A | B | C | D | E | F | G | H | |
---|---|---|---|---|---|---|---|---|
1 | FORM ED603 | |||||||
2 | Baseline 1977 PSEL Emissions Data | |||||||
3 | And Netting Basis Determination | |||||||
4 | SP Newsprint Co. (Newberg, OR) | |||||||
5 | Permit Number: 36-6142 | |||||||
6 | ||||||||
7 | Pollutant: PARTICULATE MATTER (PM) | |||||||
8 | ||||||||
9 | Throughput | Emission Factor | Emissions | |||||
10 | Emissions Unit | Parameter | Annual | Unit | Rate | Unit | Reference | ton/yr |
12 | B67-EU (Boilers #6 and #7) | Natural Gas | 354.53 | MM ft3 | 2.5 | lb/MMft3 | DEQ EF05 | 0.4 |
13 | Residual Oil | 279.93 | Mgal | 20.8 | lb/Mgal | DEQ EF04 | 2.9 | |
14 | Boiler 6 & 7 Subtotal | 3.4 | ||||||
16 | Recovery Boiler #8 | Sulfite Pulp | 68,284 | ADT | 94 | ton/year | 1977 Monitoring Data | 94.0 |
19 | B9-EU (Boiler #9) | Steam produced | 906,400 | Mlbs steam | 0.307 | lb/Mlbs steam | VEF from STs | 139.1 |
20 | Natural Gas | 160.6 | MM ft3 | 2.5 | lb/MMft3 | DEQ EF05 | 0.2 | |
21 | Boiler #9 Subtotal | 139.3 | ||||||
23 | CHS-EU (Chip Cyclones) | Chips Handled | 782,000 | ODT | 0.0378 | lb/ODT(a) | 10/12/99 ST | 14.8 |
25 | MH-EU | |||||||
26 | Chip Recvg & Dist | Chips Processed | 782,000 | ODT | 0.002 | lb/ODT | EPA, 1977 | 0.78 |
27 | HF Recvg & Dist | Hog Fuel Processed | 67,900 | ODT | 0.0075 | lb/ODT | EPA, 1977 | 0.25 |
28 | Hammer Hog | Bark Processed | 175,000 | ODT | 0.048 | lb/ODT | EPA, 1977 | 4.20 |
29 | MH-EU Subtotal | 5.2 | ||||||
31 | CSP-EU (Chip Storage Piles) | Chips Stored | 782,000 | ODT | 0.006 | lb/ODT | AP-42 | 2.3 |
33 | HFSP-EU (HF Storage Piles) | Hog Fuel Stored | 67,900 | ODT | 0.07 | lb/ODT | AP-42 | 2.4 |
35 | Whole Log Chipper Mill (Note b) | Roundwood chipped | 31,351 | ODT | 0.35 | lb/ODT | EPA, 1977 | 5.5 |
37 | PM5-EU (Paper Machine #5) | Paper Produced | 156,853 | MDT | 0.0322 | lb/MDT | EF from STs | 2.5 |
39 | UPR-EU (Unpaved Roads) | Paper Produced | 156,853 | MDT | 0.1204 | lb/MDT | AP-42 13.2.2 | 9.4 |
41 | AI (Aggregate Insignificant) | 1.0 | ||||||
44 | PM TOTAL: | 280 | ||||||
45 | Notes: | EPA Method 5 corrected to ODEQ Method 5 --> | 1980 PSD -Boiler #10 | 588 | ||||
46 | (a) Composite emission factor derived from one source tests of individual cyclones multiplied | |||||||
47 | by 3 based on process and testing variability. | Netting Basis = | 868 | |||||
48 | (b) Name corrected from Sawmill to Whole Log Chipper Mill to clarify the actual operation. |
A | B | C | D | E | F | G | H | |
---|---|---|---|---|---|---|---|---|
1 | FORM ED603 | |||||||
2 | Baseline 1977 PSEL Emissions Data | |||||||
3 | And Netting Basis Determination | |||||||
4 | SP Newsprint Co. (Newberg, OR) | |||||||
5 | Permit Number: 36-6142 | |||||||
6 | ||||||||
7 | Pollutant: PM10 | |||||||
8 | ||||||||
9 | Throughput | Emission Factor | Emissions | |||||
10 | Emissions Unit | Parameter | Annual | Unit | Rate | Unit | Reference | ton/yr |
12 | B67-EU (Boilers #6 and #7) | Natural Gas | 354.53 | MM ft3 | 2.5 | lb/MMft3 | DEQ EF05 | 0.4 |
13 | Residual Oil | 279.93 | Mgal | 19.9 | lb/Mgal | DEQ EF04 | 2.8 | |
14 | Boiler 6 & 7 Subtotal | 3.2 | ||||||
16 | Recovery Boiler #8 | Sulfite Pulp | 68,284 | ADT | 89.30 | ton/year | DEQ EF03 (95%) | 89.3 |
19 | B9-EU (Boiler #9) | Steam produced | 906,400 | Mlbs steam | 0.29 | lb/Mlbs steam | DEQ EF03 (a) | 132.2 |
20 | Natural Gas | 160.6 | MM ft3 | 2.5 | lb/MMft3 | DEQ EF05 | 0.2 | |
21 | Boiler #9 Subtotal | 132.4 | ||||||
23 | CHS-EU (Chip Cyclones) | Chips Handled | 782,000 | ODT | 0.0189 | lb/ODT | DEQ EF03 (50% PM) | 7.4 |
25 | MH-EU | |||||||
26 | Chip Recvg & Dist | Chips Processed | 782,000 | ODT | 0.001 | lb/ODT | See Note (b) | 0.39 |
27 | HF Recvg & Dist | Hog Fuel Processed | 67,900 | ODT | 0.0038 | lb/ODT | See Note (b) | 0.13 |
28 | Hammer Hog | Bark Processed | 175,000 | ODT | 0.024 | lb/ODT | See Note (b) | 2.10 |
29 | MH-EU Subtotal | 2.6 | ||||||
31 | CSP-EU (Chip Storage Piles) | Chips Stored | 782,000 | ODT | 0.003 | lb/ODT | See Note (b) | 1.2 |
33 | HFSP-EU (HF Storage Piles) | Hog Fuel Stored | 67,900 | ODT | 0.035 | lb/ODT | See Note (b) | 1.2 |
35 | Whole Log Chipper Mill (Note c) | Roundwood chipped | 31,351 | ODT | 0.175 | lb/ODT | See Note (b) | 2.7 |
37 | PM5-EU (Paper Machine #5) | Paper Produced | 156,853 | MDT | 0.0161 | lb/MDT | See Note (b) | 1.3 |
39 | UPR-EU (Unpaved Roads) | Paper Produced | 156,853 | MDT | 0.0321 | lb/MDT | AP-42 13.2.2 | 2.5 |
41 | AI (Aggregate Insignificant) | 1.0 | ||||||
44 | PM10 TOTAL: | 245 | ||||||
45 | EPA Method 5 corrected to ODEQ Method 5 --> | 1980 PSD -Boiler #10 | 588 | |||||
46 | Notes: | |||||||
47 | (a) Boiler with high efficiency wet scrubber: PM10 = 95% PM = .95 x 0.307 =0.292 lb/Mlb steam | Netting Basis = | 833 | |||||
49 | (b) PM10 emissions estimated to be 50% of PM emissions. | |||||||
51 | (c) Name corrected from Sawmill to Whole Log Chipper Mill to clarify the actual operation. |
A | B | C | D | E | F | G | H | |
---|---|---|---|---|---|---|---|---|
1 | FORM ED603 | |||||||
2 | Baseline 1977 PSEL Emissions Data | |||||||
3 | And Netting Basis Determination | |||||||
4 | SP Newsprint Co. (Newberg, OR) | |||||||
5 | Permit Number: 36-6142 | |||||||
6 | ||||||||
7 | Pollutant: CO | |||||||
8 | ||||||||
9 | Throughput | Emission Factor | Emissions | |||||
10 | Emissions Unit | Parameter | Annual | Unit | Rate | Unit | Reference | ton/yr |
12 | B67-EU (Boilers #6 and #7) | Natural Gas | 354.53 | MM ft3 | 42 | lb/MMft3 | 10/99 ST | 7.4 |
13 | Residual Oil | 279.93 | Mgal | 5 | lb/Mgal | DEQ EF04 | 0.7 | |
14 | Boiler 6 & 7 Subtotal | 8.1 | ||||||
16 | Recovery Boiler #8 | Sulfite Pulp | 68,284 | ADT | 24.8 | lb/ADT | DEQ(a) | 846.7 |
19 | B9-EU (Boiler #9) | Steam produced | 906,400 | Mlb | 0.51 | lb/Mlb | VEF from STs | 231.1 |
20 | Natural Gas | 160.6 | MM ft3 | 84 | lb/MMft3 | DEQ EF05 | 6.7 | |
21 | Boiler #9 Subtotal | 237.9 | ||||||
25 | CO TOTAL: | 1,093 | ||||||
26 | Notes: | 1980 PSD - Boiler #10 | 569 | |||||
27 | (a) AP-42 emission factor adusted to 80% flow (NCASI) | |||||||
28 | Netting Basis = | 1,662 | ||||||
29 | 2007 Unassigned Emissions Reduction | -140 | ||||||
30 | Purposed Netting Basis = | 1,522 |
A | B | C | D | E | F | G | H | |
---|---|---|---|---|---|---|---|---|
1 | FORM ED603 | |||||||
2 | Baseline 1977 PSEL Emissions Data | |||||||
3 | And Netting Basis Determination | |||||||
4 | SP Newsprint Co. (Newberg, OR) | |||||||
5 | Permit Number: 36-6142 | |||||||
6 | ||||||||
7 | Pollutant: NOx | |||||||
8 | ||||||||
9 | Throughput | Emission Factor | Emissions | |||||
10 | Emissions Unit | Parameter | Annual | Unit | Rate | Unit | Reference | ton/yr |
12 | B67-EU (Boilers #6 and #7) | Natural Gas | 354.53 | MM ft3 | 101 | lb/MMft3 | 10/99 ST | 17.9 |
13 | Residual Oil | 279.93 | Mgal | 47 | lb/Mgal | DEQ EF04 | 6.6 | |
14 | Boiler 6 & 7 Subtotal | 24.5 | ||||||
16 | Recovery Boiler #8 | Sulfite Pulp | 68,284 | ADT | 5.77 | lb/ADT | ST @ Oregon City | 197.0 |
19 | B9-EU (Boiler #9) | Steam produced | 906,400 | Mlb | 0.62 | lb/Mlb | VEF from STs | 281.0 |
20 | Natural Gas | 160.6 | MM ft3 | 76 | lb/MMft3 | EF from STs | 6.1 | |
21 | Boiler #9 Subtotal | 287.1 | ||||||
25 | NOx TOTAL: | 509 | ||||||
26 | 1980 PSD - Boiler #10 | 2,850 | ||||||
28 | Netting Basis = | 3,359 | ||||||
29 | 2007 Unassigned Emissions Reduction | -37 | ||||||
30 | Purposed Netting Basis = | 3,322 |
A | B | C | D | E | F | G | H | |
---|---|---|---|---|---|---|---|---|
1 | FORM ED603 | |||||||
2 | Baseline 1977 PSEL Emissions Data | |||||||
3 | And Netting Basis Determination | |||||||
4 | SP Newsprint Co. (Newberg, OR) | |||||||
5 | Permit Number: 36-6142 | |||||||
6 | ||||||||
7 | Pollutant: SO2 | |||||||
8 | ||||||||
9 | Throughput | Emission Factor | Emissions | |||||
10 | Emissions Unit | Parameter | Annual | Unit | Rate | Unit | Reference | ton/yr |
12 | B67-EU (Boilers #6 and #7) | Natural Gas | 354.53 | MM ft3 | 1.7 | lb/MMft3 | DEQ EF05 | 0.3 |
13 | Residual Oil | 279.93 | Mgal | 275 | lb/Mgal | DEQ EF04 | 38.5 | |
14 | Boiler 6 & 7 Subtotal | 38.8 | ||||||
16 | Recovery Boiler #8 | Sulfite Pulp | 68,284 | ADT | 402 | Tons/year | 1977 Monitoring | 402.0 |
19 | B9-EU (Boiler #9) | Steam produced | 906,400 | Mlb | 0.327 | lb/Mlb | VEF from STs | 148.2 |
20 | Used Oil (generated on site) | 8,000 | gallons | 0.079 | lb/gal | material balance | 0.3 | |
21 | Natural Gas | 160.6 | MM ft3 | 1.7 | lb/MMft3 | DEQ EF05 | 0.1 | |
22 | Boiler #9 Subtotal | 148.6 | ||||||
24 | SO2 Adsorption Tower | Sulfite Pulp | 68,284 | ADT | 48 | tons/year | 1977 Monitoring | 48.0 |
26 | Miscellaneous Vents | Sulfite Pulp | 68,284 | ADT | 1.0 | lb/ADT | Regulatory Limit | 34.1 |
29 | SO2 TOTAL: | 672 | ||||||
30 | Notes: | Boiler #10 Adjustment(a) | 249 | |||||
31 | (a) Adjustment based on the installation of #10 Boiler as reviewed & approved by the Department. | |||||||
32 | Netting Basis = | 921 |
A | B | C | D | E | F | G | H | |
---|---|---|---|---|---|---|---|---|
1 | FORM ED603 | |||||||
2 | Baseline 1977 PSEL Emissions Data | |||||||
3 | And Netting Basis Determination | |||||||
4 | SP Newsprint Co. (Newberg, OR) | |||||||
5 | Permit Number: 36-6142 | |||||||
6 | ||||||||
7 | Pollutant: H2SO4 Mist | |||||||
8 | ||||||||
9 | Throughput | Emission Factor | Emissions | |||||
10 | Emissions Unit | Parameter | Annual | Unit | Rate(b) | Unit | Reference | ton/yr |
12 | B67-EU (Boilers #6 and #7) | Natural Gas | 354.53 | MM ft3 | 0.034 | lb/MMft3 | See Note (a) | 0.0 |
13 | Residual Oil | 279.93 | Mgal | 5.5 | lb/Mgal | See Note (a) | 0.8 | |
14 | Boiler 6 & 7 Subtotal | 0.8 | ||||||
16 | Recovery Boiler #8 | Sulfite Pulp | 68,284 | ADT | 8.04 | Tons/year | See Note (a) | 8.0 |
19 | B9-EU (Boiler #9) | Steam produced | 906,400 | Mlb | 0.00654 | lb/Mlb | See Note (a) | 3.0 |
20 | Used Oil (generated on site) | 8,000 | gallons | 0.00158 | lb/gal | See Note (a) | 0.0 | |
21 | Natural Gas | 160.6 | MM ft3 | 0.034 | lb/MMft3 | See Note (a) | 0.0 | |
22 | Boiler #9 Subtotal | 3.0 | ||||||
24 | SO2 Adsorption Tower | Sulfite Pulp | 68,284 | ADT | 0.96 | tons/year | See Note (a) | 1.0 |
26 | Miscellaneous Vents | Sulfite Pulp | 68,284 | ADT | 0.0153 | lb/ADT | See Note (a) | 0.5 |
29 | H2SO4 TOTAL: | 13.3 | ||||||
30 | Notes: | Boiler #10 Adjustment(b) | 5.0 | |||||
32 | (a) Emission rates are the SO2 rates converted to H2SO4 by multiplying by 0.0153. | Netting Basis = | 18 | |||||
33 | AP-42 Chapter 1.3 (5th edition, 1998) states that 1-5% of SO2 sulfur is converted to SO3 (H2SO4) in boilers. | |||||||
34 | NCASI SARA 313, March 2002, states that 0.26% to 1.0% of the SO2 sulfur is converted to SO3 (H2SO4) in boilers. | |||||||
35 | Calculation based on 1% of the SO2 sulfur converted to SO3, which combines with H2O to form H2SO4. | |||||||
36 | 1 lb SO2 = 0.5 lb S (based on molecular wt ratio, 32 S/ 64 SO2) | |||||||
37 | 0.5 lb S = 1.53 lb H2SO4 (based on molecular wt ratio 98 H2SO4/32 S) | |||||||
38 | (1.53 lb H2SO4/ lb SO2) x 1% = 0.0153 lb H2SO4/ lb SO2 | |||||||
39 | B10-EU 2007 Pre-Boiler MACT testing indicates the above ratio to be 0.02 lb H2SO4/ lb SO2 so the combustion emission factors were changed. | |||||||
40 | (b) Adjustment based on the installation of #10 Boiler as reviewed & approved by the Department. |
A | B | C | D | E | F | G | H | |
---|---|---|---|---|---|---|---|---|
1 | FORM ED603 | |||||||
2 | Baseline 1977 PSEL Emissions Data | |||||||
3 | And Netting Basis Determination | |||||||
4 | SP Newsprint Co. (Newberg, OR) | |||||||
5 | Permit Number: 36-6142 | |||||||
6 | ||||||||
7 | Pollutant: VOC | |||||||
8 | ||||||||
9 | Throughput | Emission Factor | Emissions | |||||
10 | Emissions Unit | Parameter | Annual | Unit | Rate | Unit | Reference | tonC/yr |
12 | B67-EU (Boilers #6 and #7) | Natural Gas | 354.53 | MM ft3 | 5.5 | lb/MMft3 | DEQ EF05 | 1.0 |
13 | Residual Oil | 279.93 | Mgal | 0.76 | lb/Mgal | DEQ EF04 | 0.1 | |
14 | Boiler 6 & 7 Subtotal | 1.1 | ||||||
16 | Recovery Boiler #8 | Sulfite Pulp | 68,284 | ADT | 4.00 | lb/ADT | 1977 Monitoring | 136.6 |
19 | B9-EU (Boiler #9) | Steam produced | 906,400 | Mlb | 0.065 | lb/Mlb | VEF from STs | 29.5 |
20 | Natural Gas | 160.6 | MM ft3 | 5.5 | lb/MMft3 | DEQ EF05 | 0.4 | |
21 | Boiler #9 Subtotal | 29.9 | ||||||
23 | Sulfite Pulp Dryer | Sulfite Pulp | 20,521 | ADT | 0.1 | lb/ADT | NCASI TB 681 | 1.0 |
26 | KU-EU (Kerosene Cleaning) | Kerosene used | 1,041 | Gallons | 0.54 | lb/gal | DEQ Approved EF | 0.3 |
28 | TMP-EU (Chip Refining) | Thermo Mechnical Pulp | 110,953 | ADT | 0.28 | lbC/ADT(c) | NCASI TB 677 | 15.5 |
30 | PM5-EU (Paper Machine #5) | Paper produced | 156,853 | MDT | 0.281 | lb/MDT | EF from STs | 22.0 |
33 | WWT-EU | Wastewater treated | 4,782 | MM Gal | 7.7 | lb/MM Gal | process model | 18.4 |
34 | (Wastewater Treatment) | |||||||
36 | CHS-EU (Chip Cyclones) | Chips Handled | 782,000 | ODT | 0.00065 | lb/ODT(a) | NCASI, 1995 | 0.25 |
38 | HFSP-EU (Hog Fuel Storage Pile) | Hog Fuel Stored | 67,900 | ODT | 0.05 | lb/ODT | NCASI, 1995 | 1.7 |
40 | CSP-EU (Chip Storage Pile) | Chips Stored | 782,000 | ODT | 0.18 | lb/ODT | NCASI, 1995 | 70.4 |
42 | MH-EU | |||||||
43 | Chip Recvg & Dist | Chips Processed | 782,000 | ODT | 0.0002 | lb/ODT | NCASI, 1995 | 0.08 |
44 | Chip Washing | Chips Processed | 782,000 | ODT | 0.0002 | lb/ODT | NCASI, 1995 | 0.08 |
45 | HF Recvg & Dist | Hog Fuel Processesd | 67,900 | ODT | 0.0002 | lb/ODT | NCASI, 1995 | 0.01 |
46 | Hammer Hog | Bark Processed | 175,000 | ODT | 0.05 | lb/ODT | NCASI, 1995 | 4.4 |
47 | MH-EU Subtotal | 4.5 | ||||||
49 | Whole Log Chipper Mill (Note d) | Roundwood chipped | 31,351 | ODT | 0.05 | lb/ODT | NCASI, 1995 | 0.8 |
51 | Agg. Insignificant | 1.0 | ||||||
54 | VOC TOTAL: | 303 | ||||||
55 | 1980 PSD - Boiler #10(b) | 189 | ||||||
57 | Netting Basis = | 492 | ||||||
58 | Notes: | |||||||
59 | (a) Composite emission factor based on the aggregate of the individual devices and the NCASI emission factor of 0.0002 lb/ODT. | |||||||
60 | ||||||||
61 | (b) The 1980 PSD Permit issued by EPA allowed 569 tons as C per year of VOC emissions based on the source off setting that amount. | |||||||
62 | 189 tons were actually off set, thus the adjustment to baseline is limited to that amount. | |||||||
64 | (c) Emission Factor converted, 0.31 lbC/ODT to 0.28 lbC/ADT | |||||||
66 | (d) Name corrected from Sawmill to Whole Log Chipper Mill to clarify the actual operation. |
A | B | C | D | E | F | G | H | |
---|---|---|---|---|---|---|---|---|
1 | FORM ED603 | |||||||
2 | Baseline 1977 PSEL Emissions Data | |||||||
3 | And Netting Basis Determination | |||||||
4 | SP Newsprint Co. (Newberg, OR) | |||||||
5 | Permit Number: 36-6142 | |||||||
6 | ||||||||
7 | Pollutant: TRS | |||||||
8 | ||||||||
9 | Throughput | Emission Factor | Emissions | |||||
10 | Emissions Unit | Parameter | Annual | Unit | Rate | Unit | Reference | ton/yr |
12 | WWT-EU | Wastewater | 4,782.0 | MMgal | 12.1 | lb/MMgal | Engineering Estimate (CH2M Hill) | 29 |
17 | Wastewater Treatment and Handling | TRS TOTAL: | 29 | |||||
18 | ||||||||
19 | Netting Basis = | 29 |
A | B | C | D | E | F | G | H | |
---|---|---|---|---|---|---|---|---|
1 | FORM ED603 | |||||||
2 | Baseline 1977 PSEL Emissions Data | |||||||
3 | And Netting Basis Determination | |||||||
4 | SP Newsprint Co. (Newberg, OR) | |||||||
5 | Permit Number: 36-6142 | |||||||
6 | ||||||||
7 | Pollutant: Pb | |||||||
8 | ||||||||
9 | Throughput | Emission Factor | Emissions | |||||
10 | Emissions Unit | Parameter | Annual | Unit | Rate | Unit | Reference | ton/yr |
12 | B67-EU (Boilers #6 and #7) | Residual Oil | 279.93 | Mgal | 0.00151 | lb/Mgal | AP-42 (1.3-11) | 0.0 |
13 | Natural Gas | 354.53 | MMft3 | 0.0005 | lb/MMft3 | AP-42 | 0.0 | |
15 | Recovery Boiler #8 | Residual Oil | 1,255.212 | Mgal | 0.0008 | lb/Mgal(a) | AP-42 (1.3-11) | 0.0 |
16 | Sulfite Pulp | 68,284 | ADT | 102 | lb/10^6 ADT | NCASI 3/2002 (b) | 0.0 | |
18 | B9-EU (Boiler #9) | Steam produced | 906,400 | Mlb | 0.00216 | lb/Mlb | ST 00, 01 Avg | 1.0 |
19 | Natural Gas (Aux. Burners) | 160.6 | MMft3 | 0.0005 | lb/MMft3 | AP-42 | 0.0 | |
23 | Notes: | Pb TOTAL: | 1.0 | |||||
24 | (a) EF = (0.00151 lb Pb/Mgal)(50% reduction for wet scrubber) = 0.0008 | |||||||
25 | Netting Basis = | 1.0 | ||||||
26 | (b) Emission factor converted from tons of Red Liquor Solids to ADT based on pulping yield. |