Eastern RegionSTANDARD AIR CONTAMINANT DISCHARGE PERMIT
REVIEW REPORT
Department of Environmental Quality
Source Information:
SIC | 2421 |
NAICS | 321113 |
Source Categories (Table 1 Part, Code) | B-13 B-71 |
Public Notice Category | II |
Compliance and Emissions Monitoring Requirements:
FCE | Yes |
Compliance schedule | No |
Unassigned emissions | No |
Emission credits | No |
Special Conditions | Yes |
Source test [date(s)] | 1/1/15 |
COMS | No |
CEMS | No |
PEMS | No |
Ambient monitoring | No |
Reporting Requirements
Annual report (due date) | Feb. 15th |
Quarterly report (due dates) | No |
Monthly report (due dates) | No |
Excess emissions report | Yes |
Other (specify) |
Air Programs
Synthetic Minor (SM) | No |
SM -80 | No |
NSPS (list subparts) | No |
NESHAP (list subparts) | JJJJJJ |
Part 68 Risk Management | No |
CFC | No |
Title V | No |
NSR | No |
PSD | No |
RACT | No |
TACT | No |
TABLE OF CONTENTS
PERMITTING 3
SOURCE DESCRIPTION 3
COMPLIANCE 4
EMISSIONS 5
TITLE V MAJOR SOURCE APPLICABILITY 6
ADDITIONAL REQUIREMENTS 6
SOURCE TESTING 7
PUBLIC NOTICE 8
EMISSION DETAIL SHEETS 9
PERMITTING
PERMITTEE IDENTIFICATION
1. Ochoco Lumber Company is located at Malheur Lumber Company, 60339 West Highway 26, John Day, Oregon 97845.
PERMITTING ACTION
2. The proposed permit is a renewal of an existing Air Contaminant Discharge Permit (ACDP) that was issued on September 21, 2007, and was originally scheduled to expire on February 1, 2012. The existing ACDP remains in effect until the proposed permit is issued because the permittee submitted a timely and complete application for renewal.
OTHER PERMITS
3. No other permits have been issued or are required by the DEQ for this source.
ATTAINMENT STATUS
4. The source is located within 10 kilometers of the Strawberry Mountain Wilderness Class I Air Quality Protection Area, but this is neither a new or modified source.
SOURCE DESCRIPTION
OVERVIEW
5. The permittee operates a sawmill and planing facility in John Day, Oregon. The plant consists of two existing 16,500 lb/hr steam Wellons hogged fuel boilers with multiclones and drying kilns. The annual pounds of steam produced from the combined boilers is approximately 160 MM lb/year – steam. The facility commenced operation in 1984.
6. On October 29, 2010, the facility was issued a permit modification for the construction and operation of a compressed wood process that manufactures wood bricks and pellets. Chips, sawdust, shavings or waste wood are placed on an asphalt storage pad with an automated chain reclaimer. The wood is conveyed and milled in a primary hammermill; dried in a horizontal, steam heated, moving belt dryer; ground in a secondary hammermill; and, compressed in brick and pellet machines. The dryer is heated from the two existing Wellons hogged fuel boilers. Pellets are cooled and stored in a silo. Pellets and bricks are shipped in bulk or bagged. Production capacity is 4 – 6 oven dried (OD) tons per hour or approximately 25,000 OD tons per year. The new pellet and brick process added five emission points to the facility: two dyer cyclones, a pellet cooler cyclone, a wood silo vent filter, and a pellet bin vent filter. The facility does not have the steam capacity to operate the wood chip process dryer concurrently with the drying kilns. The cooler cyclone and vent filters contribute negligible emissions. For these reasons the addition of the wood pellet and brick process did not increase the Plant Site Emission Limits.
PROCESS AND CONTROL DEVICES
7. Existing air contaminant sources at the facility consist of the following:
a. Two 16,500 lb/hr Wellons hogged fuel boilers, with model #W-24 multiclone emission controls, installed in 1983.
b. One cyclone which exhausts directly to the atmosphere, handling planer shavings, installed in 1983.
c. Seven tracks of lumber drying kilns, with no emission controls, installed in 1983.
d. Two dyer cyclones, a pellet cooler cyclone, a wood silo vent filter, and a pellet bin vent filter installed in 2010.
e. Fugitive emissions from vehicular traffic and miscellaneous operations.
COMPLIANCE
8. The facility will be inspected by DEQ personnel to ensure compliance with the permit conditions.
9. The facility was not inspected during the prior permit period.
10. During the prior permit period there were no complaints recorded for this facility.
11. During the prior permit period there were no enforcement actions taken against the source.
EMISSIONS
12. Proposed Plant Site Emission Limits:
Pollutant | Baseline Emission Rate (tons/yr) | Netting Basis | Plant Site Emission Limits (PSEL) |
Previous (tons/yr) | Proposed (tons/yr) | Previous PSEL (tons/yr) | Proposed PSEL (tons/yr) | PSEL Increase (tons/yr) | ||
PM | 0 | 0 | 0 | 24 | 24 | 0 |
PM10 | 0 | 0 | 0 | 17 | 17 | 0 |
PM2.5 | NA | NA | 3 | NA | 12 | NA |
SO2 | 0 | 0 | 0 | 39 | 39 | 0 |
NOx | 0 | 0 | 0 | 39 | 39 | 0 |
CO | 0 | 0 | 0 | 99 | 99 | 0 |
VOC | 0 | 47 | 47 | 86 | 86 | 0 |
a. The proposed PSELs for all pollutants, except VOC, PM10 and PM2.5, are equal to the Generic PSEL in accordance with OAR 340-222-0041. Although the Generic PSEL for PM2.5 is 9.0 tons/year, a Netting Basis of up to 5.0 tons/year may be added to the PM2.5 Generic PSEL in order to prevent PM2.5 emissions from initially exceeding SER (OAR 340-200-0020).
b. The PSEL for VOC is based on the netting basis plus 39 tons requested by the source. The netting basis was established based on the interpretation of the rules in effect during previous permitting action.
c. During the previous permit term, approximately 98% of the lumber produced was derived from pine species. Therefore, the VOC levels from kiln drying are based exclusively on the pine emission factor.
d. As the CH4 and N2O emissions (Anthropogenic CO2e short tons) are emitted at diminimis levels (< 2,750 tons/year) for baseline and current emissions, neither a baseline nor a PSEL for GHGs are established in this 2012 permit action. The basis for this may be found in the Emission Detail Sheets provided at the end of this review report.
e. The basis for the PSELs may be found in the Emission Detail Sheets provided at the end of this review report.
f. The PSEL is a federally enforceable limit on the potential to emit.
SIGNIFICANT EMISSION RATE ANALYSIS
13. For each pollutant, the proposed Plant Site Emission Limit is less than the Netting Basis plus the significant emission rate, thus no further air quality analysis is required.
TITLE V MAJOR SOURCE APPLICABILITY
CRITERIA POLLUTANTS
14. A major source is a facility that has the potential to emit 100 tons/yr or more of any criteria pollutant. For greenhouse gases, the source must also have the potential to emit 100,000 tons/year or more CO2e to be a major source. This facility is not a major source of criteria pollutant emissions.
15. The capacity of the facility is based on the following maximum operating rates for each device/activity and 8,424 hours per year, assuming that the plant is shut down for two weeks per year for routine maintenance. It should be noted that the theoretical capacity of the facility is probably much higher than the practical capacity due to production limiting steps in the process, such as the planer, saws, and actual kiln and pellet chip drying times.
Device/Activity | Maximum Operating Rate | Units |
Boilers (2) | 16,500 (each) | Pounds of steam per hour |
Cyclone | 23 | Tons of material throughput per hour |
Kilns | 4,400 | Average Board feet of lumber dried per hour |
Pellet Chip Dryer | 6 | Tons of throughput per hour |
HAZARDOUS AIR POLLUTANTS
16. A major source is a facility that has the potential to emit 10 tons/yr or more of any single HAP or 25 tons/yr or more of combined HAPs. This source is not a major source of hazardous air pollutants. The HAP emissions detail is provided at the end of this report.
ADDITIONAL REQUIREMENTS
NSPS APPLICABILITY
17. There are no sources at this facility for which NSPS standards have been promulgated. The boilers were installed in 1983, before the applicability date of 40 CFR Part 60, Subpart Dc.
NESHAPS/MACT APPLICABILITY
The NESHAPS/MACT Standard for Industrial, Commercial and Institutional Boilers and - Boiler Area Source MACT (40 CFR Part 63 Subpart JJJJJJ) applies to this source because the boiler combusts biomass. The permittee is required to perform biennial tune-ups beginning in March 2013 and a one-time energy assessment by March 2014.
RACT APPLICABILITY
18. The RACT rules are not applicable to this source because it is not in the Portland AQMA, Medford AQMA, or Salem SKATS.
SOURCE TESTING
PRIOR TESTING RESULTS
19. The results of the most recent source tests are listed below:
Emission Device | Test Date | Production Rate (M lb/hr steam) | Pollutant | Emission Factor (lb/M lb Steam) |
Boiler (1) | 3/12/1985 | 16.5 | PM | 0.145 |
Boiler (2) | 0.158 | |||
Combined Boilers (1) & (2) | August 10th & 11th, 1999 | 23.4 | PM | 0.20 |
CO | 0.26 | |||
NOX | 0.47 | |||
Boiler (1) | 10/14/2009 | 11.160 | PM | 0.19 |
CO | 0.42 | |||
NOX | 0.35 | |||
Boiler (2) | 10/15/2009 | 11.907 | PM | 0.17 |
CO | 0.47 | |||
NOX | 0.29 | |||
Average Emissions for the Combined Boilers (1) & (2) | Pollutant | Emission Factor | Units |
PM | 0.17 | (lb/M lb-Steam) | |
CO | 0.38 | ||
NOx | 0.37 |
Emission Device | Test Date | Pollutant | Emission Factor | Units |
Pellet Chip Dryers (DMM2A & DMM2B) | April 19th & 20th, 2011 | PM | 0.26 | (lb/ODT) |
VOC | 2.85 |
Grain Loading Measurements:
Emission Device | Test Date | Measured Value |
Boiler (1) | 03/12/1985 | 0.054 gr/dscf |
Boiler (2) | 03/12/1985 | 0.058 gr/dscf |
Combined Boilers | 08/10/1999 | 0.1 gr/dscf |
Boiler (1) | 10/14/2009 | 0.06 gr/dscf |
Boiler (2) | 10/15/2009 | 0.05 gr/dscf |
Dryer DMM2A | 04/19/2011 | <0.0075 gr/dscf |
Dryer DMM2B | 04/20/2011 | <0.0067 gr/dscf |
PROPOSED TESTING
20. The Wellons hogged fuel boilers will be tested at least once during the permit term for Particulate Matter (PM) emissions. The following production and control device parameters will be recorded during the boiler tests: steam production rate, steam temperature, the pressure drop across the multiclones, NOx emissions rate, CO emissions rate, and opacity. The pellet chip dryer cyclones (DMM2A & B) will also be tested at least once during this permit term for Particulate Matter Emissions (PM) and Volatile Organic Compounds (VOCs). The following production and control device parameters will be recorded during the pellet dryer tests: The species and amount of wood processed through each dryer cyclone, pressure drop across dryer cyclones, operating and exhaust temperatures (oF) of each dryer cyclone, and opacity.
PUBLIC NOTICE
21. Pursuant to OAR 340-216-0066(4)(a)(A), issuance of Standard Air Contaminant Discharge Permits require public notice in accordance with OAR 340-209-0030(3)(b), which requires DEQ to provide notice of the proposed permit action and a minimum of 30 days for interested persons to submit written comments. The public notice was issued on May 31, 2012 and the comment period ended on July 2, 2012. No comments were received in response to the public notice and no changes have been made to the permit.
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EMISSION DETAIL SHEETS
Current Emissions
PM
Emission Point Operating Parameters Emission Factor Reference Emissions
Rate
Hog Fuel Boilers 160 MM lb/yr steam 0.17 lb/M lb steam 1985, 1999 & 2009 ST 13.6
Cyclone (Med. Eff.) 30,000 BDT/yr 0.5 lb/BDT DEQ (AQ-EF02) 7.5
Kilns 38 MM bd. ft/yr 0.02 lb/M bd. ft 1996 NCASI 0.4
Pellet Chip Dryer Cyclones 25,000 ODT/yr 0.26 lb/ ODT 2011 ST 3.25
Pellet Cooler Cyclone 25,000 ODT/yr 0.03 lb/ODT Supplier Est. 0.4
Aggregate Insignificant 1
Total PM Emissions 23
|
PM10
Emission Point Operating Parameters Emission Factor Reference Emissions
Rate
Hog Fuel Boilers 160 MM lb/yr steam 0.15 lb/M lb steam DEQ Est. 12
Cyclone 30,000 BDT/yr 0.25 lb/BDT
3.75
Kilns 38 MM bd. ft/yr 0.02 lb/M bd. ft 1996 NCASI 0.4
Pellet Chip Dryer Cyclones 25,000 ODT/yr 0.25 lb/BDT DEQ (AQ-EF03) 2.6
Pellet Cooler Cyclone 25,000 ODT/yr 0.015 lb/ODT Supplier Est. 0.2
Aggregate Insignificant 1
Total PM10 Emissions 17
|
PM2.5
Emission Point Operating Parameters Emission Factor Reference Emissions
Rate
Hog Fuel Boilers 160 MM lb/yr steam 0.09 lb/M lb steam DEQ (AQ-EF08) 7.2
Cyclone 30,000 BDT/yr 0.25 lb/BDT DEQ (AQ-EF03) 3.75
Kilns 38 MM bd. ft/yr 0.02 lb/M bd. ft 1996 NCASI 0.4
Pellet Chip Dryer Cyclones 25,000 ODT/yr 0.21 lb/BDT DEQ (AQ-EF03) 2.6
Pellet Cooler Cyclone 25,000 ODT/yr 0.015 lb/ODT Supplier Est. 0.2
Aggregate Insignificant 1
Total PM2.5 Emissions 12
|
SO2
Emission Point Operating Parameters Emission Factor Reference Emissions
Rate
Hog Fuel Boilers 160 MM lb/yr steam 0.014 lb/Mlb steam DEQ 1.1
Aggregate Insignificant 1
Total SO2 Emissions 2.1
|
NOx
Emission Point Operating Parameters Emission Factor Reference Emissions
Rate
Hog Fuel Boilers 160 MM lb/yr steam 0.37 lb/Mlb steam 1999& 2009 ST 29.6
Aggregate Insignificant 1
Total NOX Emissions 31
|
CO
Emission Point Operating Parameters Emission Factor Reference Emissions
Rate
Hog Fuel Boilers 160 MM lb/yr steam 0.38 lb/Mlb steam 1999& 2009 ST 30.4
Aggregate Insignificant 1
Total CO Emissions 31
|
VOC
Emission Point Operating Parameters Emission Factor Reference Emissions
Rate
Hog Fuel Boilers 160 MM lb/yr steam 0.13 lb/M lb steam DEQ 10.4
Kilns 38 MM bd. ft/yr 2.7 lb/M bd. ft. (All Pine) 1996 NCASI 51.3
Pellet Chip Dryer 15,000 ODT/yr 2.85 ODT/yr (Pine) 2011 ST & DEQ 21.4
7,500
0.33 ODT/yr (Hem/WF)
1.2
2,500
0.6 ODT/yr (Fir)
0.75
Aggregate Insignificant 1
Total VOC Emissions 63
|
Note: Total emissions are calculated based on the highest emission rate with either the kiln and cyclones or the pellet chip dryer. The combined boilers have a limited steam capacity to operate the kiln or pellet chip dryer. Simultaneous operation of these processes is not possible.
GHG Emissions
Calculating greenhouse gas emissions from steam production Equation C-2c: CO2 = (0.001)(Steam)(B)(EF) Equation C-9b: CH4 or N2O = (0.001)(Steam)(B)(EF) Equations C-2c and C-9b are from EPA's Mandatory Greenhouse Gas Reporting Rule, 40 CFR Part 98, Subpart C |
Total CO2e (short tons): | 19,256.47 |
Anthropogenic CO2e (short tons): | 396.90 |
Biogenic CO2 (short tons): | 18,859.58 |
Input Data |
[Steam] = Total mass of steam generated by MSW or solid fuel combustion during the reporting year (lb steam) | 160,000,000 |
[B] = Ratio of the boiler's maximum rated heat input capacity to its design rated steam output capacity (MMBtu/lb steam) | 0.00114 |
[.001] = Conversion Factor from kg to metric tons (constant) | 0.001 |
[EF] = Fuel-Specific Default CO2 Emission Factor, from Table C-1 (kg CO2/MMBtu) | 93.8 |
[EF] = Fuel-Specific Default CH4 Emission Factor, from Table C-2 (kg CH4/MMBtu) | 0.032 |
[EF] = Fuel-Specific Default N2O Emission Factor, from Table C-2 (kg N2O/MMBtu) | 0.0042 |
Is the fuel biomass? | yes |
Emissions by Mass (short tons) |
CO2 Emissions for the Specific Fuel Type (short tons) from Equation C-2c | 18859.58 |
CH4 Emissions for the Specific Fuel Type (short tons) from Equation C-9b | 6.43 |
N2O Emissions for the Specific Fuel Type (short tons) from Equation C-9b | 0.84 |
CH4 Emissions Converted to Carbon Dioxide Equivalent (short tons CO2e) |
Global Warming Potential for CH4 | 21 |
Annual CH4 emissions from combustion of the specified fuel (metric tons CO2e) | 135.11 |
N2O Emissions Converted to Carbon Dioxide Equivalent (short tons CO2e) |
Global Warming Potential for N2O | 310 |
Annual N2O emissions from combustion of the specified fuel (metric tons CO2e) | 261.78 |
GHG - CO2e Emissions |
Emission Unit | Annual Throughput | Pollutant | Emission Factor | EF Units | Reference | Emissions (metric tons) |
Boiler (Hogged Fuel) | 160,000,000 lb/yr –Steam | GHG-CH4 | 7.30E-05 | lb/lb steam | DEQ -GHG Calculator | 123 |
(GWP=21) | ||||||
GHG-CO2 | 0.2139 | 17,109 | ||||
(GWP=1) | ||||||
GHG-N2O | 9.58E-06 (GWP=310) | 237 |
Total GHG CO2e (metric tons): | 17,469 | |
GHG Anthropogenic CO2e (short tons): | 397 | |
GHG Biogenic CO2e (short tons): | 18,860 | |
Total GHG CO2e (short tons): | 19,256 |
Regulation of biogenic carbon dioxide (CO2) emissions derived from hogged fuel boilers have been deferred by EPA until the global warming effects of biogenic carbon dioxide can be further evaluated. For the purpose of this permit renewal action only the anthropogenic CO2 emissions generated from CH4 and N2O are to be addressed. The anthropogenic CO2 emissions are emitted below deminimis levels (< 2,750 short tons/year). Due to the deminimis emissions, a GHG PSEL is not proposed for this permit renewal. If the biogenic CO2 deferral is removed, the PSEL will be adjusted to include biogas CO2 emissions and the permit will be revised.
HAPs
Hogged Fuel Boilers:
Pollutant | Production Parameter | Emission Factor lb/MMlbSteam(1) | Reference | Annual Esmissions (Tons/yr) |
Phenol | 160 (MM lb/yr-Steam) | 0.056 | AP-42; 9/03 | Negligible |
Acrolein | 4.40 | AP-42; 9/03 | 0.4 | |
Formaldehyde | 1.43 | NCASI TB 858; 2/03 | 0.11 | |
Acetaldehyde | 0.91 | AP-42; 9/03 | 0.07 | |
Benzene | 3.63 | NCASI TB 858; 2/03 | 0.3 | |
Naphthalene | 0.107 | AP-42; 9/03 | 0.01 | |
Chromium | 0.00066 | NCASI TB 858; 2/03 | Negligible | |
Chlorine | 0.869 | AP-42; 9/03 | 0.07 | |
Cobalt | 0.000209 | NCASI TB 858 | Negligible | |
Arsenic | 0.0011 | NCASI TB 858; 2/03 | Negligible | |
Cadmium | 0.00451 | AP-42; 9/03 | Negligible | |
Manganese | 0.165 | NCASI TB 858; 2/03 | 0.01 | |
Mercury | 0.00109 | NCASI TB 858; 2/03 | Negligible | |
Nickel | 0.0363 | AP-42; 9/03 | Negligible | |
Selenium | 0.0033 | NCASI TB 858; 2/03 | Negligible | |
Hydrogen Chloride | 0.737 | NCASI TB 858; 2/03 | 0.06 | |
Styrene | 2.09 | AP-42; 9/03 | 0.2 | |
Toluene | 1.01 | AP-42; 9/03 | 0.08 | |
Xylenes (total) | 0.0275 | AP-42; 9/03 | Negligible | |
Methanol | 0.91 | NCASI TB 858; 2/03 | 0.07 | |
Lead compounds | 0.0064 | NCASI TB 858; 2/03 | Negligible |
Total HAP | 1.4 |
(1) Assumes 1100 Btu per pound of steam
Drying Kilns: (*White Fir > 200oF Drying Temp)
Pollutant | Production Parameter | EF (lb/MM bd ft.) | Reference | HAP Emissions (Tons/Yr) |
Methanol | 38 (MM Bd.-Ft/Year) | 183 | OSU/NCASI 2007 Drying Kiln Study | 3.5 |
Formadehyde | 2.8 | 0.5 |
Acetaldehyde | 113 | 2.1 |
Propionaldehyde | 1.0 | 0.02 |
Acrolein | 1.6 | 0.03 |
Total HAPs | 6.2 |
* The permittee processes only fir and pine species. White fir at >200oF was chosen since the most conservative emission factors were derived from this species and temperature range.
Pellet Chip Drying:
Pollutant | Production Parameter | EF (lb/ODT) | Reference | HAP Emissions (Tons/Yr) |
Methanol | 25000 (Tons/Year) | 0.014 | AP 42 10.6.2-3 (SCC 3-07-006-07) | 0.18 |
Formadehyde | 0.025 | 0.31 |
Acetaldehyde | 0.013 | 0.16 |
Total HAPs | 0.65 |
Total HAPs: 8.3 tons/year