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.

 

 

 

 

 

 

WW:mf

 

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