12.5
Average Delta P (mm H20)= 40.1
Average Stack Temperature (C)= 82
Dry Molecular Weight= 30.50
Wet Molecular Weight= 28.88
Average Square Root of Delta P (mm H20)= 5.8992
% Isokinetic= ' 101.7
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,368
.Flow rate (Actual, Cubic m/min)= 3,319
Flow rate (Standard, Wet, Cubic m/min)= 2,562
Flow rate (Standard, Dry, Cubic m/min)= 2,230
Particulate Loading - Front Half
Particulate Weight (g)= 0.0116
Particulate Loading, Dry Std. (mg/cu m)= 15.3
Particulate Loading, Actual (mg/cu m)= 10.3
Emission Rate (kg/hr)= 2.05
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:05:48
Corr. to 7% 02
12.8
& 12% C02
12.6
26
RCA#2 APPENDK B
-------
FILE NAME - 34A
RUN # - 34 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 1450-1614
PROJECT # - 104703.1.002.05.01
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 09:05:48
Delta P
in. H20)
2.200
2.600
2.200
1.800
0.320
2.200
2.100
2.000
0.850
0.110
2.200
1.900
1.700
0.730
0.030
2.300
2 .200
2.000
0.720
0.120
2.600
2.300
2.300
1.800
0.150
Delta H
(in
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
. H20)
.68
.81
.68
.56
.10
.69
.65
.62
.26
.03
.69
.59
.53
.23
.01
.72
.68
.63
.22
.03
.82
.72
.72
.56
.04
Stack
(F)
180
179
178
180
179
177
181
179
179
178
178
179
179
179
179
179
182
178
178
178
178
180
180
180
179
T Meter T
In(F)
59
58
59
60
61
61
61
62
63
63
63
62
64
66
65
63
63
65
66
66
65
66
68
68
69
Out (F)
58
58
58
58
59
59
59
59
60
60
60
60
60
61
61
61
61
62
62
62
63
63
63
63
63
Fraction
DRY CATCH
FILTER
Fraction
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3081 3.2993 0.0000 0.0088
Final Wt. Tare Wt.
(g) (g)
PROBE RINSE 3.7852 3.7824
IMPINGERS 0.0000 0.0000
Probe Rinse Blank (mg/ml)= 0.0000
Impinger Blank (mg/ml)= 0.0000
Vol.
(mi;
21.8
0.0
Net Wt
(g)
0.0028
0 .0000
RCA#2 APPENDIX B
27
-------
FILE NAME - 34B
RUN # - 34 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 1450-1615
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Feet)= 978.838
Final Meter Volume (Cubic Feet)= 1007.228
Meter Factor= 1.010
Final Leak Rate (cu ft/min)= 0.003
Net Meter Volume (Cubic Feet)= 28.674
Gas Volume (Dry Standard Cubic Feet)= 28.895
Barometric Pressure (in Hg)= 29.96
Static Pressure (Inches H20)= -27.39
Percent Oxygen= 4.2
Percent Carbon Dioxide= 14.6
Moisture Collected (ml)= 87.3
Percent Water= 12.5
Average Meter Temperature (F)= 65
Average Delta H (in H20)= 0.41
Average Delta P (in H20)= 1.262
Average Stack Temperature (F)= 182
Dry Molecular Weight= 30.50
Wet Molecular Weight= 28.95
Average Square Root of Delta P (in H20)= 1.1174
% Isokinetic= 101.4
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 85.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 4,287
Flow Rate (Actual, Cubic ft/min)= 112,010
.Flow rate (Standard, Wet, Cubic ft/min)= 86,083
Flow Rate (Standard, Dry, Cubic ft/min)= 75,359
Particulate Loading - Front Half
Particulate Weight (g)= 0.0137
Particulate Loading, Dry Std. (gr/scf)= 0.0073
Particulate Loading, Actual (gr/cu ft)= 0.0049
Emission Rate (lb/hr)= 4.72
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:05:58
Corr. to 7% 02 & 12% C02
0.0061 0.0060
28
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 34B
RUN # - 34 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 1450-1615
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Meters)= 27.717
Final Meter Volume (Cubic Meters)= 28.521
Meter Factor= 1.010
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.812
Gas Volume (Dry Standard Cubic Meters)= 0.818
Barometric Pressure (mm Hg)= 761
Static Pressure (mm H20)= -696
Percent Oxygen= 4.2
Percent Carbon Dioxide= 14.6
Moisture Collected (ml)= 87.3
Percent Water= 12.5
Average Meter Temperature (C)= 18
Average Delta H (mm H20)= 10.3
Average Delta P (mm H20) = 32.0
Average Stack Temperature (C)= 83
Dry Molecular Weight= 30.50
Wet Molecular Weight= 28.95
Average Square Root of Delta P (mm H20)= 5.6314
% Isokinetic= 101.4
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 85.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,307
Flow rate (Actual, Cubic m/min)= 3,172
Flow rate (Standard, Wet, Cubic m/min)= 2,438
Flow rate (Standard, Dry, Cubic m/min)= 2,134
Particulate Loading - Front Half
Particulate Weight (g)= 0.0137
Particulate Loading, Dry Std. (mg/cu m)= 16.7
Particulate Loading, Actual (mg/cu m) = 11.3
Emission Rate (kg/hr)= 2.14
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:05:58
Corr. to 7% O2
14 .0
& 12% C02
13 .8
RCA#2 APPENDIX B
29
-------
FILE NAME - 34B
RUN # - 34 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/17/99 Time: 1450-1615
PROJECT # - 104703.1.002.05.02
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
PROG.=VER 06/27/89
11-23-1999 09:05:58
Delta P
(in. H20)
1.300
1.200
0.870
1.400
1.400
1.300
0.830
1.400
1.100
1.200
1.200
1.800
1.300
1.000
1.600
1.600
0.950
Delta H
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
42
39
28
45
45
42
26
45
35
39
39
58
42
32
52
52
31
Stack
(F)
182
181
183
181
183
182
182
183
181
181
181
181
181
182
180
181
184
T Meter T
In(F)
63
63
63
63
64
63
64
66
66
66
66
67
68
69
69
70
70
Out (F)
63
63
63
63
63
63
62
63
63
64
64
67
64
65
66
66
67
Fraction
DRY CATCH
FILTER
Fraction
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.2867 3.2733 0.0000 0.0134
Final Wt
(g) (g)
PROBE RINSE 3.6078 3.6075
IMPINGERS 0.0000 0.0000
Probe Rinse Blank (mg/ml)= 0.0000
Impinger Blank (mg/ml)= 0.0000
Tare Wt. Vol.
(ml)
26.8
0.0
Net Wt
(g)
0.0003
0.0000
30
RCA#2 APPENDIX B
-------
FILE NAME - 35A
RUN # - 35 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18/99 Time: 0852-1013
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Feet)= 368.652
Final Meter Volume (Cubic Feet)= 393.401
Meter Factor= 0.996
Final Leak Rate (cu ft/min)= 0.002
Net Meter Volume (Cubic Feet)= 24.650
Gas Volume (Dry Standard Cubic Feet)= 25.758
Barometric Pressure (in Hg)= 30.18
Static Pressure (Inches H20) = -25.00
Percent Oxygen= 3 . 8
Percent Carbon Dioxide= 15.0
Moisture Collected (ml)= 74.8
Percent Water= 12.0
Average Meter Temperature (F)= 50
Average Delta H (in H20)= 0.44
Average Delta P (in H20)= 1.456
Average Stack Temperature (F)= 179
Dry Molecular Weight= 30.55
Wet Molecular Weight= 29.04
Average Square Root of Delta P (in H20)= 1.1225
% Isokinetic= 100.7
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 4,261
Flow Rate (Actual, Cubic ft/min)= 111,323
Flow rate (Standard, Wet, Cubic ft/min)= 87,122
Flow Rate (Standard, Dry, Cubic ft/min)= 76,640
Particulate Loading - Front Half
Particulate Weight (g)= 0.0144
Particulate Loading, Dry Std. (gr/scf)= 0.0086
Particulate Loading, Actual (gr/cu ft)= 0.0059
Emission Rate (lb/hr)= 5.65
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:06:10
Corr. to 7% 02 & 12% C02
0.0070 0.0069
RCA#2 APPENDIX B
31
-------
* * METRIC UNITS * *
FILE NAME - 35A
RUN # - 35 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18/99 Time: 0852-1013
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Meters)= 10.439
Final Meter Volume (Cubic Meters)= 11.140
Meter Factor= 0.996
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.698
Gas Volume (Dry Standard Cubic Meters)= 0.729
Barometric Pressure (mm Hg)= 767
Static Pressure (mm H20)= -635
Percent Oxygen= 3 . 8
Percent Carbon Dioxide= 15.0
Moisture Collected (ml)= 74.8
Percent Water= 12 . 0
Average Meter Temperature (C)= 10
Average Delta H (mm H20)= 11.2
Average Delta P (mm H20)= 37.0
Average Stack Temperature (C)= 82
Dry Molecular Weight= 30.55
Wet Molecular Weight= 29.04
Average Square Root of Delta P (mm H20) = 5.6572
% Isokinetic= 100.7
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,299
.Flow rate (Actual, Cubic m/min) = 3,152
Flow rate (Standard, Wet, Cubic m/min)= 2,467
Flow rate (Standard, Dry, Cubic m/min)= 2,170
Particulate Loading - Front Half
Particulate Weight (g)= 0.0144
Particulate Loading, Dry Std. (mg/cu m)= 19.7
Particulate Loading, Actual (mg/cu m)= 13.6
Emission Rate (kg/hr)= 2.57
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:06:10
Corr. to 7% 02 & 12% C02
16.1 15.8
32
RCA#2 APPENDIX B
-------
FILE NAME - 35A
RUN # - 35 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18/99 Time: 0852-1013
PROJECT # - 104703.1.002.05.01
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 09:06:10
Delta P
(in. H20)
2.300
2.200
1.800
1.100
0.280
2.200
1.800
1. 900
0.730
0.070
2.200
1.800
1.800
0.700
0. 090
2.300
2.000
1.800
0.810
0.050
2.400
2.500
2.200
1.200
0.170
Delta H
(in
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
. H20)
.69
.66
.54
.33
.08
.67
.54
.58
.22
.02
.67
.55
.55
.21
.02
.71
.61
.55
.25
.01
.74
.77
.68
.37
.05
Stack
(F)
178
179
179
179
178
178
180
180
179
179
178
180
179
180
178
178
180
180
179
178
178
181
180
180
179
T Meter T
In(F)
41
43
44
45
46
46
47
49
50
51
51
51
53
54
55
54
55
57
58
58
58
58
59
61
61
Out (F)
40
41
42
42
43
43
44
45
45
46
46
47
48
49
49
50
50
51
52
52
53
54
54
55
55
Fraction
DRY CATCH
FILTER
Fraction
PROBE RINSE
IMPINGERS
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3161 3.3027 0.0000 0.0134
Final Wt
(g)
3.6943
0.0000
Probe Rinse Blank (mg/ml)= 0
Tare Wt,
(g)
3.6933
0.0000
0000
Vol.
(ml)
27.2
0.0
Net Wt
(g)
0.0010
0.0000
Impinger Blank (mg/ml)= 0.0000
RCA#2 APPENDIX B
33
-------
FILE NAME - 35B
RUN # - 35 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18/99 Time: 0853-1013
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Feet)= 14.138
Final Meter Volume (Cubic Feet}= 40.414
Meter Factor= 1.010
Final Leak Rate (cu ft/min)= 0.003
Net Meter Volume (Cubic Feet)= 26.539
Gas Volume (Dry Standard Cubic Feet)= 27.751
Barometric Pressure (in Hg)= 30.18
Static Pressure (Inches H20)= -25.00
Percent Oxygen= 3 . 8
Percent Carbon Dioxide= 15.0
Moisture Collected (ml)= 75.7
Percent Water= 11.4
Average Meter Temperature (F}= 50
Average Delta H (in H20)= 0.40
Average Delta P (in H20)= 1.293
Average Stack Temperature (F)= 181
Dry Molecular Weight= 30.55
Wet Molecular Weight= 29.12
Average Square Root of Delta P (in H20)= 1.1337
% Isokinetic= 100.3
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= - 4,306
Flow Rate (Actual, Cubic ft/min)= 112,484
.Flow rate (Standard, Wet, Cubic ft/min)= 87,707
Flow Rate (Standard, Dry, Cubic ft/min)= 77,721
Particulate Loading - Front Half
Particulate Weight (g)= 0.0088
Particulate Loading, Dry Std. (gr/scf)= 0.0049
Particulate Loading, Actual (gr/cu ft)= 0.0034
Emission Rate (lb/hr)= 3.25
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:06:27
Corr. to 7% 02 & 12% C02
0.0040 0.0039
34
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 35B
RUN # - 35 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18/99 Time: 0853-1013
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Meters)= 0.400
Final Meter Volume (Cubic Meters)= 1.144
Meter Factor= 1.010
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.751
Gas Volume (Dry Standard Cubic Meters)= 0.786
Barometric Pressure (mm Hg)= 767
Static Pressure (mm H20)= -635
Percent Oxygen= 3 . 8
Percent Carbon Dioxide= 15.0
Moisture Collected (ml)= 75.7
Percent Water= 11.4
Average Meter Temperature (C)= 10
Average Delta H (mm H20)= 10.3
Average Delta P (mm H20)= 32.8
Average Stack Temperature (C)= 83
Dry Molecular Weight= 30.55
Wet Molecular Weight= 29.12
Average Square Root of Delta P (mm H20)= 5.7136
% Isokinetic= 100.3
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,312
Flow rate (Actual, Cubic m/min)= 3,185
Flow rate (Standard, Wet, Cubic m/min)= 2,484
Flow rate (Standard, Dry, Cubic m/min)= 2,201
Particulate Loading - Front Half
Particulate Weight (g)= 0.0088
Particulate Loading, Dry Std. (mg/cu m)= 11.2
Particulate Loading, Actual (mg/cu m)= 7.7
Emission Rate (kg/hr)= 1.48
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:06:27
Corr. to 7% 02 &. 12% C02
9.1 9.0
RCA#2 APPENDIX B
35
-------
FILE NAME - 35B
RUN # - 35 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18/99 Time: 0853-1013
PROJECT # - 104703.1.002.05.02
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
PROG.=VER 06/27/89
11-23-1999 09:06:27
Delta P
(in. H20)
1.200
1.500
1.300
1.300
1.300
0.780
1.200
1.200
1.200
1.500
1.400
1.300
1.200
1.600
1.500
1.200
Delta H
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
37
47
40
40
40
24
37
37
38
47
44
41
38
51
48
38
Stack
(F)
180
180
180
181
182
181
182
182
182
181
183
182
181
181
183
182
T Meter T
In(F)
43
44
44
45
47
48
49
50
52
53
54
55
56
56
57
58
Out (F)
42
43
43
44
45
46
46
47
49
50
51
53
53
54
55
56
Fraction
DRY CATCH
FILTER
Fraction
PROBE RINSE
IMPINGERS
Probe Rinse Blank
Impinger Blank (mg/ml)= 0.0000
Final Wt. Tare Wt. Blank Wt. Net Wt,
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3168 3.3080 0.0000 0.0088
Final Wt. Tare Wt. Vol. Net Wt,
(g) (g) (ml) (g)
3.8241 3.8241 23.7 0.0000
0.0000 0.0000 0.0 0.0000
= 0.0000
36
RCA#2 APPENDIX B
-------
FILE NAME - 36A
RUN # - 36 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18/99 Time: 1105-1224
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Feet)= 393.787
Final Meter Volume (Cubic Feet)= 418.247
Meter Factor= 0.996
Final Leak Rate (cu ft/min)= 0.003
Net Meter Volume (Cubic Feet)= 24.362
Gas Volume (Dry Standard Cubic Feet)= 24.832
Barometric Pressure (in Hg)= 30.19
Static Pressure (Inches H20)= -25.91
Percent Oxygen= 3.8
Percent Carbon Dioxide= 14.9
Moisture Collected (ml)= 69.5
Percent Water= 11.6
Average Meter Temperature (F)= 63
Average Delta H (in H20)= 0.42
Average Delta P (in H20)= 1.365
Average Stack Temperature (F)= 179
Dry Molecular Weight= 30.54
Wet Molecular Weight= 29.08
Average Square Root of Delta P (in H20)= 1.0837
% Isokinetic= 100.3
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 4,116
Flow Rate (Actual, Cubic ft/min)= 107,535
Flow rate (Standard, Wet, Cubic ft/min)= 83,968
Flow Rate (Standard, Dry, Cubic ft/min)= 74,188
Particulate Loading - Front Half
Particulate Weight (g)= 0.0271
Particulate Loading, Dry Std. (gr/scf)= 0.0168
Particulate Loading, Actual (gr/cu ft)= 0.0116
Emission Rate (lb/hr)= 10.69
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:06:39
Corr. to 7% 02 & 12% C02
0.0137 0.0135
RCA#2 APPENDIX B
37
-------
* * METRIC UNITS * *
FILE NAME - 36A
RUN # - 36 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18/99 Time: 1105-1224
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Meters)= 11.150
Final Meter Volume (Cubic Meters)= 11.843
Meter Factor= 0.996
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.690
Gas Volume (Dry Standard Cubic Meters)= 0.703
Barometric Pressure (mm Hg)= 767
Static Pressure (mm H20) = -658
Percent Oxygen= 3.8
Percent Carbon Dioxide= 14.9
Moisture Collected (ml)= 69.5
Percent Water= 11.6
Average Meter Temperature (C)= 17
Average Delta H (mm H20)= 10.8
Average Delta P (mm H20)= 34.7
Average Stack Temperature (C)= 82
Dry Molecular Weight= 30.54
Wet Molecular Weight= 29.08
Average Square Root of Delta P (mm H20)= 5.4617
% Isokinetic= 100.3
Pitot Coefficients 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,255
Flow rate (Actual, Cubic m/min)= 3,045
Flow rate (Standard, Wet, Cubic m/min)= 2,378
Flow rate (Standard, Dry, Cubic m/min)= 2,101
Particulate Loading - Front Half
Particulate Weight (g)= 0.0271
Particulate Loading, Dry Std. (mg/cu m)= 38.5
Particulate Loading, Actual (mg/cu m)= 26.6
Emission Rate (kg/hr)= 4.85
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:06:39
Corr. to 7% 02
31.4
& 12% C02
31.0
38
RCA#2 APPENDIX B
-------
FILE NAME - 36A
RUN # - 36 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18/99 Time: 1105-1224
PROJECT # - 104703.1.002.05.01
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 09:06:39
Delta P
in
2.
2.
2.
0.
0.
2.
1.
1.
0.
0.
2.
1.
1.
0.
0.
2.
1.
1.
0.
0.
2.
2.
1.
0.
0.
. H20)
200
400
000
890
270
000
900
600
680
090
000
800
600
640
030
200
600
900
750
050
300
500
600
880
240
Delta H
(in
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
. H20)
.68
.74
.62
.27
.08
.62
.59
.50
.21
.02
.63
.56
.50
.20
.01
.69
.50
.60
.23
.01
.72
.79
.50
.28
.07
Stack
(F)
180
181
180
180
180
179
178
180
180
179
178
182
182
181
179
179
180
179
179
177
179
178
178
177
176
T Meter T
In(F)
57
59
59
61
62
61
61
63
64
64
64
64
66
67
66
65
66
68
68
68
66
68
69
70
70
Out (F)
57
58
58
58
59
59
59
60
60
60
61
61
62
62
62
63
63
63
63
64
64
64
65
65
65
Fraction
DRY CATCH
FILTER
Fraction
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3653 3.3398 0.0000 0.0255
Final Wt. Tare Wt. Vol. Net Wt
(g) (g) (ml) (g)
PROBE RINSE 3.8339 3.8323 31.6 0.0016
IMPINGERS 0.0000 0.0000 0.0 0.0000
Probe Rinse Blank (mg/ml)= 0.0000
Impinger Blank (mg/ml)= 0.0000
RCA#2 APPENDIX B
39
-------
FILE NAME - 36B
RUN # - 36 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18/99 Time: 1105-1225
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Feet)= 40.759
Final Meter Volume (Cubic Feet)= 66.777
Meter Factor= 1.010
Final Leak Rate (cu ft/min)= 0.004
Net Meter Volume (Cubic Feet)= 26.278
Gas Volume (Dry Standard Cubic Feet)= 26.769
Barometric Pressure (in Hg)= 30.19
Static Pressure (Inches H20) = -25.91
Percent Oxygen= 3 . 3
Percent Carbon Dioxide= 14.9
Moisture Collected (ml)= 81.5
Percent Water= 12.5
Average Meter Temperature (F)= 63
Average Delta H (in H20)= 0.39
Average Delta P (in H20)= 1.210
Average Stack Temperature (F)= 182
Dry Molecular Weight= 30.54
Wet Molecular Weight= 28.96
Average Square Root of Delta P (in H20)= 1.0961
% Isokinetic= 101.2
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 4,179
Flow Rate (Actual, Cubic ft/min)= 109,175
Flow rate (Standard, Wet, Cubic ft/min)= 84,940
Flow Rate (Standard, Dry, Cubic ft/min)= 74,287
Particulate Loading - Front Half
Particulate Weight (g)= 0.0171
Particulate Loading, Dry Std. (gr/scf)= 0.0098
Particulate Loading, Actual (gr/cu ft)= 0.0067
Emission Rate (lb/hr)= 6.26
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:06:51
Corr. to 7% 02 & 12% C02
0.0080 0.0079
40
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 36B
RUN # - 36 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18/99 Time: 1105-1225
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Meters)= 1.154
Final Meter Volume (Cubic Meters)= 1.891
Meter Factor= 1.010
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.744
Gas Volume (Dry Standard Cubic Meters)= 0.758
Barometric Pressure (mm Hg)= 767
Static Pressure (mm H20)= -658
Percent Oxygen= 3 . 8
Percent Carbon Dioxide= 14.9
Moisture Collected (ml)= 81.5
Percent Water= 12.5
Average Meter Temperature (C)= 17
Average Delta H (mm H20)= 9.9
Average Delta P (mm H20)= 30.7
Average Stack Temperature (C)= 83
Dry Molecular Weight= 30.54
Wet Molecular Weight= 28.96
Average Square Root of Delta P (mm H20)= 5.5243
% Isokinetic= 101.2
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity "(Actual, m/min)= 1,274
Flow rate (Actual, Cubic m/min)= 3,091
Flow rate (Standard, Wet, Cubic m/min)= 2,405
Flow rate (Standard, Dry, Cubic m/min)= 2,104
Particulate Loading - Front Half
Particulate Weight (g)= 0.0171
Particulate Loading, Dry Std. (mg/cu m)= 22.6
Particulate Loading, Actual (mg/cu m)= 15.3
Emission Rate (kg/hr)= 2.84
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:06:51
Corr. to 7% O2 & 12% CO2
18.4 18.2
RCA#2 APPENDIX B
41
-------
FILE NAME - 36B
RUN # - 36 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18/99 Time: 1105-1225
PROJECT # - 104703.1.002.05.02
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
PROG.=VER 06/27/89
11-23-1999 09:06:51
Delta P
in. H20)
1.300
1.200
1.200
0.860
1.300
1.100
1.300
0 .870
1.300
1.300
0.930
1.300
1.000
1.500
1.400
1.500
Delta H
(in. H20)
0.41
0.38
0.38
0.27
0.42
0.35
0.42
0.28
0.42
0.42
0.30
0.42
0.32
0.49
0.46
0.49
Stack
(F)
183
182
182
182
182
182
182
183
184
182
182
181
180
179
180
179
T Meter T
In(F)
59
59
60
61
62
62
63
64
65
65
66
67
68
68
69
69
Out (F)
58
58
59
59
60
61
61
62
63
64
64
65
65
66
66
67
Fraction
DRY CATCH
FILTER
Fraction
PROBE RINSE
IMPINGERS
Probe Rinse Blank (mg/ml)=
Impinger Blank (mg/ml)= 0.0000
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3951 3.3780 0.0000 0.0171
Final
(g)
3.8595
0.0000
g/ml)=
Wt
0
. Tare Wt .
(g)
3 .8595
0.0000
.0000
Vol.
(ml)
25.4
0.0
0
0
Net Wt
(g)
.0000
.0000
42
RCA#2 APPENDIX B
-------
FILE NAME - 37A
RUN # - 37 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18-19/99 Time: 2324-0043
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Feet)= 418.645
Final Meter Volume (Cubic Feet)= 440.240
Meter Factor= 0.996
Final Leak Rate (cu f t/min) = 0.001
Net Meter Volume (Cubic Feet)= 21.509
Gas Volume (Dry Standard Cubic Feet)= 22.534
Barometric Pressure (in Hg) = 30.20
Static Pressure (Inches H20)= -17.09
PROG.=VER 06/27/89
11-23-1999 09:14:43
Percent Oxygen=
Percent Carbon Dioxide=
Moisture Collected (ml}=
Percent Water=
6 . 1
13.5
56
10
1
5
Average Meter Temperature (F) = 49
Average Delta H (in H20)= 0.34
Average Delta P(inH20)= 1.070
Average Stack Temperature (F) = 177
Dry Molecular Weight= 30.40
Wet Molecular Weight= 29.10
Average Square Root of Delta P (in H20)= 0.9635
% Isokinetic= 99.7
Pitot Coefficient= 0.84
Sampling Time (Minutes) = 75.0
Nozzle Diameter (Inches) = 0.146
Stack Axis #1 (Inches) = 57.0
Stack Axis #2 ( Inches) = 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min) = 3,609
Flow Rate (Actual, Cubic f t/min) = 94,290
Flow rate (Standard, Wet, Cubic f t/min) = 75,633
Flow Rate (Standard, Dry, Cubic f t/min) = 67,695
Particulate Loading - Front Half
Particulate Weight (g) = 0.0512
Particulate Loading, Dry Std. (gr/scf)= 0.0350
Particulate Loading, Actual (gr/cu ft)= 0.0251
Emission Rate (lb/hr)= 20.30
No Back Half Analysis
Corr. to 7% 02 & 12% C02
0.0329 0.0311
RCA#2 APPENDIX B
43
-------
* * METRIC UNITS * *
FILE NAME - 37A
RUN # - 37 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18-19/99 Time: 2324-0043
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Meters)=
Final Meter Volume (Cubic Meters)=
Meter Factor=
Final Leak Rate (cu m/min)=
Net Meter Volume (Cubic Meters)=
Gas Volume (Dry Standard Cubic Meters)=
Barometric Pressure (mm Hg)=
Static Pressure (mm H20)=
Percent Oxygen=
Percent Carbon Dioxide=
Moisture Collected (ml)=
Percent Water=
PROG.=VER 06/27/89
11-23-1999 09:14:43
Average Meter Temperature (C)=
Average Delta H (mm H20)=
Average Delta P (mm H20)=
Average Stack Temperature (C)=
Dry Molecular Weight=
Wet Molecular Weight=
Average Square Root of Delta P (mm H20)=
% Isokinetic=
Pitot Coefficient=
Sampling Time (Minutes)=
Nozzle Diameter (mm)=
Stack Axis #1 (Meters)=
Stack Axis #2 (Meters)=
Rectangular Stack
Stack Area (Square Meters)=
Stack Velocity (Actual, m/min)=
Flow rate (Actual, Cubic m/min)=
Flow rate (Standard, Wet, Cubic m/min)=
Flow rate (Standard, Dry, Cubic m/min)=
Particulate Loading - Front Half
Particulate Weight (g)=
Particulate Loading, Dry Std. (mg/cu m)=
Particulate Loading, Actual (mg/cu m)=
Emission Rate (kg/hr)=
No Back Half Analysis
11.854
12.466
0.996
0.0000
0.609
0.638
767
-434
6.1
13.5
56.1
10.5
9
8.5
27.2
80
30.40
29.10
4.8560
99.7
0.84
75.0
3 .71
1.448
1.676
2.427
1,100
2,670
2,142
1,917
0.0512
80.2
57.6
9.22
Corr. to 7% 02 & 12% C02
75.4 71.3
44
RCA#2 APPENDIX B
-------
FILE NAME - 37A
RUN # - 37 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18-19/99 Time: 2324-0043
PROJECT # - 104703.1.002.05.01
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 09:14:43
Delta P
(in. H20)
1.700
1.600
1.400
0.770
0.140
1.600
1.400
1.400
0.540
0.080
1.400
1.300
1.100
0.420
0. 070
1.700
1.400
1.500
0.520
0. 080
1.800
1.800
1.600
1.300
0.120
Delta H
(in. H20)
0.54
0.50
0.44
0.24
0.04
0.50
0.44
0.44
0.17
0.02
0.44
0.41
0.35
0.13
0.02
0.54
0.44
0.47
0.16
0.02
0.57
0.57
0.51
0.41
0.03
Stack
(F)
177
178
176
177
176
176
177
177
177
176
176
177
177
177
176
177
177
178
178
177
177
177
178
178
172
T Meter T
In(F)
48
47
47
47
48
47
48
49
49
49
49
49
50
51
51
50
50
52
53
52
50
51
52
53
53
Out (F)
47
47
47
47
47
47
47
47
47
48
48
48
48
48
48
48
48
49
49
49
49
49
49
49
50
Fraction
DRY CATCH
FILTER
Fraction
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.4202 3.3734 0.0000 0.0468
Final Wt. Tare Wt. Vol. Net Wt.
(g) (g) (ml) (g)
PROBE RINSE 3.4512 3.4468 35.7 0.0044
IMPINGERS 0.0000 0.0000 0.0 0.0000
Probe Rinse Blank (mg/ml)= 0.0000
Impinger Blank (mg/ml)= 0.0000
RCA#2 APPENDIX B
45
-------
FILE NAME - 37B
RUN # - 37 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18-19/99 Time: 2324-0044
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Feet)= 76.934
Final Meter Volume (Cubic Feet)= 98.720
Meter Factor= 1.010
Final Leak Rate (cu ft/min)= 0.003
Net Meter Volume (Cubic Feet)= 22.004
Gas Volume (Dry Standard Cubic Feet)= 23.021
Barometric Pressure (in Hg)= 30.20
Static Pressure (Inches H20)= -17.09
Percent Oxygen= 6 .1
Percent Carbon Dioxide= 13.5
Moisture Collected (ml)= 53.1
Percent Water= 9.8
Average Meter Temperature (F}= 50
Average Delta H (in H20)= 0.27
Average Delta P (in H20)= 0.833
Average Stack Temperature (F)= 179
Dry Molecular Weight= 30.40
Wet Molecular Weight= 29.19
Average Square Root of Delta P (in H20) = 0.9112
% Isokinetic= 100.6
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 3,415
Flow Rate (Actual, Cubic ft/min)= 89,219
.Flow rate (Standard, Wet, Cubic ft/min)= 71,280
Flow Rate (Standard, Dry, Cubic ft/min)= 64,295
Particulate Loading - Front Half
Particulate Weight (g) = 0.0333
Particulate Loading, Dry Std. (gr/scf)= 0.0223
Particulate Loading, Actual (gr/cu ft)= 0.0160
Emission Rate (lb/hr)= 12.27
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:14:57
Corr. to 7% 02 & 12% C02
0.0209 0.0198
46
RCA#2 APPENDDC B
-------
* * METRIC UNITS * *
FILE NAME - 37B
RUN # - 37 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18-19/99 Time: 2324-0044
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Meters)= 2.178
Final Meter Volume (Cubic Meters)= 2.795
Meter Factor= 1.010
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.623
Gas Volume (Dry Standard Cubic Meters)= 0.652
Barometric Pressure (mm Hg)= 767
Static Pressure (mm H20)= -434
Percent Oxygen= 6 .1
Percent Carbon Dioxide= 13.5
Moisture Collected (ml)= 53.1
Percent Water= 9 . 8
Average Meter Temperature (C)= 10
Average Delta H (mm H20)= 7.0
Average Delta P (mm H20) = 21.2
Average Stack Temperature (C)= 82
Dry Molecular Weight= 30.40
Wet Molecular Weight= 29.19
Average Square Root of Delta P (mm H20)= 4.5925
% Isokinetic= 100.6
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,041
Flow rate (Actual, Cubic m/min)= 2,526
Flow rate (Standard, Wet, Cubic m/min)= 2,018
Flow rate (Standard, Dry, Cubic m/min)= 1,821
Particulate Loading - Front Half
Particulate Weight (g)= 0.0333
Particulate Loading, Dry Std. (mg/cu m)= 51.1
Particulate Loading, Actual (mg/cu m)= 36.8
Emission Rate (kg/hr)= 5.57
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:14:57
Corr. to 7% O2 & 12% C02
48.0 45.4
RCA#2 APPENDIX B
47
-------
FILE NAME - 37B
RUN ft - 37 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/18-19/99 Time: 2324-0044
PROJECT # - 104703.1.002.05.02
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
PROG.=VER 06/27/89
11-23-1999 09:14:57
Delta P
(in
0 .
0.
0 .
0.
0.
0.
0.
0.
0.
0.
0.
0.
0 .
0.
0.
0 .
. H20)
910
840
870
870
940
860
830
800
770
820
650
890
820
950
910
600
Delta H
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
30
28
29
29
31
28
27
26
25
27
21
30
27
32
30
20
Stack
(F)
180
179
180
179
180
179
179
180
179
179
180
178
180
179
179
179
T Meter T
In(F)
48
48
48
48
48
49
49
49
50
50
50
51
52
52
53
53
Out (F)
48
48
48
48
48
48
49
49
49
49
49
50
51
51
51
51
Fraction
DRY CATCH
FILTER
Fraction
PROBE RINSE
IMPINGERS
Probe Rinse Blank (mg/ml)=
Impinger Blank (mg/ml)= 0.0000
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3931 3.3611 0.0000 0.0320
Final Wt
(g)
.8260
.0000
7ml )= 0
. Tare Wt .
(g)
3.8247
0.0000
.0000
Vol.
(ml)
29.9
0.0
Net Wt
(g)
0.0013
0.0000
48
RCA#2 APPENDIX B
-------
FILE NAME - 38A
RUN # - 38 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/19/99 Time: 0137-0256
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Feet)= 440.664
Final Meter Volume (Cubic Feet)= 462.344
Meter Factor= 0.996
Final Leak Rate (cu ft/min)= 0.003
Net Meter Volume (Cubic Feet)= 21.593
Gas Volume (Dry Standard Cubic Feet)= 22.620
Barometric Pressure (in Hg)= 30.20
Static Pressure (Inches H20)= -17.08
Percent Oxygen= 5 . 7
Percent Carbon Dioxide= 13.0
Moisture Collected (ml)= 61.7
Percent Water= 11.4
Average Meter Temperature (F}= 49
Average Delta H (in H20)= 0.34
Average Delta P(inH20)= 1.066
Average Stack Temperature (F)= 177
Dry Molecular Weight= 30.31
Wet Molecular Weight= 28.91
Average Square Root of Delta P (in H20)= 0.9565
% Isokinetic= 101.6
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity '(Actual, Feet/min) = 3,597
Flow Rate (Actual, Cubic ft/min)= 93,959
Flow rate (Standard, Wet, Cubic ft/min)= 75,308
Flow Rate (Standard, Dry, Cubic ft/min)= 66,734
Particulate Loading - Front Half
Particulate Weight (g)= 0.0331
Particulate Loading, Dry Std. (gr/scf)= 0.0225
Particulate Loading, Actual (gr/cu ft)= 0.0160
Emission Rate (lb/hr)= 12.89
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:15:15
Corr. to 7% 02 & 12% C02
0.0206 0.0208
RCA#2 APPENDIX B
49
-------
* * METRIC UNITS * *
FILE NAME - 38A
RUN # - 38 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/19/99 Time: 0137-0256
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Meters)= 12.478
Final Meter Volume (Cubic Meters)= 13.092
Meter Factor= 0.996
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.611
Gas Volume (Dry Standard Cubic Meters)= 0.640
Barometric Pressure (mm Hg)= 767
Static Pressure (mm H20)= -434
Percent Oxygen= 5 . 7
Percent Carbon Dioxide= 13.0
Moisture Collected (ml)= 61.7
Percent Water= 11.4
Average Meter Temperature (C)= 9
Average Delta H (mm H20)= 8.7
Average Delta P (mm H20)= 27.1
Average Stack Temperature (C)= 81
Dry Molecular Weight= 30.31
Wet Molecular Weight= 28.91
Average Square Root of Delta P (mm H20)= 4.8208
% Isokinetic= 101.6
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,096
Flow rate (Actual, Cubic m/min)= 2,661
Flow rate (Standard, Wet, Cubic m/min)= 2,132
Flow rate (Standard, Dry, Cubic m/min)= 1,890
Particulate Loading - Front Half
Particulate Weight (g)= 0.0331
Particulate Loading, Dry Std. (mg/cu m)= 51.7
Particulate Loading, Actual (mg/cu m)= 36.7
Emission Rate (kg/hr)= 5.85
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:15:15
Corr. to 7% 02
47.3
& 12% C02
47.7
50
RCA#2 APPENDIX B
-------
FILE NAME - 38A
RUN # - 38 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/19/99 Time: 0137-0256
PROJECT # - 104703.1.002.05.01
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 09:15:15
Delta P
in. H20)
1.700
1.700
1.600
0.820
0.140
1.600
1.400
1.300
0.560
0.070
1.600
1.400
1.200
0.400
0.030
1.600
1.500
1.400
0.580
0.050
1.700
1.800
1.200
1.200
0.100
Delta H
(in
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
. H20)
.55
.55
.51
.26
.04
.52
.45
.42
.18
.02
.52
.45
.39
.13
.01
.52
.49
.45
.18
.01
.55
.58
.39
.39
.03
Stack
(F)
177
178
179
178
176
178
178
178
177
177
174
178
177
179
177
177
177
177
178
176
177
177
178
177
177
T Meter T
In(F)
48
47
48
49
49
49
5-0
50
51
50
50
50
50
51
51
50
50
52
52
52
50
50
51
53
52
Out (F)
48
47
47
47
47
47
48
47
48
48
48
47
47
48
48
48
48
48
48
48
48
48
48
49
49
Fraction
DRY CATCH
FILTER
Fraction
PROBE RINSE
IMPINGERS
Final Wt. Tare Wt. Blank Wt. Net Wt,
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3855 3.3564 0.0000 0.0291
Final Wt
(g)
3 .3977
0.0000
Tare Wt
(g)
3.3937
0.0000
Probe Rinse Blank (mg/ml)= 0.0000
Impinger Blank (mg/ml)= 0.0000
Vol
(ml)
26.2
0.0
Net Wt
(g)
0.0040
0.0000
RCA#2 APPENDIX B
51
-------
FILE NAME - 38B
RUN # - 38 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/19/99 Time: 0137-0257
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Feet)= 99.002
Final Meter Volume (Cubic Feet)= 121.140
Meter Factor= 1.010
Final Leak Rate (cu ft/min)= 0.002
Net Meter Volume (Cubic Feet)= 22.359
Gas Volume (Dry Standard Cubic Feet)= 23.379
Barometric Pressure (in Hg)= 30.20
Static Pressure (Inches H20)= -17.08
Percent Oxygen= 5 . 7
Percent Carbon Dioxide= 13.0
Moisture Collected (ml)= 55.6
Percent Water= 10.1
Average Meter Temperature (F)= 50
Average Delta H (in H20)= 0.29
Average Delta P (in H20)= 0.862
Average Stack Temperature (F)= 180
Dry Molecular Weight= 30.31
Wet Molecular Weight= 29.07
Average Square Root of Delta P (in H20}= 0.9280
% Isokinetic= 100.4
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 3,486
Flow Rate (Actual, Cubic ft/min)= 91,065
Flow rate (Standard, Wet, Cubic ft/min)= 72,735
Flow Rate (Standard, Dry, Cubic ft/min)= 65,408
Particulate Loading - Front Half
Particulate Weight (g)= 0.0222
Particulate Loading, Dry Std. (gr/scf)= 0.0146
Particulate Loading, Actual (gr/cu ft)= 0.0105
Emission Rate (lb/hr)= 8.20
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:15:26
Corr. to 7% 02 & 12% C02
0.0134 0.0135
52
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 38B
RUN # - 38 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/19/99 Time: 0137-0257
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Meters)= 2.803
Final Meter Volume (Cubic Meters)= 3.430
Meter Factor= 1.010
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.633
Gas Volume (Dry Standard Cubic Meters)= 0.662
Barometric Pressure (mm Hg)= 767
Static Pressure (mm H20)= -434
Percent Oxygen= 5.7
Percent Carbon Dioxide= 13.0
Moisture Collected (ml)= 55.6
Percent Water= 10.1
Average Meter Temperature (C)= 10
Average Delta H (mm H20)= 7.3
Average Delta P (mm H20) = 21.9
Average Stack Temperature (C)= 82
Dry Molecular Weight= 30.31
Wet Molecular Weight= 29.07
Average Square Root of Delta P (mm H20)= 4.6772
% Isokinetic= 100.4
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,062
Flow rate (Actual, Cubic m/min)= 2,579
Flow rate (Standard, Wet, Cubic m/min)= 2,060
Flow rate (Standard, Dry, Cubic m/min)= 1,852
Particulate Loading - Front Half
Particulate Weight (g)= 0.0222
Particulate Loading, Dry Std. (mg/cu m)= 33.5
Particulate Loading, Actual (mg/cu m)= 24.1
Emission Rate (kg/hr)= 3.72
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:15:26
Corr. to 7% 02
30.7
& 12% C02
31.0
RCA#2 APPENDIX B
53
-------
FILE NAME - 38B
RUN # - 38 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/19/99 Time: 0137-0257
PROJECT # - 104703.1.002.05.02
'oint #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
Delta P
(in
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
. H20)
870
920
900
870
830
790
790
960
920
840
820
820
860
880
870
850
Delta H
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
29
30
30
29
27
26
26
32
31
28
27
27
29
29
29
28
Stack
(F)
178
179
179
179
180
181
180
178
179
181
180
179
180
181
179
179
T Meter T
In(F)
49
48
48
49
49
50
50
51
51
51
51
51
51
52
52
52
Out (F)
48
48
48
49
49
49
49
49
50
50
50
50
50
50
50
51
PROG.=VER 06/27/89
11-23-1999 09:15:26
Fraction
DRY CATCH
FILTER
Fraction
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3188 3.2989 0.0000 0.0199
Final Wt. Tare Wt. Vol. Net Wt
(g) (g) (ml) (g)
PROBE RINSE 3.6497 3.6474 27.7 0.0023
IMPINGERS 0.0000 0.0000 0.0 0.0000
Probe Rinse Blank (mg/ml)= 0.0000
Impinger Blank (mg/ml)= 0.0000
54
RCA#2 APPENDIX B
-------
FILE NAME - 39A
RUN # - 39 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/19/99 Time: 0335-0504
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Feet)= 463.012
Final Meter Volume (Cubic Feet)= 484.276
Meter Factor= 0.996
Final Leak Rate (cu ft/min)= 0.002
Net Meter Volume (Cubic Feet)= 21.179
Gas Volume (Dry Standard Cubic Feet)= 22.196
Barometric Pressure (in Hg) = 30.20
Static Pressure (Inches H20)= -16.15
Percent Oxygen= 5 . 3
Percent Carbon Dioxide= 13.3
Moisture Collected (ml)= 54.8
Percent Water= 10.4
Average Meter Temperature (F) = 49
Average Delta H (in H20)= 0.33
Average Delta P (in H20)= 1.030
Average Stack Temperature (F) = 177
Dry Molecular Weight= 30.34
Wet Molecular Weight= 29.05
Average Square Root of Delta P (in H20)= 0.9415
% Isokinetic= 100.3
PROG.=VER 06/27/89
11-23-1999 09:15:42
Pitot Coefficient= 0.84
Sampling Time (Minutes) = 75.0
Nozzle Diameter (Inches) = 0.146
Stack Axis #1 (Inches) = 57.0
Stack Axis #2 ( Inches) = 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min) = 3,525
Flow Rate (Actual, Cubic ft/min) = 92,098
Flow rate (Standard, Wet, Cubic f t/min) = 74,051
Flow Rate (Standard, Dry, Cubic ft/min) = 66,337
Particulate Loading - Front Half
Particulate Weight (g) = 0.0311
Particulate Loading, Dry Std. (gr/scf ) = 0.0216
Particulate Loading, Actual (gr/cu ft)= 0.0155
Emission Rate (lb/hr)= 12.27
No Back Half Analysis
Corr. to 7% 02 & 12% C02
0.0192 0.0195
RCA#2 APPENDIX B
55
-------
* * METRIC UNITS * *
FILE NAME - 39A
RUN # - 39 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/19/99 Time: 0335-0504
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Meters)= 13.111
Final Meter Volume (Cubic Meters)= 13.713
Meter Factor= 0.996
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.600
Gas Volume (Dry Standard Cubic Meters)= 0.629
Barometric Pressure (mm Hg)= 767
Static Pressure (mm H20)= -410
Percent Oxygen= 5.3
Percent Carbon Dioxide= 13.3
Moisture Collected (ml)= 54.8
Percent Water= 10.4
Average Meter Temperature (C)= 9
Average Delta H (mm H20)= 8.4
Average Delta P (mm H20) = 26.2
Average Stack Temperature (C)= 80
Dry Molecular Weight= 30.34
Wet Molecular Weight= 29.05
Average Square Root of Delta P (mm H20)= 4.7449
% Isokinetic= 100.3
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,075
Flow rate (Actual, Cubic m/min)= 2,608
'Flow rate (Standard, Wet, Cubic m/min)= 2,097
Flow rate (Standard, Dry, Cubic m/min)= 1,878
Particulate Loading - Front Half
Particulate Weight (g)= 0.0311
Particulate Loading, Dry Std. (mg/cu m)= 49.5
Particulate Loading, Actual (mg/cu m)= 35.6
Emission Rate (kg/hr)= 5.57
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:15:42
Corr. to 7% 02 & 12% C02
44.1 44.6
56
RCA#2 APPENDIX B
-------
FILE NAME - 39A
RUN # - 39 - Method 17'Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/19/99 Time: 0335-0504
PROJECT # - 104703.1.002.05.01
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 09:15:42
Delta P
(in. H20)
1.700
1.700
1.600
0.750
0.200
1.600
1.400
1.300
0.400
0.090
1.500
1.300
1.050
0.450
0.030
1.600
1.000
1.000
0.600
0. 050
1.800
1.800
1.700
1.000
0.120
Delta H
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
55
55
52
24
06
52
45
42
13
02
48
42
34
14
01
52
32
32
19
01
58
58
55
32
03
Stack
(F)
177
177
177
177
176
177
177
177
177
177
177
178
177
177
174
177
179
177
177
172
177
178
177
176
177
T Meter T
In(F)
48
46
48
48
48
48
48
49
50
50
49
49
50
51
51
50
50
51
51
51
50
50
52
52
52
Out (F)
47
47
47
47
47
47
47
47
47
48
48
48
48
48
48
48
48
48
48
48
48
48
49
49
49
Fraction
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
DRY CATCH
FILTER
Fraction
PROBE RINSE
IMPINGERS
Probe Rinse Blank
0.0000
3.3416
Final
(g)
3.5236
0.0000
(mg/ml) =
0.0000
3.3143
Wt . Tare Wt .
(g)
3.5198
0.0000
0.0000
0.0000
0.0000
Vol.
(ml)
21.6
0.0
0.0000
0 .0273
Net Wt
(g)
0.0038
0 .0000
Impinger Blank (mg/ml)= 0.0000
RCA#2 APPENDIX B
57
-------
FILE NAME - 39B
RUN # - 39 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/19/99 Time: 0335-0504
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Feet}= 121.391
Final Meter Volume (Cubic Feet)= 143.689
Meter Factor= 1.010
Final Leak Rate (cu ft/min)= 0.004
Net Meter Volume (Cubic Feet)= 22.521
Gas Volume (Dry Standard Cubic Feet)= 23.595
Barometric Pressure (in Hg)= 30.20
Static Pressure (Inches H20)= -16.15
Percent Oxygen= 5.3
Percent Carbon Dioxide= 13.3
Moisture Collected (ml)= 57.7
Percent Water= 10.3
Average Meter Temperature (F)= 49
Average Delta H (in H20)= 0.29
Average Delta P(inH20)= 0.888
Average Stack Temperature (F) = 179
Dry Molecular Weight= 30.34
Wet Molecular Weight= 29.07
Average Square Root of Delta P (in H20)= 0.9414
% Isokinetic= 100.0
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 3,531
Flow Rate (Actual, Cubic ft/min)= 92,255
Flow rate (Standard, Wet, Cubic ft/min)= 73,881
Flow Rate (Standard, Dry, Cubic ft/min)= 66,250
Particulate Loading - Front Half
Particulate Weight (g) = 0.0228
Particulate Loading, Dry Std. (gr/scf)= 0.0149
Particulate Loading, Actual (gr/cu ft)= 0.0107
Emission Rate (lb/hr)= 8.45
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:15:58
Corr. to 7% 02 & 12% C02
0.0133 0.0134
58
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 39B
RUN # - 39 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/19/99 Time: 0335-0504
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Meters)= 3.437
Final Meter Volume (Cubic Meters)= 4.069
Meter Factor= 1.010
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.638
Gas Volume (Dry Standard Cubic Meters)= 0.668
Barometric Pressure (mm Hg) = 767
Static Pressure (mm H20)= -410
Percent Oxygen= 5.3
Percent Carbon Dioxide= 13.3
Moisture Collected (ml)= 57.7
Percent Water= 10.3
Average Meter Temperature (C)= 9
Average Delta H (mm H20)= 7.5
Average Delta P (mm H20)= 22.5
Average Stack Temperature (C) = 82
Dry Molecular Weight= 30.34
Wet Molecular Weight= 29.07
Average Square Root of Delta P (mm H20)= 4.7444
% Isokinetic= 100.0
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= . 2.427
Stack Velocity (Actual, m/min)= 1,076
Flow rate (Actual, Cubic m/min)= 2,612
Flow rate (Standard, Wet, Cubic m/min)= 2,092
Flow rate (Standard, Dry, Cubic m/min)= 1,876
Particulate Loading - Front Half
Particulate Weight (g)= 0.0228
Particulate Loading, Dry Std. (mg/cu m)= 34.1
Particulate Loading, Actual (mg/cu m)= 24.5
Emission Rate (kg/hr)= 3.84
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:15:58
Corr. to 7% 02 & 12% C02
30.4 30.8
RCA#2 APPENDIX B
59
-------
FILE NAME - 39B
RUN # - 39 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/19/99 Time: 0335-0504
PROJECT # - 104703.1.002.05.02
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
PROG.=VER 06/27/89
11-23-1999 09:15:58
Delta P
in
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
1.
0.
0.
. H20)
900
880
870
920
840
840
760
970
920
860
840
800
920
050
970
860
Delta H
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
30
29
29
30
28
28
25
32
31
28
28
26
31
35
32
29
Stack
(F)
179
179
179
180
179
179
180
180
179
180
180
179
179
180
179
178
T Meter T
In(F)
48
48
48
48
49
49
49
49
49
49
50
49
49
50
50
50
Out (F)
48
48
48
48
48
48
49
49
49
49
49
49
49
49
49
50
Fraction
DRY CATCH
FILTER
Fraction
Final Wt. Tare Wt. Blank Wt. Net Wt,
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3137 3.2929 0.0000 0.0208
Final Wt. Tare Wt.
(g) (g)
PROBE RINSE 3.7299 3.7279
IMPINGERS 0.0000 0.0000
Probe Rinse Blank (mg/ml)= 0.0000
Impinger Blank (mg/ml)= 0.0000
Vol.
(ml)
23.4
0.0
Net Wt,
(g)
0.0020
0.0000
60
RCA#2 APPENDIX B
-------
FILE NAME - 40A
RUN # - 40 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 0900-1020
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Feet)= 485.988
Final Meter Volume (Cubic Feet)= 507.367
Meter Factor= 0.996
Final Leak Rate (cu ft/min)= 0.004
Net Meter Volume (Cubic Feet)= 21.293
Gas Volume (Dry Standard Cubic Feet)= 21.591
Barometric Pressure (in Hg)= 30.08
Static Pressure (Inches H20)= -17.10
Percent Oxygen= 6.3
Percent Carbon Dioxide= 12.5
Moisture Collected (ml)= 64.7
Percent Water= 12.4
Average Meter Temperature (F)= 64
Average Delta H (in H20)= 0.32
Average Delta P (in H20)= 1.033
Average Stack Temperature (F)= 179
Dry Molecular Weight= 30.25
Wet Molecular Weight= 28.74
Average Square Root of Delta P (in H20)= 0.9439
% Isokinetic= 99.4
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 3,572
Flow Rate (Actual, Cubic ft/min)= 93,323
Flow rate (Standard, Wet, Cubic ft/min)= 74,270
Flow Rate (Standard, Dry, Cubic ft/min)= 65,084
Particulate Loading - Front Half
Particulate Weight (g)= 0.0107
Particulate Loading, Dry Std. (gr/scf)= 0.0076
Particulate Loading, Actual (gr/cu ft)= 0.0053
Emission Rate (lb/hr)= 4.26
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:16:08
Corr. to 7% 02 & 12% C02
0.0073 0.0073
RCA#2 APPENDIX B
61
-------
* * METRIC UNITS * *
FILE NAME - 40A
RUN # - 40 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 0900-1020
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Meters)= 13.761
Final Meter Volume (Cubic Meters)= 14.367
Meter Factor= 0.996
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.603
Gas Volume (Dry Standard Cubic Meters)= 0.611
Barometric Pressure (mm Hg)= 764
Static Pressure (mm H20)= -434
Percent Oxygen= 6.3
Percent Carbon Dioxide= 12.5
Moisture Collected (ml)= 64.7
Percent Water= 12.4
Average Meter Temperature (C)= 18
Average Delta H (mm H20)= 8.1
Average Delta P (mm H20)= 26.2
Average Stack Temperature (C)= 82
Dry Molecular Weight= 30.25
Wet Molecular Weight= 28.74
Average Square Root of Delta P (mm H20) = 4.7571
% Isokinetic= 99.4
Pitot Coefficient^ 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,089
Flow rate (Actual, Cubic m/min)= 2,643
'Flow rate (Standard, Wet, Cubic m/min)= 2,103
Flow rate (Standard, Dry, Cubic m/min)= 1,843
Particulate Loading - Front Half
Particulate Weight (g)= 0.0107
Particulate Loading, Dry Std. (mg/cu m)= 17.5
Particulate Loading, Actual (mg/cu m)= 12.2
Emission Rate (kg/hr)= 1.93
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:16:08
Corr. to 7% 02
16.7
12% C02
16.8
62
RCA#2 APPENDIX B
-------
FILE NAME - 40A
RUN # - 40 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 0900-1020
PROJECT # - 104703.1.002.05.01
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 09:16:09
Delta P
in. H20)
1.700
1.700
1.500
0. 770
0.110
1.500
1.400
1.100
0.460
0.060
1.300
1.100
0.970
0.400
0.040
1.600
1.600
1.400
0.570
0. 080
1.800
1.800
1.400
1.300
0.170
Delta H
(in. H20)
0.53
0.52
0.46
0.24
0.03
0.46
0.43
0.34
0.14
0.01
0.40
0.34
0.30
0.12
0.01
0.50
0.50
0.44
0.18
0.02
0.57
0.57
0.44
0.41
0.05
Stack
•(F)
179
181
179
177
174
179
180
179
178
177
179
179
178
178
178
179
180
180
179
178
179
182
182
183
181
T Meter T
In(F)
57
58
59
59
61
60
61
63
64
63
63
65
66
66
67
66
67
69
70
70
70
70
72
74
74
Out (F)
57
57
58
58
58
58
59
60
60
60
61
61
62
62
63
63
64
65
65
65
66
67
67
68
68
Fraction
DRY CATCH
FILTER
Fraction
Final Wt. Tare Wt. Blank Wt. Net Wt,
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3183 3.3086 0.0000 0.0097
Final Wt
(g)
PROBE RINSE 3 .5353
IMPINGERS 0.0000
Probe Rinse Blank (mg/ml)=
Tare Wt.
(g)
3.5343
0.0000
0.0000
Vol.
(ml)
19.5
0.0
Net Wt
(g)
0.0010
0.0000
Impinger Blank (mg/ml)= 0.0000
RCA#2 APPENDIX B
63
-------
FILE NAME - 4OB
RUN # - 40 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 0900-1020
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Feet)= 153.440
Final Meter Volume (Cubic Feet)= 174.366
Meter Factor= 1.010
Final Leak Rate (cu ft/min)= 0.002
Net Meter Volume (Cubic Feet)= 21.135
Gas Volume (Dry Standard Cubic Feet)= 21.430
Barometric Pressure (in Hg)= 30.08
Static Pressure (Inches H20)= -17.10
Percent Oxygen= 6.3
Percent Carbon Dioxide= 12.5
Moisture Collected (ml}= 64.3
Percent Water= 12.4
Average Meter Temperature (F}= 64
Average Delta H (in H20}= 0.25
Average Delta P (in H20)= 0.779
Average Stack Temperature (F)= 181
Dry Molecular Weight= 30.25
Wet Molecular Weight= 28.73
Average Square Root of Delta P (inH20)= 0.8808
% Isokinetic= 99.3
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 3,339
Flow Rate (Actual, Cubic ft/min)= 87,237
Flow rate (Standard, Wet, Cubic ft/min)= 69,182
'Flow Rate (Standard, Dry, Cubic f t/min) = 60,616
Particulate Loading - Front Half
Particulate Weight (g)= 0.0089
Particulate Loading, Dry Std. (gr/scf)= 0.0064
Particulate Loading, Actual (gr/cu ft)= 0.0044
Emission Rate (lb/hr)= 3.32
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:16:19
Corr. to 7% 02 & 12% C02
0.0061 0.0061
64
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 4 OB
RUN # - 40 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 0900-1020
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Meters)= 4.345
Final Meter Volume (Cubic Meters)= 4.937
Meter Factor= 1.010
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.598
Gas Volume (Dry Standard Cubic Meters)= 0.607
Barometric Pressure (mm Hg)= 764
Static Pressure (mm H20) = -434
Percent Oxygen= 6.3
Percent Carbon Dioxide= 12.5
Moisture Collected (ml)= 64.3
Percent Water= 12.4
Average Meter Temperature (C)= 18
Average Delta H (mm H20)= 6.3
Average Delta P (mm H20) = 19.8
Average Stack Temperature (C)= 83
Dry Molecular Weight= 30.25
Wet Molecular Weight= 28.73
Average Square Root of Delta P (mm H20)= 4.4390
% Isokinetic= 99.3
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,018
Flow rate (Actual, Cubic m/min)= 2,470
Flow rate (Standard, Wet, Cubic m/min)= 1,959
Flow rate (Standard, Dry, Cubic m/min)= 1,716
Particulate Loading - Front Half
Particulate Weight (g)= 0.0089
Particulate Loading, Dry Std. (mg/cu m)= 14.7
Particulate Loading, Actual (mg/cu m)= 10.2
Emission Rate (kg/hr)= 1.51
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:16:19
Corr. to 7% 02 & 12% C02
14.0 14.1
RCA#2 APPENDIX B
65
-------
FILE NAME - 4OB
RUN # - 40 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 0900-1020
PROJECT # - 104703.1.002.05.02
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
PROG.=VER 06/27/89
11-23-1999 09:16:19
Delta P
(in
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
1.
0.
. H20)
780
800
820
700
700
730
650
670
720
700
750
770
820
790
100
970
Delta H
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
25
25
26
22
22
23
21
21
23
22
24
25
26
25
36
31
Stack
(F)
181
182
179
180
182
180
181
182
180
181
182
182
181
182
184
183
T Meter T
In(F)
59
59
60
60
61
62
63
64
65
66
66
68
68
70
71
72
Out (F)
58
58
59
59
59
60
61
62
63
64
64
65
66
67
68
69
Fraction
DRY CATCH
FILTER
Fraction
PROBE RINSE 3.5574
IMPINGERS 0.0000
Probe Rinse Blank (mg/ml)=
Impinger Blank (mg/ml)= 0.0000
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
o.oooo o.oooo o.oooo o.oooo
3.3225 3.3157 0.0000 0.0068
(g)
t. Tare Wt.
(g)
3.5553
0.0000
0.0000
Vol.
(ml)
33 .2
0.0
Net Wt
(g)
0.0021
0.0000
66
RCA#2 APPENDIX B
-------
FILE NAME - 41A
RUN # - 41 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 1112-1231
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Feet)= 507.643
Final Meter Volume (Cubic Feet)= 530.756
Meter Factor= 0.996
Final Leak Rate (cu ft/min)= 0.001
Net Meter Volume (Cubic Feet)= 23.021
Gas Volume (Dry Standard Cubic Feet)= 22.684
Barometric Pressure (in Hg)= 30.07
Static Pressure (Inches H20)= -18.10
Percent Oxygen= 5 . 9
Percent Carbon Dioxide= 13.3
Moisture Collected (ml)= 68.4
Percent Water= 12.4
Average Meter Temperature (F)= 79
Average Delta H (in H20)= 0.37
Average Delta P (in H20)= 1.152
Average Stack Temperature (F)= 180
Dry Molecular Weight= 30.36
Wet Molecular Weight= 28.83
Average Square Root of Delta P (in H20)= 0.9915
% Isokinetic= 99.9
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 3,754
Flow Rate (Actual, Cubic ft/min)= 98,076
Flow rate (Standard, Wet, Cubic ft/min)= 77,729
Flow Rate (Standard, Dry, Cubic ft/min)= 68,063
Particulate Loading - Front Half
Particulate Weight (g)= 0.0223
Particulate Loading, Dry Std. (gr/scf)= 0.0151
Particulate Loading, Actual (gr/cu ft)= 0.0105
Emission Rate (lb/hr)= 8.83
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:16:31
Corr. to 7% 02 & 12% C02
0.0140 0.0137
RCA#2 APPENDIX B
67
-------
* * METRIC UNITS * *
FILE NAME - 41A
RUN # - 41 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 1112-1231
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Meters)= 14.374
Final Meter Volume (Cubic Meters)= 15.029
Meter Factor= 0.996
Final Leak Rate (cu m/min)= 0.0000
Net Meter Volume (Cubic Meters)= 0.652
Gas Volume (Dry Standard Cubic Meters)= 0.642
Barometric Pressure (mm Hg)= 764
Static Pressure (mm H20)= -460
Percent Oxygen= 5 . 9
Percent Carbon Dioxide= 13.3
Moisture Collected (ml)= 68.4
Percent Water= 12.4
Average Meter Temperature (C)= , 26
Average Delta H (mm H20)= 9.4
Average Delta P (mm H20)= 29.3
Average Stack Temperature (C)= 82
Dry Molecular Weight= 30.36
Wet Molecular Weight= 28.83
Average Square Root of Delta P (mm H20)= 4.9969
% Isokinetic= 99.9
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,144
Flow rate (Actual, Cubic m/min)= 2,777
Flow rate (Standard, Wet, Cubic m/min)= 2,201
Flow rate (Standard, Dry, Cubic m/min)= 1,927
Particulate Loading - Front Half
Particulate Weight (g)= 0.0223
Particulate Loading, Dry Std. (mg/cu m) = 34.7
Particulate Loading, Actual (mg/cu m)= 24.1
Emission Rate (kg/hr)= 4.01
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:16:31
Corr. to 7% 02 & 12% C02
32.2 31.3
68
RCA#2 APPENDIX B
-------
FILE NAME - 41A
RUN # - 41 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 1112-1231
PROJECT # - 104703.1.002.05.01
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 09:16:31
Delta P
in. H20)
1.700
1.700
1.600
0.780
0.120
1.700
1.600
1.300
0.570
0.050
1.700
1.400
1.400
0.500
0.030
1.700
1.700
1.500
0.530
0.030
1.900
2.100
1.500
1.500
0.190
Delta H
(in
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
. H20)
.54
.54
.51
.25
.03
.54
.51
.42
.18
.01
.54
.45
.45
.16
.01
.55
.55
.48
.17
.01
.62
.68
.48
.49
.06
Stack
(F)
180
181
182
181
180
181
181
180
182
180
182
180
180
179
179
180
179
179
181
176
179
180
180
177
179
T Meter T
In(F)
74
75
76
77
77
77
77
79
80
80
79
80
81
82
82
81
82
83
83
84
82
83
84
85
86
Out (F)
74
74
74
74
75
75
75
76
76
76
76
77
77
78
78
78
79
79
79
79
80
80
80
80
81
Fraction
DRY CATCH
FILTER
Fraction
Final Wt. Tare Wt. Blank Wt. Net Wt,
(g) (g) (g) (g)
o.oooo o.oooo o.oooo o.oooo
3.3323 3.3124 0.0000 0.0199
PROBE RINSE
IMPINGERS
Probe Rinse Blank (mg/ml)=
Final Wt. Tare Wt. Vol. Net Wt,
(g) (g) (ml) (g)
3.3624 3.3600 29.9 0.0024
0.0000 0.0000 0.0 0.0000
0.0000
Impinger Blank (mg/ml)= 0.0000
RCA#2 APPENDIX B
69
-------
FILE NAME - 4IB
RUN # - 41 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 1112-1232
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Feet)= 174.154
Final Meter Volume (Cubic Feet) = 198.331
Meter Factor= 1.010
Final Leak Rate (cu ft/min)= 0.002
Net Meter Volume (Cubic Feet)= 24.419
Gas Volume (Dry Standard Cubic Feet)= 24.054
Barometric Pressure (in Hg)= 30.07
Static Pressure (Inches H20)= -18.10
Percent Oxygen= 5 . 9
Percent Carbon Dioxide= 13.3
Moisture Collected (ml) = 72.2
Percent Water= 12.4
Average Meter Temperature (F)= 79
Average Delta H (in H20)= 0.33
Average Delta P (in H20)= 0.991
Average Stack Temperature (F)= 182
Dry Molecular Weight= 30.36
Wet Molecular Weight= 28.83
Average Square Root of Delta P (in H20)= 0.9912
% Isokinetic= 99.4
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 3,759
Flow Rate (Actual, Cubic ft/min)= 98,212
.Flow rate (Standard, Wet, Cubic f t/min) = 77,562
Flow Rate (Standard, Dry, Cubic ft/min)= 67,955
Particulate Loading - Front Half
Particulate Weight (g)= 0.0136
Particulate Loading, Dry Std. (gr/scf)= 0.0087
Particulate Loading, Actual (gr/cu ft)= 0.0060
Emission Rate (Ib/hr)= 5.07
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:16:42
Corr. to 7% 02 & 12% C02
0.0081 0.0079
70
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 4IB
RUN # - 41 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 1112-1232
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Meters)= 4.931
Final Meter Volume (Cubic Meters)= 5.616
Meter Factor= 1.010
Final Leak Rate (cu tn/min) = 0.0001
Net Meter Volume (Cubic Meters)= 0.691
Gas Volume (Dry Standard Cubic Meters)= 0.681
Barometric Pressure (mm Hg)= 764
Static Pressure (mm H20)= -460
PROG.=VER 06/27/89
11-23-1999 09:16:42
Percent Oxygen= 5 . 9
Percent Carbon Dioxide= 13.3
Moisture Collected (ml)= 72.2
Percent Water= 12.4
Average Meter Temperature (C)= 26
Average Delta H (mm H20)= 8.3
Average Delta P (mm H20) = 25.2
Average Stack Temperature (C)= 83
Dry Molecular Weight= 30.36
Wet Molecular Weight= 28.83
Average Square Root of Delta P (mm H20)= 4.9955
% Isokinetic= 99.4
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,146
Flow rate (Actual, Cubic m/min)= 2,781
Flow rate (Standard, Wet, Cubic m/min)= 2,196
Flow rate (Standard, Dry, Cubic m/min)= 1,924
Particulate Loading - Front Half
Particulate Weight (g)= 0.0136
Particulate Loading, Dry Std. (mg/cu m)= 20.0
Particulate Loading, Actual (mg/cu m)= 13.8
Emission Rate (kg/hr)= 2.30
No Back Half Analysis
Corr. to 7% 02 & 12% C02
18.5 18.0
RCA#2 APPENDIX B
71
-------
FILE NAME - 4IB
RUN # - 41 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 1112-1232
PROJECT # - 104703.1.002.05.02
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
PROG.=VER 06/27/89
11-23-1999 09:16:42
Delta P
in
0.
0.
1.
0.
0.
0.
1.
0.
1.
1.
1.
0.
1.
0.
1.
1.
. H20)
840
630
000
930
890
910
000
880
000
100
000
940
000
930
400
400
Delta H
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
27
20
33
30
29
30
33
29
33
36
33
31
33
31
47
47
Stack
(F)
182
183
183
183
183
183
184
183
182
181
181
182
181
182
182
180
T Meter T
In(F)
74
75
75
76
78
78
79
80
81
81
82
83
83
83
84
84
Out (F)
73
74
74
75
76
76
77
78
79
79
80
81
81
82
82
82
Fraction
DRY CATCH
FILTER
Fraction
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3070 3.2939 0.0000 0.0131
Final Wt. Tare Wt.
(g) (g)
PROBE RINSE 3.3260 3.3255
IMPINGERS 0.0000 0.0000
Probe Rinse Blank (mg/ml)= 0.0000
Impinger Blank (mg/ml)= 0.0000
Vol.
(ml)
32.2
0.0
Net Wt
(g)
0.0005
0.0000
72
RCA#2 APPENDIX B
-------
FILE NAME - 42A
RUN # - 42 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 1350-1512
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Feet)= 531.164
Final Meter Volume (Cubic Feet)= 553.900
Meter Factor= 0.996
Final Leak Rate (cu ft/min)= 0.003
Net Meter Volume (Cubic Feet)= 22.645
Gas Volume (Dry Standard Cubic Feet)= 22.059
Barometric Pressure (in Hg)= 29.98
Static Pressure (Inches H20)= -18.07
Percent Oxygen= 5.1
Percent Carbon Dioxide= 14.1
Moisture Collected (ml)= 66.0
Percent Water= 12.4
Average Meter Temperature (F)= 83
Average Delta H (in H20)= 0.35
Average Delta P (in H20)= 1.092
Average Stack Temperature (F)= 181
Dry Molecular Weight= 30.46
Wet Molecular Weight= 28.92
Average Square Root of Delta P (in H20)= 0.9699
% Isokinetic= 99.6
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 3,675
Flow Rate (Actual, Cubic ft/min)= 96,004
Flow rate (Standard, Wet, Cubic ft/min)= 75,745
Flow Rate (Standard, Dry, Cubic ft/min)= 66,390
•Particulate Loading - Front Half
Particulate Weight (g)= 0.0346
Particulate Loading, Dry Std. (gr/scf)= 0.0242
Particulate Loading, Actual (gr/cu ft)= 0.0167
Emission Rate (lb/hr)= 13.74
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:16:53
Corr. to 7% 02 & 12% C02
0.0213 0.0206
RCA#2 APPENDIX B
73
-------
* * METRIC UNITS * *
FILE NAME - 42A
RUN # - 42 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 1350-1512
PROJECT # - 104703.1.002.05.01
Initial Meter Volume (Cubic Meters)= 15.040
Final Meter Volume (Cubic Meters)= 15.684
Meter Factor= 0.996
Final Leak Rate (cu m/min)= 0.0001
Net Meter Volume (Cubic Meters)= 0.641
Gas Volume (Dry Standard Cubic Meters)= 0.625
Barometric Pressure (mm Hg)= 761
Static Pressure (mm H20)= -459
Percent Oxygen= 5.1
Percent Carbon Dioxide= 14.l
Moisture Collected (ml)= 66.0
Percent Water= 12.4
Average Meter Temperature (C}= 29
Average Delta H (mm H20)= 8.9
Average Delta P (mm H20)= 27.7
Average Stack Temperature (C) = 83
Dry Molecular Weight= 30.46
Wet Molecular Weight= 28.92
Average Square Root of Delta P (mm H20)= 4.8883
% Isokinetic= 99.6
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 75.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,120
Flow rate (Actual, Cubic m/min)= 2,719
Flow rate (Standard, Wet, Cubic m/min)= 2,145
Flow rate (Standard, Dry, Cubic m/min)= 1,880
Particulate Loading - Front Half
Particulate Weight (g)= 0.0346
Particulate Loading, Dry Std. (mg/cu m)= 55.4
Particulate Loading, Actual (mg/cu m)= 38.3
Emission Rate (kg/hr)= 6.24
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:16:53
Corr. to 7% 02 & 12% C02
48.8 47.1
74
RCA#2 APPENDIX B
-------
FILE NAME - 42A
RUN # - 42 - Method 17 Train A for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 1350-1512
PROJECT # - 104703.1.002.05.01
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
PROG.=VER 06/27/89
11-23-1999 09:16:53
Delta P
in. H20)
1.600
1.600
1.500
0.700
0.270
1.800
1.800
1.500
0.630
0.060
1.700
1.500
1.200
0.350
0.030
1.700
1.700
1. 050
0.620
0.030
1.700
1.700
1.100
1.300
0.170
Delta H
(in. H20)
0.51
0.51
0.48
0.22
0.08
0.58
0.58
0.48
0.20
0.01
0.55
0.48
0.39
0.11
0.01
0.55
0.55
0.34
0.20
0.01
0.55
0.55
0.35
0.42
0.05
Stack
(F)
182
182
183
182
182
180
182
181
181
179
179
182
182
180
178
181
181
181
182
176
180
180
183
181
181
T Meter T
In(F)
80
80
81
81
82
82
82
84
84
85
84
85
• 86
86
86
85
85
87
88
86
85
86
86
87
88
Out (F)
80
80
80
80
80
80
81
81
81
81
82
82
82
82
83
83
83
84
84
85
84
85
84
85
85
Fraction
DRY CATCH
FILTER
Fraction
PROBE RINSE
IMPINGERS
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3485 3.3191 0.0000 0.0294
Final Wt.
(g)
3.7267
0. 0000
Tare Wt. Vol.
Probe Rinse Blank (mg/ml)= 0
Impinger Blank (mg/ml)= 0.0000
(g)
3.7215
0.0000
0000
(ml]
30.1
0.0
Net Wt
(g)
0.0052
0.0000
RCA#2 APPENDIX B
75
-------
FILE NAME - 42B
RUN # - 42 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 1350-1512
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Feet)= 208.689
Final Meter Volume (Cubic Feet)= 231.754
Meter Factor= 1.010
Final Leak Rate (cu ft/min)= 0.001
Net Meter Volume (Cubic Feet)= 23.296
Gas Volume (Dry Standard Cubic Feet)= 22.643
Barometric Pressure (in Hg)= 29.98
Static Pressure (Inches H20)= -18.07
Percent Oxygen= 5.i
Percent Carbon Dioxide= 14.1
Moisture Collected (ml)= 60.9
Percent Water= 11.2
Average Meter Temperature (F)= 84
Average Delta H (in H20)= 0.29
Average Delta P (in H20)= 0.875
Average Stack Temperature (F)= 184
Dry Molecular Weight= 30.46
Wet Molecular Weight= 29.06
Average Square Root of Delta P (in H20)= 0.9323
% Isokinetic= 98.9
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (Inches)= 0.146
Stack Axis #1 (Inches)= 57.0
Stack Axis #2 (Inches)= 66.0
Rectangular Stack
Stack Area (Square Feet)= 26.13
Stack Velocity (Actual, Feet/min)= 3,532
Flow Rate (Actual, Cubic ft/min)= 92,262
•Flow rate (Standard, Wet, Cubic f t/min) = 72,471
Flow Rate (Standard, Dry, Cubic ft/min)= 64,323
Particulate Loading - Front Half
Particulate Weight (g)= 0.0210
Particulate Loading, Dry Std. (gr/scf)= 0.0143
Particulate Loading, Actual (gr/cu ft)= 0.0100
Emission Rate (lb/hr)= 7.87
No Back Half Analysis
PROG.=VER 06/27/89
11-23-1999 09:17:04
Corr. to 7% 02 & 12% C02
0.0126 0.0122
76
RCA#2 APPENDIX B
-------
* * METRIC UNITS * *
FILE NAME - 42B
RUN # - 42 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 1350-1512
PROJECT # - 104703.1.002.05.02
Initial Meter Volume (Cubic Meters)=
Final Meter Volume (Cubic Meters)=
Meter Factor=
Final Leak Rate (cu m/min)=
Net Meter Volume (Cubic Meters)=
Gas Volume (Dry Standard Cubic Meters)=
Barometric Pressure (mm Hg)=
Static Pressure (mm H20) =
Percent Oxygen=
Percent Carbon Dioxide=
Moisture Collected (ml)=
Percent Water=
PROG.=VER 06/27/89
11-23-1999 09:17:04
Average Meter Temperature (C)=
Average Delta H (mm H20)=
Average Delta P (mm H20)=
Average Stack Temperature (C)=
Dry Molecular Weight=
Wet Molecular Weight=
Average Square Root of Delta P (mm H20)
% Isokinetic=
5.909
6.562
1.010
0.0000
0.660
0.641
761
-459
5.1
14 .1
60.9
11.2
29
7.4
22.2
84
30.46
29.06
4.6986
98.9
Pitot Coefficient= 0.84
Sampling Time (Minutes)= 80.0
Nozzle Diameter (mm)= 3.71
Stack Axis #1 (Meters)= 1.448
Stack Axis #2 (Meters)= 1.676
Rectangular Stack
Stack Area (Square Meters)= 2.427
Stack Velocity (Actual, m/min)= 1,076
Flow rate (Actual, Cubic m/min)= 2,613
Flow rate (Standard, Wet, Cubic m/min)= 2,052
Flow rate (Standard, Dry, Cubic m/min)= 1,821
Particulate Loading - Front Half
Particulate Weight (g)= 0.0210
Particulate Loading, Dry Std. (mg/cu m)= 32.8
Particulate Loading, Actual (mg/cu m)= 22.8
Emission Rate (kg/hr)= 3.57
No Back Half Analysis
Corr. to 7% 02 & 12% C02
28 .8 27.9
RCA#2 APPENDIX B
77
-------
FILE NAME - 42B
RUN # - 42 - Method 17 Train B for PM
LOCATION - Unit 2A Baghouse Outlet Duct
DATE - 11/20/99 Time: 1350-1512
PROJECT # - 104703.1.002.05.02
Point #
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
PROG.=VER 06/27/89
11-23-1999 09:17:04
Delta P
(in
0.
0.
0.
0.
1.
0.
0.
0.
0.
0.
0.
0.
1.
0.
0.
0.
. H20)
840
820
850
840
300
780
870
950
950
760
830
670
000
930
970
640
Delta H
(in.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
0.
H20)
28
27
28
28
43
26
29
31
32
25
28
22
33
31
32
21
Stack
(F)
184
184
185
185
184
184
183
184
184
183
183
183
185
182
183
183
T Meter T
In(F)
82
82
82
82
83
84
85
85
86
86
87
87
87
88
88
88
Out (F)
81
82
82
82
82
83
83
83
84
84
85
85
86
86
86
87
Fraction
DRY CATCH
FILTER
Fraction
PROBE RINSE
IMPINGERS
Probe Rinse Blank
Impinger Blank (mg/ml)= 0.0000
Final Wt. Tare Wt. Blank Wt. Net Wt
(g) (g) (g) (g)
0.0000 0.0000 0.0000 0.0000
3.3340 3.3140 0.0000 0.0200
Final Wt. Tare Wt. Vol. Net Wt
(g) (g) (ml) (g)
3.6897 3.6887 25.4 0.0010
0.0000 0.0000 0.0 0.0000
= 0.0000
78
RCA#2 APPENDK B
-------
Particulate Matter Concentration Results Converted To Other Units
Standard Temperature = 68 °F
Standard Pressure = 29.92 in. Hg
RCA#2
Run Number-
Train Number
30-A
30-B
31-A
31-B
32-A
32-B
33-A
33-B
34-A
34-B
35-A
35-B
36-A
36-B
37-A
37-B
38-A
38-B
39-A
39-B
40-A
40-B
41-A
41-B
42-A
42-B
* 1 l_ :i _i;t; _
PM
collected,
grams
0.0409
0.0335
0.0293
00188
0.0208
0.0142
0.0279
00260
00116
0.0137
0.0144
0.0088
00271
0.0171
0.0512
0.0333
0.0331
0.0222
0.0311
0.0228
0.0107
0.0089
00223
0.0136
0.0346
00210
PM
collected,
mg
409
33.5
29.3
188
20.8
14.2
279
260
11.6
13.7
144
88
27.1
17.1
51.2
33.3
33.1
22.2
31.1
22.8
10.7
8.9
22.3
13.6
346
21.0
Sample
Volume,
dscf
35365
35886
27.394
28.037
26412
28660
34.856
35.334
26.738
28895
25.758
27.751
24.832
26.769
22.534
23.021
22.620
23.379
22.196
23.595
21.591
21.430
22.684
24.054
22.059
22.643
Sample
Volume,
dscm
1.001
1.016
0.776
0794
0.748
0.812
0987
1.001
0757
0.818
0.729
0.786
0.703
0.758
0.638
0.652
0641
0.662
0629
0.668
0.611
0607
0.642
0.681
0.625
0.641
Average
Gas Temp.,
°F
178
180
177
180
177
180
178
180
179
182
179
181
179
182
177
179
177
180
177
179
179
181
180
182
181
184
Barometric
Pressure,
in. Hg
2965
29.65
2960
29.60
29.97
29.97
30.00
30.00
29.96
29.96
30.18
30.18
30.19
30.19
30.20
3020
30.20
30.20
30.20
30.20
30.08
30.08
30.07
30.07
29.98
29.98
Static
Pressure,
in. w.c.
-25.90
-25.90
-26.00
-26.00
-27.12
-27.12
-2685
-26.85
-27.39
-27.39
-25.00
-25.00
-25.91
-25.91
-1709
-17.09
-17.08
-17.08
-16.15
-16.15
-17.10
-17.10
-18.10
-18.10
-18.07
-18.07
Gas
Pressure,
in. Hg
27.75
27.75
27.69
27.69
27.98
27.98
28.03
28.03
27.95
27.95
28.34
28.34
2828
28.28
28.94
28.94
28.94
2894
29.01
29.01
28.82
2882
28.74
28.74
28.65
28.65
Gas
Moisture,
percent
11 1%
1 1 0%
12.2%
1 1 0%
11.3%
11.9%
12.3%
11.6%
13.0%
12.5%
12.0%
11.4%
11.6%
12.5%
10.5%
9.8%
11.4%
10.1%
10.4%
10.3%
12.4%
12.4%
12.4%
12.4%
12.4%
11.2%
PM Loading,
27.85
22.44
25.43
16.08
19.11
11.89
19.21
17.74
10.28
11.25
13.59
7.74
26.60
15.34
57.56
36.82
36.70
24.05
3562
24.52
12.20
10.19
24.09
13.81
38.26
22.83
PM Loading,
mg/dry m3
@ std. temp.*
4046
32.66
37.35
23.42
27.85
17.52
28.33
26.04
15.34
16.76
19.91
11.29
38.87
22.75
80.96
51 54
52.14
33.83
49.92
34.43
17.59
14.74
34.88
2006
5548
32.80
PM Loading,
mg/dscm
40.84
32.97
37.77
2368
27.81
1750
28.27
25.99
15.32
16.74
19.74
11.20
38.54
22.56
8024
51.08
51.68
33.53
49.48
34.12
17.50
14.67
34.72
19.97
5539
32.75
RSD,
10.7%
22.9%
22.8%
4.2%
4.4%
27.6%
26.2%
22.2%
21.3%
18.4%
8.8%
27.0%
25.7%
co
PMCONV6X.WK4 11/23/99 0850AM
-------
40 CFR 60, APPENDIX A, METHOD 1 -
LOCATION OF TRAVERSE POINTS IN A RECTANGULAR DUCT
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Date: 11/15/99
For Run Numbers: All
75.4"
62.2"
49.0"
35.8"
22.6"
A-5 •
• A-4
A-3
• A-2
• A-1
as
93
o
c
CO
(O
B
D
57 inches
Compass Direction ^" North
Flow is away from observer and is downward
Inside of far wall to outside of port (Distance A):
Inside of near wall to outside of port (Distance B):
Traverse distance (A - B):
Internal duct dimension normal to traverses:
Equivalent diameter:
Cross-sectional area of duct:
Number of test ports:
Distance between port centers:
Distance of nearest flow disturbance upstream from ports:
Distance of nearest flow disturbance downstream from ports:
Number of test points per traverse (i.e., per port):
Distance between test points on a traverse:
Dimensions obtained by/from: direct measurements and blueprints
Data recorded by: D. Griffin
COMMENTS:
82.0
16.0
66.0
57.0
61.17
26.125
5
11.4
82
128
5
13.2
inches
inches
inches
inches
inches
square feet
inches
inches
inches
inches
DUCTR6CT.WPD October 14, 1998 (rev. DUCTREC3.WPD November 10, 19991
80
RCA#2 APPENDIX B
-------
METHOD 5 METERING CONSOLE QUALITY CONTROL CHECK
MRI Project No.
Metering Console No.
Dry Gas Meter Factor (Y):
Orifice Meter Delta-H @, in. w.c.
Barometric Pressure, in. Hg
104703.1.002.05.
N-12
0.996
1.810
30.00
Date:
Operator:
11/16/99
C. Clapsaddle
n
£
KJ
Run 1
Final
Initial
Run 2
Final
Initial
Run 3
Final
Initial
Time, i!
seconds
Dry Gas
.Meter , ,
Volume, ,
ft.s
, ; Orifice
- , Meter
' f-\_ li*» • 1 f •.•' !. ,1
, Delta-H, ,
' in, w.c,
'; Dry Gas
Meter Jnlet
Temperature,
°F
Dry Gas
Meter Outlet
Temperature,
. ,"°F'
Dry Gas
, Meter
Factor •
(Yc)
600
0
600
299.606
292.193
7.413
1.81
~ 1.81
1.81
59
54
52
52
514 °R
600
b
600
307.064
299.606
7.458
1.81
1.81
1.81
62
58
53
53
516 °R
- -
--
- -
°R
0.997
0.993
Average Yc: 0.995
Acceptability Criterion: 0.97Y < Yc < 1.03Y
QC Check Result. Metering Console Is Acceptable
00
M5QCHECK.WK4 11/01/99 (rev. N12QCHK.WK4 11/23/99 08:49 AM)
-------
Alternative Method 5 Post-Test Calibration
MRI Project No. 104703.1.002.05.01
Sampling Location: Unit 2A Baghouse Outlet
Run No. 30-TrnA Run Date: 11/16/99
Console No. N-12
data
line
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
Orifice
delta H
0.72
0.69
0.53
0.20
0.01
0.78
0.75
0.66
0.24
0.03
0.79
0.79
0.76
0.47
0.07
0.76
0.72
0.69
0.38
005
0.73
0.67
0.57
0.21
0.03
sqrt
delta H
0.84853
0.83066
0.72801
0.44721
0.10000
0.88318
0.86603
0.81240
0.48990
0.17321
0.88882
0.88882
0.87178
0.68557
0.26458
0.87178
0.84853
0.83066
0.61644
0.22361
0.85440
0.81854
0.75498
0.45826
0.17321
DGM temperature (tm)
inlet, "F
51
52
53
53
54
53
54
55
57
57
55
57
58
59
59
58
58
60
60
60
59
61
61
62
61
outlet, "F
51
52
53
52
53
53
53
54
54
54
54
55
55
55
56
56
56
57
57
57
58
58
58
58
58
DGM delta H@:
1.81 in. w.c.
Orifice delta H (average):
0.49200 in. w.c.
sqrt delta H (average):
0.64916
DGM temperature (average):
515.75 °R
Barometric pressure:
29.65 in. Hg
Dry gas molecular weight (Md):
30.58 Ib/lb-mole
Total sampling time'
100 minutes
Sample volume (unconnected)
as read on DGM:
34.993 dcf
DGM correction factor (Y):
0.996
Yqa 0.9990
Difference 0.30%
Result: PASS
YQA48PT.WK4 10/19/99 (rev. YQAN12.WK4 11/23/99 08:52 AM)
Page 1
82
RCA#2 APPENDIX B
-------
METHOD 5 METERING CONSOLE QUALITY CONTROL CHECK
MRI Project No.
Metering Console No.
Dry Gas Meter Factor (Y):
Orifice Meter Delta-H @, in. w.c.
Barometric Pressure, in. Hg
104703.1.002.05.
N-11
1.010
1.898
30.00
Date:
Operator:
11/16/99
C. Clapsaddle
n
S
m
w
,
, ,
Time, '
seconds
Dry Gas '
Meter , ,:;
Volume; :
ft,s
, ..Orifice, , , „
, Meter
, Delta-H, '
in, w.c.
•, Dry Gas,
, Meter Inlet
Temperature,
,. ', "F -.
, Dry Gas ,;
Meter Outlet
Temperature;
-•• °F'.' '•
,- Dry Gas
, Meter,
Factor
(Vc)
Run 1
Final
Initial
600
0
600
932.994
925.421
7.573
1.90
1.90
1.90
64
60
60
58
520 °R
0.982
Run 2
Final
Initial
600
0
600
940.462
932.994
7.468
1.90
1.90
1.90
65
63
60
60
522 °R
0.997
Run 3
Final
Initial
°R
Average Yc: 0.990
Acceptability Criterion: 0.97Y < Yc < 1.03Y
QC Check Result: Metering Console Is Acceptable
CO
CO
M5QCHECK.WK4 11/01/99 (rev. N11QCHK.WK4 11/23/99 08:46 AM)
-------
Alternative Method 5 Post-Test Calibration
MRI Project No.
Sampling Location:
Run No.
1047031.002.05.01
Unit 2A Baghouse Outlet
30-TrnB Run Date: 11/16/99
Console No. N-11
data
line
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
Orifice
delta H
0.85
0.81
0.68
0.35
0.05
0.78
0.65
0.58
0.23
0.03
0.75
0.68
0.58
0.22
0.03
0.75
0.71
0.68
0.30
0.04
0.88
0.85
0.75
0.55
0.04 ,
sqrt
delta H
0.92195
0.90000
0.82462
0.59161
0.22361
0.88318
0.80623
0.76158
0.47958
0.17321
0.86603
0.82462
0.76158
0.46904
0.17321
0.86603
0.84261
0.82462
0.54772
0.20000
0.93808
0.92195
0.86603
0.74162
0.20000
DGM temperature (tm)
inlet, °F outlet, °F
54
54
55
55
55
55
55
56
57
57
57
58
57
58
58
58
58
59
59
60
59
59
61
62
62
53
54
54
55
55
55
55
55
56
56
56
57
56
57
57
57
57
58
58
58
59
59
60
60
60
DGM delta H@:
1.898 in. w.c.
Orifice delta H (average):
0.51280 in. w.c.
sqrt delta H (average):
0.66435
DGM temperature (average):
516.77 °R
Barometric pressure:
29.65 in. Hg
Dry gas molecular weight (Md):
30.58 !b/lb-mole
Total sampling time:
100 minutes
Sample volume (uncorrected)
as read on DGM:
35.084 dcf
DGM correction factor (Y):
1.010
Yqa 0.9967
Difference -1.31%
Result: PASS
YQA48PT.WK4 10/19/99 (rev. YQAN11.WK4 11/23/99 08:51 AM)
Page 1
84
RCA#2 APPENDIX B
-------
ON SITE MERCURY BAROMETER READING CORRECTION
AND ANEROID BAROMETER CALIBRATION CHECK AT TEST LOCATION
Mercury Barometer Description: Princo Model 453, S/N W13559
Mercury Barometer Location: Plant Control Room
Distance Of Barometer From Test Site: 0.00 miles
Altitude Of Barometer Above Sea Level: 124.0 feet
Latitude (north): 36 degrees, 0.00 minutes
Facility: Cogentrix of Rocky Mount, North Carolina
Test Site And Sampling Location: Unit 2A Baghouse Outlet Duct
MRI Project No. 104703.1.002.05.01
Date: 11/21/99
Time: 0958
Readings Obtained By: J. Surman y^'
Observed Barometer Reading: 30.20 in. Hg
Mercury Column Temperature: 74 °F
Correction For Temperature: -0.12 in. Hg
Reading Corrected For Temperature: 30.08 in. Hg
Correction For Gravity: -0.03 in. Hg
Temperature Corrected Reading Corrected For Gravity: 30.05 in. Hg
Aneroid Barometer I.D. No.: Y-2101
Reading Before Adjustment: 30.03 in. Hg
Calibration Check Result: within 0.1 in. Hg
Reading After Adjustment: in. Hg
Remarks:
BAROMETR.WK4 10/19/98 (rev. BAR04703.WK4 11/23/99 08:37 AM)
85
RCA#2 APPENDIX B
-------
RCA #2 Appendix C
M17 Field Sampling Data Sheets
MRJ-OPPT\R4703-02-07 Appendices Covers WPD
-------
FIELD SAMPLING DATA FOR METHOD 17 TRAINS
I
KJ
H
o
Run No.
Dale
Projecl No. 104703.1.002.05.01
Clienl U.S. EPA OAQPS EMAD EMC
Source Cogenlrix Unil 2A _
Sampling Localion Baghouse Outlet
Operator
Record dala every
Baromeler No. Y-2021
t
minules
Baromelric Pressure
Elevation lo Meier Boxes
Meier Box P,
in Hg
34 fl
bar
Elevalion lo Sampling Loc.
Sampling Localion Pbar
Static Pressure —*1*\* •
in Hg
34 fl
. in Hg
Train A No. M17-A
Probe No. A Lenalh: 1 0 fl
Nozzle No. M17-^ Tip Dia. d.H^ in
Pilol Tube No. A CD 0.84
Slack Thermocouple No. 31 58 A
Filler Holder No. /
Filler Assembly No. r •""/
Impinqer Box No. A- /
Umbilical/lmpinger Hookup UH- 30
Umbilical No. ^f^"\_i <\-*b
Meier Box No. ^Jfij? ^'\L>
DGM Correclion (Y) +#tf\- ^'^^
Orifice Meier AH@ "^ I -ol% * ^
Final
w
ftoM
1
Inilial
(oi^
If
.00 (,
Final Meier Volume
Inilial Meier Volume
Leak Check Volume
Initial
Final
Initial
Final
Final
/m 9
^
, 00^1
Initial
Initial
Trait
Final
Initial
Final
Train B Pilot Tube
Initial
{0^1^
i A Sampling System Leak C
Final
Initial
Final
\^\^>
^h^>
rfecks
Final
Initial
Pressure Measurement System Leak Checks
Final
Initial
Initial
Final
Initial
Final
Inilial Final
Final
•*
Inilial
Final
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Inilial
(0^
ff1
too\
Final Meter Volume
Inilial Meier Volume
Leak Check Volume
Final
IHil
to
.oof
Initial
Final
Inilial
vt'fn
Mrf
Final
Inilial
tt,0
-------
Run No.
Date
Sampling Location Unit 2A Baahouse Outlet Duct
Project No. 104703.1.002.05.01
Operator.
page.
of
Sampling Data for Method 1 7 Train A No. M1 7-A
Traverse
Point
Sampling
Time,
min.
0
Clock
Time
(24-Hr)
Dry Gas Meter Reading
(VJ, ft3
Initial
Desired Actual
Velocity
Head
(Ap),
in. H20
Orifice Pressure
Differential
(AH),
in. H20
Desired Actual
Stack
Temp.
(ts),
°F
Dry Gas Meter
Temperature
Inlet
Outlet
Pump
Vacuum,
in. Hg
/7V
J_L
ef-
Z-Z.
/71
/*-
/77
2*9.
.0 1
/v
D-r
n
0.7')
I.)
•/
~tfr
•7/
^Z3-
J&+
S7S
5*7
5"
sr-1
0,7?
9-
ft,
z.y
0.76
S77
ft,
nrf
£ f
tt?
t,-?
A"/
l^t
It
1^7
0-18-
5*7
fl-X
•2.1
0.6,7
&-
for
&2-1
S7?
•7
loo
/?#•
r)
li/7
Samplinq Data for Method 17 Train B No. M17-B
/3J.I
AM
V
f
JZ-
•7-t
j£-
#30,
a.'tf
/.*
/71
nr
r*
~W
&./Z.
•fZ-
"Sfoirfr
V
<2£_
5?
3*?
/av~
&-
t-
~r
tt
-7
/*2-
0-75
L5L£_
sv-
{,$
fYfr
^_
-2..;
Ft
Ml
0,93
-L-7
JO
0,*S
/O
<%O-
i
Cff_
Remarks and Notes:
M17DPG2.WPD September 3, 1999
Tot:
W5I
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
Run No.
Date
Project No. 104703.1.002.05.01
Sample Type (Multi-Point, Single-Point)
Flow Control Device (Valve, Critical Orifice)
Method 5 Meter Box No. /
MSB Pump Type diaphram
MSB Pump No. /
Client/Source U.S. EPA / Coaentrix Unit 2A
Sampling Location Unit 2A Baghouse Outlet
Operator <
Bag Type Tedlar
Method SB Train No._
MSB Flow Meter Type.
MSB Flow Meter No.
Sample No.
NA
NA
rotameter
Desired Sampling Rate .
Leak Check Before Sampling.
Total Sampling Time 77
cc/min
Flow Rate, cc/min: Average
Estimated Total Sample Volume
O After Sampling
min Average Flow Meter Reading
Highest
Lowest
liters
Time
(24-Hr)
Flow
Meter
Reading
Start
Purge
Start
Sampling
Stop
Sampling
Sampling
Remarks and Notes
2-0
tiri
M3BSAMP.WPD June 18. 1998
RCA#2 APPENDIX C
-------
I
*
n
40 CFR 60. APPENDIX A, METHOD 3B. GAS ANALYSIS BY ORSAT
Run No.
Date
Project No. 104703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time _
NA
Sample Type (Bag, Grab)
Analyst
3
1 ;93
2 ;9,3
3
Net
Value
X£>-
y.x
2
Actual
Reading
1 s&s
2 /yr'
3
1 J<)3
2 ;9^3
3
Net
Value
S&-
^"•^
3
Actual
Reading
i ;&o
2 ;£".&
3
1 /9&
2 ;9,z
3
Net
Value
/•£>'&
4>Z
Average
Net
Value
(% v/v)
S&".J
y.^.
Acceptance Criteria per Method 3B
C02 >4% 0.3% v/v O2 >.15% 0.2% v/v
<4% 0.2% v/v <15% 0.3% v/v
Remarks and Notes:
M3BANAL WPD September 3. 1999
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY TRAIN SET-UP DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No. 30 Sampling Train A No.
Sampling Train B No.
Set-up person(s):
Transfer to Sampler:
Relinquished By
Date/Time
REAGENT
LOADING DATA
0$ JO
TRAIN A
TRAIN B
Sampling Nozzle (Quartz)*
Filter Assembly and Holder* .
Filter Type: Whatman QM-A
Probe (316 SS)
Sample Transfer/Vacuum Line
Male 1st Impinger Inlet Blank-Off
Nozzle I.D. No.
Fitter Assembly No.
Fflter Holder No.
1st Impinger (Mod-GBS) 100-200 mLs ASTM Type I Water
U-Connector (A) .: .
2nd Impinger (GBS) 100-200 mLs ASTM Type I Water
U-Connector (B)
3rd Impinger (Mod-GBS) Empty
U-Connector (C)
4th Impinger (Mod-GBS) "200 g indicating silica gel
U-Connector (D)
5th Impinger (Mod-GBS) "200 g indicating silica gel
Impinger Outlet Connector
Connector I.D. No.
/
Initial Weights (grams)
Before and after sampling: Nozzle inlet opening and filter assembly holder outlet opening covered with Teflon® tape, and
entire filter assembly holder with filter assembly and nozzle wrapped in aluminum foil and placed in Ziploc® bag. 1 st impinger
inlet sealed with glass blank-off.
Comments:
M17DSUP.WPD May 13, 1999 (rev. M17DSUP3.WPD November 10, 1999I
RCA#2 APPENDIX C
-------
40 CFP 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY SAMPLE RECOVERY DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Sampling Train A No.
Sampling Train B No.
7-fi
Impinger Box A No.
Impinger Box B No.
~ J
Transfer for Recovery:
Relinquished By & &SJTTJSI _ Received By
Sample recovery person(s): t/
Weights below are in grams.
Date/Time
Date:
BACK HALF RECOVERIES
TRAIN A
1st
Impinger:
Final Wt.
Initial V
Net Wt.
Total Condensate Collected:
Description and/or color:
2nd
3rd
4th & 5th
1st
% Blue
TRAIN B
2nd
3rd
4th & 5th
•7/23
A*
% Blue
..; FRONT HALF RECOVERIES
TRAIN A
FILTER ASSEMBLY:
Sample Number: 3$ 102
PM Description/color:
TRAIN RINSES:
Sample Number:
Components Rinsed*: nozzle, filter holder front
TRAIN B
104
* Acetone rinses with brushing 3 times or more until perceivably clean.
COMMENTS: Acetone rinses are transferred directly to tared Teflon® beaker liners for analysis.
M17DRCV.WPD May 13, 1999 (rev. M17DRCV3.WPD November 10. 19991
RCA#2 APPENDIX C
-------
FIELD SAMPLING DATA FOR METHOD 17 TRAINS
O
Run No.
Date
Project No. 1 04703.1 .002.05.01
Client U.S. EPA OAQPS EMAD EMC
Source Coqentrix Unit 2A _
Sampling Location Baghouse Outlet
Operator <£r>Tt*'~~ _
Record data every A-3 g-5 minutes
Barometer No. Y-2021 _
in Hg
34 ft
m Hg
ft
Barometric Pressure ,2-7-y 3
Elevation to Meter Boxes
Meter Box Pbat '2-%it0
Elevation to Sampling Loc.
Sampling Location p. 2-/'<
.M
34
,
Static Pressure/
.in Hg
Train A No. M17-A
Probe No. A Lenath: 1 0 ft
Nozzle No. M17-/V Tip Dia. O. /^lf in
Pitot Tube No. A CD 0.84
Stack Thermocouple No. 31 58A
Filter Holder No. ?
Filter Assemblv No. ?''*)
Impinqer Box No. A- 1-
Umbilical/lmoinaer Hookup UH-V /
Umbilical No. A/**?"^
Meter Box No. /uVz_-
DGM Correction (Y) O, 91?//
Orifice Meter AH@ /,$/ '
DGM Correction (Y) /,<5/O
Orifice Meter AH@ /,#?$'
page 1 of,
Y
1 •
Assumed Moisture
% Assumed %CO,
lAJ LfiJ LcJ LoJ l£j
Traverse Point Layout
Compass Direction > North
Nozzles are quartz-glass.
Time (24 Hr)
Pass or Fail
Train A Pitot Tube Pressure Measurement System Leak Checks
Initial
w
Final
ll/W
0°°
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Train B Pitot Tube Pressure Measurement System Leak Checks
Initial
'^
Final
ll
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
l^o
?
,oO^
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial
IW}^
^i
,ooM
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
lu«H
-7
,m
Initial
Final
Initial
Final
Initial
IMLrt0!
TJ&Xtf
T--1.1J.O
Final
Initial
^F^.^/2-
VWl'}
2-T.f-r-i
Final
Remarks and Notes: List any other equipment requiring calibration below.
TRAIN A
M17DPQ1 WPD Seplembei 3, 1999
Meter Volume at Start of Run
Meter Volume at End of Run
Total Leak Check or Non-Sample Volume
Adjusted Final Volume
-------
No.
Date
Sampling Location Unit 2A Baahouse Outlet Duct
Project No. 104703.1.002.05.01
page.
of 2—
Operator.
Sampling Data for Method 17 Train A No. M17-A
Traverse
Point
Sampling
Time,
min.
Clock
Time
(24-Hr)
Dry Gas Meter Reading
(VJ, ft3
Initial
Desired Actual
Velocity
Head
-------
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
Run No..
Date
Project No. 104703.1.002.05.01
Sample Type (Multi-Point, Single-Point)
Flow Control Device (Valve, Critical Orifice)
Method 5 Meter Box No._
MSB Pump Type diaphram
MSB Pump No. A/2-
Client/Source U.S. EPA / Cogentrix Unit 2A
Sampling Location Unit 2A Baahouse Outlet
Operator
Bag Type Tedlar
Method SB Train No._
MSB Flow Meter Type.
MSB Flow Meter No.
Sample No.
NA
NA
rotameter
Desired Sampling Rate
Leak Check Before Sampling
Total Sampling Time
cc/min
Flow Rate, cc/min: Average
Estimated Total Sample Volume
^_ After Sampling
min Average Flow Meter Reading
^- ° Highest
3-0
Lowest
liters
Time
(24-Hr)
Flow
Meter
Reading
Start
Purge
Start
Sampling
Stop
Sampling
Sampling
Remarks and Notes
Sfio
2- ,
2- -
1.0-
tft*
M3BSAMP.WPD June 18. 1998
RCA#2 APPENDIX C
-------
s
o
40 CFR 60, APPENDIX A, METHOD 3B, GAS ANALYSIS BY ORSAT
Run No.
Date
Project No. 104703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time _
NA
Sample Type (Bag, Grab)
Analyst c
Baa
Orsat Leak Check Before Analysis:
Burrete A/v Change in 4 Minutes
Pipettes tA/e Change in 4 Minutes
Orsat Leak Check After Analysis:
Burrete A/P Change in 4 Minutes
Pipettes /Y'o Change in 4 Minutes
Analysis
Gas
C02
O2 (Net is actual reading
minus actual CO2 reading)
1
Actual
Reading
1 W
2 W-b
3
1 /*;
2 /$.<>
3
Net
Value
y,j>
2
Actual
Reading
1 ;*>i
2 /*>,(*
3
1 JJ.&~
3
Actual
Reading
1 /*>£•
2 /V.<£
3
1 ;?.;
2 ;9,J
3
Net
Value
S4/.6'
^^S"
Average
Net
Value
(% v/v)
s&t.
y.i5~
Acceptance Criteria per Method 3B
C02
>4%
<4%
0.3% v/v
0.2% v/v
O2
<15%
0.2% v/v
0.3% v/v
Remarks and Notes:
M3BANAL WPD September 3, 1999
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY TRAIN SET-UP DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No. <3j Sampling Train A No. /&J?~S9 Impinger Box A No..
Sampling Train B No. /^/^-^ Impinger Box B No..
Set-up person(s): 'J> St.fr'jrnSr? Date:
Transfer to Sampler:
Relinquished By c/ £us~j7r&t Received By £?> 6f' f~T> n Date/Time
TRAIN COMPONENT REAGENT LOADING DATA
TRAIN A TRAIN B
Sampling Nozzle (Quartz)* ;. Nozzle l.D. No.
Initial Weights (grams)
Filter Assembly and Holder* ; Fitter Assembly No. _
Filter Type: Whatman QM»A . •":
Probe (316 SS) : Filter Holder No. _
Sample TransferA/acuum Line . • . ::
Male 1st Impinger Inlet Blank-Off
1 st Impinger (Mod-GBS) 100-200 mLs ASTM Type I Water .. _
U-Connector (A) . : ; .
2nd Impinger (GBS) 100-200 mLs ASTM Type I Water _
U-Connector (B)
3rd Impinger (Mod-GBS) Empty _
U-Connector (C)
4th Impinger (Mod-GBS) "200 g indicating silica gel
U-Connector (D)
5th Impinger (Mod-GBS) "200 g indicating silica gel
Impinger Outlet Connector Connector l.D. No.
* Before and after sampling: Nozzle inlet opening and filter assembly holder outlet opening covered with Teflon® tape, and
entire filter assembly holder with filter assembly and nozzle wrapped in aluminum foil and placed in Ziploc® bag. 1 st impinger
inlet sealed with glass blank-off.
Comments: -r? />
D////11
M17DSUPWPD May 13, 1999 (rev M17DSUP3.WPD November 10, 1999)
11
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY SAMPLE RECOVERY DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Sampling Train A No. SW- S9
Sampling Train B No.
Transfer for Recovery:
Relinquished By .£?
Received By t). ~
Impinger Box A No.
Impinger Box B No.
Date/Time
Sample recovery person(s):
Weights below are in grams.
t).
Date:
BACK HALF RECOVERIES
TRAIN A
TRAIN B
Impinger: 1st
Final Wt.
Initial Wt. J
Net Wt.
2nd
3rd
4th & 5th
1st
2nd
3rd
4th & 5th
Total Condensate Collected:
Description and/or color:
"7.2
% Blue
% Blue
FRONT HALF RECOVERIES
TRAIN A
TRAIN B
FILTER ASSEMBLY: :
Sample Number: ^^102 o?,> 104
PM Description/color: fr^^k J?)*£j
TRAIN RINSES:
Sample Number: ^]/101 &j 103
Components Rinsed*: nozzle, fitter holder front
* Acetone rinses with brushing 3 times or more until perceivably clean.
COMMENTS: Acetone rinses are transferred directly to tared Teflon® beaker liners for analysis.
M17DRCV WPD May 13. 1999 (rev. M17DRCV3 WPD November 10, 19991
12
RCA#2 APPENDIX C
-------
I
10
FIELD SAMPLING DATA FOR METHOD 17 TRAINS
Run No.
Date
Project No. 104703.1.002.05.01
Client U.S. EPA OAQPS EMAD EMC
Source Coaentrix Unit 2A
Sampling Location
Operator G
aahouse Outlet
Record data every A'S
Barometer No. Y-2021
minutes
Barometric Pressure 2L
Elevation to Meter Boxes
Meter Box Pha,
L__inHg
34 ft
Elevation to Sampling Loc.
Sampling Location Pba, g-
in Hg
34 ft
Static Pressure/y ^"^ "•
. in Hg
Train A No. M17-A
Probe No. A Lenath: 10 ft
Nozzle No. M17- 9 Tip Dia. 0,lW in
Pitot Tube No. A CD 0.84
Stack Thermocouple No. 3158A
Filter Holder No. /"
Filter Assembly No. pf
Impinger Box No. A- /
Umbilical/lmpinaer Hookup UH- Tti
Umbilical No. /V &- V
Meter Box No. /V/2-
DGM Correction IY) £>* ?%
Orifice Meter AH@ /. }?JO
TrainB No. M17-B
Probe No. B Lenath: 10 ft
Nozzle No. M17-/£>Tio Dia. ^-I^Ue in
Pitot Tube No. B C_ 0.84
Stack Thermocouple No. 31 58B
Filter Holder No. £
Filter Assembly No. f (s
Impinqer Box No. B- (
Umbilical/lmpinqer Hookup UH- TZ-
Umbilical No. /^^- 1
Meter Box No. A/ '~ ^
DGM Correction (Y) S^/0
Orifice Meter AH@ /- ??#
Assumed Moisture
//
page 1 of
1
% Assumed %CO2
l">
%O2
lAl LBj Ld LfiJ l£j
Traverse Point Layout
Compass Direction s* North
Nozzles are quartz-glass.
Time (24 Hr)
Pass or Fail
Train A Pitot Tube Pressure Measurement System Leak Checks
Initial
ffl\
Final
ion
Sl&QO
1*
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Train B Pitot Tube Pressure Measurement System Leak Checks
Initial
$?3J>
Final
ioM
c&ss>
Initial
Final
Initial
Final
Initial
Final
Initial
Final
O
Train A Sampling System Leak Checks
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial
Cflftls
ti
,0o<\
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
\Q\°(
7
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial
08"57
/£
Jo'h
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
\Q^>
2
.no^
Initial
Final
Initial
Final
Initial
W'&f
W"fll
1f.1ff
Final
Initial
Itlr t»f
rtlrfll
27.^3^
Final
CO
Remarks and Notes: List any other equipment requiring calibration below.
TRAIN A
M17DPQ1 WPD Septembers, 1999
Meter Volume at Start of Run
Meter Volume at End of Run
Total Leak Check or Non-Sample Volume
Adjusted Final Volume
-------
Run No.
Date
Sampling Location Unit 2A Baohouse Outlet Duct
Project No. 104703.1.002.05.01
Operator C^v ft?-—
page.
of
Sampling Data for Method 17 Train A No. M17-A
Traverse
Point
Sampling
Time,
min.
Clock
Time
(24-Hr)
Dry Gas Meter Reading
,
°F
Dry Gas Meter
Temperature
Inlet
Outlet
Pump
Vacuum,
in. Hg
Silica Gel
Impinger
Outlet
Temp.,
°F
A-f
efrft
2*7 S&
a
0,6
7(3
tf
//7
-5.4
2.7
2-0
•2.7 ?;
7V
2.
2-7
•2.-7-7-Z/
-if
/77_
vs
Z2£_
/77
3"'
/77
rt.70
T/
y?*
Z-Y
T'S
-2,3
2-
72-
/of*
75
ft
Sampling Data for Method 17 Train B No. M17-B
twit
fit?
. VX
52
Remarks and Notes:
M17DPG2.WPD September 3. 1999
14
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
Date X/-/7-ff
Run No._
Project No. 104703.1.002.05.01
Sample Type (Multi-Point, Single-Point)
Flow Control Device (Valve, Critical Orifice)
Method 5 Meter Box No. /1//2-
MSB Pump Type diaphram
MSB Pump No.
Client/Source U.S. EPA / Coaentrix Unit 2A
Sampling Location Unit 2A Baghouse Outlet
Operator
Bag Type Tedlar
Method SB Train No._
MSB Flow Meter Type.
MSB Flow Meter No. _
Sample No.
NA
NA
rotameter
Desired Sampling Rate
Leak Check Before Sampling.
Total Sampling Time ^
cc/min
Flow Rate, cc/min: Average _
Estimated Total Sample Volume
^ After Sampling
min Average Flow Meter Reading
Highest ^
Lowest
liters
Time
(24-Hr)
Flow
Meter
Reading
Start
Purge
Start
Sampling
Stop
Sampling
Sampling
Remarks and Notes
"1.
M3BSAMP WPD June 18. 1998
15
RCA#2 APPENDIX C
-------
o>
o
40 CFR 60, APPENDIX A, METHOD 3B, GAS ANALYSIS BY ORSAT
Run No.
Date
Project No. 104703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time .
NA
Sample Type (Bag, Grab)
Analyst c
Baa
Orsat Leak Check Before Analysis:
Burrete xVfr Change in 4 Minutes
Pipettes «/K> Change in 4 Minutes
Orsat Leak Check After Analysis:
Burrete /& Change in 4 Minutes
Pipettes /y& Change in 4 Minutes
Analysis
Gas
CO2
02 (Net is actual reading
minus actual CO2 reading)
1
Actual
Reading
1 M-7
2 S&7
3
2 /9£'
3
Net
Value
Stf.7
4.$-
2
Actual
Reading
\'%
3
2 ;9sf
3
Net
Value
yy.7
*j
3
Actual
Reading
1 /V.7
3
2 ;$A£~
3
Net
Value
,*•*
**
Average
Net
Value
(% v/v)
;*7
«f
Acceptance Criteria per Method 3B
C0
0.3% v/v
0.2% v/v
0.2% v/v
0.3% v/v
Remarks and Notes:
M3BANAL.WPD Septembers, 1999
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY TRAIN SET-UP DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No. <3£Z Sampling Train A No. ^yy-^ Impinger Box A No.
Sampling Train B No. S3?/J7-{3 Impinger Box B No.
Set-up person(s): «-/. £iJ/s&>&s? Date:
Transfer to Sampler:
Relinquished By **• £*Js'/??l>si Received By ^ &sSrr"~> Date/Time _,
TRAIN COMPONENT REAGENT LOADING DATA
TRAIN A TRAIN B
Sampling Nozzle (Quartz)* I Nozzle I.D. No. /*}*?->>
Filter Assembly and Holder* Fitter Assembly No.
Filter Type: Whatman Qft/t-A \ . \
Probe (316 SS) : Filter Holder No.
Sample Transfer/Vacuum Line : ; !
Male 1st Impinger Inlet Blank-Off ;
j Initial Weights (grams)
1st Impinger (Mod-GBS) 100-200 mLs ASTM Type I Water . _
U-Connector (A)
2nd Impinger (GBS) 100-200 mLs ASTM Ty:pe t Water _
U-Connector (B)
3rd Impinger (Mod-GBS) Empty _
U-Connector (C)
4th Impinger (Mod-GBS) "200 g indicating silica gel
U-Connector (D)
5th Impinger (Mod-GBS) "200 g indicating silica gel
Impinger Outlet Connector Connector I.D. No.
* Before and after sampling: Nozzle inlet opening and filter assembly holder outlet opening covered with Teflon® tape, and
entire filter assembly holder with filter assembly and nozzle wrapped in aluminum foil and placed in Ziploc® bag. 1 st impinger
inlet sealed with alass blank-off.
Comments:
/
lirlfi
M17DSUPWPD May 13, 1999 (rev M17DSUP3.WPD November 10. 1999)
17
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY SAMPLE RECOVERY DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Sampling Train A No.
Sampling Train B No..
Transfer for Recovery:
Relinquished By £?• &si ^rjr>
Sample recovery person(s):
Weights below are in grams.
Received By cA
Impinger Box A No..
Impinger Box B No..
Date/Time
S/0e>
Datp-
BACK HALF RECOVERIES
TRAIN A
Impinger: 1st
Final Wt. 7&&?7
Initial Wt. &'^'S'
Net Wt.
2nd
3rd
4th & 5th
1st
Total Condensate Collected:
Description and/or color:
frtft'
% Blue
TRAIN B
2nd
3rd
4th & 5th
£3.3
•?*
,%
% Blue
FRONT HALF RECOVERIES
TRAIN A
FILTER ASSEMBLY:
Sample Number: ^3^102
PM Description/color:
TRAIN RINSES:
Sample Number:
Components Rinsed*: nozzle, filter holder front
TRAIN B
* Acetone rinses with brushing 3 times or more until perceivably clean.
COMMENTS: Acetone rinses are transferred directly to tared Teflon® beaker liners for analysis.
M17DRCV.WPD May 13, 1999 (rev. M17DRCV3.WPD November 10, 1999)
18
RCA#2 APPENDIX C
-------
FIELD SAMPLING DATA FOR METHOD 17 TRAINS
g
to
fc
r>
Run No..
Project No. 104703.1.002.05.01
Client U.S. EPA OAQPS EMAD EMC
Source Coaentrix Unit 2A
Sampling Location-, Baohouse Outlet
Operator.
•fKl A 1 S - tt,
mutes
r" mi
Y-2021
in Hg
34 ft
Record data ev
Barometer No..
Barometric Pressure %
Elevation to Meter Boxes
Meter Box Pba, /}p,OO jn Hg
Elevation to Sampling Loc. 34 ft
Sampling Location^3,,.,, 'jOrOG jn Hg
Static
Train A No. M17-A
Probe No. A Lenath: 1 0 ft
Nozzle No. M17- f^Tm Dia. O-iHk in
Pitot Tube No. A CD 0.84
Stack Thermocouple No. 31 58A
Filter Holder No. ~1
Filter Assembly No. £*^
Impinger Box No. A- ^
Umbilical/lmpinqer Hookup UH-
Umbilical No. fJ^O -4
Meter Box No. A/ \T-
DGM Correction (Yl 3*fL> in
Pitot Tube No. B C. 0.84
Stack Thermocouple No. 31 58B
Filter Holder No. &
Filter Assembly No. r'-'tf
Impinaer Box No. B- Z~
Umbilical/lmpinqer Hookup UH-'2-
Umbilical No. /l/"?^'/
Meter Box No. /v' / /
DGM Correction (Y) / -* North
Nozzles are quartz-glass.
Time (24 Hr)
Pass or Fail
Train A Pitot Tube Pressure Measurement System Leak Checks
Initial
11 If
Final
I'M
J36^>
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Train B Pitot Tube Pressure Measurement System Leak Checks
Initial
Illtf
Final
fW/
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Train A Sampling System Leak Checks
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial
m
.5
.w\
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
\VHJ
fl
,00\
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial
(11-0
.5
•fl(K
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
vw
1
.00?)
Initial
Final
Initial
Final
Initial
V/.Ht-
7.'^
W.nt
Final
Initial
Vt.
-------
Run No.
Date /
Sampling Location Unit 2A Baahouse Outlet Duct
Project No. 104703.1.002.05.01
Operator.
page.
of 2-
Sampling Data for Method 17 Train A No. M17-A
Traverse
Point
Sampling
Time,
min.
Clock
Time
(24-Hr)
Dry Gas Meter Reading
(VJ, ft3
Initial
Desired
Actual
Velocity
Head
(Ap),
in. H20
Orifice Pressure
Differential
(AH),
in. H20
Desired Actual
Stack
Temp.
(ts),
Dry Gas Meter
Temperature
(U,
°F
Inlet Outlet
Pump
Vacuum,
in. Hg
2,7
"
¥
/So
It
,o f
&.
5V
a.%,
-
7
v-n
yy
I2Z?
31
/7T
t-l
60
A -
0,72-
(Kit
T
Z
52
0, -27
/77
'*"?
:.^
r
of
0-72-
71.
4.
-76
OL
pot
$61,20
0,0%
Ft
IZ£.
V
2. ,-
/ft
'9
CM
a. 75"
0,15
-7$
//y
/oo
S"
Remarks and Notes:
M17DPG2WPD September 3. 1999
20
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
Run No..
Date
Project No. 104703.1.002.05.01
Sample Type (Multi-Point, Single-Point)
Flow Control Device (Valve, Critical Orifice)
Method 5 Meter Box No. tf/T,
MSB Pump Type diaphram
MSB Pump No.
Client/Source U.S. EPA / Coqentrix Unit 2A
Sampling Location Unit 2A Baahouse Outlet
Operator
Bag Type Tedlar
Method 3B Train No. _
MSB Flow Meter Type.
MSB Flow Meter No.
Sample No.
NA
NA
rotameter
Desired Sampling Rate
Leak Check Before Sampling.
Total Sampling Time ffi?
cc/min
Flow Rate, cc/min: Average
Estimated Total Sample Volume
After Sampling
min Average Flow Meter Reading
J** Highest
Lowest
liters
Time
(24-Hr)
Flow
Meter
Reading
Start
Purge
Start
Sampling
Stop
Sampling
Sampling
Remarks and Notes
Utf
tfft
V
r efi
M3BSAMP.WPD June 18, 1998
21
RCA#2 APPENDIX C
-------
ro
n
*
to
fc
"a
w
R
o
CFR 60, APPENDIX A, METHOD 3B, GAS ANALYSIS BY ORSAT
Run No.
Date
Project No. 104703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time
NA
Sample Type (Bag, Grab)
Analyst J.
Bag
Orsat Leak Check Before Analysis:
Burrete tfo Change in 4 Minutes
Pipettes A£» Change in 4 Minutes
Orsat Leak Check After Analysis:
Burrete Afe Change in 4 Minutes
Pipettes Svv Change in 4 Minutes
Analysis
Gas
C02
O2 (Net is actual reading
minus actual CO2 reading)
1
Actual
Reading
1 S*~*
2 /&*/
3
1 Sf.7
2/^.7
3
Net
Value
'
3. '3
2
Actual
Reading
1 A£7y
2 }£~.^
3
1 ;Y
3,3
Average
Net
Value
(% v/v)
'
3.3
Acceptance Criteria per Method 3B
C0
,<4%
0.3% v/v
0.2% v/v
02
<15%
0.2% v/v
0.3% v/v
Remarks and Notes:
M3BANALWPD September 3, 1999
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY TRAIN SET-UP DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Impinger Box A No. /*"*<
Impinger Box B No. &•"&•
Run No. 33 Sampling Train A No.
Sampling Train B No.
Set-up person(s): c/. t$t>^v^rr^^?
Transfer to Sampler:
Relinquished By
Date:
Date/Time
TRAIN COMPONENT
REAGENT
LOADING DATA
TRAIN A
TRAIN B
Sampling Nozzle (Quartz)*
Filter Assembly and Holder*
Filter Type: Whatman QM>A
Probe (316 SS)
Sample Transfer/Vacuum Line :
Male 1st Impinger Inlet Blank-Off
Nozzle I.D. No.
Fitter Assembly No.
: Filter Holder No.
1st Impinger (Mod-GBS) 100-200 mLs ASTM Type I Water
U-Connector (A) • =_ . •
2nd Impinger (GBS) 100-200 mLs ASTM Type I Water
U-Connector (B)
3rd Impinger (Mod-GBS) Empty
U-Connector (C)
4th Impinger (Mod-GBS) "200 g indicating silica gel
U-Connector (D)
5th Impinger (Mod-GBS) "200 g indicating silica gel
Impinger Outlet Connector
Connector I.D. No.
Initial Weights (grams)
•73#,
Before and after sampling: Nozzle inlet opening and filter assembly holder outlet opening covered with Teflon® tape, and
entire filter assembly holder with filter assembly and nozzle wrapped in aluminum foil and placed in Ziploc® bag. 1 st impinger
inlet sealed with glass blank-off.
Comments:
///#•/?*
M17DSUP.WPD May 13, 1999 (rev. M17DSUP3.WPD November 10, 19991
23
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY SAMPLE RECOVERY DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Sampling Train A No.
Sampling Train B No.
Transfer for Recovery:
Relinquished By Z?- £>sjr~T'''S?
Sample recovery person(s):
Weights below are in grams.
Received By <)•
-------
FIELD SAMPLING DATA FOR METHOD 17 TRAINS
I
a
o
page 1 of.
/rj
Run No. 77
Date /7"/7-?f
Project No. 104703.
1.002.05.01
Client U.S. EPA OAQPS EMAD EMC
Source Coaentrix Unit 2A
Sampling Loce
Operator 6j
Record data e
Barometer No
Barometric Pre
Elevation to IV
Meter Box Pb3I
Elevation to S
Sampling Loce
Static Pressur
Time (24 Hr)
Pass or Fail
tion Baahouse
i/erv 1^1 & ^
Outlet
minutes
Y-20?1
assure
23 o
eter Boxes
ampling
tion Pba,
B.^fe
1f\,%
Loc.
1 in
34
in
34
ifc in
Hg
ft
Hg
ft
Hg
^-#7,3? inH,0
Train A No. M17-A
Probe No.
A
Nozzle No. Ml 7-
Pitot Tube No.
Le
^.Tip
A
Stack Thermocouple No.
Filter Holder No. /
Filter Assembly h
Impinger Box No.
Umbilical/Impinge
Umbilical No.
lo. ?
A-
r Hooki
/(^-
>ngth: _
Dia. 9, /
CP
10 ft
yl/ in
0.84
3158A
-*?
(
JD UH-
y
*)0
Meter Box No. A /2-~
DGM Correction (Y) O.'i'Mt
Orifice Meter AH<3> 1- $!&
Assumed
Moisture
a
Train B No.
Probe No.
Nozzle No._
Pitot Tube h
Stack Them
Filter Holde
Filter Assen
Impinger Bo
Umbilical/In
Umbilical N
Meter Box I
DGM Corre
Orifice Met<
M17-B
B
Jo. B
nocoupl
No.
ibly No
x No.
ipinger
3. A'
-\o.
Lenq
. Tip Dia
e No.
2~
F-K>
B-/
-lookup
/5?/-y
th:_L
o. Mb
Cp-Q.
3158B
Q_ft
in
84_
UH-'H-"
A/V/
:tion (Y) / OIO
jr AH@
% Assumed %CO, /
Train A Pitot Tube Pressure Measurement System Leak Checks
Initial
/^O?
Final
((f\$
^A
Initial
Final
Initial
Final
Initial
Final
Initial
Final
/,n
•?
5 %o2 6
Ct
i
•
r
•
•
• •
LAJ LBJ LcJ LoJ u=J
Traverse Point Layout
)mpass Direction > North
Nozzles are quartz-glass.
Train B Pitot Tube Pressure Measurement System Leak Checks
Initial
/Y37
Final
{tfl'"
ftJ^A
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Train A Sampling System Leak Checks
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial
ltV)
ft
,n4
-------
Run No.
Date f(-f7-M
Sampling Location Unit 2A Baahouse Outlet Duct
Project No. 1 04703.1.002.05.01
Operator.
page.
of 2-
Sampling Data for Method 17 Train A No. M17-A
Traverse
Point
Sampling
Time,
min.
0
Clock
Time
(24-Hr)
Dry Gas Meter Reading
(VJ, ft3
Initial
Desired
Actual
Velocity
Head
(Ap),
in. H20
Orifice Pressure
Differential
(AH),
in. H20
Desired Actual
Stack
Temp.
"7
'60
35
•7
-7
i?y
/*-
/.*
a.
G ,5P
^Z
13-
g tf~
-70
an, 9
£12,
7
&)
IblG
-70
, 23-2
-7
Remarks and Notes:
M17DPQ2.WPD September 1, 1999
26
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
Run No.
Date
Project No. 104703.1.002.05.01
Sample Type (Multi-Point, Single-Point)
Flow Control Device (Valve, Critical Orifice)
Method 5 Meter Box No.
MSB Pump Type diaphram
MSB Pump No. A- ft-
Client/Source U.S. EPA / Cogentrix Unit 2A
Sampling Location Unit 2A Baghouse Outlet
Operator do'-tf/U
Bag Type Tedlar
Method SB Train No._
MSB Flow Meter Type.
MSB Flow Meter No.
Sample No.
NA
NA
rotameter
Desired Sampling Rate
Leak Check Before Sampling
Total Sampling Time ^
cc/min
Flow Rate, cc/min: Average
Estimated Total Sample Volume
C After Sampling
min Average Flow Meter Reading
^/-^ Highest '•^e-f
Lowest
liters
Time
(24-Hr)
Flow
Meter
Reading
Start
Purge
Start
Sampling
Stop
Sampling
Sampling
Remarks and Notes
IS
l&i
frif
10
M3BSAMP.WPD June 18, 1998
27
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
Date
Run No.
Project No. 104703.1.002.05.01
Sample Type (Multi-Point, Gingle-Pc
rt)
Flow Control Device (Valve, Critical Orifice)
Method 5 Meter Box No. A)~ll
MSB Pump Type diaohram
MSB Pump No. A^"//
Client/Source U.S. EPA / Cogentrix Unit 2A
Sampling Location Unit 2A Baahouse Outlet
Operator
-------
40 CFR 60, APPENDIX A, METHOD 3B, GAS ANALYSIS BY ORSAT
Run No.
n
Date
Project No. 104703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time
NA
Sample Type (Bag, Grab)
Analyst c/,
Bag
Orsat Leak Check Before Analysis:
Burrete ^o Change in 4 Minutes
Pipettes A/o Change in 4 Minutes
Orsat Leak Check After Analysis:
Burrete /Sc> Change in 4 Minutes
Pipettes A4? Change in 4 Minutes
Analysis
Gas
C02
02 (Net is actual reading
minus actual C02 reading)
1
Actual
Reading
1 /*/,(*
2 S^lo
3
1 / cf. j cf
2 a A jfr*
r{J*£f
3
Net
Value
/•*.(*
'
2
Actual
Reading
1 /*i4
2 /y&
3
1 tf.P
2 s/:?
3
Net
Value
;#.£•
y,z<
3
Actual
Reading
1
2
3
1
2
3
Net
Value
Average
Net
Value
(% v/v)
S*J-&
4% 0.3% v/v 02 >_15% 0.2% v/v
.<_4% 0.2% v/v <15% 0.3% v/v
Remarks and Notes:
S3
co
M3BANAL WPD September 3, 1999
-------
CO
o
I
KJ
o
40 Cf/7 60. APPENDIX A, METHOD 3B, GAS ANALYSIS BY ORSAT
Run No.
Date
Project No. 104703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time .
NA
Sample Type (Bag, Grab)
Analyst
Bag
Orsat Leak Check Before Analysis:
Burrete /*£ Change in 4 Minutes
Pipettes /y£> Change in 4 Minutes
Orsat Leak Check After Analysis:
Burrete Wo Change in 4 Minutes
Pipettes yy'o Change in 4 Minutes
Analysis
Gas
CO2
02 (Net is actual reading
minus actual C02 reading)
1
Actual
Reading
1 /*.?
2 S^,?
3
1 S9.S
2 /$,/
3
Net
Value
;yS
2 S&f
3
1 /9J
2 J$;J
3
Net
Value
s^.$>
"^'
3
Actual
Reading
1
2
3
1
2
3
Net
Value
Average
Net
Value
(% v/v)
/**
T
Acceptance Criteria per Method 3B
CO,
0.3% v/v
0.2% v/v
0.2% v/v
0.3% v/v
Remarks and Notes:
M3BANALWPD September 3, 1999
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY TRAIN SET-UP DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Sampling Train A No.
Sampling Train B No..
Impinger Box A No.
Impinger Box B No..
Set-up person(s):
Transfer to Sampler:
Relinquished By «J.
Date:
Received By £>/
Date/Time
TRAIN COMPONENT
REAGENT
LOADING DATA
TRAIN A
TRAIN B
Sampling Nozzle (Quartz)*
Filter Assembly and Holder*
Filter Type: Whatman QM-A
Probe (316 SS)
Sample Transfer/Vacuum Line
Male 1st Impinger Inlet Blank-Off
Nozzle I.D. No.
Fitter Assembly No.
. Filter Holder No.
Initial Weights (grams)
1st Impinger (Mod-GBS) 100-200 mLs ASTM Type I Water
U-Connector (A) • '•_••
2nd Impinger (GBS) 100-200 mLs ASTM Type I Water
U-Connector (B)
3rd Impinger (Mod-GBS) Empty
U-Connector (C)
4th Impinger (Mod-GBS) "200 g indicating silica gel
U-Connector (D)
5th Impinger (Mod-GBS) "200 g indicating silica gel
Impinger Outlet Connector
Connector I.D. No.
Before and after sampling: Nozzle inlet opening and filter assembly holder outlet opening covered with Teflon® tape, and
entire filter assembly holder with filter assembly and nozzle wrapped in aluminum foil and placed in Ziploc® bag. 1st impinger
inlet sealed with glass blank-off.
Comments:
M17DSUPWPD May 13, 1999 (rev M17DSUP3.WPD November 10, 1999)
31
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY SAMPLE RECOVERY DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Sampling Train A No.
Sampling Train B No..
Impinger Box A No. &fsf~T>r>
Sample recovery person(s):
Weights below are in grams.
Received By
Date/Time
Date:
BACK HALF RECOVERIES
TRAIN A
Impinger: 1st
Final Wt.
Initial Wt.
Net Wt.
Total Condensate Collected:
Description and/or color:
2nd
3rd
4th & 5th
1st
79.7
% Blue
TRAIN B
2nd
3rd
$.3 - ^
4th & 5th
7-7
$7,3
% Blue
FRONT HALF RECOVERIES
TRAIN A
102
FILTER ASSEMBLY:
Sample Number:
PM Description/color:
TRAIN RINSES:
Sample Number: .3V 101
Components Rinsed*: nozzle, filter holder front
TRAIN B
103
* Acetone rinses with brushing 3 times or more until perceivably clean.
COMMENTS: Acetone rinses are transferred directly to tared Teflon® beaker liners for analysis.
/
/ / lam
M17DRCV.WPD May 13. 1999 (rev. M17DRCV3.WPD November 10, 1999)
32
RCA#2 APPENDIX C
-------
£
K)
o
ft
FIELD SAMPLING DATA FOR METHOD 17 TRAINS
page 1 of
Run No. TI
Date /'(a''
Project No. 104703.
1.002.05.01
Client U.S. EPA OAQPS EMAD EMC
Source Coqentrix Unit 2A
Sampling Locz
Operator fait.
r tfij
Record data e
Barometer No
Barometric Prt
Elevation to IV
Meter Box Pba
Elevation to S
Sampling Loce
Static Pressur
Time (24 Hr)
Pass or Fail
ition Baqhouse Outlet^
/p/v
very A--1)
W^h minutes
Y-20?1
assure
ffrU
in Hg
eter Boxes 34 ft
ampling
ition Pbar
e —2--
70,1$
in Hq
Loc. 34 ft
10 •-!•?
-J^pHg
Train A No. M17-A
Probe No
A
L
Nozzle No. Ml 7-// Tip
Pitot Tube No. A
Stack Thermocouple No.
Filter Holder No. j
Filter Assembly h
Impinger Box No.
Umbilical/Impinge
Umbilical No.
Meter Box No.
DGM Correction
3ngth: _
Cp
10 ft
f% in
0.84
3158A
Jo. F~H
A-
;r Hooki
^
jp UH-
^
/
A' !'2~
Y)
C- yib
Orifice Meter AH(3> /, ?/Y;
•) Pii't-J** /fa (-|2o Assumed
Moisture
I!
Train B No.
Probe No.
Nozzle No..
Pitot Tube Is
Stack Them
Filter Holde
Filter Assen
Impinger Bo
Umbilical/lrr
Umbilical N
Meter Box I
M17-B
B
Lena
MW-fi Tip Dia
•Jo. B
nocoupl
No.
ibly No
x No.
e No. ,
a
/£-/!
B--7
ipinger Hookup
th: 1
CP_CL
3158B
i
UH- 2
P_ft
in
3A—
3. A' £•>('" I
•Jo.
"A-''-//
f
DGM Correction (Y) /.- &/f''
Orifice Meter AH@
% Assumed %CO3 _/
Train A Pitot Tube Pressure Measurement System Leak Checks
Initial
fL/i 1 \
L^3/*"V
Final Ini
jt3i<6
rtW>0
I
tial Final
Initial
Final
Initial
Final
Initial
Final
/•/f
^ %o, 5
>
i
LAJ LBJ LcJ LoJ LeJ
Traverse Point Layout
Compass Direction > North
Nozzles are quartz-glass.
Train B Pitot Tube Pressure Measurement System Leak Checks
Initial
oy^o
Final
{Q'ti
Q*i/vrt
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial
O3i*
\<7
•ooz*
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
(Oil
-7
.on"
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial
OW
h
.*&
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
IOM
-7
tQ&
Initial
Final
Initial
Final
Initial
1J.4CI
fcsT, Lit,
M'lH'f
Final
e
Initial
w.w
tH-M
Ht.lli*
Final
co
CO
Remarks and Notes: List any other equipment requiring calibration below.
TRAIN A
M17DPQ1 WPD September 3, 1999
Meter Volume at Start of Run
Meter Volume at End of Run
Total Leak Check or Non-Sample Volume
Adjusted Final Volume
-------
Run No.
Date
Sampling Location Unit 2A Baahouse Outlet Duct
Project No. 104703.1.002.05.01
Operator fay.
3,/vrl ••>-
page.
of
Sampling Data for Method 17 Train A No. M17-A
Traverse
Point
Sampling
Time,
min.
0
Clock
Time
(24-Hr)
Dry Gas Meter Reading
*£.
-37
JS.
<2$U-
Z-2.
*
2L
0-91
/to
yy
-3*5
yy
£-7
173,2-0
•35-
0.07
tf.bl
¥*•
3-
39
-£&-
-r
5V
0-6 t
•7
JL£.
-7
5*7
ISI- 72-
a-01
STtf
53*
V
6-71
/#/
"7
3?
•72-
0-3-7
/So
75
£1
7W
0
Sampling Data for Method 17 Train B No. M17-B
•r
./. 2-
OSS7
V/
-7
^L
_/i.
i^=-
G.I*')
Y/
(VI
?¥
a^
5, /c
yz.
& -f 5"
•7
3&7V
-7
L2=-
7-.-?
Remarks and Notes:
M17DPG2.WPD Septembers, 1999
34
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
Run No.
35"
Date
Project No. 104703.1.002.05.01 _
Sample Type (Multi-Point, Single-Point)
Flow Control Device (Valve, Critical Orifice)
Method 5 Meter Box No.
MSB Pump Type diaphram
MSB Pump No.
Client/Source U.S. EPA / Cogentrix Unit 2A
Sampling Location Unit 2A Baghouse Outlet
Operator
Bag Type Tedlar
Method SB Train No._
MSB Flow Meter Type
MSB Flow Meter No. _
Sample No.
NA _
NA
rotameter
Desired Sampling Rate
Leak Check Before Sampling
Total Sampling Time ~1D
cc/min
Flow Rate, cc/min: Average
Estimated Total Sample Volume
0 After Sampling
min Average Flow Meter Reading
Highest
Lowest
liters
Time
(24-Hr)
Flow
Meter
Reading
Start
Purge
Start
Sampling
Stop
Sampling
Sampling
Remarks and Notes
^L.
0%
'b.o
ta£_
M3BSAMP WPD June 18, 1998
35
RCA#2 APPENDIX C
-------
co
Oi
s
to
fc
*ti
w
o
40 CFR 60, APPENDIX A, METHOD 3B, GAS ANALYSIS BY ORSAT
Run No.
Date
Project No. 1Q4703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time _
NA
Sample Type (Bag, Grab)
Analyst J.
Bag
Orsat Leak Check Before Analysis:
Burrete x^o Change in 4 Minutes
Pipettes /*£ Change in 4 Minutes
Orsat Leak Check After Analysis:
Burrete XV£ Change in 4 Minutes
Pipettes /*£> Change in 4 Minutes
Analysis
Gas
C02
02 (Net is actual reading
minus actual CO2 reading)
1
Actual
Reading
1 ss:*
2 /J>,£>
3
1 S&7
2 ;&7
3
Net
Value
SJ»'i?
3,7
2
Actual
Reading
1 s&v
2 s&e
3
1 /eft.?
o y*£ C?
3
Net
Value
/&'O
3.8
3
Actual
Reading
1 AST*
2 /'.5">£
3
21 &- &
Sfji£.j
3
Net
Value
;<5~.o
3,£
Average
Net
Value
(% v/v)
/&,O
x,8
Acceptance Criteria per Method 3B
C02 >4% 0.3% v/v O2 >:15% 0.2% v/v
<4% 0.2% v/v <15% 0.3% v/v
Remarks and Notes:
M3BANALWPD Septembers, 1999
-------
40 CFft 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY TRAIN SET-UP DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Set-up person(s):
Transfer to Sampler:
Relinquished By
Sampling Train A No.
Sampling Train B No.
Received By
TRAIN COMPONENT
REAGENT
Impinger Box A No.
Impinger Box B No.
Date:
.^
Date/Time JJ/jfW
LOADING DATA
TRAIN A
TRAIN B
Sampling Nozzle (Quartz)*
Filter Assembly and Holder* .
Filter Type: Whatman QM-A
Probe (31 6 SS)
Sample Transfer/Vacuum Line
Male 1st Impinger Inlet Blank-Off
Nozzle I.D. No.
Filter Assembly No.
: .
Filter Holder No.
1st Impinger (Mod-GBS) 100-200 mLs ASTM Type I Water
U-Connector (A) •''-"...:
2nd Impinger (GBS) 100-200 mLs ASTM Type :l Water
U-Connector (B)
3rd Impinger (Mod-GBS) Empty
U-Connector (C)
4th Impinger (Mod-GBS) "200 g indicating silica gel
U-Connector (D)
5th Impinger (Mod-GBS) "200 g indicating silica gel
Impinger Outlet Connector
Connector I.D. No.
Initial Weights (grams)
• ~
,
/ z **f
f
'<>"•
Before and after sampling: Nozzle inlet opening and filter assembly holder outlet opening covered with Teflon® tape, and
entire filter assembly holder with filter assembly and nozzle wrapped in aluminum foil and placed in Ziploc® bag. 1 st impmger
inlet sealed with glass blank-off.
Comments:
M17DSUP.WPD May 13, 1999 (rev M17DSUP3.WPD November 10, 1999]
37
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICIPATE MATTER TRAIN (M17)
FIELD LABORATORY SAMPLE RECOVERY DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Sampling Train A No.
Sampling Train B No.
Impinger Box A No..
Impinger Box B No.
Transfer for Recovery:
Relinquished By Z7,
Sample recovery person(s):
Weights below are in grams.
C/- £i
Received By
Date/Time
Date:
BACK HALF RECOVERIES
TRAIN A
1st
Impinger:
Final Wt.
Initial Wt.
Net Wt.
Total Condensate Collected:
Description and/or color:
2nd
3rd
4th & 5th
1st
% Blue
TRAIN B
2nd
3rd
4th & 5th
% Blue
FRONT HALF RECOVERIES
TRAIN A
FILTER ASSEMBLY:
Sample Number: J£5"102
PM Description/color: }?)&£>*-
TRAIN RINSES:
Sample Number: c35""101
Components Rinsed*: nozzle, filter holder front
TRAIN B
* Acetone rinses with brushing 3 times or more until perceivably clean.
COMMENTS: Acetone rinses are transferred directly to tared Teflon® beaker liners for analysis.
M17DRCV WPD May 13, 1999 (rev. M17DRCV3.WPD November 10, 19991
38
RCA#2 APPENDIX C
-------
n
o
co
co
FIELD SAMPLING DATA FOR METHOD 17 TRAINS
Run No.
Date
Project No. 104703.1.002.05.01
Client U.S. EPA OAOPS EMAD EMC
Source Coaentrix Unit 2A
Sampling Location Baahouse Outlet
Operator
Record data every A-?
Barometer No. Y-2021
' '
minutes
Barometric Pressure nu<
i
Elevation to Meter Boxes
Meter Box Pbar ty'
in Hg
.34 ft
Elevation to Sampling Loc.
Sampling Location Pbar ^
Static Pressure ~
in Hg
34 ft
in Hg
jn H2O
Train A No. M17-A
Probe No. A Lenath: 10 ft
Nozzle No. M17-p Tic Dia. 0. >Hif in
Pitot Tube No. A CD 0.84
Stack Thermocouple No. 31 58A
Filter Holder No. (e
Filter Assembly No. r n
Impinger Box No. A- /
Umbilical/lmpinqer Hookup UH- 7&
Umbilical No. fU'J&^tf
Meter Box No. A/'^
DGM Correction (Y) d'^%
Orifice Meter AH(5> (fS'lO
Train B No. M17-B
Probe No. B Lenath: 10
Nozzle No. M17-*) Tio Dia. (")rl^
Pitot Tube No. B Cp 0.£
Stack Thermocouple No. 31 588
r—
Filter Holder No. -->
Filter Assembly No. r' '(?>
Impinqer Box No. B- /
Umbilical/lmpinqer Hookup UH- y2
Umbilical No. A/1^?- /
_ft
in
i4_
^~
Meter Box No. /V/7
DGM Correction (Yl / tf/tS
Orifice Meter AH(3> /jBtfa
page 1 of
1
Assumed Moisture
% Assumed %CO,
%O,
LA] LfiJ Lai LoJ LEJ
Traverse Point Layout
Compass Direction >• North
Nozzles are quartz-glass.
Time (24 Hr)
Pass or Fail
Train A Pitot Tube Pressure Measurement System Leak Checks
Initial
10%
Final
ltf/\
tofiA
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Train B Pitot Tube Pressure Measurement System Leak Checks
Initial
/tilUr
Final
{'2?Jt
rtn&
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Train A Sampling System Leak Checks
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial
l"fa
tf
.**>
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
M
1
.PCftf
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial
*#
1$
<6G\
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
(Vft
4
.a*
Initial
Final
Initial
Final
Initial
W. Wl
w,w
^"Hi3f)
Final
Initial
u,-w
io,itf
'itf,oi $
Final
Remarks and Notes: List any other equipment requiring calibration below.
TRAIN A
TRAIN B
M17DPG1.WPD Septembers, 1999
Meter Volume at Start of Run
Meter Volume at End of Run
Total Leak Check or Non-Sample Volume
Adjusted Final Volume
-------
Run No.
Date
-36
Sampling Location Unit 2A Baohouse Outlet Duct
Project No. 104703.1.002.05.01
Operator
page
of 2.
Sampling Data for Method 17 Train A No. M17-A
Traverse
Point
Sampling
Time,
min.
0
Clock
Time
(24-Hr)
Dry Gas Meter Reading
(VJ, ft3
Initial
Desired
Actual
Velocity
Head
(Ap),
in. H20
Orifice Pressure
Differential
(AH),
in. H^p
Desired
Actual
Stack
Temp.
(t.).
°F
Dry Gas Meter
Temperature
Inlet
Outlet
Pump
Vacuum
in. Hg
Silica Gel
Impinger
Outlet
Temp.,
°F
f/ffif
0-&8
/ro
nu
/MY
"toi, •%
0-6-i.
/$0
-7
I
a n
0,2.1
(\1*
r&_
"
fgv
&o_
2.
•z?
^2,
4=
Alb
^L
^S.
ittL
0-2*
&
71
ill-W
0,60
63-
£-<
&Ul$-
0-Ti-
0/?2-
TT
6,73
$k
63-
0.73
0,23
•7
"75
Sampling Data for Method 17 Train B No. M17-B
73L
u&-
JZ.
^L
o.-zn
/S'Z
lllcL
ifirfO
±Z-
?
0-36
&L.
5?
0.11-
0''L2
£L
-7
0-12-
*S7
f?
ftf-
^L
0MZ-
6-7
f,0
Mo
65
-7
70
&i
W&
"
o-W
i3o_
W-
(2J*
.£L
Remarks and Notes:
M17DPG2.WPD September 3, 1999
40
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
Run No.
Date
Project No. 104703.1.002.05.01
Sample Type (Multi-Point, Single-Point)
Flow Control Device (Valve, Critical Orifici
Method 5 Meter Box No.
MSB Pump Type diaohram
MSB Pump No.
Client/Source U.S. EPA / Cogentrix Unit 2A
Sampling Location Unit 2A Baahouse Outlet
Operator
Bag Type Tedlar
Method SB Train No.
MSB Flow Meter Type
MSB Flow Meter No.
Sample No.
NA _
NA
rotameter
Desired Sampling Rate
Leak Check Before Sampling.
Total Sampling Time "TO
cc/min
Flow Rate, cc/min: Average
Estimated Total Sample Volume
<^> After Sampling
min Average Flow Meter Reading
Highest
Lowest
liters
Time
(24-Hr)
Flow
Meter
Reading
Start
Purge
Start
Sampling
Stop
Sampling
Sampling
Remarks and Notes
Hot
//£/
HU-
{&_
v\o
ftw
n-w
M3BSAMP.WPD June 18, 1998
41
RCA#2 APPENDIX C
-------
s
to
n
40 CF/? 60, APPENDIX A, METHOD 3B, GAS ANALYSIS BY ORSAT
Run No.
Date
Project No. 104703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time .
NA
Sample Type (Bag, Grab)
Analyst
Baa
Orsat Leak Check Before Analysis:
Burrete xVp Change in 4 Minutes
Pipettes /yi> Change in 4 Minutes
Orsat Leak Check After Analysis:
Burrete /?£ Change in 4 Minutes
Pipettes /K? Change in 4 Minutes
Analysis
Gas
C02
02 (Net is actual reading
minus actual C02 reading)
1
Actual
Reading
1 ;*>.<)
2 J*J ^
3
1 />/.7
2 ;.?
2 J&9
3
1 /tf.7
2y/,7
3
Net
Value
/*>. 9
**
3
Actual
Reading
1 ;w
2 /y,?
3
2 ^,7
3
Net
Value
/y. ^
^/-
Average
Net
Value
(% v/v)
/V.J
*,*
Acceptance Criteria per Method 3B
C02
0.3% v/v
0.2% v/v
0,
0.2% v/v
0.3% v/v
Remarks and Notes:
M3BANALWPD September 3, 1999
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY TRAIN SET-UP DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
"9_ Impinger Box A No. rj~/
? Impinger Box B No. fi')
Run No. <3&> Sampling Train A No.
Sampling Train B No.
Set-up person(s): *J> •
Date:
Transfer to Sampler:
Relinquished By cl
Received By /?,
Date/Time /J/jS]/97
TRAIN COMPONENT
REAGENT
LOADING DATA
Sampling Nozzle (Quartz)*
Filter Assembly and Holder*
Filter Type: Whatman QM*A
Probe (31 6 SS) :
Sample Transfer/Vacuum Line :
Male 1st Impinger Inlet Blank-Off
Nozzle I.D. No.
Fitter Assembly No.
: : • •
Filter Holder No.
1st Impinger (Mod-GBS) 100-200 mLs ASTM Type I Water
U-Connector (A)
2nd Impinger (GBS) 100-200 mLs ASTM Type t Water
U-Connector (B)
3rd Impinger (Mod-GBS) Empty
U-Connector (C)
4th Impinger (Mod-GBS) "200 g indicating silica gel
U-Connector (D)
5th Impinger (Mod-GBS) "200 g indicating silica gel
Impinger Outlet Connector
TRAIN A
TRAIN B
~ 9
-5
Initial Weights (grams)
"73"Z?*'2.
Connector I.D. No. t>jj-31>
OH -3 A
Before and after sampling: Nozzle inlet opening and filter assembly holder outlet opening covered with Teflon® tape, and
entire filter assembly holder with filter assembly and nozzle wrapped in aluminum foil and placed in Ziploc® bag. 1 st impinger
inlet sealed with glass blank-off.
Comments:
M17DSUP WPO May 13, 1999 (rev. M17DSUP3.WPD November 10, 1999)
43
RCA#2 APPENDK C
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN {Ml 7)
FIELD LABORATORY SAMPLE RECOVERY DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Sampling Train A No. SWS1?-/?
Sampling Train B No. _
Transfer for Recovery:
Relinquished By P>
Received By \J.,
Impinger Box A No. rf'/
Impinger Box B No. &"/
Date/Time
Sample recovery person(s):
Weights below are in grams.
tj, S
Date: JtJj})*'.
BACK HALF RECOVERIES
TRAIN A
TRAIN B
1st
Impinger:
Final Wt.
Initial Wt.
Net Wt.
Total Condensate Collected:
Description and/or color:
2nd
3rd
4th & 5th
1 st 2nd 3rd 4th & 5th
•733£
4 &
%Blue
% Blue
FRONT HALF. RECOVERIES
TRAIN A
TRAIN B
FILTER ASSEMBLY:
Sample Number: i?£>102
PM Description/color: j?)ftJ*-
TRAIN RINSES:
Sample Number:
36, 104
103
Components Rinsed*: nozzle, filter holder front
* Acetone rinses with brushing 3 times or more until perceivably clean.
COMMENTS: Acetone rinses are transferred directly to tared Teflon® beaker liners for analysis.
M17DRCV.WPD May 13, 1999 Irev. M17DRCV3.WPD November 10. 19991
44
RCA#2 APPENDIX C
-------
FIELD SAMPLING DATA FOR METHOD 17 TRAINS
I
n
. 71
Date
Run No
Project No. 104703.1.002.05.01
Client U.S. EPA OAQPS EMAD EMC
Source Coaentrix Unit 2A _
Sampling Location Bauhouse Outlet
Operator /an'Tr*-' _
Record data every n-' V'~ ? minutes
Barometer No. Y-2021 _
Barometric Pressure "%?/• 2-J
Elevation to Meter Boxes
Meter Box Pba, 10,1-0
Elevation to Sampling Loc.
Sampling Location^P,
Static
in Hg
34 ft
in Hg
34 ft
- in Hg
. in H2O
Train A No. M17-A
Probe No. A Lenath: 10 ft
Nozzle No. M 17-f^ Tip Dia.rf.fft in
Pitot Tube No. A Cp 0.84
Stack Thermocouple No. 31 58A
Filter Holder No. "7
Filter Assembly No. f~ 1?
Impinaer Box No. A- 2^
Umbilical/lmpinaer Hookup UH- /
Umbilical No. /^^" "/
Meter Box No. /V /2-
DGM Correction (Y) O. fffr
Orifice Meter AH@ /,#/&
Train B No. M17-B
Probe No. B Lenath: 1 0 ft
Nozzle No. M1 7- /"f Tip Dia. ff, f1^^, in
Pitot Tube No. B Cp 0.84
Stack Thermocouole No. 3 1 58B
Filter Holder No. %
Filter Assembly No. r Iff
Impinaer Box No. B- 2—-
Umbilical/lmpinqer Hookup UH- 2^-
Umbilical No. A^So-^/
Meter Box No. /V//
DGM Correction (Y) / - North
Nozzles are quartz-glass.
Time (24 Hr)
Pass or Fail
Train A Pitot Tube Pressure Measurement System Leak Checks
Initial
l
\t>
ton
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
QC#h
6
tort
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Remarks and Notes: List any other equipment requiring calibration below.
TRAIN A
;i
M17DPG1 WPD September 3, 1999
Meter Volume at Start of Run
Meter Volume at End of Run
Total Leak Check or Non-Sample Volume
Adjusted Final Volume
-------
Run No.
Date __
•U/ >
Sampling Location . Unit 2A Baohouse Outlet Duct
Project No. 104703.1.002.05.01
Operator.
page.
of
A4
Sampling Data for Method 17 Train A No. M17-A
Traverse
Point
Sampling
Time,
min.
a
Clock
Time
(24-Hr)
Dry Gas Meter Reading
(VJ, ft3
Initial
Desired
Actual
Velocity
Head
(Ap),
in. H20
Orifice Pressure
Differential
(AH),
in. H20
Desired Actual
Stack
Temp.
(ts),
°F
Dry Gas Meter
Temperature
Inlet
Outlet
Pump
Vacuum,
in. Hg
Silica Gel
Impinger
Outlet
Temp.,
°F
¥7
Z-
37
V
- r
ffi
a,
5~
y
•z.1
aac^g
/77
'¥9
5-
7S
1.1
An
5"
75
0,"2-
IX GO
A3
Iff
/77
52?
5-
f?
•35
II
122-
f/
35
92-
57
0,08
*/•
75
35.
tf
S7&
6
72.
ye
0,12,
V
Sampling Data for Method 17 Train B No. M17-B
^^
10
•79-11
&-?#
01,10
•LJL.
Q-Fn
o.-z?
20
•r
0.1 i
6"
Y?
0,80
2,5"
0-2.7
5"
55
OrCf'l
0-Z.t
/&&
V?
-fT
0.F7
6.2-7
&-2-1
3-7
OS12-
5"
37
O-CeC
57
5-
32.
Remarks and Notes:
M17DP62.WPD September 3. 1999
46
RCA#2 APPENDIX C
-------
37 Date
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
to'It
Run No.
Project No. 104703.1.002.05.01
Sample Type (Multi-Point, Single-Point)
Flow Control Device (Valve, Critical Orifice)
Method 5 Meter Box No.
MSB Pump Type diaphram
MSB Pump No
Client/Source U.S. EPA / Cogentrix Unit 2A
Sampling Location Unit 2A Baghouse Outlet
Operator _
Bag Type Tedlar
Method SB Train No._
MSB Flow Meter Type.
MSB Flow Meter No.
Sample No.
NA
NA
rotameter
Desired Sampling Rate .
Leak Check Before Sampling
Total Sampling Time
cc/min
Flow Rate, cc/min: Average _
Estimated Total Sample Volume
I After Sampling
min Average Flow Meter Reading
Highest
Lowest
liters
Time
(24-Hr)
Flow
Meter
Reading
Start
Purge
Start
Sampling
Stop
Sampling
Sampling
Remarks and Notes
5.0
1.0
uc • |
0
GO/
ki-.-.—
M3BSAMPWPD June 18, 1998
47
RCA#2 APPENDIX C
-------
CO
o
40 CFR 60, APPENDIX A, METHOD 3B, GAS ANALYSIS BY ORSAT
Run No.
Date
Project No. 104703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time
NA
Sample Type (Bag, Grab)
Analyst J, •
Baa
Orsat Leak Check Before Analysis:
Burrete A*e> Change in 4 Minutes
Pipettes jVo Change in 4 Minutes
Orsat Leak Check After Analysis:
Burrete Ag Change in 4 Minutes
Pipettes A/P Change in 4 Minutes
Analysis
Gas
C02
O2 (Net is actual reading
minus actual CO2 reading)
1
Actual
Reading
1 S3,*r
2 s^.^
3
1 J9,6>
2 ;9.6>
3
Net
Value
SS'S
&,/
1
Actual
Reading
1 y>5.j>~
2 >;£j>~
3
1 /£^
2 ;9.&
3
Net
Value
S3ji£~
6'J
3
Actual
Reading
1 t3.f
2 ;-jsS~
3
1 Sf-Cr
2 J9.6
3
Net
Value
S3.5~
6.J
Average
Net
Value
(% v/v)
/J?A5~
6J
Acceptance Criteria per Method 3B
C02 >4% 0.3% v/v 02 .£.15% 0.2% v/v
j<4% 0.2% v/v <15% 0.3% v/v
Remarks and Notes:
l/io/11
M3BANAL WPD September 3, 1999
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY TRAIN SET-UP DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Set-up person(s): v>L
Transfer to Sampler:
Relinquished By J- St
Sampling Train A No.
Sampling Train B No.
Impinger Box A No.
Impinger Box B No..
Date:
Received By 47,
Date/Time
TRAIN COMPONENT
REAGENT
LOADING DATA
TRAIN A
TRAIN B
Sampling Nozzle (Quartz)*
Filter Assembly and Holder*
Filter Type: Whatman QM-A
Probe (316 SS)
Sample Transfer/Vacuum Line
Male 1st Impinger Inlet Blank-Off
Nozzle I.D. No.
Fitter Assembly No.
Filter Holder No.
1st Impinger (Mod-GBS) 100-200 mLs ASTM Type I Water
U-Connector (A) ::v
2nd Impinger (GBS) 100-200 mLs ASTM Type I Water
U-Connector (B)
3rd Impinger (Mod-GBS) Empty
U-Connector (C)
4th Impinger (Mod-GBS) "200 g indicating silica gel
U-Connector (D)
5th Impinger (Mod-GBS) "200 g indicating silica gel
Impinger Outlet Connector
Connector I.D. No.
Initial Weights (grams)
* Before and after sampling: Nozzle inlet opening and filter assembly holder outlet opening covered with Teflon® tape, and
entire filter assembly holder with filter assembly and nozzle wrapped in aluminum foil and placed in Ziploc® bag. 1 st impinger
inlet sealed with glass blank-off.
Comments:
M17DSUP.WPD May 13. 1999 Irev M17DSUP3.WPD November 10. 19991
49
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY SAMPLE RECOVERY DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Sampling Train A No.
Sampling Train B No.
Transfer for Recovery:
Relinquished By # j
Received By cJ. £
Impinger Box A No.
Impinger Box B No..
Date/Time
Sample recovery person(s):
Weights below are in grams.
Date:
BACK HALF RECOVERIES
TRAIN A
TRAIN B
1st
Impinger:
Final Wt.
Initial Wt.
NetWt.
Total Condensate Collected:
Description and/or color:
2nd
3rd
4th & 5th
1st
2nd
3rd
4th & 5th
7.J
. J
Blue :
FRONT HALF RECOVERIES
% Blue
TRAIN A
TRAIN B
FILTER ASSEMBLY:
Sample Number: .57102
PM Description/color:
TRAIN RINSES:
Sample Number:
CJ7104
.103
Components Rinsed*: nozzle, filter holder front
* Acetone rinses with brushing 3 times or more until perceivably clean.
COMMENTS: Acetone rinses are transferred directly to tared Teflon® beaker liners for analysis.
M17DRCV.WPD May 13. 1999 (rev. M17DRCV3.WPD November 10. 19991
50
RCA#2 APPENDIX C
-------
FIELD SAMPLING DATA FOR METHOD 17 TRAINS
§
to
fc
o
Run No.
Date
Project No. 104703.1.002.05.01
Client U.S. EPA OAQPS EMAD EMC
Source Coaentrix Unit 2A _
Sampling Location Baahouse Outlet
Operator &r\ flr*^ _
minutes
Record data every *» ~~ 9 P ''
Barometer No. Y-2021
Barometric Pressure ^yff
Elevation to Meter Boxes
Meter Box Pbaf ^/
in Hg
34 ft
Elevation to Sampling Loc.
Sampling Location Pba
jy
Static Pressure
in Hg
34 ft
in Hg
Train A No. M17-A
Probe No. A Lenath: 1 0 ft
Nozzle No. M17-//0 Tip Dia. ( ,SlO
Train B No. M17-B
Probe No. B Lenath: 10
Nozzle No. M17-? Tio Dia. ^M>
Pitot Tube No. B Cp 0.8-:
Stack Thermocouple No. 31 58B
Filter Holder No.
Filter Assembly No. f~l^
Impinqer Box No. B- /
Umbilical/lmpinqer Hookup U|H- 32-
Umbilical No. /)/ & " !
_ft
in
L_
Meter Box No. A'//
DGM Correction (Y) /,OIO
Orifice Meter AH@ (- 3 '}£
page
1 of 2—
1
Assumed Moisture
% Assumed %CO2 C) %O2 £-
lAj LBJ UlJ UlOEj
Traverse Point Layout
Compass Direction >• North
Nozzles are quartz-glass.
<
Time (24 Hr) l
Pass or Fail
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Train A Pitot Tube Pressure Measurement System Leak Checks
^Initial
ffr
(2ll5
Final
^f
nl^b
\
Initiafjli)
jftfT&lll
P
iQQ3?
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Initial
Final
Final
03£\
•-7
Initial
Final
Initial
Initial
Trair
Final
i A Sam
Final
Initial
pling £
Final
ystem
Initial
Train B Pitot Tube
Initial
<f
Leak C
Final
Oj(£>
f^rz^
hecks
Final
Initial
Pressure Measurement System Leak Checks
Final
Initial
Initial
Final
Initial
Final
Initial Final
Final
Initial
Final
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial^
jp&Cdfl
6
t®n~
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
0%
(f
tfffls
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Remarks and Notes: List any other equipment requiring calibration below.
TRAIN A
M17DPG1 WPD September 3, 1999
Meter Volume at Start of Run
Meter Volume at End of Run
Total Leak Check or Non-Sample Volume
Adjusted Final Volume
-------
Run No.
Date
Sampling Location Unit 2A Baohouse Outlet Duct
Project No. 104703.1.002.05.01
page.
of.
Operator.
Sampling Data for Method 17 Train A No. M17-A
Traverse
Point
Sampling
Time,
min.
a
Clock
Time
(24-Hr)
Dry Gas Meter Reading
-------
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
Run No.
Date
Project No. 104703.1.002.05.01
Sample Type (Multi-Point, Single-Point)
Flow Control Device (Valve, Critical Orifi&e)
Method 5 Meter Box No..
MSB Pump Type diaphram
MSB Pump No. A//2-
Desired Sampling Rate _
Leak Check Before Sampling.
Total Sampling Time ~7d>
Client/Source U.S. EPA / Coaentrix Unit 2A
Sampling Location Unit 2A Baahouse Outlet
Operator.
Bag Type Tedlar
Method SB Train No._
MSB Flow Meter Type.
MSB Flow Meter No.
Sample No.
NA
NA
rotameter
cc/min
Flow Rate, cc/min: Average _
Estimated Total Sample Volume
£> After Sampling
min Average Flow Meter Reading
Highest __2j!£L__
Lowest
liters
Time
(24-Hr)
Flow
Meter
Reading
Start
Purge
Start
Sampling
Stop
Sampling
Sampling
Remarks and Notes
3*
'*•*
M3BSAMP.WPD June 18. 1998
53
RCA#2 APPENDIX C
-------
en
I
K)
o
40 C/7? 60, APPENDIX A, METHOD 3B, GAS ANALYSIS BY ORSAT
Run No.
Date
Project No. 104703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time 03J&
NA
Sample Type (Bag, Grab)
Analyst
Baa
Orsat Leak Check Before Analysis:
Burrete ___^£___ Change in 4 Minutes
Pipettes Srt> Change in 4 Minutes
Orsat Leak Check After Analysis:
Burrete />£•> Change in 4 Minutes
Pipettes /^t> Change in 4 Minutes
Analysis
Gas
CO2
O2 (Net is actual reading
minus actual C02 reading)
1
Actual
Reading
1 SJ.6
2 /#>&
3
1 /^7
2 /^7
3
Net
Value
XX «?
c^T/7
2
Actual
Reading
1 S3>0
2 S3,c
3
1 /£7
2 /^/7
3
Net
Value
J3.2
^"7
3
Actual
Reading
1 /3>o
2 /^T/C>
3
1 7/-7
2 xJ/^7
3
Net
Value
J3-0
^?''7
Average
Net
Value
(% v/v)
Jj.ti
&-7
Acceptance Criteria per Method 3B
C02 >4% 0.3% v/v 02 >.15% 0.2% v/v
.<4% 0.2% v/v < 15% 0.3% v/v
Remarks and Notes:
M3BAHALWPD September 3, 1999
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY TRAIN SET-UP DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Set-up person(s): J.
Transfer to Sampler:
Relinquished By
Sampling Train A No.
Sampling Train B No.
Impinger Box A No. r7~/
Impinger Box B No. l?'s
Date:
Received By Q,
Date/Time
TRAIN COMPONENT
REAGENT
LOADING DATA
TRAIN A
TRAIN B
Sampling Nozzle (Quartz)*
Filter Assembly and Holder*
Filter Type: Whatman QM-A
Probe (316 SS)
Sample Transfer/Vacuum Line
Male 1st Impinger Inlet Blank-Off
Nozzle I.D. No.
Filter Assembly No.
Filter Holder No,
1st Impinger (Mod-GBS) 100-200 mLs ASTM Type I Water
U-Connector (A) ;
2nd Impinger (GBS) 100-200 mLs ASTM Type I Water
U-Connector (B)
3rd Impinger (Mod-GBS) Empty
U-Connector (C)
4th Impinger (Mod-GBS) "200 g indicating silica gel
U-Connector (D)
5th Impinger (Mod-GBS) "200 g indicating silica gel
Impinger Outlet Connector
Connector I.D. No.
Initial Weights (grams)
Before and after sampling: Nozzle inlet opening and filter assembly holder outlet opening covered with Teflon® tape, and
entire filter assembly holder with filter assembly and nozzle wrapped in aluminum foil and placed in Ziploc® bag. 1st impinger
inlet sealed with glass blank-off.
Comments:
M17DSUP WPD May 13, 1399 (rev. M17DSUP3.WPD November 10, 1999)
55
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY SAMPLE RECOVERY DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Impinger Box A No. <#•/
Impinger Box B No. &'/
Run No. t-ZS" Sampling Train A No.
Sampling Train B No..
Transfer for Recovery:
Relinquished By iP, Gnri-rfcn Received By «/
Sample recovery person(s): J. >
Weights below are in grams.
Date/Time
6330
Date:
BACK HALF RECOVERIES
TRAIN A
TRAIN B
1st
Impinger:
Final Wt.
Initial Wt.
Net Wt.
Total Condensate Collected:
Description and/or color:
2nd
3rd
4th & 5th
1st
2nd
LS&3
3rd
4th & 5th
, 7
647.3
/7,3
% Blue
% Blue
FRONT HALF 'RECOVERIES
TRAIN A
TRAIN B
FILTER ASSEMBLY:
Sample Number: ^,fl02
PM Description/color:
TRAIN RINSES:
Sample Number:
oy-104
Components Rinsed*: nozzle, filter holder front
* Acetone rinses with brushing 3 times or more until perceivably clean.
COMMENTS: Acetone rinses are transferred directly to tared Teflon® beaker liners for analysis.
M17DRCV.WPD May 13, 1999 (rev. M17DHCV3.WPD November 10. 1999)
56
RCA#2 APPENDIX C
-------
FIELD SAMPLING DATA FOR METHOD 17 TRAINS
o
en
—J
Run No.
Date
Project No. 104703.1.002.05.01
Client U.S. EPA OAQPS EMAD EMC
Source Cogentrix Unit 2A
Sampling Location Baghouse Outlet
Operator
Record data every f^^i
Barometer No. Y-2021
minutes
Barometric Pressure JC'-
Elevation to Meter Boxes
Meter Box Pbar 3 61
Elevation to Sampling Loc.
Sampling Location Pbar
Static Pressure '~(k
in Hg
34 ft
in Hg
34 ft
_ in Hg
. in H2O
Train A No. M17-A
Probe No. A Lenath: 1 0 ft
Nozzle No. M1 7-/Y Tio Dia. ^'I'ilf in
Pitot Tube No. A C_ 0.84
Stack Thermocouple No. 3158A
Filter Holder No. 1
Filter Assembly No. r~M
Imoinqer Box No. A- '2-
Umbilical/lmpinaer Hookup UH- /
Umbilical No. /\} /^;
Orifice Meter AH /, S^tf
page 1 of.
v
1
Assumed Moisture
% Assumed %CO2
TAJ LaJ LoJ LoJ l£j
Traverse Point Layout
Compass Direction >• North
Nozzles are quartz-glass.
Time (24 Hr) '
Pass or Fail
Train A Pitot Tube Pressure Measurement System Leak Checks
Initial
»/. .•
W*
Ifal
Final
tfcn
•rt&>
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Train B Pitot Tube Pressure Measurement System Leak Checks
Initial
m
&*>-&
1 Final
c?5/!
A)^Xi
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Train A Sampling System Leak CHecks
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial^.
^ifytf d3^
' &
.Off
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Y
1 Final
CKy?*1)
ft
. o
-------
Run No.
Date
Sampling Location Unit 2A Baohouse Outlet Duct
Project No. 104703.1.002.05.01
Operator.
page
of
Sampling Data for Method 17 Train A No. M17-A
>/**
Traverse
Point
Sampling
Time,
min.
Clock
Time
(24-Hr)
Dry Gas Meter Reading
(VJ, ft3
Initial
Desired Actual
Velocity
Head
(Ap),
in. H20
Orifice Pressure
Differential
(AH),
in. H20
Desired Actual
Stack
Temp.
(ts),
°F
Dry Gas Meter
Temperature
Inlet
Outlet
Pump
Vacuum,
in. Hg
Silica Gel
Impmger
Outlet
Temp.,
°F
t
2
777
7*7
777
•5-7
0,20
*1
l£-
u^.
777
5"
Z22_
jfzL
&,
777
A-
5"?
tZL
ZL
772-
57
7*
77^
777
2,
'3TQI
-o
/27_
0
Sampling Data for Method 17 Train B No. M17-B
j£L
25^.
(2.5-
3?
-S
&.2J3
<^T
0.2$
/&>
5"
V'/
^2L
o.JI
-"57
£22.
C?.Zj?
'57
f 31.70
fT?
^'^
/
779
6-3%
fifo
Z^L
-
Remarks and Notes:
>- _ * * ,o
- '" tpf
•
58
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
Run No.
Date
Project No. 104703.1.002.05.01
Sample Type (Multi-Point, Single-Point)
Flow Control Device (Valve, Critical Orifice)
Method 5 Meter Box No.
MSB Pump Type diaphram
MSB Pump No. A//2-
Client/Source U.S. EPA / Coaentrix Unit 2A
Sampling Location Unit 2A Baghouse Outlet
Operator
Bag Type Tedlar
Method SB Train No. _
MSB Flow Meter Type.
MSB Flow Meter No. _
Sample No.
NA
NA
rotameter
Desired Sampling Rate
Leak Check Before Sampling.
Total Sampling Time *7O
cc/min
Flow Rate, cc/min: Average
Estimated Total Sample Volume
After Sampling
min Average Flow Meter Reading
Highest
Lowest ^**&
7!
liters
Time
(24-Hr)
Flow
Meter
Reading
Start
Purge
Start
Sampling
Stop
Sampling
Sampling
Remarks and Notes
3,0
dfol-
$.0
anon
ofot
10
M3BSAMPWPD June 18, 1998
59
RCA#2 APPENDIX C
-------
1
o
40 C/7? 60, APPENDIX A, METHOD 3B, GAS ANALYSIS BY ORSAT
Run No.
Date
Project No. 104703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time
NA
Sample Type (Bag, Grab)
Analyst j
^T^>
3
Actual
Reading
1 S33
2 J-3,3
3
1 W.t,
2 ;$-,&•
3
Net
Value
J33
&,?
Average
Net
Value
(% v/v)
;33
2
Acceptance Criteria per Method 3B
CO,
0.3% v/v
0.2% v/v
0,
0.2% v/v
0.3% v/v
Remarks and Notes:
M3BANAL.WPD September 3. 1999
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY TRAIN SET-UP DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No. &s Sampling Train A No. /$?SJ?-/9 Impinger Box A No.
Sampling Train B No. ^V 7 & Impinger Box B No.
_
Set-up person(s): J • $usy?r3s~r _ Date:
Transfer to Sampler:
Relinquished By J- Stjx^^^^-ry Received By &. &^-jf^~J r? Date/Time _/J//9/9<3'
^
TRAIN COMPONENT __ REAGENT __ LOADING DATA
TRAIN A TRAIN B
Sampling Nozzle (Quartz)* . Nozzle I. D. No. /"J&-
Filter Assembly and Holder* ... Fitter Assembly No. _ /_2
Filter Type: Whatman QM-A '."'-'
Probe (31 6 SS) Filter Holder No, <3 _ ^
Sample Transfer/Vacuum Line . .
Male 1st Impinger Inlet Blank-Off . .:
Initial Weights (grams)
1st Impinger (Mod-GBS) 100-200 mLs ASTM Type I Water
U-Connector (A)
2nd Impinger (GBS) 100-200 mLs ASTM Type I Water
U-Connector (B)
3rd Impinger (Mod-GBS) Empty
U-Connector (C)
4th Impinger (Mod-GBS) "200 g indicating silica gel
U-Connector (D)
5th Impinger (Mod-GBS) "200 g indicating silica gel
Impinger Outlet Connector Connector I.D. No. UH -)
Before and after sampling: Nozzle inlet opening and filter assembly holder outlet opening covered with Teflon® tape, and
entire filter assembly holder with filter assembly and nozzle wrapped in aluminum foil and placed in Ziploc® bag. 1 st impinger
inlet sealed with glass blank-off.
Comments:
M17DSUP WPD May 13, 1999 {rev M17DSUP3 WPD November 10. 1999)
61
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY SAMPLE RECOVERY DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Impinger Box A No. /#'**
Impinger Box B No. &'&•
Run No. 39 Sampling Train A No.
Sampling Train B No.
Transfer for Recovery:
Relinquished By 47 fenfJ-Jn Received By J, £usjtr>'2s-> Date/Time
Sample recovery person(s): d, Sujfj?? &.si
Weights below are in grams.
BACK HALF RECOVERIES
TRAIN A
Impinger: 1st
Final Wt.
Initial Wt.
Net Wt.
Total Condensate Collected:
Description and/or color:
2nd
1*9*3
3rd
4th & 5th
1st
L^.L
% Blue
TRAIN B
2nd
723 sj
3rd
0
4th & 5th
% Blue
FRONT 'HALF RECOVERIES
TRAIN A
TRAIN B
FILTER ASSEMBLY:
Sample Number: >59 102
PM Description/color:
TRAIN RINSES:
Sample Number:
Components Rinsed*: nozzle, filter holder front
^5104
103
* Acetone rinses with brushing 3 times or more until perceivably clean.
COMMENTS: Acetone rinses are transferred directly to tared Teflon® beaker liners for analysis.
M17DRCV.WPD May 13, 1999 (rev. M17DRCV3.WPD November 10. 19991
62
RCA#2 APPENDIX C
-------
FIELD SAMPLING DATA FOR METHOD 17 TRAINS
Run No. 'TO Date Ij'^'^l
Project No. 104703.1.002.05.01
Client U.S. EPA OAQPS EMAD EMC
Source Cogentrix Unit 2A
Sampling Location Baahouse Outlet
Operator ^u^-~~~
Record data every A'? \>- s minutes
Barometer No. Y-2021
Barometric Pressure t
Elevation to Meter Boxes
Meter Box Pbar /:
in Hg
34 ft
Elevation to Sampling Loc.
Sampling Location P
Static Pressure
in Hg
34 ft
. in Hg
Train A No. M17-A
Probe No. A Length: 10 ft
Nozzle No. M17-? Tio Dia. O-M \n
Pilot Tube No. A C 0.84
Stack Thermocouple No. 3158A
Filter Holder No. ?
Filter Assembly No. /"2-f
Impinger Box No. A- f
Umbilical/lmpinqer Hookup UH- ")°
Umbilical No. N^O-i
Meter Box No. /V i V-
DGM Correction (Yi ffr6^^
Orifice Meter AH<5> {'8l&
TrainB No. M17-B
Probe No. B Length: 10
ft
Nozzle No. M 17- /OTip Dia.£>"' $ in
Pilot Tube No. B C, 0.84
Stack Thermocouple No. 31 58B
Filter Holder No. £>•
Filter Assemblv No. f^H^
Impinqer Box No. B- /
Umbilical/lmpinger Hookup UH- ~3~l —
Umbilical No. A/ ^O - /
Meter Box No. A/ ll
DGM Correction M (rOl&
Orifice Meter AH@ /.%°)%
page 1 of
•
>
•
• • • •
f
1 • • • •
Assumed Moisture
Assumed %CO2.
%02
Laf uu LnJ L£J
Traverse Point Layout
Compass Direction > North
Nozzles are quartz-glass.
Time (24 Hr)
Pass or Fail
Train A Pitot Tube Pressure Measurement System Leak Checks
Initial
QffH
Final
(Ol'l'
U&&P
\
Initial
Final
Initial
Final
Initial
Train
Final
Initial
Final
A Sampling System
Train B Pitot Tube Pressure Measurement System Leak Checks
Initial
C/frf3
Leak C
Final
/tiff'
too^
iecks
Initial
Final
Initial
Final
Initial
Final
Initial
Final
a
o
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial
o?,Hl
1^
,0IV
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
(GVl
(f
/'Of
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial
(W
-------
Run No.
Date
Sampling Location Unit 2A Baohouse Outlet Duct
Project No. 104703.1.002.05.01
Operator.
page
of
Sampling Data for Method 17 Train A No. M17-A
Sampling
Time,
Traverse
Point
min.
0
Clock
Time
(24-Hr)
Dry Gas Meter Reading
(Vm), ft3
Initial
Desired
Actual
Velocity
Head
(Ap),
in. H20
Orifice Pressure
Differential
(AH),
in. H20
Desired Actual
Stack
Temp.
It.).
°F
Dry Gas Meter
Temperature
Inlet Outlet
Pump
Vacuum,
in. Hg
Silica Gel
Impinger
Outlet
Temp.,
°F
0-53
tffoi
&ZL
3£L
6&-
ffrT),
'-4-
&&.
-V
a •
-*-
4^
#
S&L.
U:-
6,1-1
(
IY
0.72-
O.'Z-'T-
7^
Iff 0(1
0-2-5
JK
V-7
SOlO
-
A -7"!
2$"
h -
3b
-------
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
Run No.
Date
Project No. 104703.1.002.05.01
Sample Type (Multi-Point, Single-Point)
Flow Control Device (Valve, Critical Orifice)
Method 5 Meter Box No.
MSB Pump Type diaphram
MSB Pump No. /Vf2-
Client/Source U.S. EPA / Coaentrix Unit 2A
Sampling Location Unit 2A Baahouse Outlet
Operator.
Bag Type Tedlar
Method SB Train No._
MSB Flow Meter Type.
MSB Flow Meter No.
Sample No.
NA
NA
rotameter
Desired Sampling Rate
Leak Check Before Sampling.
Total Sampling Time
cc/min
Flow Rate, cc/min: Average
Estimated Total Sample Volume
• (? After Sampling
min Average Flow Meter Reading
Highest _
Lowest
liters
Time
(24-Hr)
Flow
Meter
Reading
Start
Purge
Start
Sampling
Stop
Sampling
Sampling
Remarks and Notes
09 if
erftf
oft.
v
1*0
•to
M3BSAMP WPD June 18, 1998
65
RCA#2 APPENDIX C
-------
I
KJ
m
o
40 CFR 60, APPENDIX A. METHOD 3B, GAS ANALYSIS BY ORSAT
Run No.
Date
Project No. 104703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time .
NA
Sample Type (Bag, Grab)
Analyst J.
Baa
Orsat Leak Check Before Analysis:
Burrete A^ Change in 4 Minutes
Pipettes Ab Change in 4 Minutes
Orsat Leak Check After Analysis:
Burrete /Vp Change in 4 Minutes
Pipettes M> Change in 4 Minutes
Analysis
Gas
CO2
O2 (Net is actual reading
minus actual C02 reading)
1
Actual
Reading
1 S&.&"
2 /£££"
3
1 ;&?
2 Jfr JP*
3
Net
Value
^,
;&.&
&.3
2
Actual
Reading
1 sao-
2 S&sT'
3
1/tk fa*
/\J tO
2 jJr fr
3
Net
Value
;#.£>
6.3
3
Actual
Reading
1 ^2£-
2 jX.g'
3
1 s*.r
2 jJ^ P*
3
Net
Value
/^7-cS-
£,.3
Average
Net
Value
(% v/v)
S&'V
4, ,3
Acceptance Criteria per Method 3B
C02
0.3% v/v
0.2% v/v
02
<15%
0.2% v/v
0.3% v/v
Remarks and Notes:
M3BANAL.WPD September 3, 1999
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY TRAIN SET-UP DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No. #0 Sampling Train A No.
Sampling Train B No.
Set-up person(s): J,
Impinger Box A No.
Impinger Box B No..
/7~/
Date:
Transfer to Sampler:
Relinquished By
Received By O>£SJT>> *
Date/Time
TRAIN COMPONENT
REAGENT
LOADING DATA
TRAIN A
TRAIN B
Sampling Nozzle (Quartz)*
Filter Assembly and Holder*
Filter Type: Whatman QM-A,
Probe (316 SS)
Sample Transfer/Vacuum Line
Male 1st Impinger Inlet Blank-Off
j Nozzle I.D. No.
I'.. Filter Assembly No.
; Filter Holder No-
Initial Weights (grams)
1st Impinger (Mod-GBS) 100-200 mLs ASTM Type I Water
U-Connector (A) ; .
2nd Impinger (GBS) 100-200 mLs ASTM Type I Water
U-Connector (B)
3rd Impinger (Mod-GBS) Empty
U-Connector (C)
4th Impinger (Mod-GBS) "200 g indicating silica gel
U-Connector (D)
5th Impinger (Mod-GBS) "200 g indicating silica gel
. -3
Impinger Outlet Connector
Connector I.D. No.
* Before and after sampling: Nozzle inlet opening and filter assembly holder outlet opening covered with Teflon® tape, and
entire filter assembly holder with filter assembly and nozzle wrapped in aluminum foil and placed in Ziploc® bag. 1 st impinger
inlet sealed with glass blank-off.
Comments:
M17DSUP WPD May 13. 1999 (rev. M17DSUP3 WPD November 10, 19991
67
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (Ml7)
FIELD LABORATORY SAMPLE RECOVERY DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Sampling Train A No.
Sampling Train B No.
Impinger Box A No.
Impinger Box B No..
&'}
Transfer for Recovery:
Relinquished By D> &*•;•£+'n Received By
Sample recovery person(s): J.
Weights below are in grams.
Date/Time
Date-
BACK HALF RECOVERIES
TRAIN A
TRAIN B
Impinger: 1st
Final Wt. (#^£$
Initial Wt. -£~96.t>
Net Wt.
2nd
3rd
4th & 5th
*?£>?, 1+7t>K~}
1st
2nd
3rd
4th & 5th
. -7
y.9
Total Condensate Collected:
Description and/or color:
% Blue
FRONT HALF RECOVERIES
% Blue
TRAIN A
TRAIN B
FILTER ASSEMBLY:
Sample Number: ^#102
PM Description/color:
TRAIN RINSES:
Sample Number:
Components Rinsed*: nozzle, filter holder front
* Acetone rinses with brushing 3 times or more until perceivably clean.
COMMENTS: Acetone rinses are transferred directly to tared Teflon® beaker liners for analysis.
M17DRCV.WPD May 13. 1999 (rev M17DRCV3.WPD November 10, 19991
68
RCA#2 APPENDIX C
-------
FIELD SAMPLING DATA FOR METHOD 17 TRAINS
Run No.
Date
Project No. 104703.1.002.05.01
Client U.S. EPA OAQPS EMAD EMC
Source Cogenlrix Unil 2A
Sampling Localion Baohouse Outlet
Qperalor
Record dala every A'*?
Barometer No. Y-2021
minutes
Baromelric Pressure Qu
Elevalion lo Meier Boxes
Meier Box Pbar ^O'C^
_ in Hg
34 ft
in Hg
34 fl
Elevalion lo Sampling Loc.
Sampling Localion Pbar "¥)' Ol in Hg
Static PressureM"ZffJ~ •')«••' in H2O Assumed Moisture
Train A No. M17-A
Probe No. A Length: 1 0 ft
Nozzle No. Miy-te Tin Dia. (W/b in
Pilot Tube No. A Cp 0.84
Stack Thermocouple No. 31 58A
Filler Holder No. "7
Filler Assembly No. r^b
Impinqer Box No. A- £-
Umbilical/lmpinger Hookup UH- ^
Umbilical No. (0 ty'^
Meier Box No. & /2-
DGM Correclion (Y) & 'Fffi
Orifice Meier AH@ ('#{0
Train B No. M17-B
Probe No. B f Lenalh: 10 fl
Nozzle No. M1 7-'^.J:ip Dia. ^V^ in
r-1
Pilol Tube No. B C 0.84
Stack Thermocouple No. 3158B
Filler Holder No. %F
Filler Assemblv No. f*2jtf
Impinqer Box No. B-^£-
Umbilical/lmpinqer Hookup UH- ^*'"~
Umbilical No. p^"!
Meter Box No. /V / 1
DGM Correction (Y) S'O(&
Orifice Meter AH@ //• &?&'
page 1 of.
• 5 •
Y
• 1
% Assumed %CO2 (<7 %O2
TAJ LBJ LcJ LnJ L£J
Traverse Point Layout
Compass Direction > North
Nozzles are quartz-glass.
Time (24 Hr)
Pass or Fail
Train A Pilot Tube Pressure Measurement System Leak Checks
Initial
tttff
Final
llM
wnA
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Train B Pilot Tube Pressure Measurement System Leak Checks
Initial
(tfft
Final
frW
OC
Final Meier Volume
Initial Meier Volume
Leak Check Volume
ti
Final
W\o
7
b
-------
Run No.
Date
Sampling Location Unit 2A Baahouse Outlet Duct
Project No. 104703.1.002.05.01
Operator
page,
of
Sampling Data for Method 17 Train A No. M17-A
.//•IT
Traverse
Point
Sampling
Time,
min.
Clock
Time
(24-Hr)
Dry Gas Meter Reading
(VJ, ft3
Initial
Desired Actual
Velocity
Head
(Ap),
in. H20
Orifice Pressure
Differential
(AH),
in. H;0
Desired Actual
Stack
Temp.
Dry Gas Meter
Temperature
(tj,
°F
Inlet
Outlet
Pump
Vacuum,
in. Hg
tt-
£3-
&L
JL
-t
xV
/&/
Sf&
-77
2Z_
, 7!
ffe-
XSL
9*
77
C,
-77
ZZfL
3-5"
^J
&%-
yz.
!?*>
7*5
z.
725.26
0-17
•77
\L\le
a.&r
•5*3
7
ZT
/22_
Sampling Data for Method 17 Train B No. M17-B
10
^_
25
Affe
JSL
35
^^:
:S.
Wl&
33-
(ICZ.
/ftf'F0
ft
55"
ZiC
fUi-
^^^
s~
£^_
Zfg,
a^/7
^-
J7_
Remarks and Notes:
"(3 ^/^
M17DPQ2.WPD September 3. 1999
70
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
Run No.
T/
Date
Project No. 104703.1.002.05.01
Sample Type (Multi-Point, Single-Point)
Flow Control Device (Valve, Critical Orific
Method 5 Meter Box No..
MSB Pump Type diaphram
MSB Pump No.
Client/Source U.S. EPA / Coaentrix Unit 2A
Sampling Location Unit 2A Baahouse Outlet
Operator
Bag Type Tedlar
Method 3B Train No. _
MSB Flow Meter Type
MSB Flow Meter No. _
Sample No.
NA _
NA
rotameter
Desired Sampling Rate _
Leak Check Before Sampling.
Total Sampling Time ^2?
cc/min
Flow Rate, cc/min: Average
Estimated Total Sample Volume
\ After Sampling
min Average Flow Meter Reading
Highest _
Lowest
liters
Time
(24-Hr)
Flow
Meter
Reading
Start
Purge
Start
Sampling
Stop
Sampling
Sampling
Remarks and Notes
10
mi
*>.
-------
s
n
40 C/7? 60, APPENDIX A, METHOD 3B. GAS ANALYSIS BY ORSAT
Run No.
Date
Project No. 104703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time
NA
Sample Type (Bag, Grab)
Analyst J.
Bag
Orsat Leak Check Before Analysis:
Burrete Ai> Change in 4 Minutes
Pipettes /fo Change in 4 Minutes
Orsat Leak Check After Analysis:
Burrete //£> Change in 4 Minutes
Pipettes A^D Change in 4 Minutes
Analysis
Gas
C02
O2 (Net is actual reading
minus actual CO2 reading)
1
Actual
Reading
1 /2-£
2 J3.Z
3
2 Jfy2^
3
Net
Value
/J/
£-.9
2
Actual
Reading
1 #3
2 /J>3
3
1 ;?.z-
3
Net
Value
//•
M
.479
3
Actual
Reading
1 &3
2 /3,3
3
2 /0.Z-
3
Net
Value
/*->-'
*'^
Average
Net
Value
(% v/v)
«?
CO,
Acceptance Criteria per Method 3B
. 0.3% v/v 02 ^.15% 0.2% v/v
. 0.2% v/v <15% 0.3% v/v
Remarks and Notes:
M3BANALWPD Septembef 3. 1999
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY TRAIN SET-UP DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Sampling Train A No.
Sampling Train B No.
Set-up person(s):
Transfer to Sampler:
Relinquished By
Impinger Box A No.
Impinger Box B No. .
Date:
TRAIN COMPONENT
Received By O> &JTJ/-/>>»
REAGENT
Date/Time
LOADING DATA
TRAIN A
TRAIN B
Sampling Nozzle (Quartz)*
Filter Assembly and Holder*
Filter Type: Whatman QM-A
Probe (316 SS) :
Sample Transfer/Vacuum Line :.
Male 1st Impinger Inlet Blank-Off
Nozzle I.D. No.
Fitter Assembly No.
Filter Holder No,
Initial Weights (grams)
1st Impinger (Mod-GBS) 100-200 mLs ASTM Type I Water
U-Connector (A) j.
2nd Impinger (GBS) 100-200 mLs ASTM Tyjje 1 Water
U-Connector (B)
3rd Impinger (Mod-GBS) Empty
U-Connector (C)
4th Impinger (Mod-GBS) "200 g indicating silica gel
U-Connector (D)
5th Impinger (Mod-GBS) "200 g indicating silica gel
Impinger Outlet Connector
Connector I.D. No.
* Before and after sampling: Nozzle inlet opening and filter assembly holder outlet opening covered with Teflon® tape, and
entire filter assembly holder with filter assembly and nozzle wrapped in aluminum foil and placed in Ziploc® bag. 1st impinger
inlet sealed with glass blank-off.
Comments:
M17DSUP.WPD May 13. 1999 Irev. M17DSUP3.WPD November 10, 19991
73
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY SAMPLE RECOVERY DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Sampling Train A No.
Sampling Train B No.
Impinger Box A No.
Impinger Box B No.
Transfer for Recovery:
Relinquished By ft,
Received By
Date/Time
Sample recovery person(s):
Weights below are in grams.
-------
FIELD SAMPLING DATA FOR METHOD 17 TRAINS
s
K>
fc
"•d
tn
n
Run No.
Date
Project No. 104703.1.002.05.01
Client U.S. EPA OAQPS EMAD EMC
Source Coaentrix Unit 2A
Sampling Location Baghouse Outlet
Operator
Record data every A*
Barometer No. Y-2021
**) minutes
in Hg
34 ft
Barometric Pressure
Elevation to Meter Boxes _
Meter Box Pba, '2AtC{i
Elevation to Sampling Loc.
Sampling Location Pbaf "xV' '3 in Hg
/ffl*2£f" if-t>7
Static Pressure y^f^ " '••" in H2O Assumed Moisture
in Hg
34 ft
Train A No. M17-A
Probe No. A Lenath: 10 ft
Nozzle No. M17- °j Tio Dia. ^Hlf in
Pitot Tube No. A Cp 0.84
Stack Thermocouple No. 31 58 A
Filter Holder No. (
Filter Assembly No. £2%
Impinqer Box No. A- /
(
Umbilical/lmpinger Hookup UH-^£3>
Umbilical No. /IJGWH
Meter Box No. Ai 12^
DGM Correction (Y) nfflff
Orifice Meter AH {'&!&
Train B No. M17-B
Probe No. B Lenath: 10 ft
Nozzle No. M 17- l&Tm Dia. <9-/Y<^ in
Pitot Tube No. B Cp 0.84
Stack Thermocouple No. 3158B
Filter Holder No. ?-
Filter Assembly No. F^
Impinger Box No. B- |
Umbilical/lmpinger Hookup UH-^2 —
Umbilical No. (J IX?- \
Meter Box No. (Jl\
DGM Correction (Y) (tO(^
Orifice Meter AH@> /'f*^
TT
page 1 of.
1
Assumed %CO,
/*•?
TAJ LfiJ Lcj LoJ LEJ
Traverse Point Layout
Compass Direction >• North
Nozzles are quartz-glass.
Time (24 Hr)
Pass or Fail
Train A Pitot Tube Pressure Measurement System Leak Checks
Initial
\w>
Final
tit
ttp*
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Train B Pitot Tube Pressure Measurement System Leak Checks
Initial
lW
Final
/W
$&a
Initial
Final
Initial
Final
Initial
Final
Initial
Final
Train A Sampling System Leak Cnecks
Time (24 Hr)
Vacuum, in Hg
Leak Rate, cfm
Initial
(W6
iT
,ocfa
Final Meter Volume
Initial Meter Volume
Leak Check Volume
Final
-------
Run No.
Date
Sampling Location Unit 2A Baahouse Outlet Duct
Project No. 104703.1.002.05.01
Operator
page.
of 2_
Sampling Data for Method 17 Train A No. M17-A
Sampling
Time,
Traverse
Point
Clock
Time
(24-Hr)
Dry Gas Meter Reading
(VJ, ft3
Initial
Desired
Actual
Velocity
Head
(Ap),
in. H20
Orifice Pressure
Differential
(AH),
in. H20
Desired Actual
Stack
Temp.
It.).
°F
Dry Gas Meter
Temperature
Inlet
Outlet
Pump
Vacuum,
in. Hg
Silica Gel
Impinger
Outlet
Temp.,
°F
£o_
Y
&-
<2*>
S'f
4J
M=_
^_
$
3-
o/&
G--3?
32^.
&**
0r/(
4-Z-
f*
, 16,
#3
ML
ftoff
-Z
&L-
f
•7
3"7
-7
&L
Sampling Data for Method 17 Train B No. M17-B
M-
^SL
22L
fft*
£3
-7
0,97
0,23
a,??
$3
ZZJ'lf
Sf
S&3
•f?
t>#3
m-
A3
•2-Z1,
i
££.
OL
t#S
r?
Remarks and Notes:
M17DPG2.WPD Septembers. 1999
76
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 3B
INTEGRATED GAS SAMPLING DATA
Run No..
Date
Project No. 104703.1.002.05.01 _
Sample Type (Multi-Point, Single-Point)
Flow Control Device (Valve, Critical Orifice)
Method 5 Meter Box No.
MSB Pump Type diaohram
MSB Pump No. A} it
Client/Source U.S. EPA / Cogentrix Unit 2A
Sampling Location Unit 2A Baghouse Outlet
Operator 6
Bag Type Tedlar
Method 3B Train No. _
MSB Flow Meter Type.
MSB Flow Meter No.
Sample No.
NA
NA
rotameter
Desired Sampling Rate
Leak Check Before Sampling.
Total Sampling Time "/O
cc/min
Flow Rate, cc/min: Average _
Estimated Total Sample Volume
3; After Sampling
min Average Flow Meter Reading
Highest _
Lowest
liters
Time
(24-Hr)
Flow
Meter
Reading
Start
Purge
Start
Sampling
Stop
Sampling
Sampling
Remarks and Notes
Mel
&
Hffi
/tftz
ffto
1*
o
ftfo
Mfi- -
M3BSAMP WPD June IS, 1993
77
RCA#2 APPENDIX C
-------
co
s
TJ
o
40 CF/? 60, APPENDIX A, METHOD 3B, GAS ANALYSIS BY ORSAT
Run No.
Date
Project No. 104703.1.002.05.01 Sample No. .
Sampling Location Unit 2A Baghouse Outlet Duct
Analysis Start Time
NA
Sample Type (Bag, Grab)
Analyst J>
Bag
Orsat Leak Check Before Analysis:
Burrete /Y® Change in 4 Minutes
Pipettes x^> Change in 4 Minutes
Orsat Leak Check After Analysis:
Burrete >>,/>
3
1 ^>
2 %-T^~
3
Net
Value
/y. '
>5~' <*
3
Actual
Reading
1 /*>.'
2 ;>JJ
3
V^-2.
2 ^2,
3
Net
Value
/#•)
£~'J
Average
Net
Value
(% v/v)
/^>/
<£~J
CO,
Acceptance Criteria per Method 3B
• 0.3% v/v 02 >J5% 0.2% v/v
, 0.2% v/v <15% 0.3% v/v
Remarks and Notes:
M3BANALWPD Septembers, 1999
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY TRAIN SET-UP DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
9 Impinger Box A No. <&~'
£ Impinger Box B No. ~~S
Run No. * Sampling Train A No.
Sampling Train B No.
Set-up person(s): J.
Date:
Transfer to Sampler:
Relinquished By J
Received By
Date/Time
TRAIN COMPONENT
REAGENT
LOADING DATA
TRAIN A
TRAIN B
Sampling Nozzle (Quartz)*
Filter Assembly and Holder*
Filter Type: Whatman QM-A
Probe (316 SS)
Sample Transfer/Vacuum Line
Male 1st Impinger Inlet Blank-Off
Nozzle I.D. No.
Filter Assembly No.
Filter Holder No-
Initial Weights (grams)
1st Impinger (Mod-GBS) 100-200 mLs ASTM Type I Water
U-Connector (A) ;
2nd Impinger (GBS) 100-200 mLs ASTM Tyjpe I Water
U-Connector (B)
3rd Impinger (Mod-GBS) Empty
U-Connector (C)
4th Impinger (Mod-GBS) "200 g indicating silica gel
U-Connector (D)
5th Impinger (Mod-GBS) "200 g indicating silica gel
Impinger Outlet Connector
Connector I.D. No.
* Before and after sampling: Nozzle inlet opening and filter assembly holder outlet opening covered with Teflon® tape, and
entire filter assembly holder with filter assembly and nozzle wrapped in aluminum foil and placed in Ziploc® bag. 1 st impinger
inlet sealed with glass blank-off.
Comments:
M17DSUP.WPD May 13, 1999 (rev. M17DSUP3.WPD November 10, 1999]
79
RCA#2 APPENDIX C
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD LABORATORY SAMPLE RECOVERY DATA FOR TWO TRAINS
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Run No.
Sampling Train A No.
Sampling Train B No..
Transfer for Recovery:
Relinquished By P, 6fj-f-br>
Sample recovery person(s):
Weights below are in grams.
Received By J, £
J. Su.
Impinger Box A No. >?">?
Impinger Box B No. 13-J
5""j
Date/Time
/5VP
Date:
BACK HALF RECOVERIES
TRAIN A
Impinger: 1st
Final Wt.
Initial Wt.
Net Wt.
2nd
3rd
4th & 5th
1 st
6,3 -0,1
Total Condensate Collected:
Description and/or color:
5/7
% Blue
TRAIN B
2nd
3rd
4th & 5th
A 5* -£>,-2-
30
*
% Blue
FRONT HALF RECOVERIES:
TRAIN A
FILTER ASSEMBLY:
Sample Number: -jiS? 102
PM Description/color:
TRAIN RINSES:
Sample Number:
Components Rinsed*: nozzle, filter holder front
TRAIN B
* Acetone rinses with brushing 3 times or more until perceivably clean.
COMMENTS: Acetone rinses are transferred directly to tared Teflon® beaker liners for analysis.
M17DRCV.WPD May 13, 1999 (rev M17DRCV3.WPD November 10, 19991
80
RCA#2 APPENDIX C
-------
RCA #2 Appendix D
M17 Field Laboratory Particulate Weight Data
MR]-OPPT\R4703-0:-07 Appendices Covers WPD
-------
PARTICULATE MATTER (FRONT-HALF) RINSES ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: tJ- •2>Mj
Beaker Liner Size and Type: 250-mL Teflon®
Acetone Lot No. BO 363
Sample Treatment: Acetone samples evaporated at ambient temperature and pressure in an
enclosure with HEPA-filtered air; then, desiccated and weighed to a constant weight.
Weight Unit: grams
Run No. J~-& Beaker No. ' Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weiahts
Gross Wt. Date Time
. ^i s\ **J
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = & mg/mL
Volume for data entry = ??/.(& mLs
Comments:
C50
Run No. J~&
Sample Volume
Beaker No. £? Samole No.
+ Acetone Rinses of Bottle
3o;»3
Beaker Liner
Gross Wt.
+ Sample Residue Weiahts
Date Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = O_ mg/mL
Volume for data entry = 3Sj& mLs
Comments:
3*.
Run No. J?-S-) Beaker No. 3 Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weiahts
Gross Wt. Date Time
. jf* ** j+ ~
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = O_ mg/mL
Volume for data entry = &&&• mLs
Comments:
NOTE: Control iiner and reagent blank weight data and balance check data are documented on other forms.
M5IPMRIX.WPD June 5, 1998 (rev. M17PMRI3.WPD November 10, 1999)
RCA#2 APPENDIX D
-------
PARTICULATE MATTER (FRONT-HALF) RINSES ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: J, £<.4ys9?zir->
Beaker Liner Size and Type: 250-mL Teflon®
Acetone Lot No. BO 363
Sample Treatment: Acetone samples evaporated at ambient temperature and pressure in an
enclosure with HEPA-filtered air; then, desiccated and weighed to a constant weight.
Weight Unit: grams
Run No. ff-(3 Beaker No. ^ Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
^. Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt. /ffZ&b £_.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = &_ mg/mL
Volume for data entry = ff1^-? mLs
Comments:
Run No. Zf-Jr Beaker No. • =T Sample No..
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt. S33-7
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
„__
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data: 3*'.
Acetone Blank for data entry = &_ mg/mL
Volume for data entry = a&£-7 mLs
Comments:
Run No. C7-.P Beaker No. & Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = S rnLs
Comments:
NOTE: Control liner and reagent blank weight data and balance check data are documented on other forms.
M5IPMRIX.WPD June 5, 1998 (rev M17PMRI3.WPD November 10. 1999)
RCA#2 APPENDIX D
-------
PARTICULATE MATTER (FRONT-HALF) RINSES ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: tJ
Beaker Liner Size and Type: 250-mL Teflon®
Acetone Lot No. BO 363
Sample Treatment: Acetone samples evaporated at ambient temperature and pressure in an
enclosure with HEPA-filtered air; then, desiccated and weighed to a constant weight.
Weight Unit: grams
Run No. ^~/9 Beaker No. "7 Sample No.,
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = £/ mg/mL
Volume for data entry = Z?3,C mLs
Comments:
Run No. V-/? Beaker No. a Sample No.
Sample Volume + Acetone Rinses of Bottle .. Beaker Liner + Sample Residue Weights
Gross Wt. Date. Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = O_ mg/mL
Volume for data entry = ^3,3 mLs
Comments:
Run No. -3~-/-) Beaker No. 2_ Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = Q mg/mL
Volume for data entry = rV^S1 mLs
Comments:
NOTE: Control liner and reagent blank weight data and balance check data are documented on other forms.
M5IPMRIX WPD JuneS, 1998 (rev M17PMRI3.WPD November 10, 1999)
RCA#2 APPENDIX D
-------
PARTICULATE MATTER (FRONT-HALF) RINSES ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: (J, Si4/^j*r**^j*?
Beaker Liner Size and Type: 250-mL Teflon®
Acetone Lot No. BO 363
Sample Treatment: Acetone samples evaporated at ambient temperature and pressure in an
enclosure with HEPA-filtered air; then, desiccated and weighed to a constant weight.
Weight Unit: grams
Run No. s5"-5 Beaker No. SO Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt, Date Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt. .
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = <2 mg/mL
Volume for data entry = 3?&,S' mLs
Comments:
3S- . \
Run No. ^ "iff Beaker No. -^> Beaker No. SZi Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt. sS'J.^ ^3 .
Beaker + Liner Tare Wt. _
Sample + Rinses Wt. _
Acetone Wt./0.79 = mLs Acetone: _
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = 0 mg/mL
Volume for data entry = S'J-'J mLs
Comments:
NOTE: Control liner and reagent blank weight data and balance check data are documented on other forms.
M5IPMRIX.WPD June 5. 1998 (rev. M17PMRI3.WPD November 10, 19991
RCA#2 APPENDIX D
-------
PARTICULATE MATTER (FRONT-HALF) RINSES ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: J, Su^m^t?
Beaker Liner Size and Type: 250-mL Teflon®
Acetone Lot No. BO 363
Sample Treatment: Acetone samples evaporated at ambient temperature and pressure in an
enclosure with HEPA-filtered air; then, desiccated and weighed to a constant weight.
Weight Unit: grams
Run No. "7-s? Beaker No. S3 Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weiahts
Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = &. mg/mL
Volume for data entry = c?!/-^ mLs
Comments: • :
-56,
Run No. *? -3 Beaker No. ^V Sample No..
Sample Volume + Acetone Rinses of Bottle . - Beaker Liner + Sample Residue Weiahts
. . :. _ Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt. ,
Beaker + Liner Tare Wt. .
Sample + Rinses Wt. .
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = £_ mg/mL
Volume for data entry = ff&~.*J mLs
Comments:
Run No. $-J9 Beaker No. /£>" Sample No. 3
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weiahts
^ ^ Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt. /f>^>"3> 3
Sample + Rinses Wt. _
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = £/_ mg/mL
Volume for data entry = 3&s'? mLs
Comments:
NOTE: Control liner and reagent blank weight data and balance check data are documented on other forms.
M5IPMRIX.WPD June 5, 1998 (rev M17PMRI3.WPD November 10, 1999)
RCA#2 APPENDIX D
-------
PARTICULATE MATTER (FRONT-HALF) RINSES ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: tJ* £+-*r's-r*£>sf
Beaker Liner Size and Type: 250-mL Teflon®
Acetone Lot No. BO 363
Sample Treatment: Acetone samples evaporated at ambient temperature and pressure in an
enclosure with HEPA-filtered air; then, desiccated and weighed to a constant weight.
Weight Unit: grams
3?
Run No. 8~£ Beaker No. S6> Sample No. 3?S03
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weiahts
Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = 0 mg/mL
\ Volume for data entry = £*9.7 mLs
Comments: i
Run No. *?-& Beaker No. s/ :- Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weiahts
Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = ^ mg/mL
Volume for data entry = jZ>£jZ2. mLs
Comments:
Run No. 7 -& Beaker No. '& Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weiahts
.,.»,-,.~ Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = &_ mg/mL
Volume for data entry = £?'2'7 mLs
Comments:
NOTE: Control liner and reagent blank weight data and balance check data are documented on other forms.
I"
M5IPMRIX.WPD June 5. 1998 (rev. M17PMRI3.WPD November 10. 1999)
RCA#2 APPENDIX D
-------
PARTICULATE MATTER (FRONT-HALF) RINSES ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: JJ.
Beaker Liner Size and Type: 250-mL Teflon®
Acetone Lot No. BO 363
Sample Treatment: Acetone samples evaporated at ambient temperature and pressure in an
enclosure with HEPA-filtered air; then, desiccated and weighed to a constant weight.
Weight Unit: grams
Run No. S&-/2 Beaker No. S9 Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt. Date Time
. j».t r\
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry: ^
Beaker Liner Tare Weight from Tare Weight Data: 3. z5~S
Acetone Blank for data entry = ^ mg/mL
= Volume for data entry = &J.£ mLs
Comments:
Run No. S&-& Beaker No. *(& ; Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt. 4O.f
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry: 3>
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = *s O mg/mL
Volume for data entry = /l>iiP^£*&.•¥ mLs
Comments: /
Run No. / )~ri Beaker No. a*/ Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt. SSZi.'r 3i S3 SSL
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone: .
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = O_ mg/mL
Volume for data entry = ^^_S mLs
Comments:
NOTE: Control liner and reagent blank weight data and balance check data are documented on other forms.
M5IPMRIX.WPD June 5, 1998 (rev. M17PMRI3.WPD November 10, 19991
RCA#2 APPENDIX D
-------
PARTICULATE MATTER (FRONT-HALF) RINSES ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: -7
Beaker Liner Size and Type: 250-mL Teflon®
Acetone Lot No. BO 363
Sample Treatment: Acetone samples evaporated at ambient temperature and pressure in an
enclosure with HEPA-filtered air; then, desiccated and weighed to a constant weight.
Weight Unit: grams
Run No. SJ-& Beaker No. ZZ- Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0. 79 = mLs Acetone: 3?,2-
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data: 3;
Acetone Blank for data entry = £? mg/mL
Volume for data entry = 33-Z— mLs
Comments:
Run No. /&-J9 Beaker No. xvJ? Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt. Date Time
_ —« t
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = O mg/mL
Volume for data entry = £*).*? mLs
Comments:
Run No. /&-& Beaker No. &*+• Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt. Date Time
. . _ ^*
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt. /
-------
PARTICULATE MATTER (FRONT-HALF) RINSES ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst:
Beaker Liner Size and Type: 250-mL Teflon®
Acetone Lot No. BO 363
Sample Treatment: Acetone samples evaporated at ambient temperature and pressure in an
enclosure with HEPA-filtered air; then, desiccated and weighed to a constant weight.
Weight Unit: grams
Run No. S3~J? Beaker No. Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
^, Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt. /%%v^>
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = «2 mg/mL
Volume for data entry = &&.) mLs
Comments: .
Run No. S&-& Beaker No. Z?£c Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt. D.ate Time
Beaker + Liner + Sample + Rinses Wt. /&&-8
Beaker + Liner Tare Wt. /d^S?
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = O mg/mL
Volume for data entry = jj2£7«»* mLs
Comments:
Run No. Beaker No. Sample No.
Sample Volume + Acetone Rinses of Bottle Beaker Liner + Sample Residue Weights
Gross Wt. Date Time
Beaker + Liner + Sample + Rinses Wt.
Beaker + Liner Tare Wt.
Sample + Rinses Wt.
Acetone Wt./0.79 = mLs Acetone:
Beaker Liner + Residue Gross Weight used for data entry:
Beaker Liner Tare Weight from Tare Weight Data:
Acetone Blank for data entry = mg/mL
Volume for data entry = mLs
Comments:
NOTE: Control liner and reagent blank weight data and balance check data are documented on other forms.
MSIPMRIX.WPD June 5. 1998 (rev M17PMHI3.WPD November 10. 19991
RCA#2 APPENDIX D
-------
PARTICULATE MATTER IN FILTER ASSEMBLY ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: c/
Filter Size and Type: 47mm diameter, Whatman QM-A quartz glass fiber filter
Filter Lot No. 25460
Assembly Components: filter, aluminum foil gasket, and 316 stainless steel filter support
Filter Assembly Treatment: HydL at lUb "L fui 3-l-njulST desiccate and weigh to a constant weight.
Weight Unit: grams 1&
Run No. /-v# Assembly No. / _ Sample No.
Gross Wt. Date Time Comments:
Assembly Gross Weight used for data entry: *-*••
Assembly Tare Weight from Tare Weight Data: J
Run No. A-*? _ Assembly No. ^ _ Sample No.
Gross Wt. Date ...Time :. . Comments:
3,
Assembly Gross Weight used for data entry:
Assembly Tare Weight from Tare Weight Data: 3. "<3&S
Run No. #-<& Assembly No. -3 _ Sample No.
Gross Wt. Date Time Comments:
3.
Assembly Gross Weight used for data entry:
Assembly Tare Weight from Tare Weight Data:
NOTE: Control and blank assembly weight data and balance check data are documented on other forms.
M5IPMFIX.WPD JuneS. 1998 (rev M17PMFI3.WPD November 10. 1999}
RCA#2 APPENDIX D
-------
PARTICULATE MATTER IN FILTER ASSEMBLY ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: Sample No.
Gross Wt. Date Time Comments:
Assembly Gross Weight used for data entry:
Assembly Tare Weight from Tare Weight Data:
NOTE: Control and blank assembly weight data and balance check data are documented on other forms.
M6IPMFIX.WPD June 5. 1998 Irev. M17PMFI3.WPD November 10. 1999)
11
RCA#2 APPENDIX D
-------
PARTICULATE MATTER IN FILTER ASSEMBLY ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: o/,
Filter Size and Type: 47mm diameter, Whatman QM-A quartz glass fiber filter
Filter Lot No. 25460
Assembly Components: filter, aluminum foil gasket, and 316 stainless steel filter support
Filter Assembly Treatment: I lent at 105-^C for 3 hows, desiccate and weigh to a constant weight.
Weight Unit: grams $& i\ljt>)W
Run No. V-i/9 Assembly No. "7 Sample No.
Gross Wt. Date Time Comments:
Assembly Gross Weight used for data entry:
Assembly Tare Weight from Tare Weight Data:
33 •
Run No. 4-8 Assembly No. S _ ' Sample No.
Gross Wt. Date . Time : Comments:
Assembly Gross Weight used for data entry:
Assembly Tare Weight from Tare Weight Data:
Run No. &-S9 Assembly No. 9 _ Sample No.
Gross Wt. Date Time Comments:
3,3**)
Assembly Gross Weight used for data entry:
Assembly Tare Weight from Tare Weight Data:
NOTE: Control and blank assembly weight data and balance check data are documented on other forms.
M5IPMFIX.WPD June 5, 1998 (rev. M17PMFI3.WPD November 10. 19991
12
RCA#2 APPENDIX D
-------
PARTICULATE MATTER IN FILTER ASSEMBLY ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: *J. <
Filter Size and Type: 47mm diameter, Whatman QM-A quartz glass fiber filter
Filter Lot No. 25460
Assembly Components: filter, aluminum foil gasket, and 316 stainless steel filter support
Filter Assembly Treatment: +reaTdl lOb "LI lul 'J hwuts, desiccate and weigh to a constant weight.
Weight Unit: grams f-3 :
Run No. 3-J5 Assembly No. /& _ Sample No.
Gross Wt. Date Time Comments:
Assembly Gross Weight used for. data entry:
Assembly Tare Weight from Tare Weight Data:
. . . = • :
Run No. ^V? Assembly No. M Sample No,
Gross Wt. Date Time Comments:
Assembly Gross Weight used for data entry:
Assembly Tare Weight from Tare Weight Data:
Run No. &> ~& Assembly No. S^Z Sample No.
Gross Wt. Date Time Comments:
Assembly Gross Weight used for data entry: *=*"
Assembly Tare Weight from Tare Weight Data:
NOTE: Control and blank assembly weight data and balance check data are documented on other forms.
u
M5IPMFIX.WPD June 5, 1998 (rev M17PMF13.WPD November 10, 1999)
13
RCA#2 APPENDIX D
-------
PARTICULATE MATTER IN FILTER ASSEMBLY ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: t-A
Filter Size and Type: 47mm diameter, Whatman QM-A quartz glass fiber filter
Filter Lot No. 25460
Assembly Components: filter, aluminum foil gasket, and 316 stainless steel filter support
Filter Assembly Treatment: ^Heat at 105 "C toi 3 IH-HUS, desiccate and weigh to a constant weight.
Weight Unit: grams »|3oM
Run No. 7-S3 Assembly No. X^ Sample No.
Gross Wt. Date Time Comments:
Assembly Gross Weight used for data entry: 3.
Assembly Tare Weight from Tare Weight Data: •
Run No. 7-8 Assembly No. /^ Sample No.
Gross Wt. Date . Time ...... Comments:
S'J/ffo
Assembly Gross Weight used for data entry:
Assembly Tare Weight from Tare Weight Data: 3* "3 7&O
Run No. 0-S) Assembly No. S^S* Sample No.
Gross Wt. Date Time Comments:
Assembly Gross Weight used for data entry: J,-
Assembly Tare Weight from Tare Weight Data: 3.
NOTE: Control and blank assembly weight data and balance check data are documented on other forms.
MSIPMFIX.WPD June 5, 1998 (rev M17PMFI3.WPD November 10, 19991
14
RCA#2 APPENDIX D
-------
PART1CULATE MATTER IN FILTER ASSEMBLY ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: <)•
Filter Size and Type: 47mm diameter, Whatman QM-A quartz glass fiber filter
Filter Lot No. 25460
Assembly Components: filter, aluminum foil gasket, and 316 stainless steel filter support
Filter Assembly Treatment: rHear at I Ob U(J TGI 3 liuw*, desiccate and weigh to a constant weight.
Weight Unit: grams i \bo~IW
37
Run No. %-& Assembly No. SCe _ Sample No.
Gross Wt. Date Time Comments:
3..
Assembly Gross Weight used for data entry: •& '2*2 "3 S
Assembly Tare Weight from Tare Weight Data: 3.- '
__
Run No. 9-/? Assembly No. /7 Sample No.
Gross Wt. Date Time Comments:
Assembly Gross Weight used for data entry:
Assembly Tare Weight from Tare Weight Data:
Run No. 9-J& Assembly No. /
-------
PARTICULATE MATTER IN FILTER ASSEMBLY ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: cA
Filter Size and Type: 47mm diameter, Whatman QM-A quartz glass fiber filter
Filter Lot No. 25460
Assembly Components: filter, aluminum foil gasket, and 316 stainless steel filter support
Filter Assembly Treatment: Hoot at 1-90 "C fill 3 hoUr> desiccate and weigh to a constant weight.
Weight Unit: grams ^
Run No. /J-^9 Assembly No. S9 Sample No.
Gross Wt. Date Time Comments:
-^/i 3
Assembly Gross Weight used for data entry: &••
Assembly Tare Weight from Tare Weight Data:
Run No. /'
-------
PARTICULATE MATTER IN FILTER ASSEMBLY ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst:
-------
PARTICULATE MATTER IN FILTER ASSEMBLY ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: *J->
Filter Size and Type: 47mm diameter, Whatman QM-A quartz glass fiber filter
Filter Lot No. 25460
Assembly Components: filter, aluminum foil gasket, and 316 stainless steel filter support
Filter Assembly Treatment: neat ai 'liffi PC fui 3imycs. desiccate and weigh to a constant weight.
Weight Unit: grams ^nb'ty*
Run No. S3~,& Assembly No. tf^ Sample No.
Gross Wt. Date Time Comments:
Assembly Gross Weight used for data entry:
Assembly Tare Weight from Tare Weight Data:
Run No. /^-
-------
PARTICULATE MATTER CONTROLS ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Sampling Team Leader: Jim Surman Analyst: *J'
Balance: AND ER-120A, MRI #12007
Weight Unit: grams
Control Filter Assembly Weights & Balance Checks:
Assembly No. 33 NIST Weight: Assembly No. **** NIST Weight:
Original Tare Wt.: ..?- '3 3¥(t> 1 gram Original Tare Wt.: •?-> '38^'? 1 gram
Current Wt. Date Time Balance Reading Current Wt. Date Time Balance Reading
3,3335~ /JJJ9J&? 0330 ,
3' 331k //Jfft>}99 S60? J.t>t?£>£>
Comments:
Control Beaker Liner Weights & Balance Checks:
Beaker No. 33 NIST Weight: Beaker No. ->y NIST Weight:
Original Tare Wt.: 3^ •J^&b 1 gram Original Tare Wt.: &-• ~?&S'? 1 gram
Current Wt. Date Time Balance Reading Current Wt. Date Time Balance Reading
3,-
3
3230
A-'MS? /'/MJW
Comments:
Controls are filter assemblies and beaker liners selected from the original prepared lots that are used for sampling and analysis. They
are processed along with the assemblies and liners containing samples during analysis, i.e., they are.heated, desiccated, and weighed
along with the assemblies and liners containing samples. The results are not used for correcting analytical data, but are useful in
monitoring changes between original tare weights and weights obtained during analysis of samples. Significant changes could
indicate problems in maintaining relatively constant environmental conditions in the laboratory, processing procedures not replicating
those used when tare weights were obtained, instrumentation calibration drift, and desiccant deterioration.
Each time filter assemblies or beaker liners are weighed, the balance is checked for accuracy by weighing NIST certified weights
approximating the weights of the assemblies or liners.
M5IPMCOX.WPD June 5. 1998 (rev. M17PMC03.WPO November 10. 19991 ]]!''''
19
RCA#2 APPENDIX D
-------
PARTICULATE MATTER REAGENT BLANK ANALYSIS DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Analyst: cA
Sampling Team Leader: Jim Surman
Beaker Liner Size and Type: 250-mL Teflon®
Acetone Lot No. BO 363
Sample Treatment: Acetone samples evaporated at ambient temperature and pressure in an
enclosure with HEPA-filtered air; then, desiccated and weighed to a constant weight.
Filter Size and Type: 47mm diameter, Whatman QM-A quartz glass fiber filter
Filter Lot No. 25460
Assembly Components: filter, aluminum foil gasket, 316 stainless steel filter support
Filter Assembly Treatment: •l.leamJ Jl 10G °C for 3 hours, desiccated and weighed to a constant weight.
Weight Unit: grams
Acetone Blank Determination: For Run No.(s)
Beaker No.
A.
Acetone Reagent Blank Sample Volume
Beaker + Liner + Acetone Sample Wt.
Beaker + Liner Tare Wt.
Acetone Sample Wt.
Acetone Wt./0.79 = mLs Acetone:
Sample No.
Beaker Liner
Gross Wt.
+ Sample Residue Weights
Date Time
SC&.J
87,3
3 *
B.
Comments:
Beaker Liner + Residue Gross Weight used for blank determination:
Beaker Liner Tare Weight from Tare Weight Data:
Net Weight of Residue in beaker liner:
Acetone Blank (B x 1000/A) for.data entry:
O
mg/mL
Filter Assembly Blank Determination: For Run No.(s)
Gross Wt. Date Time Comments:
Assembly No.
A.
B.
Assembly Gross Weight used for blank determination:
Assembly Tare Weight from Tare Weight Data:
Net Assembly Weight Difference (A - B) for data entry:
[retain minus sign if value is negative]
Sample No.
NOTE: Control liner and filter assembly weights and balance check data are documented on another form.
II
M5IPMBLX.WPD June 5, 1998 (rev. Ml 7PMBL3.WPD November 10, 19991
20
RCA#2 APPENDIX D
-------
40 CFR 60, APPENDIX A, METHOD 17 - PARTICULATE MATTER TRAIN (M17)
FIELD REAGENT BLANK PREPARATION DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Blank(s) Prepared By: J. ^Uj'jivSirr Date: /S/J6/99
Weights below are in grams.
Sample Bottle Tare Bottle Gross Net Sample
Reagent Blank Description Number Weiaht Weiaht Weiaht
Acetone for particulate matter
Volume needed: 100 mLs
Lot Number: BO 363
Filter Assembly for particulate matter ; J'srts' -fas' &»
Type: Whatman QM-A .'-,'
Filter Assembly Number:
-------
BEAKER LINER TARE WEIGHT DATA
MRI Project No. 104703.1.002.05.01
Sampling Team Leader: Jim Surman Analyst: •
Beaker Liner Size and Type: 250-mL Teflon®
Beaker Liner Treatment: Wash to clean, rinse with Dl water, dry at 105 "C, insert into glass beakers previously
cleaned in the same manner, desiccate for 24 hours, and weigh to a constant.
Weight Unit: grams
Date:
Time Started:
Balance Check before beaker liners are weighed:
Balance Used:
Weight Value: /^ Sty
Balance Reads: />&&*& AM0&
Average Weight
Beaker Liner in or Weight to be
Beaker I.D. No. First Weighing Second Weighing Third Weighing Used as the Tare
3,6,93 •/
3, S3 ?? 3,833$ 3,33X3
3.3118
Balance Check after beaker liners are weighed:
Balance Reads:
COMMENTS:
3,3937
M5IBEAKX.WPD June 4, 1998 Irev M17BEAK3.WPD November 10, 19991
22 RCA#2 APPENDIX D
-------
BEAKER LINER TARE WEIGHT DATA
MRI Project No. 104703.1.002.05.01
Sampling Team Leader: Jim Surman Analyst:
Beaker Liner Size and Type: 250-mL Teflon®
Beaker Liner Treatment: Wash to clean, rinse with Dl water, dry at 105 °C, insert into glass beakers previously
cleaned in the same manner, desiccate for 24 hours, and weigh to a constant.
Weight Unit: grams
Date: _
Time Started:
Balance Check before beaker liners are weighed:
Balance Used: /9XP ££-
Weight Value: /fV"
Balance Reads: ••
Average Weight
Beaker Liner in or Weight to be
Beaker I.D. No. First Weighing Second Weighing Third Weighing Used as the Tare
23
3. '
3 ,<*
3,
33
Balance Check after beaker liners are weighed:
Balance Reads: /.£>&
-------
FILTER ASSEMBLY TARE WEIGHT DATA
MRI Project No. 104703.1.002.05.01
Sampling Team Leader: Jim Surman
Analyst:
Filter Size and Type: 47mm diameter, Whatman QM-A quartz glass fiber filter
Filter Lot No. 25460
Assembly Components: filter, aluminum foil gasket, and 316 stainless steel filter support
Filter Assembly Treatment: Heat at 105 °C for 3 hours, desiccate, and weigh to a constant weight.
Weight Unit: grams
Date: '' '' '
Time Started:
Assemblv No.
1
JL
it
it
I*
0
Balance Check before filter assembles are weighed:
Balance Used:
Weight Value:
Balance Reads:
First Weiahina
Second Weiahina
Third Weiahina
Average Weight
or Weight to be
Used as the Tare
. 2-7 T2,
1.27^3
<*.**> 2L
5/V3
Balance Check after filter assemblies are weighed:
Balance Reads: 1
COMMENTS:
M5IFILTX.WPD June 4, 1998 Irev. M17FILT3.WPD November 5. 19991
24
RCA#2 APPENDIX D
-------
FILTER ASSEMBLY TARE WEIGHT DATA
MRI Project No. 104703.1.002.05.01
Sampling Team Leader: Jim Surman Analyst: _
Filter Size and Type: 47mm diameter, Whatman QM-A quartz glass fiber filter
Filter Lot No. 25460
Assembly Components: filter, aluminum foil gasket, and 316 stainless steel filter support
Filter Assembly Treatment: Heat at 105 °C for 3 hours, desiccate, and weigh to a constant weight.
Weight Unit: grams
Date:
Time Started:
Balance Check before filter assembies are weighed:
Balance Used:
Weight Value:
Balance Reads:
Average Weight
or Weight to be
Assembly No. First Weighing Second Weighing Third Weighing Used as the Tare
^\
v
•y "iffim/ 7, 'Witf 'Z3?J-/7
, HI '1£>
"A
Balance Check after filter assemblies are weighed:
Balance Reads: t^Tl"" "<
COMMENTS: 16
M5IFILTX.WPD June 4, 1998 (rev M17HLT3.WPD November 5. 1999)
25
RCA#2 APPENDIX D
-------
RCA #2 Appendix E
M17 Post-Test Calibration Sheets
MRJ-OPPT\R4703-02-07 Appendices Covers WPD
-------
METHOD 5 METERING CONSOLE CALIBRATION WITH CRITICAL ORIFICE
MR1 Project No.
Date:
Operator.
104703.1.002
11/21/99
D. Neal
Metering Console No.
=revious Dry Gas Meter Factor (Y):
Calibrated Critical Orifice No.
Critical Orifice Coefficient in English Units (K1):
| Ambient Temperature Meter No.
N11
1.010
D12
0.32080
Y-0783
CALIBRATION GAS VOLUME DATA
Initial Dry Gas Meter Gas Volume, ft.3
Final Dry Gas Meter Gas Volume, ft.3
Net Dry Gas Meter Gas Volume (Vm), ft.3
CALIBRATION CONDITIONS DATA
Dry Gas Meter Temperature, °F:
Initial Inlet Temperature, °F
Final Inlet Temperature, °F
Initial Outlet Temperature, °F
Final Outlet Temperature, °F
Average Dry Gas Meter Temperature (tj, °F
Time, seconds
Orifice Meter AH, inches H2O
Barometric Pressure, in. Hg
Critical Orifice Inlet (Ambient) Temperature, °F:
Initial Ambient Temperature, °F
Final Ambient Temperature, °F
Avg. Critical Orifice Inlet Temperature (tamb), °F
Pump Vacuum, in. Hg
COMPUTED CALIBRATION RESULTS
Critical Orifice Gas Volume (Vo.^)), standard ft.3
ry Gas Meter Gas Volume (Vm (ad)), standard ft.3
Dry Gas Meter Calibration Factor (Y)
Orifice Meter AH@
AVERAGE CALIBRATION RESULTS
Average Dry Gas Meter Calibration Factor (Y)
Average Orifice Meter AH@
CALIBRATION RESULTS COMPARISON
Criterion: Y Must Be Within 2% Of Average Y
Percent Difference Of Y From Average Y
Tolerance Result
COMPARISON WITH PRETEST RESULTS
Criterion: Y Must Be Within 5% Of Previous Y
% Difference Of Average Y From Previous Y
Tolerance Result
Run 1
269.601
273.772
4.171
76.0
77.0
74.0
75.0
75.5
600
0.540
30.01
69.0
70.0
69.5
18
4.185
4.130
1.013
1.720
1.013
1.717
0.01%
PASS
0.31%
PASS
Run 2
273.772
277.937
4.165
77.0
78.0
75.0
76.0
76.5
600
0.540
30.01
69.0
70.0
69.5
18
4.185
4.117
1.017
1.716
Run 3
277.937
282.137
4.200
78.0
79.0
76.0
77.0
77.5
600
0.540
30.01
70.0
70.0
70.0
18
4.183
4.143
1.010
1.715
0.34%
PASS
0.35%
PASS
Y = 1 013163954203880
Remarks:
ft
CRORCALB.xls 10/29/99 (rev. N11CALB112199 11/21/99 10:51 AM)
RCA#2 APPENDIX E
-------
CONSOLE CALIBRATION WORKSHEET
Job No. /OY703 . /• °0^ Console No. /I///
Date //-<7L/*^f Orifice No. 2
Performed By /J. /vffloo K Factor 0,32-0%
Barometer 5°» °) in. Hg. Previous Y -^r&£&- />oi
NOTE: Prior to running calibration, connect mercury manometer
to sample orifice. Turn on pump and bring mercury manometer up
to 18.0 in. Hg. Record mercury manometer and console vacuum
gauge readings below. Insert critical orifice into console
sample orifice. Set console vacuum gauge at 18.0 in. Hg. +/-
the console vacuum gauge correction factor calculated below.
Mercury manometer readings: .A//* + fJ/x = 18.0 In. Hg.
Console vacuum gauge reading: A//O In. Hg.
Console vacuum gauge correction factor: w//t In. Hg.
RUN #1 RUN #2 RUN #3
DGM Initial Volume-. 34f. fo/ **""*'•**
Initial: -341J-6+ ^73.771 £77,937
Final: £7J.77> 277-9J7
DGM Inlet Temperature:
Initial: 7£ 77 7
-------
M5 CONSOLE POST TEST CHECKLIST
Job No.
/.
Date
Console No.
/V7/
Performed By
Place a check (in black ink) in the space provided after the
required checks are performed.
1. \, Perform positive leak check of Delta H manometer.
(See back of this sheet.)
2. \ Leak check Delta P manometer.
3. A/A1 Clean pump.
4. \/ Clean muffler jar(s) .
5. \ Inspect/refill oiler jar.
6. \, Calibrate DGM
Note: Reading must be
Within +/-5.4°F
thermocouples :
DGM Inlet:
DGM Outlet:
Reference
Thermometer*
°F
6 s.i
tf'l
DGM
Thermometer*
°F
7. \y Digital clock/timer in place and functional.
8. \ Vacuum check. (Leak check at 25 in. Hg. vacuum. Leak
rate should be zero.)
\ Check indicator lights.
\, Check thermocouple switched.
Check fan.
Vy Check pump heater.
Check heat controllers.
V
9.
10
11
12
13
14
If any of the above items were replaced or repaired, please
document that information below:
V
Check Orsat pump and rotameter.
* Reference Thermometer:
Serial Number:
Calibration Records\Calibration Forms\M5check.doc
Revised 10/28/98
RCA#2 APPENDIX E
-------
Procedure for positive leak check Delta H manometer:
1. Pump must not be run prior to this test. Pump needs to be
cool in order to get an accurate reading.
2. Pump pressure and vacuum lines must be connected to console.
3. Null switch on console must be in the down position so
solenoid valve is open to the sampling stream as it is
during testing.
4. Plug meter exhaust and clamp off bottom tube from exhaust
which goes to the Orsat pump.
5. Plug sample orifice.
6. Close main flow control valve.
7. Open fine control valve.
8. Disconnect right side Delta H manometer tube on front of
console.
9. Blow into tubing until manometer reads 5 to 7 inches of
water, and clamp off.
There should be no change in manometer reading.
10. Make certain you remove plug and clamp from meter exhaust
immediately after this test to avoid damage to the meter
pump when pump is started up!
calibrec\m5check 03/09/98
RCA#2 APPENDIX E
-------
METHOD 5 METERING CONSOLE CALIBRATION WITH CRITICAL ORIFICE
CALIBRATION(S) PERFORMED INCORRECTLY - MUST BE REDONE!!!
MR1 Project No.
Date:
Operator
104703.1.002
11/21/99
D. Neal
Metering Console No.
Previous Dry Gas Meter Factor (Y):
Calibrated Critical Orifice No.
Critical Orifice Coefficient in English Units (K1):
| Ambient Temperature Meter No.
N12
0.996
D12
0.32080
Y-0783
CALIBRATION GAS VOLUME DATA
Initial Dry Gas Meter Gas Volume, ft.3
Final Dry Gas Meter Gas Volume, ft.3
Net Dry Gas Meter Gas Volume (Vm), ft.3
CALIBRATION CONDITIONS DATA
Dry Gas Meter Temperature, °F:
Initial Inlet Temperature, °F
Final Inlet Temperature, °F
Initial Outlet Temperature, °F
Final Outlet Temperature, °F
Average Dry Gas Meter Temperature (tm), °F
Time, seconds
Orifice Meter AH, inches H2O
Barometric Pressure, in. Hg
Critical Orifice Inlet (Ambient) Temperature, °F:
Initial Ambient Temperature, °F
Final Ambient Temperature, °F
Avg. Critical Orifice Inlet Temperature (tarTlt)), °F
Pump Vacuum, in. Hg
COMPUTED CALIBRATION RESULTS
;ritical Orifice Gas Volume (Vcr(std)), standard ft.3
ry Gas Meter Gas Volume (Vm (eta)), standard ft.3
Dry Gas Meter Calibration Factor (Y)
Orifice Meter AH@
AVERAGE CALIBRATION RESULTS
Average Dry Gas Meter Calibration Factor (Y)
Average Orifice Meter AH@
CALIBRATION RESULTS COMPARISON
Criterion: Y Must Be Within 2% Of Average Y
Percent Difference Of Y From Average Y
Tolerance Result
COMPARISON WITH PRETEST RESULTS
Criterion: Y Must Be Within 5% Of Previous Y
% Difference Of Average Y From Previous Y
Tolerance Result
Run 1
588.598
592.772
4.174
79.0
79.0
74.0
75.0
76.8
600
0.530
30.01
72.0
72.0
72.0
18
4.175
4.123
1.013
1.692
1.010
1.692
0.23%
PASS
1 .43%
PASS
Run 2
592.772
596.969
4.197
79.0
80.0
75.0
76.0
77.5
600
0.530
30.01
73.0
73.0
73.0
18
4.171
4.140
1.007
1.692
Run 3
596.969
601.160
4.191
"' ; '^-"'M-V;": "•"•}.
81.0
81.0
77.0
77.0
79.0
600
0.530
30.01
74.0
74.0
74.0
4.167
4.123
1.011
1.691
0.28%
PASS
0.05%
PASS
Y = 1 010267285942600
-vi /I
Remarks:
CRORCALB-xIs 10/29/99 (rev. N12CALB112199 11/21/99 10:58 AM)
RCA#2 APPENDIX E
-------
CONSOLE CALIBRATION WORKSHEET
Job No. /OY7f>3- /i g^P" Console No.
Date //-^/^ ?? Orifice No.
Performed By ft. fJfoL K Factor
Barometer 3°'° / _ in. Hg. Previous Y -/.&JQ- &,o = _ 18 . 0 In. Hg .
Console vacuum gauge reading: /J/xt In. Hg.
Console vacuum gauge correction factor: fJ* In. Hg.
RUN #1 RUN #2 RUN #3
DGM Initial Volume:
Initial: SQS.W8
Final
DGM Inlet Temperature :
Initial: ?7 7^ gf
Final: 7? gO 81
DGM Outlet Temperature:
Initial: ?y 7.f 77
Final: if li 11
Time of run ( In Seconds ) : 6oO 6^° £oj
Orifice Delta H (in. H20) :
-------
METHOD 5 METERING CONSOLE CALIBRATION
CRITICAL ORIFICE BRACKETING DATA
MRI Project No.
Date:
Operator
Metering Console No.
Dry Gas Meter Factor (Y):
Orifice Used for the Calibration:
Ambient Temperature Meter No.
104703.1.002
11/21/99
D. Neai
N12
1.010
D12
Y-0783
Note' Critical orifice coefficients are in English units.
|
Critical Orifice Being Evaluated
Critical Orifice No.
D12
Critical Orifices Used For Bracketing
First Orifice
Critical Orifice No.
Coefficient (K1):
Second Orifice
Critical Orifice No.
Coefficient (K1):
D16
0.44410
D19
0.51210
CALIBRATION GAS VOLUME DATA
Initial Dry Gas Meter Gas Volume, ft.3
Final Dry Gas Meter Gas Volume, ft.3
Net Dry Gas Meter Gas Volume (VJ, ft.3
CALIBRATION CONDITIONS DATA
Dry Gas Meter Temperature, °F:
Initial Inlet Temperature, °F
Final Inlet Temperature, °F
Initial Outlet Temperature, °F
Final Outlet Temperature, °F
Average Dry Gas Meter Temperature (tm), °F
Time, seconds
Orifice Meter AH, inches H2O
Barometric Pressure, in. Hg
Critical Orifice Inlet (Ambient) Temperature, °F:
Initial Ambient Temperature, °F
Final Ambient Temperature, °F
Average Critical Orifice Inlet Temperature (tamb), "F
Pump Vacuum, in. Hg
COMPUTED CALIBRATION RESULTS
Critical Orifice Gas Volume (Vor(sta)), standard ft.3
Dry Gas Meter Gas Volume (Vm (sts)), standard ft.3
Factor (Y) Obtained With Bracketing Orifice
CRITICAL ORIFICE ACCEPTABILITY
Criterion: All Ys Must Be Within 2% Of All Other Ys
Larger % Difference Between Dry Gas Meter Factor (Y)
And Factor (Y) Obtained With The Bracketing Orifice
Larger % Difference Between Factors (Ys)
Obtained With Bracketing Orifices
Acceptability Result
First Orifice
601.801
607.618
5.817
82.0
84.0
78.0
78.0
80.5
600
1.000
30.01
74.0
75.0
74.5
18
5.766
5.713
1.009
0.07%
0.29%
Second Orifice
607.901
614.637
6.736
84.0
86.0
79.0
79.0
82.0
600
1.400
30.01
75.0
75.0
75.0
18
6.646
6.604
1.006
0.36%
All Orifices Are Acceptable
Remarks:
CRORBRKT.xls 10/29/98 (rev. N12BRKT112199 11/21/99 11:03 AM)
RCA#2 APPENDIX E
-------
CONSOLE BRACKETING WORKSHEET
Job No. /QYloj . /. oo2- Console No. ///>•
Date //"-^' _ Bracketing Orifice No . 1
Performed By • /l/» 6. _ K Factor O ,
Calibration Orifice No. ^/> Bracketing Orifice No. 2 2) /f
New Y Factor K Factor __£
Barometer 1?°^ °' in. Hg.
NOTE: Prior to running calibration, connect mercury manometer
to sample orifice. Turn on pump and bring mercury manometer up
to 18.0 in. Hg. Record mercury manometer and console vacuum
gauge readings 'below. Insert critical orifice into console
sample orifice. Set console vacuum gauge at 18.0 in. Hg. +/-
the console vacuum gauge correction factor calculated below.
Mercury manometer readings: A//* + A//C = 18.0 in. Hg.
Console vacuum gauge reading: - ;J/x> in. Hg.
Console vacuum gauge correction factor: A///fl in. Hg.
RUN #1 RUN #2
DGM Initial Volume:
Initial: 6°l
Final: 6o7. 6/8 6fif- 637
DGM Inlet Temperature:
Initial -.
Final: I? S6_
DGM Outlet Temperature:
Initial:
Final: 7g 7J_
Time of run ( In Seconds ): 600 600
Orifice Delta H(in. H20) : /, 0 /•
Room Temperature:
Initial: 7? 7
Final: 75"
Pump Vacuum (in. Hg ) : _ 18 . 0 _ _ 18 . 0
Calibration Records\Calibration Forms\conbrkws4d.doc pty/temgrOs^ -ft ' •£. Y"f>lv^ Revised 02/03/99
O
RCA#2 APPENDIX E
-------
M5 CONSOLE POST TEST CHECKLIST
Job No.
Date
Console No.
///>-
Performed By
Place a check (in black ink) in the space provided after the
required checks are performed.
1.
2.
3.
4.
5.
\ Perform positive leak check of Delta H manometer.
(See back of this sheet.)
V Leak check Delta P manometer.
tJ/A Clean pump.
\ Clean muffler jar(s).
Inspect/refill oiler jar.
\,
6. \/ Calibrate DGM
Note: Reading must be
Within +/-5.4°F
thermocouples :
DGM Inlet:
DGM Outlet:
Reference
Thermometer*
°F
t$->
£ S.f
DGM
Thermometer*
7. \, Digital clock/timer in place and functional.
8. \, Vacuum check. (Leak check at 25 in. Hg. vacuum. Leak
rate should be zero.)
V Check indicator lights.
9.
10.
11.
12.
13.
14.
If any of the above items were replaced or repaired, please
document that information below:
V Check thermocouple switched.
V Check fan.
v Check pump heater.
*\* Check heat controllers .
y Check Orsat pump and rotameter.
* Reference Thermometer:
Serial Number:
-------
Procedure for positive leak check Delta H manometer:
1. Pump must not be run prior to this test. Pump needs to be
cool in order to get an accurate reading.
2. Pump pressure and vacuum lines must be connected to console.
3. Null switch on console must be in the down position so
solenoid valve is open to the sampling stream as it is
during testing.
4. Plug meter exhaust and clamp off bottom tube from exhaust
which goes to the Orsat pump.
5. Plug sample orifice.
6. Close main flow control valve.
7. Open fine control valve.
8. Disconnect right side Delta H manometer tube on front of
console.
9. Blow into tubing until manometer reads 5 to 7 inches of
water, and clamp off.
There should be no change in manometer reading.
10. Make certain you remove plug and clamp from meter exhaust
immediately after this test to avoid damage to the meter
pump when pump is started up?
calibrcc\m5check 03/09/98
10
RCA#2 APPENDIX E
-------
STACK THERMOCOUPLE CALIBRATION DATA FORM
Job No.
Date
. /. QQ >•
//
Stack Thermocouple No. J/
-------
STACK THERMOCOUPLE CALIBRATION DATA FORM
Job No. /of 763. ! .
Date //
Stack Thermocouple No. 3/Sff
Probe No. 13
Performed By ^.
Pyrometer No.
Avg. Stack Temp.(°F) /BO
Reference Instrument: Hart Scientific Model No. 9100A, Serial
No. 84414 Dry-well, HDRC Handheld Block A. This instrument
is calibrated in accordance with ITS-90 and ANSI/NCSL Z540-1
Reference Instrument
Temp. ( °F )
Pyrometer Temp.
Temp. Difference
Temp. Difference
O.
/QJ
- o.
(ref. Temp., F + 460) - (pyro. Temp., F + 460]
(ref. Temp., F + 460)
X 100 < 1.5%
Calibration Records\Calibration Forms\STCHartdoc
Revised 10/29/98
12
RCA#2 APPENDIX E
-------
GOOSENECK THERMOCOUPLE CALIBRATION DATA FORM
Job No.
Date
Pyrometer No.
A///
Reference Thermometer
ASTM
Performed By &
Pyrometer Temp.
(°F)
68
68
Temp. Difference
Tolerance: +/- 2 °F
+ 0.^
o.c
Calibration Records\Calibration Forms\Gntccal.doc
Revised 10/28/98
13
RCA#2 APPENDIX E
-------
GOOSENECK THERMOCOUPLE CALIBRATION DATA FORM
Job No. _/'o0
Ref. Thermometer
Temperature (°F)
^^
"w^frt' t LS
67
Pyrometer Temp.
CF)
/r
^j'
Temp. DifTerence
Tolerance: +/- 2 °F
-Ag
-}<*>
Calibration Records\Calibration Forms\Gntccal.doc
Revised 10/28/98
14
RCA#2 APPENDK E
-------
Tvoe S Pitot Tube Inspection Data Form
Pitot Tube #: (3 Date: /X^Aff Performed By:
Probe #: 8
Pitot tube assembly level?
Pitot tube openings damaged?
a, = _0 °
Y = 0 °, 9 =
z = A sin Y Q
co = A sin 6 (?
(in),
Calibration required?
Comments:
I/ Yes
Yes (explain below)
A =
(in)
(in); (< 0.125 in)
(in); (< 0.03125 in)
(in), DT = 0,2%
Yes // No
No
No
(in)
A Tube Axis TT ~ -=^
( £_^—
^ >*»
Longitudinal
Tube Axis —*• —
0.48 CM < Dt < 0.95 CM
(3/16 in.) (3/8 in.)
Transverse
Tube Axis
Transverse
Tube Axis
Calibration Records\CaIibration Forms\newpitotdoc
RCA#2 APPENDIX E
01/18/99
/J
n/ul"
15
-------
Type S Pitot Tube Inspection Data Form
Pitot Tube #:
Probe #:
Date:
Job#:
Pitot tube assembly level?
Pitot tube openings damaged?
Pi = _6
Y = _
z = A sin Y
cp = A sin 8
PA =
6 =
Performed By:
6.0
Calibration required?
Comments:
Yes
Yes (explain below)
(in)
(in); (< 0.03125 in)
(in),
Yes
No
J/l
No
No
(in)
16
-Ik,
A - Side Plane
Longitudinal (,
A Tube Axis — -,
Ftowt
Longitudinal r
Tube Axis -*— f
| •! Note:
DT A \X l1^. f l.Q5Dt
-------
ON SITE MERCURY BAROMETER READING CORRECTION
AND AfccRQiiJ SAi\Gftr Tf» mperattire: ;IH,I>H in Hg
Correction K>r GiriVfly: -o,»X5 in. Hn
R«auiiiU Coiiufckrd FuJ tsfriviiy: bO.uo ui.
t 0. No.:
usinntnj; 30.tX> in. Hu
«.«a«f»r**i«jf» «.J»w* kesuii' wishin*' 1 IP. mi
After Auiusijnent: _________ ui. i iq
RCA#2 APPENDIX E
-------
GO
SAMPLING NOZZLE CALIBRATION CHECK DATA
MRI Project No. 4702.02.04.09
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
I
W
Nozzle I.D. Number or
Dedicated Sampling
Train Number
Nozzle Type
(Shape and Material
of Construction)
n
st
t/
COMMENTS:
Three Measured Diameters, inches
D1 D2 D3
OJ92-
Average
Diameter,
inches
ASM
Measured Bv
Date
a;fa J.sPC,
NOZZLCAX.WPD April 29, 1996 (lev. NOZZLCA1.WPO July 2, 1999)
-------
SAMPLING NOZZLE CALIBRATION CHECK DATA
MRI Project No. 104703.1.002.05.01
Client/Source: U.S. EPA OAQPS EMAD EMC / Cogentrix Unit 2A
Source Location: Rocky Mount, North Carolina
Sampling Location: Baghouse (Fabric Filter) Outlet Duct
Nozzle I.D. Number or
Dedicated Sampling
Train Number
Nozzle Type
(Shape and Material
of Construction)
Three Measured Diameters, inches
D1 D2 D3
Average
Diameter,
inches
I
K>
Measured Bv
Date
tr)
COMMENTS:
NOZZLCAX.WPD April 29, 1996 (rev NOZZLCA3.WPD November 1O, 1999)
-------
RCA #2 Appendix F
PM CEMS Data for Each Run
MRI-OPPT\R4703-0:-07 Appendices Covers WPD
-------
RCA #2 Testing - Run 30: High PM concentration
11/16/99 ESCP5B Durag 300-40 Durag F904K Moisture Temp.
Time raw mA raw ra mA raw mA % deg C
12:15
12:16
12:17
12:18
12:19
12:20
12:21
12:22
12:23
12:24
12:25
12:26
12:27
12:28
12:29
12:30
12:31
12:32
12:33
12:34
12:35
12:36
12:37
12:38
12:39
12:40
12:41
12:42
12:43
12:44
12:45
12:46
12:47
12:48
12:49
12:50
12:51
12:52
12:53
12:54
12:55
12:56
12:57
12:58
12:59
13:00
13:01
13:02
13:03
14.54
12.15
9.88
10.43
9.90
11.02
11.31
11.26
10.94
11.19
11.39
10.91
10.77
11.47
11.35
9.76
10.11
10.09
11.51
13.81
13.49
11.94
9.86
9.97
9.79
11.12
11.81
11.81
11.25
11.91
11.70
11.94
11.58
11.60
12.09
10.64
10.29
10.63
10.83
13.51
14.56
13.24
9.87
10.00
10.43
11.01
11.86
11.76
11.44
20.32 Moisture monitor not working properly
20.47 F904K not working properly
23.20
24.01
20.65
19.27
19.11
19.93
16.54
18.52
18.91
17.34
18.50
19.93
20.83
26.05
29.08
28.39
20.02
20.11
20.08
18.79
22.12
22.66
22.33
19.18
19.99
21.13
18.41
19.17
19.45
19.21
18.70
20.32
21.04
24.37
29.92
30.79
22.54
20.74
21.13
21.40
22.99
24.58
26.11
20.17
21.58
21.46
19.33
RCA#2 APPENDIX F
-------
13:04
13:05
13:06
13:07
13:08
13:09
13:10
13:11
13:12
13:13
13:14
13:15
13:16
13:17
13:18
13:19
13:20
13:21
13:22
13:23
13:24
13:25
13:26
13:27
13:28
13:29
13:30
13:31
13:32
13:33
13:34
13:35
13:36
13:37
13:38
13:39
13:40
13:41
13:42
13:43
13:44
13:45
13:46
13:47
13:48
13:50
13:51
13:52
13:52
13:53
13:54
13:55
11.61
11.91
11.71
11.85
11.39
11.75
10.72
10.22
11.37
11.15
13.45
13.91
14.47
10.45
9.96
10.84
10.70
11.59
11.70
11.79
11.48
11.74
12.46
11.58
11.32
11.50
11.75
9.78
10.82
10.67
11.62
13.52
13.69
11.01
10.00
10.67
10.55
11.69
11.82
12.72
10.84
11.46
11.96
11.92
11.15
12.21
10.09
10.16
10.32
10.60
12.59
14.26
18.12
18.44
19.16
17.98
20.11
20.08
21.91
27.91
27.55
24.82
18.94
20.53
20.74
21.22
23.92
25.36
20.86
21.55
20.35
20.65
17.64
18.38
19.29
17.56
19.14
19.48
21.73
28.33
28.69
27.25
17.44
19.87
20.62
19.36
23.17
24.46
22.12
20.38
20.50
21.34
18.00
19.09
19.41
18.34
18.85
20.23
25.36
28.45
28.30
27.52
17.98
21.43
RCA#2 APPENDIX F
-------
13:56
13:57
13:58
13:59
14:00
14:01
14:02
14:03
14:04
14:05
14:06
14:07
14.77
10.82
9.97
10.67
11.40
12.13
12.45
12.54
11.58
12.35
12.38
12.29
20.11
20.71
24.88
26.41
23.62
23.14
22.84
22.18
19.21
20.26
21.10
19.48
Average
Minimum
Maximum
Run 30
11.
49
9.76
14.
77
For P5B &
M17
Results
Train A
Train B
Average
300-40
mg/acm
27
22
25.
.9
.4
15
21.56 #DIV/0!
16.54 0.00
30.79 0.00
For RSD &
F904K
mg/dscm
40.8
33
36.9
Failed precision
#DIV/0!
0.00
0.00
test.
#DIV/0!
0.00
0.00
#DIV/0!
Moisture
%
11.1
11
11.05
RCA#2 APPENDIX F
-------
RCA #2 Testing - Run 31 : High PM concentration
11/16/99 ESCP5B Durag 300-40 Durag F904K Moisture Temp.
Time raw mA raw ra mA raw mA % deg C
15:20
15:21
15:22
15:23
15:24
15:25
15:26
15:27
15:28
15:29
15:30
15:31
15:32
15:33
15:34
15:35
15:36
15:37
15:38
15:39
15:40
15:41
15:42
15:43
15:44
15:45
15:46
15:47
15:48
15:49
15:50
15:51
15:52
15:53
15:54
15:55
15:56
15:57
15:58
15:59
16:00
16:01
16:02
16:03
16:04
16:05
16:06
16:07
16:08
10.91
10.12
11.60
12.05
12.06
11.90
11.92
11.95
11.92
11.78
12.38
12.56
9.98
10.39
11.32
12.13
14.43
14.65
12.08
9.93
10.89
9.95
10.87
11.54
11.21
11.58
11.75
12.71
12.98
11.47
12.22
12.34
11.18
10.45
11.12
11.41
13.77
14.82
14.07
10.16
10.58
10.88
10.85
11.74
11.94
12.28
11.47
11.58
11.71
27.10 Moisture monitor not working properly
23.53 F904K not working properly
21.40
21.37
22.15
19.45
19.16
19.72
18.98
19.69
20.53
20.80
26.35
29.50
28.90
18.64
20.29
20.71
21.28
22.87
24.73
23.17
20.65
20.62
20.71
19.09
19.57
21.19
22.09
19.06
21.31
22.36
25.27
33.34
32.50
26.20
20.11
21.67
23.35
21.94
25.09
26.89
21.67
21.04
21.61
20.77
18.53
19.21
20.44
RCA#2 APPENDIX F
-------
16:09
16:10
16:11
16:12
16:13
16:14
16:15
16:16
16:17
16:18
16:19
16:20
16:21
16:22
16:23
16:24
16:25
16:26
16:27
16:28
16:29
16:30
16:31
16:32
16:33
16:34
16:35
16:36
16:37
16:38
16:39
16:40
16:41
16:42
16:43
16:44
16:45
16:46
11.58
12.03
11.70
10.62
9.85
10.68
11.67
12.48
13.79
14.56
10.03
10.50
10.55
10.24
11.41
12.05
12.20
11.21
12.52
12.28
11.78
11.83
12.52
11.56
9.93
10.33
11.21
12.10
14.91
15.00
11.14
9.91
10.08
9.83
11.67
11.87
11.93
12.24
18.40
19.24
19.61
22.18
28.06
29.29
27.28
17.86
19.72
20.44
21.04
24.49
24.22
22.06
21.13
21.82
21.82
18.40
19.83
19.99
17.82
19.39
21.07
21.91
27.85
31.60
30.25
21.37
22.30
23.74
21.82
23.86
25.96
23.17
21.40
21.82
21.40
19.30
Average
Minimum
Maximum
11.69
9.83
15.00
22.41
17.82
33.34
#DIV/0!
0.00
0.00
#DIV/0!
0.00
0.00
#DIV/0!
0.00
0.00
#DIV/0!
RCA#2 APPENDIX F
-------
Run 31
For P5B &
M17 300-40
Results mg/acm
Train A
Train B
Average
25.4
25.4
Single point 16.1
For RSD &
F904K
mg/dscm
37.8
37.8
23.7
Moisture
%
12.2
12.2
11
RCA#2 APPENDIX F
-------
RCA #2 Testing - Run 32: Mid-high PM concentration
11/17/99 ESCP5B Durag 300-40 Durag F904K Moisture
Time raw mA raw ra mA raw mA %
8:54
8:55
8:56
8:57
8:58
8:59
9:00
9:01
9:02
9:03
9:04
9:05
9:06
9:07
9:08
9:09
9:10
9:11
9:12
9:13
9:14
9:15
9:16
9:17
9:18
9:19
9:20
9:21
9:22
9:23
9:24
9:25
9:26
9:27
9:28
9:29
9:30
9:31
9:32
9:33
9:34
9:35
9:36
9:37
9:38
9:39
9:40
9:41
9:42
9.30
9.82
10.07
9.88
10.08
10.08
10.24
10.68
9.47
10.10
10.10
8.97
8.65
9.03
9.74
10.67
11.26
13.48
8.50
8.46
8.83
8.78
9.55
9.86
9.68
9.44
9.61
10.08
10.18
10.29
10.02
9.91
9.02
8.85
9.48
10.88
11.82
11.86
8.94
8.92
9.06
8.81
9.84
9.84
9.96
9.45
10.44
10.86
10.22
20.95
17.38
17.41
17.72
15.32
15.50
16.62
16.95
15.00
17.02
17.29
19.33
24.19
23.95
20.74
15.18
17.26
17.49
16.57
18.78
19.46
15.87
16.68
16.53
16.42
13.89
14.49
15.32
14.16
16.62
16.89
18.28
23.23
23.26
24.37
15.38
16.90
17.34
16.14
19.24
19.72
18.94
18.24
17.69
18.30
15.19
16.34
17.02
15.75
F904K broken 10.62
10.74
10.38
10.40
10.44
10.92
10.92
10.80
10.56
10.98
10.98
10.86
10.74
10.50
10.50
10.86
10.86
10.86
10.74
10.62
10.26
10.26
10.50
10.62
10.50
10.38
10.53
10.68
10.31
10.62
10.62
10.74
10.50
10.62
10.62
10.50
10.38
10.50
10.50
10.38
10.50
10.50
10.62
10.74
10.62
10.62
10.74
10.62
10.26
Temp.
degC
82
82
82
83
84
84
84
84
84
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
83
84
84
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
RCA#2 APPENDIX F
-------
9:43
9:44
9:45
9:46
9:47
9:48
9:49
9:50
9:51
9:52
9:53
9:54
9:55
9:56
9:57
9:58
9:59
10:00
10:01
10:02
10:03
10:04
10:05
10:06
10:07
10:08
10:09
10:10
10:11
10:12
10:13
10:14
Average
Minimum
Maximum
Run 32
M17
Results
Train A
Train B
Average
Single point
9.62
10.04
10.62
8.90
9.88
9.71
10.40
12.47
12.65
10.53
8.97
9.55
9.44
10.17
10.46
11.42
10.47
11.20
11.19
10.85
10.32
10.14
11.22
9.65
9.02
9.53
9.99
12.07
12.11
11.39
8.62
9.36
10.06
8.46
13.48
For P5B &
300-40
mg/acm
19.1
19.1
11.9
16.88
17.57
17.68
23.11
25.18
26.29
16.08
18.64
18.97
17.86
21.73
22.48
22.06
18.56
19.15
20.14
18.20
18.23
17.75
17.49
17.52
18.74
19.99
24.04
26.02
24.94
20.05
18.17
18.78
18.90
19.00
20.98
18.64
13.89
26.29
For RSD &
F904K
mg/dscm
27.8
27.8
17.5
10.50
10.50
10.50
10.38
10.38
10.38
10.38
10.26
10.26
10.38
10.62
10.86
10.74
10.86
11.10
10.86
10.74
10.86
10.74
10.38
10.50
10.50
10.38
10.26
10.26
10.50
10.38
10.38
10.50
10.50
10.38
10.62
10.57
10.26
11.10
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82.20
82.00
84.00
180
Moisture
%
11.3
11.3
11.9
RCA#2 APPENDIX F
-------
RCA #2 Testing - Run 33: Mid-high PM concentration
11/17/99 ESCP5B Durag 300-40 Durag F904K Moisture
Time raw mA raw ra mA raw mA %
11:33
11:34
11:35
11:36
11:37
11:38
11:38
11:39
11:40
11:41
11:42
11:43
11:44
11:45
11:46
11:47
11:48
11:49
11:50
11:51
11:52
11:53
11:54
11:55
11:56
11:57
11:58
11:59
12:00
12:01
12:02
12:03
12:04
12:05
12:06
12:07
12:08
12:09
12:10
12:11
12:12
12:13
12:14
12:15
12:16
12:17
12:18
12:19
12:20
11.74
9.38
9.20
9.64
9.51
10.48
10.34
10.90
10.01
9.77
10.23
10.26
9.49
10.08
10.26
9.05
9.52
9.37
9.77
11.37
11.45
11.32
8.60
9.31
8.74
8.67
9.83
9.68
9.76
9.30
9.47
9.93
9.35
9.26
9.69
8.78
8.26
8.30
9.12
10.53
11.21
11.29
8.68
8.75
9.07
9.48
10.33
10.17
10.68
20.62
20.05
20.95
22.57
18.48
19.51
19.54
19.78
17.65
16.10
15.89
15.88
15.10
16.78
17.24
20.17
24.79
25.42
20.32
16.29
17.90
18.07
18.46
19.42
20.62
16.30
17.51
17.90
16.63
13.93
14.59
15.41
14.73
15.93
16.59
16.86
20.80
20.95
20.47
13.84
16.19
16.85
17.55
19.60
21.04
20.23
19.03
18.66
18.93
F904K broken 10.20
10.32
10.32
10.32
10.44
10.56
10.56
10.56
10.56
10.44
10.44
10.32
10.20
10.44
10.32
10.44
10.68
10.68
10.68
10.68
10.44
10.68
11.05
11.05
11.05
10.92
11.05
11.01
10.86
10.98
11.10
10.98
10.74
10.86
10.98
10.98
10.74
10.62
10.62
10.50
10.62
10.74
10.86
10.86
11.10
10.98
11.10
11.10
11.10
Temp.
degC
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
83
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
RCA#2 APPENDIX F
-------
12:21 9.74 15.08 11.10 82
12:22 10.03 15.91 11.10 82
12:23 10.16 16.47 11.23 82
12:24 9.78 14.59 10.98 82
12:25 9.09 15.51 10.98 82
12:26 9.36 16.44 10.86 82
12:27 9.13 17.86 10.85 82
12:28 8.00 21.67 10.68 80
12:29 8.58 23.14 10.68 80
12:30 8.82 23.23 10.71 81
12:31 9.87 15.75 10.62 82
12:32 11.34 17.07 10.62 82
12:33 11.98 17.75 10.74 82
12:34 9.15 17.38 10.74 82
12:35 8.95 19.48 10.62 82
12:36 8.71 20.20 10.62 82
12:37 8.84 18.58 10.38 82
12:38 9.86 18.00 10.26 82
12:39 9.51 17.84 10.65 83
12:40 9.92 17.62 10.80 84
12:41 9.36 14.50 10.92 84
12:42 9.46 14.71 11.05 84
12:43 9.59 15.10 11.01 83
12:44 9.43 14.44 10.86 82
12:45 8.86 14.34 10.74 82
12:46 9.28 16.51 10.86 82
12:47 9.46 16.75 10.86 82
12:48 8.40 20.26 10.74 82
12:49 8.44 22.24 10.62 82
12:50 8.92 24.82 10.62 82
12:51 9.12 15.93 10.62 82
12:52 10.88 15.27 10.50 82
12:53 10.90 15.70 10.50 82
12:54 9.46 16.18 10.50 82
12:55 8.58 16.73 10.38 82
12:56 8.68 18.41 10.50 82
12:57 8.64, 19.21 10.43 84
12:58 9.02 16.29 10.56 84
12:59 9.67 17.16 10.56 84
13:00 9.93 17.65 10.56 84
13:01 9.37 16.03 10.80 84
13:02 10.01 16.18 10.64 83
13:03 10.10 16.05 11.05 84
13:04 10.13 16.49 10.92 84
13:05 9.45 13.64 10.56 84
13:06 9.64 14.80 10.68 84
13:07 9.14 15.34 10.68 84
13:08 8.69 17.68 10.56 84
13:09 7.85 20.05 10.20 84
13:10 8.21 20.23 10.07 84
13:11 8.88 17.57 9.95 84
13:12 9.75 13.67 9.83 84
10
RCA#2 APPENDIX F
-------
13:13
13:14
13:15
13:16
13:17
13:18
13:19
13:20
13:21
13:22
13:23
13:24
10.57
11.79
8.19
8.46
9.08
8.92
9.96
10.26
10.11
9.95
10.28
10.31
15.09
17.12
15.52
19.72
20.44
17.59
18.87
18.85
18.15
15.53
15.87
16.33
9.95
10.07
10.32
10.32
10.44
10.20
10.56
10.70
10.50
10.50
10.62
10.74
84
84
84
84
84
84
84
85
86
86
86
86
Average
Minimum
Maximum
Run 33
9.60
7.85
11.98
17.77
13.64
25.42
10.66
9.83
11.23
83.05
80.00
86.00
181
For P5B &
M17 300-40
Results mg/acm
Train A
Train B
Average
19.2
17.7
18.45
For RSD &
F904K
mg/dscm
28.3
26
27.15
Moisture
12^3
11.6
11.95
RCA#2 APPENDIX F
11
-------
RCA #2 Testing - Run 34: Medium-high PM concentration
11/17/99 ESCP5B Durag 300-40 Durag F904K Moisture
Time raw mA raw ra mA raw mA %
14:50
14:51
14:52
14:53
14:54
14:55
14:56
14:57
14:58
14:59
15:00
15:01
15:02
15:03
15:04
15:05
15:06
15:07
15:08
15:09
15:10
15:11
15:12
15:13
15:14
15:15
15:16
15:17
15:18
15:19
15:20
15:21
15:22
15:23
15:24
15:25
15:26
15:27
15:28
15:29
15:30
15:31
15:32
15:33
15:34
15:35
15:36
15:37
15:38
8.89
9.50
9.06
10.47
11.56
11.48
9.13
8.99
9.05
9.19
10.21
10.50
10.78
9.45
9.74
9.69
9.83
9.52
9.72
10.04
8.20
8.42
8.41
9.67
11.30
11.29
9.54
8.50
8.55
8.24
8.86
9.14
9.44
8.72
9.05
9.61
9.52
9.38
9.39
9.45
8.70
8.56
9.42
8.93
10.72
10.86
10.76
8.17
8.60
23.29
23.89
25.51
14.85
17.75
17.07
17.26
20.86
22.57
20.74
19.93
20.80
20.23
16.22
15.42
15.39
15.08
15.26
15.53
16.04
19.15
21.46
21.64
15.65
15.51
16.00
16.24
17.82
18.47
18.25
15.60
16.28
15.99
13.73
13.64
14.45
14.66
13.47
15.28
15.75
17.20
22.42
21.67
18.52
15.37
16.11
17.16
16.59
18.70
F904K broken 10.80
10.80
10.80
10.80
10.80
10.56
10.68
10.80
10.80
10.80
10.80
10.80
10.80
10.56
10.68
10.68
10.44
10.44
10.56
10.44
10.56
10.56
10.68
10.56
10.56
10.68
10.68
10.56
10.68
10.68
10.68
10.68
10.68
10.68
10.68
10.68
10.56
10.44
10.68
10.80
10.80
10.68
10.80
10.68
10.68
10.56
10.56
10.68
10.68
Temp.
degC
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
12
RCA#2 APPENDIX F
-------
15:39
15:40
15:41
15:42
15:43
15:44
15:45
15:46
15:47
15:48
15:49
15:50
15:51
15:52
15:53
15:54
15:55
15:56
15:57
15:58
15:59
16:00
16:01
16:02
16:03
16:04
16:05
16:06
16:07
16:08
16:09
16:10
16:11
16:12
16:13
16:14
16:15
Average
Minimum
Maximum
8.56
8.71
9.16
9.50
9.55
9.60
9.81
9.98
9.74
9.83
9.98
8.87
8.57
9.17
8.78
10.40
11.03
11.67
8.17
8.47
8.30
8.50
9.02
9.70
9.79
8.92
9.43
9.51
9.52
8.89
9.07
8.84
7.95
8.31
8.57
9.12
10.71
P5B
9.42
7.95
11.67
18.77
15.61
16.14
16.66
17.07
14.54
15.25
15.93
14.74
16.05
16.43
18.07
22.24
23.65
21.49
14.65
16.56
16.88
16.48
18.14
18.97
16.75
15.97
16.93
16.43
13.40
14.08
14.90
13.79
14.57
15.21
15.56
19.69
20.89
21.13
14.06
15.69
DR 300-40
17.32
13.40
25.51
F904K
10.56
10.20
10.56
11.05
10.92
10.92
11.05
11.05
10.79
10.74
10.74
10.74
10.67
10.80
10.80
10.68
10.80
10.80
10.68
10.68
10.68
10.56
10.68
10.56
10.44
10.32
10.44
10.56
10.32
10.68
10.80
10.92
10.77
10.74
10.74
10.62
10.62
Moisture
10.68
10.20
11.05
84
84
84
84
84
84
84
84
84
82
82
82
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
83
82
82
82
82
Temp
83.83
82.00
84.00
183
RCA#2 APPENDIX F
13
-------
Run 34
For P5B &
M17 300-40
Results mg/acm
Train A
Train B
Average
10.3
10.3
Single point 11.3
For RSD &
F904K
mg/dscm
15.3
15.3
16.7
Moisture
%
13
13
12.5
14
RCA#2 APPENDIX F
-------
RCA #2 Testing - Run 35: Medium PM concentration
11/18/99 ESCP5B Durag 300-40 Durag F904K Moisture Temp.
degC
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
Time
8:52
8:53
8:54
8:55
8:56
8:57
8:58
8:59
9:00
9:01
9:02
9:03
9:04
9:05
9:06
9:07
9:08
9:09
9:10
9:11
9:12
9:13
9:14
9:15
9:16
9:17
9:18
9:19
9:20
9:21
9:22
9:23
9:24
9:25
9:26
9:27
9:28
9:29
9:30
9:31
9:32
9:33
9:34
9:35
9:36
9:37
9:38
9:39
9:40
raw mA
7.31
7.51
8.01
8.16
7.42
7.70
7.92
7.91
7.56
7.45
7.65
7.18
7.25
7.20
7.20
8.10
8.58
8.53
6.77
6.94
6.98
7.21
7.53
7.72
7.79
7.25
7.74
7.79
7.65
7.66
7.67
7.71
7.17
7.37
7.44
8.45
9.10
9.32
7.56
7.23
7.55
7.83
7.98
8.24
8.43
7.82
8.24
8.41
8.46
raw ra mA
14.08
11.57
12.25
12.36
10.93
10.31
10.62
10.93
10.03
10.55
10.87
12.05
15.23
15.35
13.57
10.27
11.50
11.24
11.23
12.97
13.68
11.67
11.86
12.17
11.65
9.70
10.33
10.65
10.46
10.69
11.31
12.19
15.57
16.49
17.03
11.06
12.36
12.28
12.18
14.27
15.73
14.23
12.89
13.66
13.39
11.90
12.18
12.20
12.35
raw mA
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
6.82
6.82
6.82
6.82
6.82
6.82
6.82
6.82
6.82
6.82
6.82
6.82
6.82
6.58
6.50
6.50
6.50
6.50
6.50
6.50
6.50
6.50
6.50
6.50
6.50
%
10.68
10.80
10.80
10.80
10.68
10.80
10.80
10.80
10.32
10.68
10.68
10.68
10.68
10.68
10.68
10.56
10.68
10.68
10.68
10.68
10.80
10.80
10.92
10.92
10.80
10.80
10.92
10.80
10.32
10.56
10.56
10.68
10.80
10.80
10.80
10.68
10.80
10.80
10.80
10.68
10.68
10.68
10.68
10.68
10.68
10.44
10.68
10.68
10.32
15
RCA#2 APPENDIX F
-------
9:41
9:42
9:43
9:44
9:45
9:46
9:47
9:48
9:49
9:50
9:51
9:52
9:53
9:54
9:55
9:56
9:57
9:58
9:59
10:00
10:01
10:02
10:03
10:04
10:05
10:06
10:07
10:08
10:09
10:10
10:11
10:12
10:13
10:14
10:15
10:16
10:17
10:18
10:19
10:20
10:21
10:22
10:23
10:24
10:25
10:26
10:27
10:28
8.14
8.44
8.69
7.63
7.71
7.65
8.43
9.44
9.58
8.46
7.30
7.38
8.15
8.06
8.30
8.35
7.77
8.27
8.40
8.40
8.03
8.16
8.44
7.88
7.98
7.54
7.79
9.17
9.53
9.38
7.57
8.15
8.43
12.49
13.78
14.08
17.85
19.39
18.88
13.73
13.57
13.64
13.46
14.92
15.64
15.91
13.33
14.11
14.35
12.44
11.91
12.70
12.78
12.44
13.26
13.82
14.83
18.35
18.57
14.76
13.03
13.41
14.68
15.60
17.25
18.36
6.50
6.97
7.13
7.13
7.13
7.13
7.13
7.13
7.13
7.13
7.13
7.13
7.13
7.13
6.98
6.82
6.82
6.82
6.82
6.82
6.82
6.82
6.82
6.82
6.82
6.82
6.82
6.96
7.38
7.38
7.38
7.38
7.38
7.38
7.38
7.38
7.38
7.38
7.38
7.38
7.38
9.21
9.21
9.21
9.21
9.21
9.21
9.21
10.68
10.80
10.80
10.80
10.80
10.80
10.68
10.68
10.80
10.80
10.68
10.68
10.56
10.68
10.68
10.68
10.56
10.68
10.68
10.44
10.56
10.68
10.68
10.68
10.68
10.68
10.56
10.56
10.68
10.68
10.80
10.80
10.68
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
16
RCA#2 APPENDIX F
-------
Average
Minimum
Maximum
Run 35
P5B
7.95
6.77
9.58
DR 300-40
13.31
9.70
19.39
F904K
7.14
6.50
9.21
Moisture
10.70
10.32
10.92
Temp
84.00
84.00
84.00
183
For P5B &
M17 300-40
Results mg/acm
Train A
Train B
Average
13.6
13.6
Single point 7.7
For BSD &
F904K
mg/dscm
19.7
19.7
11.2
Moisture
%
12
12
11.4
RCA#2 APPENDIX F
17
-------
RCA #2 Testing - Run 36: Mid-high PM concentration
Temp.
degC
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
11/18/99
Time
11:05
11:06
11:07
11:08
11:09
11:10
11:11
11:12
11:13
11:14
11:15
11:16
11:17
11:18
11:19
11:20
11:21
11:22
11:23
11:24
11:25
11:26
11:27
11:28
11:29
11:30
11:31
11:32
11:33
11:34
11:35
11:36
11:37
11:38
11:39
11:40
11:41
11:42
11:43
11:44
11:45
11:46
11:47
11:48
11:49
11:50
11:51
11:52
11:53
ESC P5B
raw mA
10.23
10.82
11.60
12.08
13.58
13.88
12.00
10.51
10.72
11.13
11.54
12.04
12.68
12.21
12.46
12.88
13.00
11.94
12.33
11.98
11.28
10.41
10.23
10.79
12.69
12.84
12.30
9.38
9.13
10.26
9.75
10.99
11.08
11.20
11.02
11.21
11.26
11.52
10.50
10.32
10.23
9.26
9.17
9.72
10.64
12.33
12.68
8.89
9.01
Durag 300-40
raw ra mA
29.80
33.52
33.28
23.11
22.63
23.11
24.04
25.78
30.16
29.95
24.85
25.81
25.09
23.26
22.06
23.35
24.46
22.06
23.80
25.33
26.08
33.13
32.23
26.77
21.67
23.26
23.20
21.16
24.85
25.51
20.47
22.27
21.31
21.01
18.83
18.81
19.03
18.15
18.64
20.41
22.60
26.05
26.47
26.29
17.11
19.63
20.29
20.23
21.97
Durag F904K
raw mA
10.65
10.65
10.65
10.65
10.65
10.65
10.65
10.65
10.65
10.65
10.65
10.65
10.65
11.25
11.45
11.45
11.45
11.45
11.45
11.45
11.45
11.45
11.45
11.45
11.45
11.45
10.45
9.45
9.45
9.45
9.45
9.45
9.45
9.45
9.45
9.45
9.45
9.45
9.45
Moistur
%
10.44
10.32
10.32
10.20
10.20
10.32
10.44
10.44
10.68
10.68
10.68
10.56
10.68
10.56
10.56
10.56
10.56
10.20
10.32
10.32
10.32
10.20
10.20
10.20
10.20
10.20
10.20
10.20
10.20
10.20
10.07
10.20
10.20
10.07
10.20
10.20
10.20
9.95
10.20
10.32
10.44
10.32
10.44
10.32
10.32
10.32
10.32
10.32
10.44
18
RCA#2 APPENDIX F
-------
11:54
11:55
11:56
11:57
11:58
11:59
12:00
12:01
12:02
12:03
12:04
12:05
12:06
12:07
12:08
12:09
12:10
12:11
12:12
12:13
12:14
12:15
12:16
12:17
12:18
12:19
12:20
12:21
12:22
12:23
12:24
12:25
12:26
12:27
12:28
12:29
12:30
12:31
12:32
12:33
9.29
9.44
10.64
10.98
11.28
10.58
11.45
11.71
11.31
10.67
10.91
10.42
9.50
9.68
9.96
10.38
12.21
13.53
12.06
9.31
9.52
9.13
10.73
10.44
11.10
10.03
10.71
11.00
11.27
10.45
11.00
10.89
23.11
20.50
20.68
22.09
22.06
17.58
19.32
19.99
18.07
19.44
20.41
20.74
25.69
28.81
28.03
17.51
19.54
20.95
20.26
22.78
24.25
22.93
20.74
20.77
21.10
16.77
17.44
18.25
18.40
18.73
20.29
20.50
9.73
10.01
10.01
10.01
10.01
10.01
10.01
10.01
10.01
10.01
10.01
10.01
10.01
10.07
10.25
10.25
10.25
10.25
10.25
10.25
10.25
10.25
10.25
10.25
10.25
10.25
10.25
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.85
10.44
10.20
10.44
10.68
10.68
10.68
10.80
10.80
10.56
10.50
10.74
10.74
10.74
10.74
10.86
10.62
10.38
10.50
10.74
10.74
10.86
10.62
10.74
10.74
10.62
10.38
10.50
10.62
10.50
10.74
10.74
10.98
Average
Minimum
Maximum
P5B
11.00
8.89
13.88
DR 300-40
22.72
16.77
33.52
F904K
10.28
9.45
11.45
Moisture
10.45
9.95
10.98
84
84
84
84
84
84
84
84
84
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
Temp
83.43
82.00
84.00
182
RCA#2 APPENDIX F
19
-------
Run 36
For P5B &
M17 300-40
Results mg/acm
Train A
Train B
Average
26.6
26.6
Single point 15.3
For RSD &
F904K
mg/dscm
38.5
38.5
22.6
Moisture
%
11.6
11.6
12.5
20
RCA#2 APPENDIX F
-------
RCA #2 Testing - Run 37: High PM concentration
11/18-19/99 ESC P5B Durag 300-40 Durag F904K Moisture Temp.
degC
84
84
84
83
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
Time
23:24
23:25
23:26
23:27
23:28
23:29
23:30
23:31
23:32
23:33
23:34
23:35
23:36
23:37
23:38
23:39
23:40
23:41
23:42
23:43
23:44
23:45
23:46
23:47
23:48
23:49
23:50
23:51
23:52
23:53
23:54
23:55
23:56
23:57
23:58
23:59
0:02
0:03
0:04
0:05
0:06
0:07
0:08
0:09
0:10
0:11
0:12
0:13
0:14
raw mA
12.94
15.14
15.49
14.68
12.84
11.66
14.58
14.60
14.40
13.70
15.18
14.17
13.95
12.47
13.72
13.74
14.32
16.07
15.86
13.05
12.68
12.68
11.89
14.20
14.69
14.25
12.14
12.10
12.25
13.64
12.75
13.43
12.94
14.41
14.20
14.88
14.36
11.82
12.68
12.94
12.31
15.04
15.03
14.69
11.52
12.20
12.24
11.76
13.40
raw ra mA
22.75
25.72
26.62
25.48
20.02
19.90
24.31
26.86
27.22
23.65
24.19
24.61
25.84
30.40
32.32
31.24
20.89
23.14
23.38
24.94
29.89
30.40
25.75
22.42
23.29
23.53
18.88
19.90
19.18
19.48
19.55
18.61
19.48
25.33
25.93
26.74
25.42
23.98
29.83
31.03
26.17
21.40
21.97
21.52
23.74
27.31
27.70
19.93
21.61
raw mA
14.89
14.89
14.89
14.89
14.89
14.89
14.89
14.89
14.89
14.89
14.89
14.89
14.89
15.13
15.21
15.21
15.21
15.21
15.21
15.21
15.21
15.21
15.21
15.21
15.21
13.84
13.84
13.84
13.84
13.84
13.84
13.84
13.84
13.84
13.84
13.84
13.84
14.10
%
8.98
9.22
9.22
9.19
9.17
9.05
9.05
9.17
9.05
8.93
9.05
9.29
9.17
9.05
9.05
8.93
9.17
9.29
9.29
9.17
9.17
9.29
9.17
9.17
9.17
9.29
9.05
9.17
9.17
9.05
8.81
9.17
9.29
9.66
9.41
9.17
9.17
9.17
9.17
9.17
9.05
9.05
9.05
9.05
9.05
9.05
9.05
9.05
9.17
21
RCA#2 APPENDIX F
-------
0:15
0:16
0:17
0:18
0:19
0:20
0:21
0:22
0:23
0:24
0:25
0:26
0:27
0:28
0:29
0:30
0:31
0:32
0:33
0:34
0:35
0:36
0:37
0:38
0:39
0:40
0:41
0:42
0:43
0:44
0:45
0:46
0:47
0:48
0:49
0:50
0:51
0:52
0:53
13.19
12.79
12.29
11.27
10.98
12.17
11.39
12.87
13.09
13.43
14.10
13.67
13.68
14.46
14.80
13.38
12.25
14.21
14.43
15.62
15.86
14.08
12.08
12.66
11.83
13.13
13.38
14.01
13.59
11.49
20.62
20.35
17.71
17.96
16.44
17.22
18.24
17.33
19.42
24.31
25.12
23.41
22.24
24.94
25.06
26.38
30.67
30.49
23.23
22.27
23.02
21.37
27.61
29.02
26.53
21.52
23.02
21.82
21.04
19.63
14.89
14.89
14.89
14.89
14.89
14.89
14.89
14.89
14.89
14.89
14.89
14.89
14.89
14.41
14.41
14.41
14.41
14.41
14.41
14.41
14.41
14.41
14.41
14.41
14.41
14.41
15.31
15.61
15.61
15.61
15.61
15.61
15.61
15.61
15.61
15.61
15.61
15.61
15.61
9.05
8.81
8.93
9.05
9.05
9.05
8.81
9.17
9.29
9.17
9.17
8.93
9.05
9.05
8.93
9.05
9.17
9.05
9.05
9.17
9.17
9.17
9.05
9.17
9.17
9.17
9.29
9.29
9.05
8.93
Average
Minimum
Maximum
P5B
13.44
10.98
16.07
DR 300-40
23.69
16.44
32.32
F904K
14.80
13.84
15.61
Moisture
9.12
8.81
9.66
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
Temp
82.09
82.00
84.00
180
22
RCA#2 APPENDIX F
-------
Run 37
For P5B &
M17 300-40
Results mg/acm
Train A
Train B
Average
57.6
57.6
Single point 36.8
For RSD &
F904K
mg/dscm
80.2
80.2
51.1
Moisture
%
10.5
10.5
9.8
RCA#2 APPENDIX F
23
-------
RCA#2 Testing - Run 38: Mid-high PM concentration
11/19/99 ESCP5B Durag 300-40 Durag F904K Moisture Temp.
deg C
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
83
84
84
84
84
83
82
82
82
Time
1:37
1:38
1:39
1:40
1:41
1:42
1:43
1:44
1:45
1:46
1:47
1:48
1:49
1:50
1:51
1:52
1:53
1:54
1:55
1:56
1:57
1:58
1:59
2:00
2:01
2:02
2:03
2:04
2:05
2:06
2:07
2:08
2:09
2:10
2:11
2:12
2:13
2:14
2:15
2:16
2:17
2:18
2:19
2:20
2:21
2:22
2:23
2:24
2:25
raw mA
8.83
9.38
9.81
9.87
10.59
10.64
11.00
9.39
9.49
9.47
9.18
8.93
9.99
9.74
9.85
10.05
10.01
10.47
10.55
10.36
11.75
11.32
10.79
11.61
11.24
12.11
10.09
10.67
10.58
11.61
12.15
12.49
11.04
9.66
9.98
10.06
10.33
10.69
11.93
10.39
9.59
9.83
9.94
10.34
9.71
10.16
9.69
9.87
10.48
raw ra mA
18.35
20.80
20.83
15.11
15.00
16.03
16.18
13.44
13.51
13.96
14.30
14.09
15.01
14.38
13.72
14.57
14.35
13.84
14.76
16.96
19.57
20.50
18.37
19.96
19.69
20.05
21.91
23.41
23.20
15.94
17.39
16.96
16.18
20.05
21.16
20.05
15.59
15.29
17.12
15.54
14.09
14.28
14.44
15.05
14.73
14.07
14.80
15.03
14.52
raw mA
11.21
11.21
11.21
11.21
11.21
11.21
11.21
11.21
11.21
11.21
11.21
11.21
11.41
11.61
11.61
11.61
11.61
11.61
11.61
11.61
11.61
11.61
11.61
11.61
11.61
11.49
11.13
11.13
11.13
11.13
11.13
11.13
11.13
11.13
11.13
11.13
11.13
11.13
%
8.93
8.69
8.81
8.81
8.93
9.05
9.05
8.81
8.93
9.05
8.93
8.93
8.69
8.93
8.93
8.81
8.93
8.81
8.81
8.93
9.05
8.93
8.69
8.69
8.69
8.81
8.81
8.81
8.81
8.93
9.17
9.05
9.05
8.93
8.81
8.81
8.81
8.81
8.57
8.45
8.58
8.74
8.86
8.86
8.86
8.95
8.93
8.93
9.05
24
RCA#2 APPENDIX F
-------
2:26
2:27
2:28
2:29
2:30
2:31
2:32
2:33
2:34
2:35
2:36
2:37
2:38
2:39
2:40
2:41
2:42
2:43
2:44
2:45
2:46
2:47
2:48
2:49
2:50
2:51
2:52
2:53
2:54
2:55
2:56
2:57
2:58
2:59
3:00
3:01
3:02
3:03
3:04
3:05
10.04
9.95
10.67
10.13
11.17
11.74
12.20
11.46
12.30
12.47
11.83
9.83
10.89
10.92
11.42
12.52
12.85
11.30
9.37
9.66
10.08
10.74
10.75
10.78
9.99
9.11
10.17
9.47
10.69
10.16
10.40
10.09
14.52
14.38
15.27
15.80
17.87
20.08
20.44
18.25
18.83
19.36
19.78
21.94
22.66
22.21
16.12
17.31
17.79
16.98
19.36
21.07
20.47
15.38
15.89
15.50
14.95
14.89
13.86
14.24
14.09
13.74
14.88
14.63
11.13
9.78
9.78
9.78
9.78
9.78
9.78
9.78
9.78
9.78
9.78
9.78
9.78
9.78
11.69
12.33
12.33
12.33
12.33
12.33
12.33
12.33
12.33
12.33
12.33
12.33
12.33
11.57
10.81
10.81
10.81
10.81
10.81
10.81
10.81
10.81
10.81
10.81
10.81
10.81
8.93
8.93
8.93
8.81
8.93
9.05
9.05
8.57
8.69
8.57
8.57
8.57
8.81
8.93
8.81
8.81
8.93
8.93
8.81
8.93
8.81
8.93
8.93
8.93
8.69
8.81
8.81
8.81
8.81
8.81
8.69
8.69
Average
Minimum
Maximum
P5B
10.53
8.83
12.85
DR 300-40
16.92
13.44
23.41
F904K
11.15
9.78
12.33
Moisture
8.85
8.45
9.17
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
Temp
82.12
82.00
84.00
180
RCA#2 APPENDIX F
25
-------
Run 38
For P5B &
M17 300-40
Results mg/acm
Train A
Train B
Average
36.7
36.7
Single point 24.1
For RSD &
F904K
mg/dscm
51.7
51.7
33.5
Moisture
%
11.4
11.4
10.1
26
RCA#2 APPENDIX F
-------
RCA #2 Testing - Run 39: Mid PM concentration
11/19/99 ESC P5B Durag 300-40 Durag F904K Moisture Temp.
degC
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
Time
3:36
3:37
3:37
3:38
3:39
3:40
3:41
3:42
3:43
3:44
3:45
3:46
3:47
3:48
3:49
3:50
3:51
3:52
3:53
3:54
3:55
3:56
3:57
3:58
3:59
4:00
4:01
4:02
4:03
4:04
4:05
4:06
4:07
4:08
4:09
4:10
4:11
4:12
4:13
4:14
4:15
4:16
4:17
4:18
4:19
4:20
4:21
4:22
4:23
raw mA
10.59
10.97
10.78
10.62
10.47
10.39
10.62
11.04
11.19
11.11
10.84
12.00
12.06
12.55
11.43
11.82
11.95
11.91
10.37
11.52
11.30
12.22
13.74
13.26
10.80
11.19
10.39
10.25
10.90
11.70
11.25
9.40
9.90
10.65
10.20
10.75
10.09
10.01
10.77
10.19
10.69
11.49
10.17
10.93
11.02
11.03
11.31
11.91
12.31
raw ra mA
15.93
15.23
15.04
14.76
15.50
16.42
14.78
15.95
15.33
15.58
16.41
19.18
22.06
21.88
19.21
19.93
20.62
21.10
25.15
27.16
25.63
17.23
18.67
18.67
17.92
22.45
23.83
18.85
17.48
16.97
17.14
15.24
13.65
14.56
13.97
14.05
14.00
14.33
15.13
14.95
14.54
15.65
16.27
16.95
16.60
16.01
15.73
21.85
22.27
raw mA
11.21
11.21
11.21
11.21
11.21
11.21
11.21
11.21
11.21
11.21
11.21
11.21
11.21
11.51
11.61
11.61
11.61
11.61
11.61
11.61
11.61
11.61
11.61
11.61
11.61
11.61
11.33
11.05
11.05
11.05
11.05
11.05
11.05
11.05
11.05
11.05
11.05
11.05
%
8.93
8.93
8.93
8.93
8.93
8.93
8.93
8.93
8.93
8.81
8.81
9.05
9.05
9.05
8.69
8.81
8.93
8.93
8.93
8.93
8.93
8.81
8.93
8.93
8.93
8.93
8.81
8.69
8.93
8.93
8.93
8.69
8.81
8.93
8.93
8.93
8.93
9.05
9.05
8.93
9.05
8.93
8.93
8.93
8.93
8.93
9.05
9.05
9.05
27
RCA#2 APPENDIX F
-------
4:24
4:25
4:26
4:27
4:28
4:29
4:30
4:31
4:32
4:33
4:34
4:35
4:36
4:37
4:38
4:39
4:40
4:41
4:42
4:43
4:44
4:45
4:46
4:47
4:48
4:49
4:50
4:51
4:52
4:53
4:54
4:55
4:56
4:57
4:58
4:59
5:00
5:01
5:02
5:03
5:04
5:05
5:06
5:07
5:08
5:09
12.50
11.18
12.64
12.30
10.42
9.89
11.12
10.50
11.93
12.45
11.97
9.59
9.71
9.68
10.09
10.66
11.20
11.06
9.64
10.01
9.48
9.97
10.96
11.40
9.97
10.51
10.21
11.23
10.95
11.72
11.48
10.48
11.04
10.94
12.15
12.15
13.05
11.94
12.19
12.52
10.48
22.21
17.93
19.69
19.42
19.45
25.18
24.13
21.19
17.44
17.66
17.55
18.64
20.98
21.28
16.80
17.50
17.59
16.15
14.34
14.97
14.51
15.07
15.79
15.12
15.98
16.25
16.53
15.84
15.69
16.21
16.14
15.58
16.10
17.02
21.82
11.05
11.11
11.29
11.29
11.29
11.29
11.29
11.29
11.29
11.29
11.29
11.29
11.29
11.29
11.29
11.69
11.69
11.69
11.69
11.69
11.69
11.69
11.69
11.69
11.69
11.69
11.69
11.69
11.09
10.89
10.89
10.89
10.89
10.89
10.89
10.89
10.89
10.89
10.89
10.89
10.89
11.53
12.16
12.16
12.16
12.16
9.05
8.69
8.93
8.93
8.93
8.93
8.93
9.05
8.93
8.93
8.93
8.93
8.93
8.93
8.81
8.93
9.05
8.93
8.93
9.05
9.05
8.81
8.81
8.93
8.81
9.05
9.05
9.05
9.05
9.05
9.17
9.17
9.17
9.17
9.17
9.17
9.05
8.69
8.93
8.93
9.05
Average
Minimum
Maximum
P5B
11.08
9.40
13.74
DR 300-40
17.76
13.65
27.16
F904K
11.34
10.89
12.16
Moisture
8.95
8.69
9.17
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
82
Temp
82.00
82.00
82.00
180
28
RCA#2 APPENDIX F
-------
Run 39
For P5B &
M17 300-40
Results mg/acm
Train A
Train B
Average
35.6
35.6
Single point 24.5
For BSD &
F904K
mg/dscm
49.5
49.5
34.1
Moisture
%
10.4
10.4
10.3
RCA#2 APPENDIX F
29
-------
RCA #2 Testing - Run 40: Low PM concentration
Temp.
deg C
84
84
84
84
84
84
83
82
82
82
82
82
82
82
82
83
84
84
84
84
84
84
82
82
82
82
82
82
83
84
84
84
84
84
84
82
82
82
82
82
82
82
82
82
83
84
84
84
84
11/20/99
Time
9:00
9:01
9:02
9:03
9:04
9:05
9:06
9:07
9:08
9:09
9:10
9:11
9:12
9:13
9:14
9:15
9:16
. 9:17
9:18
9:19
9:20
9:21
9:22
9:23
9:24
9:25
9:26
9:27
9:28
9:29
9:30
9:31
9:32
9:33
9:34
9:35
9:36
9:37
9:38
9:39
9:40
9:41
9:42
9:43
9:44
9:45
9:46
9:47
9:48
ESC P5B
raw mA
6.49
6.75
6.82
6.59
6.49
6.30
6.53
6.70
6.33
6.53
6.79
6.81
7.54
7.77
7.93
6.40
6.42
6.66
6.69
6.93
6.84
6.84
6.18
6.21
6.16
6.22
6.10
6.28
6.16
6.28
6.38
6.32
6.23
6.45
6.29
6.45
6.43
6.46
6.32
6.63
6.54
6.54
6.48
6.82
6.49
6.50
6.62
6.76
6.71
Durag 300-40
raw ra mA
8.17
8.02
9.34
8.08
7.73
7.22
7.76
8.05
8.78
10.71
11.46
9.92
8.22
8.82
9.15
9.01
10.42
10.49
8.68
8.55
8.35
8.08
7.09
7.26
7.41
7.33
7.29
7.21
7.17
7.12
7.06
7.39
7.30
7.00
7.17
7.22
7.49
7.55
7.68
7.91
7.81
7.63
7.48
7.39
8.03
8.23
8.08
7.91
8.07
Durag F904K
raw mA
6.02
6.02
6.02
6.02
6.02
6.02
6.02
6.02
6.02
6.02
6.02
6.02
6.02
6.65
6.65
6.65
6.65
6.65
6.65
6.65
6.65
6.65
6.65
6.65
6.65
6.65
6.35
6.25
6.25
6.25
6.25
6.25
6.25
6.25
6.25
6.25
6.25
6.25
Moistur
%
10.07
10.20
10.32
9.71
9.10
8.01
7.99
7.97
8.09
8.09
8.21
8.21
8.33
8.69
8.81
8.96
8.98
8.86
8.62
8.50
8.25
8.00
7.85
7.72
7.48
7.36
7.24
7.24
7.50
7.53
7.65
8.13
8.38
8.62
9.10
9.41
9.29
9.05
9.29
9.17
9.05
8.93
8.93
8.93
9.31
9.71
9.83
9.71
9.71
30
RCAS2 APPENDIX F
-------
9:49
9:50
9:51
9:52
9:53
9:54
9:55
9:56
9:57
9:58
9:59
10:00
10:01
10:02
10:03
10:04
10:05
10:06
10:07
10:08
10:09
10:10
10:11
10:12
10:13
10:14
10:15
10:16
10:17
10:18
10:19
10:20
10:21
10:22
10:23
10:24
10:25
10:26
10:27
10:28
10:29
6.79
6.79
6.77
7.45
7.31
7.23
7.11
6.93
7.28
6.66
6.70
6.93
7.18
7.82
8.29
8.33
6.76
7.41
7.44
7.61
8.81
9.67
11.22
11.30
12.85
13.84
13.46
13.30
13.77
13.51
10.82
11.55
8.59
8.33
8.39
9.19
9.45
9.52
8.99
8.96
9.22
9.77
11.79
12.06
11.77
9.17
9.55
10.19
10.68
12.73
14.83
12.97
12.93
14.73
16.80
18.55
22.75
25.69
23.53
25.36
27.52
29.20
35.86
40.03
6.25
6.25
6.25
6.25
6.25
6.25
6.25
6.25
6.25
6.25
6.25
6.25
6.25
6.25
6.15
5.85
5.85
5.85
5.85
5.85
5.85
5.85
5.85
5.85
5.85
5.85
5.85
6.15
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
9.71
9.71
9.71
9.83
9.95
9.95
9.59
9.71
9.70
9.54
9.55
9.59
9.83
10.07
10.20
10.07
10.20
10.44
10.56
10.56
10.80
11.05
11.05
11.17
11.29
11.29
10.92
10.80
10.56
10.44
10.32
10.20
Average
Minimum
Maximum
P5B
7.54
6.10
13.84
DR 300-40
11.07
7.00
40.03
F904K
6.35
5.85
7.05
Moisture
9.29
7.24
11.29
84
84
84
84
84
84
84
84
84
82
83
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
Temp
83.35
82.00
84.00
182
RCA#2 APPENDIX F
31
-------
Run 40
For P5B &
M17 300-40
Results mg/acm
Train A
Average
12.2
12.2
Single point 10.2
For BSD &
F904K
mg/dscm
17.5
17.5
14.7
Moisture
%
12.4
12.4
12.4
32
RCA#2 APPENDIX F
-------
RCA #2 Testing - Run 41: Low PM concentration
11/20/99 ESC P5B Durag 300-40 Durag F904K Moisture Temp.
degC
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
83
82
Time
11:12
11:13
11:14
11:15
11:16
11:17
11:18
11:19
11:20
11:21
11:22
11:23
11:24
11:25
11:26
11:27
11:28
11:29
11:30
11:31
11:32
11:33
11:34
11:35
11:36
11:37
11:38
11:39
11:40
11:41
11:42
11:43
11:44
11:45
11:46
11:47
11:48
11:49
11:50
11:51
11:52
11:53
11:54
11:55
11:56
11:57
11:58
11:59
12:00
raw mA
6.58
7.00
6.77
6.77
7.31
7.56
7.25
6.54
6.86
6.88
7.08
7.17
7.12
7.59
7.47
7.98
7.42
7.72
7.86
7.74
7.78
8.06
7.70
8.72
8.48
8.34
8.05
8.23
8.43
7.40
7.27
7.30
7.27
9.15
9.32
8.92
6.84
7.12
7.42
7.55
8.16
8.26
7.84
7.18
6.71
6.89
7.05
6.85
6.80
raw ra mA
10.13
11.52
12.17
9.24
9.46
9.77
9.93
8.28
8.74
8.45
9.13
9.45
9.74
9.46
9.57
10.11
10.14
9.79
9.63
10.49
10.42
10.59
10.32
12.83
12.89
12.39
11.85
11.85
11.86
12.74
16.02
15.53
13.26
11.05
11.58
11.46
11.87
13.89
14.13
11.34
12.15
11.45
10.90
8.83
8.73
8.68
8.49
8.78
9.02
raw mA
7.30
7.30
7.30
7.30
7.30
7.30
7.30
7.30
7.30
7.30
7.30
7.30
7.30
7.60
7.70
7.70
7.70
7.70
7.70
7.70
7.70
7.70
7.70
7.70
7.70
7.70
7.94
8.18
8.18
8.18
8.18
8.18
8.18
8.18
8.17
8.18
8.18
8.18
%
8.62
8.62
8.50
8.25
8.50
8.62
8.62
8.62
8.62
8.62
8.74
8.74
8.74
8.62
8.38
8.62
8.74
8.62
8.50
8.50
8.50
8.50
8.50
8.74
8.74
8.74
8.50
8.62
8.62
8.62
8.62
8.62
8.62
8.62
8.62
8.86
8.86
8.98
8.98
8.74
8.98
8.86
8.62
8.62
8.62
8.74
8.74
8.71
9.17
33
RCA#2 APPENDIX F
-------
12:01
12:02
12:03
12:04
12:05
12:06
12:07
12:08
12:09
12:10
12:11
12:12
12:13
12:14
12:15
12:16
12:17
12:18
12:19
12:20
12:21
12:22
12:23
12:24
12:25
12:26
12:27
12:28
12:29
12:30
12:31
12:32
12:33
12:34
12:35
12:36
12:37
12:38
12:39
12:40
12:41
7.10
7.18
7.38
8.13
8.48
8.32
7.58
8.05
8.43
7.88
8.28
9.30
9.77
12.70
14.78
15.66
11.23
11.68
11.77
11.38
12.52
12.88
13.60
13.14
14.14
14.37
12.99
12.95
13.46
12.77
10.43
10.41
8.98
9.39
9.73
11.58
12.52
12.02
11.32
11.95
12.75
14.40
20.89
24.52
25.39
18.85
21.49
23.41
26.11
29.77
31.51
27.40
24.04
24.25
24.61
23.20
25.75
26.71
23.83
24.79
24.58
24.37
32.56
34.12
8.18
7.80
6.65
6.65
6.65
6.65
6.65
6.65
6.65
6.65
6.65
6.65
6.65
6.65
6.65
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
7.05
10.33
10.33
10.33
10.33
10.33
10.33
10.33
10.33
10.33
10.33
10.33
10.33
10.33
9.05
9.05
8.93
9.05
9.10
9.22
9.10
9.83
9.82
9.90
9.66
9.90
10.02
10.26
10.26
10.26
10.41
10.44
10.44
10.44
10.32
10.04
9.78
9.90
9.90
9.78
9.54
9.66
9.66
9.66
9.54
9.66
Average
Minimum
Maximum
P5B
8.87
6.54
15.66
DR 300-40
14.90
8.28
34.12
F904K
7.86
6.65
10.33
Moisture
9.10
8.25
10.44
82
82
82
82
84
84
84
84
84
82
82
82
82
82
82
82
83
84
84
84
84
83
82
82
82
82
82
82
82
82
82
82
Temp
83.42
82.00
84.00
182
34
RCA#2 APPENDIX F
-------
Run 41
For P5B &
M17 300-40
Results mg/acm
Train A
Average
24.1
24.1
Single poin 13.8
For BSD &
F904K
mg/dscm
34.7
34.7
20
Moisture
%
12.4
12.4
12.4
RCA#2 APPENDIX F
35
-------
RCA #2 Testing - Run 42: High PM concentration
11/20/99 ESC P5B Durag 300-40 Durag F904K Moisture Temp.
degC
84
84
84
85
86
86
86
86
86
86
86
86
85
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
Time
13:50
13:51
13:52
13:53
13:54
13:55
13:56
13:57
13:58
13:59
14:00
14:01
14:02
14:03
14:04
14:05
14:06
14:07
14:08
14:09
14:10
14:11
14:12
14:13
14:14
14:15
14:16
14:17
14:18
14:19
14:20
14:21
14:22
14:23
14:24
14:25
14:26
14:27
14:28
14:29
14:30
14:31
14:32
14:33
14:34
14:35
14:36
14:37
14:38
rawmA
14.93
15.56
12.29
14.61
15.48
16.87
19.73
19.96
16.55
17.04
17.37
15.88
15.98
16.69
18.27
18.22
19.67
19.39
18.54
15.40
16.70
16.86
12.36
10.48
10.61
10.52
12.42
12.54
10.16
8.48
8.69
8.79
8.87
9.43
9.52
8.87
8.67
8.80
9.12
7.96
8.70
9.61
8.29
8.16
8.97
9.17
11.30
12.34
11.26
raw ra mA
27.13
31.60
39.55
44.71
45.58
32.05
36.37
37.84
41.08
143.41
56.29
81.67
36.61
37.84
36.70
36.55
39.07
37.48
34.09
32.23
33.70
32.65
35.65
37.03
33.13
21.52
20.74
20.38
18.30
19.60
21.04
21.10
16.00
16.55
17.37
14.33
13.12
13.05
12.96
12.24
13.11
15.13
16.72
21.40
22.93
21.34
16.68
18.09
17.57
raw mA
12.01
12.01
12.01
12.01
12.01
12.01
12.01
12.01
12.01
12.01
12.01
12.01
12.01
13.28
13.28
13.28
13.28
13.28
13.28
13.28
13.28
13.28
13.28
13.28
13.28
13.28
10.53
9.61
9.61
9.61
9.61
9.61
9.61
9.61
9.61
9.61
9.61
%
8.50
8.74
8.74
8.88
.9.03
9.03
9.15
9.28
9.28
9.40
9.40
9.15
9.24
9.22
9.10
8.98
9.10
8.98
8.62
8.62
8.62
8.74
8.62
8.13
7.89
7.65
7.40
7.53
7.53
7.77
8.13
8.01
8.38
8.38
8.38
8.25
8.25
8.13
8.13
7.77
8.01
8.13
8.25
8.38
8.50
8.50
8.25
8.25
8.38
36
RCA#2 APPENDIX F
-------
14:39
14:40
14:41
14:42
14:43
14:44
14:45
14:46
14:47
14:48
14:49
14:50
14:51
14:52
14:53
14:54
14:55
14:56
14:57
14:58
14:58
14:59
15:00
15:01
15:01
15:02
15:03
15:04
15:05
15:06
15:07
15:08
15:09
15:10
15:11
15:12
15:13
15:14
15:15
15:16
15:17
15:18
15:19
15:20
15:21
15:22
15:23
15:24
15:25
15:26
8.92
9.27
9.74
9.93
11.78
11.80
12.11
12.12
11.99
12.82
10.65
11.70
12.36
10.34
9.82
9.92
10.73
12.38
13.93
13.98
12.84
12.44
10.81
10.84
10.79
11.50
13.38
13.42
13.44
13.68
16.00
16.18
15.14
16.47
17.17
16.12
17.68
21.61
22.30
19.87
21.88
21.58
20.95
20.86
22.63
22.57
19.93
21.82
23.62
23.50
29.71
30.55
31.15
18.79
22.18
22.06
22.09
22.75
27.04
28.24
28.87
23.98
25.12
23.89
24.10
24.49
29.44
31.90
30.82
32.98
35.59
38.08
9.61
9.61
9.74
9.78
9.78
9.78
9.78
9.78
9.78
9.78
9.78
9.78
9.78
9.78
9.78
9.81
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.85
9.97
10.09
10.09
10.09
10.09
10.09
10.09
10.09
10.09
10.09
10.09
10.09
10.09
10.85
13.13
13.13
13.13
13.13
13.13
13.13
8.25
8.13
8.13
8.01
8.25
8.38
8.13
8.25
8.50
8.74
8.38
8.50
8.38
8.38
8.25
8.25
8.13
8.01
8.25
8.25
8.25
8.25
8.25
8.38
8.38
8.13
8.38
8.50
8.25
8.50
8.86
8.98
8.86
9.22
9.35
9.35
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
84
37
RCA#2 APPENDIX F
-------
Average
Minimum
Maximum
P5B
12.74
7.96
19.96
DR 300-40
28.30
12.24
143.41
F904K
10.92
9.61
13.28
Moisture
8.47
7.40
9.40
Run 42
Temp
84.21
84.00
86.00
184
For P5B &
M17 300-40
Results mg/acm
Train A
Average
38.3
38.3
Single point 22.8
For BSD &
F904K
mg/dscm
55.4
55.4
32.8
Moisture
%
12.4
12.4
11.2
38
RCA#2 APPENDIX F
-------
RCA #2 Appendix G
Statistical Analysis Data and Graphs from Initial
Correlation and RCA Data
MR]-OPPT\R4703-02-07 Appendices Covers WPD
-------
ESC P5B - Linear
w
H
Q
O
IB
•
60
50
40
30
20
10
VL = Variable Load
LL = Low Load
y = 1 .89x - 7.50
LL •
VL
LL
-10
10
mA
12
14
* Init. Corr.
A RCA#1
«• 3 MET coal runs
• RCA#2
Correlation Line
25% Tl
+ 25% Tl
-------
Table G-l. ESC Light Scatter - Linear
Run
13
14
15
16
17
18
19
20
21
22
23
24
1
2
, 3
4
5
6
7
8
9
10
11
12
10
11
12
31
32
33
34
35
36
37
38
39
40
41
42
x(mA)
9.60
10.01
10.54
5.87
5.78
6.00
12.00
9.45
8.97
13.16
9.57
14.50
14.66
6.38
6.41
6.40
8.51
8.35
7.70
10.34
11.23
11.92
9.07
10.17
11.40
11.76
13.88
11.69
10.06
9.60
9.42
7.95
11.00
13.44
10.53
11.08
7.54
8.87
12.74
y (mg/acm)
11.61
13.92
14.47
3.03
2.68
3.20
16.33
10.52
9.42
15.39
8.76
18.66
28.09
1.90
2.55
2.59
9.77
8.29
11.30
22.12
24.05
26.62
12.97
19.10
26.13
27.76
32.28
25.40
19.10-
18.45
10.30
13.60
26.60
57.60
36.70
35.60
12.20
24.10
38.30
ylin
10.62
11.40 i
12.40
3.58 ;
3.41
3.83
15.16
10.34
9.43
17.35
10.57
19.88
RCA #1 data
Three MET coal runs during initial correlation tests.
RCA #2 data
RCA#2 APPENDIX G
-------
o
Durag DR 300-40 - Linear
60
VL = Variable Load
LL = Low Load
LL
y = 0.71 x- 0.82
LL
VL»
30
I
"§>
£
VL
10
12
16
20
24
28
-10
* Init. Corr.
A RCA#1
* 3 MET coal runs
• RCA#2
Correlation Line
25% Tl
+ 25% Tl
Range adjusted mA
co
-------
Table G-3. Durag Light Scatter - Linear
Run
13
14
15
16
17
18
19
20
21
22
23
24
1
2
3
4
5
6
7
8
9
10
11
12
10
11
12
31
32
33
34
35
36 '
37
38
39
40
41
42
x (mA) y (mg/acm)
15.45
17.22
19.36
6.42
6.44
7.28
20.93
15.80
14.32
24.54
15.68
30.88
28.77
6.11
6.59
6.75
11.72
11.92
10.80
16.22
18.60
21.53
12.62
14.59
20.06 =.
21.82-'"
27.83
22.41 ^
18.64-"'
17.77
17.32
13.31
22.72
23.69
16.92
17.76
11.07
14.90
28.30
11.61
13.92
14.47
3.03
2.68
3.20
16.33
10-.52
9.42
15.39
8.76
18.66
28.09
1.90
2.55
2.59
9.77
8.29
11.30
22.12
24.05
26.62
12.97
19.10
26.13
27.76
32.28
25.40
19.10
18.45;
10.30
13.50
26.60
57.60
36.70
35.50
12.20
24.10
38.30
ylin
10.14 i
11.39
12.91
3.73
3.75 ;
4.34 !
14.02
10.38
9.33
16.58
10.30 ;
21.08
RCA #1 data
Three MET coal runs during initial correlation tests.
RCA #2 data
RCA#2 APPENDIX G
-------
Durag F904K - Linear
w
8
>
5t
NJ
1
tn
R
»7l/
fin
yn
fin -
cri _
o
U) ._
u)
on -
on -
m -
n -
i
-m -
VL = Variable Load
LL = Low Load
LL
y = 3.37x- 12.38
VI •
VL • LL
• + ' ' '
t
* A ^--
**•
Emission Limit = 25,5 mg/dscm A ^^"^ ^ — ^
^--""T ^--^^1--"
^-^~ j^*^^ -'""'
*^
6 8 10 12 14 1
* Init. Corr.
A RCA#1
* 3 MET coal runs
• Dr'AWO
nL»r\fft
Correlation Line
25% Tl
+ 25% Tl
3
mA
-------
Table G-2. Durag Beta Gauge - Linear
Run
13
14
15
16
17
18
19
20
21
22
23
24
1
2
3
4
5
e
7
8
9
10
11
12
10
11
12
31
32
33
34
35
36
37
38
39
40
41
42
x (mA) y (mg/dscm)
8.58
9.24
9.98
5.04
5.09
5.21
10.48
8.07
8.05
10.95
8.08
12.57
14.20
5.04
5.07
4.99
7.30
6.99
6.88
9.71
10.71
11.65
7.57
8.42
11.74 '
11.71 ..
14.49
ProS-i £>»-<
''
/)
>'
7.14
10.28
14.80
11.15
11.34
6.35
7.86
10.92
17.20
21.10
21.75
4.60
4.00
4.80
24.40
16.10
14.30
23.25
13.05
28.35
43.05
2.90
3.95
4.00
14.80
12.65
17.40
33.65
36.60
41.00
19.45
28.65
39.50
41.80
49.55
)'K
-------
TECHNICAL REPORT DATA
(Please read Instructions on reverse before completing)
1. RfiPORT NO.
EPA-454/R-00-040d
3. RECIPIENT'S ACCESSION NO.
4. TITLE AND SUBTITLE
EVALUATION OF PARTICIPATE MATTER CONTINUOUS EMISSION
MONITORING SYSTEMS
Volume 4
5. REPORT DATE September 2000
6. PERFORMING ORGANIZATION CODE
7. AUTHOR(S) Dan Bivins
Emission Monitoring and Analysis Division
8. PERFORMING ORGANIZATION REPORT NO.
). PERFORMING ORGANIZATION NAME AND ADDRESS
U.S. Environmental Protection Agency
Office of Air Quality Planning and Standards
Research Triangle Park, NC 27711
10. PROGRAM ELEMENT NO.
11. CONTRACT/GRANT NO.
68-D-98-027
2. SPONSORING AGENCY NAME AND ADDRESS
Director
Office of Air Quality Planning and Standards
Office of Ak and Radiation
U.S. Environmental Protection Agency
Research Triangle Park, NC 27711
13. TYPE OF REPORT AND PERIOD COVERED
Final
14. SPONSORING AGENCY CODE
EPA/200/04
i. SUPPLEMENTARY NOTES
i. ABSTRACT
his final report describes an extended field demonstration of three particulate matter (PM) continuous
mission monitoring systems (CEMS) at a coal-fired boiler equipped with a lime slurry scrubber and
aghouse for air pollution control. The primary objectives of the field study were to: (1) demonstrate whether
le PM CEMS could provide reliable and accurate data over an extended period, (2) evaluate the PM CEMS
>r durability, data availability, and setup/maintenance requirements, and (3) determine whether the PM
EMS satisfy all the requirements of draft PS-11 and the quality assurance (QA) criteria specified in draft
rocedure 2, or determine if changes are needed in the requirements of PS-11 and/or Procedure 2. This
port presents the results of the study involving two different PM CEMS technologies (light scatter and beta
mge) at the coal-fired boiler. The report consists of five separate volumes.
KEY WORDS AND DOCUMENT ANALYSIS
DESCRIPTORS
•11
thod 17
icedure 2
•isture CEMS
•nonstranon
nculate Matter
CEMS
DISTRIBUTION STATEMENT
Release Unlimited
b. IDENTIFIERS/OPEN ENDED TERMS
Air Pollution control
19. SECURITY CLASS (Report]
Unclassified
20. SECURITY CLASS (Page)
Unclassified
c. COSATI Field/Group
21. NO. OF PAGES
280
22. PRICE
form 2220-1 (Rev. 4-77) PREVIOUS EDITION IS OBSOLETE
------- |