                                 Attachment E
             Guidance on How to Request Small Business Fee Waivers

See web cite at, Registration Service Fees, Guidance on How to Request Small Business Fee Waivers | Pesticides | US EPA


Date: November 26, 2003 Subject: Selection of HAPs for Compliance Options in the Final Plywood and Composite Wood Products Rule EPA Contract No. 68 D 1 079; EPA Work Assignment No. 2 12 RTI Project No. 08550.002.012 From: Katie Hanks Kristin Parrish To: Mary Tom Kissell, ESD/ WCPG ( C439 03) U. S. Environmental Protection Agency Research Triangle Park, NC 27711 I. Introduction Several hazardous air pollutants ( HAP) may be emitted from plywood and composite wood products ( PCWP) process units. The proposed national emission standards for hazardous air pollutants ( NESHAP) for the PCWP industry contained production based compliance options ( PBCO) and emissions averaging compliance options based on measurement of six predominant HAP ( acetaldehyde, acrolein, formaldehyde, methanol, phenol, and formaldehyde). The proposed NESHAP also contained add on control device compliance options based on measurement of two HAP ( formaldehyde or methanol) or total hydrocarbon ( THC). The purpose of this memo is to document identification of the predominant HAP used as the basis for the PBCO and emissions averaging compliance options ( Section II) and to discuss selection of HAP for the add on control device compliance options ( Section III).

II. Identification of Predominant HAP Sources of emissions test data used in developing the NESHAP for the PCWP industry included nearly 100 emission test reports collected through EPA's MACT survey, data from EPA's Compilation of Air Pollutant Emission Factors, Volume I: Stationary Point and Area Sources ( commonly referred to as AP 42), and extensive data from the industry sponsored test program performed by the National Council of the Paper Industry for Air and Stream Improvement ( NCASI). Most of the speciated HAP emissions test data used to develop the PCWP NESHAP came from the NCASI test program. Attachment 1 explains more about which HAP were tested in the NCASI test program and an in an earlier EPA test program. 2 Table 1 lists nationwide baseline emission estimates for all of the HAP detected at least once in the compilation of HAP emissions data used in development of the PCWP NESHAP. The nationwide baseline emission estimates presented in Table 1 are sorted in descending order by mass. These estimates were developed using the methodology described in a separate memorandum. 1 The PCWP product sectors and the number of process units that had detectable emissions of each HAP are also included in Table 1.

Thriteen HAP had nationwide baseline emissions estimates greater than 10 tons per year ( tpy), and 7 HAP had nationwide baseline emissions estimates greater than 100 tpy. The percentage of uncontrolled process unit emission test runs in the emission factor data base that were below detection limit is presented in Table 2 for each of these 13 HAP. 2 More then 90 percent of the emission test runs were non detect for four of the 13 HAP. The high percentage of non detect test runs indicates that emissions of these HAP occur infrequently.

The goal of this analysis is to determine if a subset of HAP could be used to demonstrate compliance with the PCWP rule. For a compliance demonstration based on a subset of HAP to be feasible, it must ensure that MACT is achieved and reduce the cost of compliance. The subset of HAP used for compliance demonstration could be based on the predominant HAP emitted by the PCWP industry. The predominant HAP would be those emitted in detectable quantities and with high mass relative to other PCWP HAP. The predominant HAP would also be emitted from many PCWP process units. Thus, the following criteria were used to identify the predominant HAP from the PCWP industry: ( 1) HAP with nationwide baseline emissions greater than 100 tpy, ( 2) HAP emitted in the greatest mass by most PCWP sectors and process units, and ( 3) HAP with less than 90 percent of their uncontrolled emissions test runs being non detect. Based on the information in Tables 1 and 2, the HAP that meet these criteria are methanol, formaldehyde, acetaldehyde, phenol, acrolein, and propionaldehyde. Together these six HAP represent 96 percent of the mass of total HAP emissions estimated for the PCWP industry. These six HAP are found in emissions from nearly all PCWP sectors ( except for hardwood plywood, which is a sector that contains no major sources) and many process units. A single test method can be used to test for all six HAP simultaneously. These six HAP were defined as " total HAP" in the proposed PCWP rule.

The compliance demonstration for the PBCO and emissions averaging compliance options are based on the sum of the six predominant HAP. The emissions averaging provisions involve use of add on air pollution control devices ( APCD). As discussed in section III below, data indicate that when emissions of the six predominant HAP ( particularly formaldehyde and methanol because they are most often emitted in detectable amounts) are controlled using a MACT control device, the other organic HAP emitted by the PCWP industry are also reduced significantly. Review of the emission factors used to develop the emissions estimates for the PCWP source category indicates that uncontrolled emissions of HAP ( other than the six HAP) are always lower than emissions of the six HAP for every process unit with MACT control requirements. Thus, process units meeting the PBCO based on total HAP also would have low emissions of other HAP. 3 III. Relationship Between HAP Selected for Add on APCD Compliance Options The PCWP rule contains compliance options for APCD in terms of percent reduction and APCD outlet concentration for formaldehyde, methanol, and THC. The rationale for selecting these HAP for the add on APCD compliance options is explained in a separate memorandum and is further explained below. 5 Prior to proposal of the PCWP rule, it was noted that the complete set of control efficiency data showed that many HAP were emitted at levels near or below the detection limit at the inlet of the control device, which rendered them useless for determining control device performance. Attachment 3a presents the available data used in control efficiency calculations for speciated HAP emissions for 14 regenerative thermal oxidizers ( RTO), two regenerative catalytic oxidizers ( RCO), and two biofilters. The shaded control efficiencies in Attachment 3a indicate pollutants that were removed from the control efficiency analysis. The control efficiencies for these pollutants were not meaningful because either all of the inlet and outlet test runs were below detection limit, or at least two of the inlet test runs were non detects. Table 3 summarizes the number of data sets from which control efficiency calculations for each HAP were removed because of non detect measurements. As shown in Table 3, formaldehyde, methanol, and THC were the only pollutants with control efficiency calculations that were unaffected by non detect measurements in the APCD inlet. Acetaldehyde, phenol, and propionaldehyde were affected by inlet non detects, but were detected more frequently at the APCD inlet than the other pollutants. Nevertheless, enough of the acetaldehyde, acrolein, and propionaldehyde control efficiency calculations were affected by inlet non detects that it seemed unreasonable to use these HAP as the basis for a control efficiency limit given that a control device that reduces formaldehyde, methanol, or THC would also reduce these HAP ( when detectable).

Attachment 3b presents the available control efficiency data after removal of the shaded pollutant control efficiencies. The APCD performance evaluation focused on THC, methanol, and formaldehyde. These three pollutants were selected because they were: ( 1) consistently measured in detectable quantities at the inlet of the control devices, ( 2) the most prevalent pollutants emitted across the various types of process units, and ( 3) the most frequently tested pollutants ( thus, more data were available for these three pollutants). Although THC is not a HAP, THC can be a good indicator of the performance of the control device, and it is frequently used as a surrogate for volatile organic compounds ( VOC). When possible, methane was subtracted from the THC emission measurements to more closely represent VOC. The data presented in Attachment 3b show that when the THC, methanol, and/ or formaldehyde control efficiency is high ( e. g., 90 percent), the control efficiency for other HAP is also significant. The other HAP are not always reduced by 90 percent because they are present in the APCD inlet at a lower concentration ( e. g., usually less than 1 ppm and almost always less than 10 ppm). Compounds present in relatively low quantities in the uncontrolled emission stream generally ( but not always) are associated with lower control efficiencies. Additional information and discussion of control device efficiency is presented in a separate memorandum. 3 4 Based on the available data, it appears that a reduction in one predominant HAP or THC correlates with a reduction in other HAP if the other HAP is present in detectable quantities and at sufficient concentration. Thus, the data indicate that the mechanisms in RTO, RCO, and biofilter control devices that reduce emissions of formaldehyde and methanol are also likely to reduce emissions of the remaining HAP. Although biofilters do not reduce THC to the same degree as RTO and RCO ( because less water soluble non HAP components of THC, such as pinenes, are not as easily destroyed in biofilters), they achieve high reductions in formaldehyde and methanol. It follows that any biofilter that achieves a high reduction in THC would also achieve a high reduction in formaldehyde, methanol, or other HAP.

In addition, an analysis of the physical properties of the organic HAP emitted from PCWP processes indicates that nearly all of the HAP would be combusted at normal thermal oxidizer operating temperatures. Attachment 4 summarizes the ignition temperatures for the various HAP. All of the HAP ( except carbon tetrachloride and chloroform which have only been shown to be emitted in minute amounts from one type of process unit) are flammable with ignition temperatures ranging from 194oF to 1319oF. The lowest thermal oxidizer combustion chamber temperature reported in response to the MACT survey is 1425oF. 4 Thus, based on physical properties alone, it is expected that a thermal oxidizer that significantly reduces methanol and/ or formaldehyde would also reduce the other HAP emitted from the PCWP industry.

The available emissions data do not reveal any process variables that could be manipulated ( without altering the product) to achieve a quantifiable reduction in emissions. Furthermore, nothing in the data suggests that process variables could be manipulated in a way that would alter the relationship between formaldehyde and methanol reduction and reduction of other HAP. For example, switching from urea formaldehyde resin to phenol formaldehyde resin may change emissions; however, these resins are not interchangeable because the product would also change. Urea formaldehyde resins are pale and are used for interior, decorative products where the resin must not show through the products finish ( e. g., cabinets, furniture); phenol formaldehyde resins are dark brown and water proof and are used in exterior applications ( e. g. sheathing, roofing). Emissions data were revisited with respect to other process variables that could potentially be manipulated without altering the product including dryer firing method, fuel type, and in some cases wood type. However, the variability in the available emissions data is such that there is no apparent correlation between these process variables and emissions of formaldehyde and methanol. 5 Less data in the detectable range is available for HAP other than formaldehyde and methanol; therefore, if process variables cannot be shown to affect emissions of formaldehyde and methanol, then it is reasonable to conclude no such affects would be shown for other less common HAP.

IV. References:

1. Memorandum from K. Hanks and D. Bullock, MRI, to M. Kissell, EPA/ ESD. June 9, 2000. Baseline Emission Estimates for the Plywood and Composite Wood Products Industry. 5 2. Memorandum from D. Bullock, K. Hanks, and B. Nicholson, MRI to M. Kissell, EPA/ ESD. April 28, 1999. Summary of Responses to the 1998 EPA Information Collection Request ( MACT Survey)  General Survey.

3. Memorandum from R. Nicholson, MRI, to M. Kissell, EPA/ ESD. May 26, 2000. Control Device Efficiency Data for Add on Control Devices at PCWP Plants.

4. Memorandum from D. Bullock and K. Hanks, MRI, to M. Kissell, WCPG/ ESD/ EPA. Documentation of Emission Factor Development for the Plywood and Composite Wood Products Manufacturing NESHAP. April 27, 2000.

5. Memorandum from K. Parrish and K. Hanks, RTI to M. Kissell, EPA/ ESD. Review of Correlations Between Process Variables and Emissions for the Plywood and Composite Wood Products Industry. November 26, 2003. 6 Table 1. Summary of Nationwide Baseline HAP Emissions, Product Sectors, and Process Units For Which Each HAP Detected HAP Nationwide baseline emissions ( tpy) PCWP sectors with HAP detecteda No. of PCWP process units Methanol 12,000 all 32 Formaldehyde 3,400 all 29 Acetaldehyde 1,500 all 27 Phenol 690 all 20 Acrolein 330 all but HPW 17 Propionaldehyde 270 all but HPW 13 MIBK 170 all but EWP 15 Xylenes ( includes m, pxylene and o xylene) 80 PB, HB, OSB, SPW 9 Toluene 67 all but HPW 13 MEK 63 all but HPW 16 Benzene 44 all but HPW 13 Cumene 27 PB, FB, OSB 7 Styrene 10 all but HPW and FB 10 MDI 8.8 OSB, EWP 2 Methylene chloride 4.8 PB 3 Other HAPb 1.6 PB 1b Cresols ( includes m, pcresol and o cresol) 1.0 HB 1 Chloromethane 0.23 PB, HB 2 Ethyl benzene 0.15 PB, HB 3 Chloroethane 0.025 HB 1 Total 19,000 8 sectors 37 listed in Attachment 2c a The eight PCWP product sectors include medium density fiberboard ( MDF), particleboard ( PB), hardboard ( HB), fiberboard ( FB), oriented strandboard ( OSB), softwood plywood ( SPW), hardwood plywood ( HPW), and engineered wood products ( EWP). b " Other HAP" includes 1,1,1 Trichloroethane, 4 Methyl 2 pentanone, Acetophenone, Biphenyl, Bis( 2 ethylhexyl phthalate), Bromomethane, Carbon disulfide, Carbon tetrachloride, Chloroform, Chloromethane, Di n butyl phthalate, Ethyl benzene, Hydroquinone, and n Hexane. With the exception of chloroform, all of the " other HAP" were detected in two tests of two dry rotary dryers ( EPA M0010 and M0030 tests). Cholroform was detected in one green rotary dryer test ( M0030). In addition, 1,1,1 Trichloroethane was detected in a M0030 test of a particleboard veneer press. 7 c Attachment 2 lists the types of process units for which emissions were estimated according to the methodology in the baseline emissions memo and provides a breakout of HAP detected for each process unit type. 8 Table 2. Percentage of Uncontrolled Process Unit Emission Test Runs Below Detection Limit for 13 HAP with Nationwide Baseline Emissions of 10 Tons per Year or Greater HAP Nationwide baseline emissions ( tpy) Percent of uncontrolled process unit test runs in emission factor data base that were below detection limita Methanol 12,000 14%

Formaldehyde 3,400 16%

Acetaldehyde 1,500 46%

Phenol 690 73%

Acrolein 330 77%

Propionaldehyde 270 85%

MIBK 170 93%

Xylenes ( includes m, pxylene and o xylene) 80 91%

Toluene 67 85%

MEK 63 88%

Benzene 44 87%

Cumene 27 96%

Styrene 10 96%

aReference 2 9 Table 3. Number of Instances When a Pollutant Was Removed from the Speciated HAP Control Efficiency Data Set Due to Inlet Non detect Measurementsa HAP RTO ( 14 data sets) RCO ( 2 data sets) Biofilter ( 2 data sets) acetaldehyde 2 0 1 acrolein 9 1 2 benzene 11 1 2 cumeneb 12b 1b 2b formaldehyde 0 0 0 m, p xylene 11 1 2 methanol 0 0 0 methyl ethyl ketone 12 1 2 methyl isobutyl ketone 11 2 2 methylene chlorideb 4b NAb 1b o xyleneb 8b 1b 1b phenol 10 0 1 propionaldehyde 9 1 2 styrene 13 1 2 THC as carbon 0 0 0 toluene 10 1 2 aHAP were removed from the control efficiency analysis if: ( 1) all APCD inlet and outlet test runs were below detection limit, or ( 2) at least two of the APCD inlet test runs were below detection limit. bData not available in all data sets for this HAP. However, every data set containing this HAP was removed from the control efficiency analysis because of non detects in the inlet. ATTACHMENT 1 NCASI Testing Program The HAP included in the NCASI test program are listed in Table 1. Five of these HAP were not detected at any of the emission sources tested. 1 Prior to the NCASI testing program, efforts were made to characterize the HAP emitted from PCWP processes. A comprehensive sampling effort was conducted by EPA in 1992/ 1993 where HAP data were obtained from testing at four mills using three measurement methods: ( 1) Method 0011 for aldehydes and ketones, ( 2) Method 0010 for semi volatile organic compounds, and ( 3) Method 0030 for volatile organic compounds. Theoretically, these three methods combined could be expected to detect nearly all of the organic HAP present in source emissions ( if present at concentrations greater than the method detection limits). The results from this sampling effort were incorporated into EPA's AP 42 data, which were used in development of the PCWP NESHAP. The results from EPA's HAP speciation effort and others were considered when planning the NCASI sampling program in 1996/ 1997. Time constraints made it impractical for NCASI to sample for all 188 HAP. Also, because the budget for the sampling effort was set at $ 1.5 to 2 million, increasing the number of HAP sampled would increase testing costs and decrease the number of processes and mills that could be sampled. Therefore, the NCASI sampling effort focused on those HAP expected to account for the overwhelming majority of the HAP emitted by PCWP plants. 2,3 Table 1. HAP Analytes Included in the NCASI MACT Sampling Program acetaldehyde methyl ethyl ketone acrolein methyl isobutyl ketone benzene methylene chloride bromomethanea phenol chloroethanea propionaldehyde chloroethenea styrene cumene toluene a, 2 dichloroethanea a, 2,4 trichlorobenzenea formaldehyde m, p xylene methanol o xylene aThe data for these compounds were not extracted from the NCASI data base because emissions of these HAP were below the method detection limit for all test runs on all sources tested.

1. Memorandum from D. Bullock, K. Hanks, and B. Nicholson, MRI to M. Kissell, EPA/ ESD. April 28, 1999. Summary of Responses to the 1998 EPA Information Collection Request ( MACT Survey)  General Survey.

2. Volatile Organic Compound Emissions From Wood Products Manufacturing Facilities, Part VII  Test Methods, Quality Assurance, Quality Control Procedures and Data Analysis Protocol, Technical Bulletin No. 774, National Council of the Paper Industry for Air and Stream Improvement, Inc., Research Triangle Park, NC, 1999.

3. Letter from J. Cooper, American Forest & Paper Association to B. Jordan, EPA/ ESD. December 23, 1996. Discussion of HAP to be included in the NCASI sampling program. ATTACHMENT 2 HAP Potentially Emitted from Each Process Unit Type Attachment 2. Breakout of HAP Emitted from Different Process Unit Typesa Process unit type Acetaldehyde Acrolein Benzene Chloroethane Chloromethane Cumene Ethylbenzene Formaldehyde m, pcresol o cresol MDI MEK Methanol Primary tube dryers X X X X X X X Secondary Tube Dryers X X X X Conveyor Dryers X X X X X X X Rotary strand dryers X X X X X X X Conveyor strand dryers X X X X X X X Dry rotary particle dryers X X X X X X X X X Paddle type particle dryers X X X X X X X Green rotary particle dryers X X X X X X X Hardboard ovens X X X X X Hardboard humidifiers X X X X X X X X X X Fiberboard mat dryer ( bagasse)

Fiberboard mat dryers ( wood)

Press preheat ovens X X X X Veneer redryers Softwood veneer dryers X X X X X X Hardwood veneer dryers X X X Particleboard press molds Extruders X X X X X X Engineered wood products presses X X X X Plywood presses X X X X Reconstituted wood products presses X X X X X X X Reconstituted wood products board coolers X X X X X X Pressurized refiners X X X X X Atmospheric refiners X X X X X X Blenders X X Formers X X X X Sanders X X X Saws X X X Fiber washers X X X Chippers X X X Log vats  SPW X X Bin Baghouses  OSB X X Combined dust baghouse  HPW X Radio Frequency Veneer Dryer  SPW X X X Curing Ovens  I J X X Dust collection  I J X Refiners/ Hammermills/ Flakers  PB X Count of process units ( 37 total) 27 17 13 1 2 7 3 29 1 1 2 16 32 a  The process unit types listed are those for which baseline emissions were estimates. Different sets of emission factors were used to estimate baseline emissions for the same type of equipment used to make different products ( e. g., hardboard tube dryers and MDF tube dryers). An " X" appears in the table above if any one of the sets of emission factors included the HAP. Process unit type Methylene Chloride MIBK Phenol Propionaldehyde Styrene Toluene m, p xylene o xylene Primary tube dryers X X X X X X X 1,1,1 Trichloroethane Secondary Tube Dryers X X 4 Methyl 2 pentanone Conveyor Dryers X X X X X Acetophenone Rotary strand dryers X X X X X X Biphenyl Conveyor strand dryers X X X X X X Bis( 2 ethylhexyl phthalate)

Dry rotary particle dryers X X X X X X X < Other HAP: Bromomethane Paddle type particle dryers X X X X X X X Carbon Disulfide Green rotary particle dryers X X X X X X X X < Other HAP: Carbon tetrachloride Hardboard ovens X X X Chloroform Di N butyl phthalate Hardboard humidifiers X X X X X Hydroquinone Fiberboard mat dryer ( bagasse) n Hexane Fiberboard mat dryers ( wood)

Press preheat ovens X Veneer redryers Softwood veneer dryers X X X X X X X Hardwood veneer dryers X X Particleboard press molds Extruders X X Engineered wood products presses X Plywood presses X X Reconstituted wood products presses X X X X X X Reconstituted wood products board coolers X X Pressurized refiners X X X X Atmospheric refiners X X Blenders Formers X Sanders X X Saws X Fiber washers Chippers X Log vats  SPW Bin Baghouses  OSB Combined dust baghouse  HPW Radio Frequency Veneer Dryer  SPW Curing Ovens  I J Dust collection  I J Refiners/ Hammermills/ Flakers  PB Count of process units ( 37 total) 3 15 20 13 10 13 9 7 ATTACHMENT 3 Attachment 3a: Speciated HAP Control Efficiency Data Attachment 3b: Culled HAP Control Efficiency Data ATTACHMENT 3a Speciated HAP Control Efficiency Data Page 1 of 7 Unit Test No. of No. of Pre Test Inlet1, Inlet1, Inlet2, Inlet2, Total inlet, Outlet, Outlet, Cont. effic.,

code date Product runs runs BDL treatmen t APCD Pollutant method Units ppm lb/ unit ppm lb/ unit lb/ unit ppm lb/ unit % Comment B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO acetaldehyde NICM lb/ hr 0.2093 0.05501 0.05501 0.25654 0.073  33.4 all inlet and outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO acrolein NICM lb/ hr 0.14654 0.049014 0.04901 0.17634 0.064  31.0 all inlet and outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO benzene NICM lb/ hr 0.0403 0.018783 0.01878 0.0406 0.021  9.7 all inlet and outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO cumene NICM lb/ hr 0.80595 0.578026 0.57803 0.81196 0.634  9.7 all inlet and outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO formaldehyde NICM lb/ hr 43.2413 7.777488 7.77749 0.09376 0.018 99.8 all outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO m, p xylene NICM lb/ hr 0.0403 0.025528 0.02553 0.0406 0.028  9.7 all inlet and outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO methanol NICM lb/ hr 108.6 20.75225 20.7523 0.33786 0.07 99.7 all outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO methyl ethyl ketone NICM lb/ hr 0.14355 0.061755 0.06175 0.17253 0.081  30.8 all inlet and outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO methyl isobutyl ketone NICM lb/ hr 0.56457 0.338532 0.33853 0.11658 0.076 77.6 all outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO methylene chloride NICM lb/ hr 0.0403 0.020425 0.02042 0.0406 0.022  9.7 all inlet and outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO o xylene NICM lb/ hr 0.0403 0.025528 0.02553 0.0406 0.028  9.7 all inlet and outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 2 NONE RTO phenol NICM lb/ hr 0.24719 0.138655 0.13865 0.29568 0.18  29.6 2 inlet and 2 outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO propionaldehyde NICM lb/ hr 0.15993 0.055422 0.05542 0.19346 0.073  31.6 all inlet and outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO styrene NICM lb/ hr 0.0403 0.025047 0.02505 0.0406 0.027  9.7 all inlet and outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 0 NONE RTO THC as carbon M25A lb/ hr 555.985 39.84825 39.8483 4.9284 0.383 99.0 CH4 not subtracted ( not measured)

B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO toluene NICM lb/ hr 0.0403 0.022159 0.02216 0.0406 0.024  9.7 all inlet and outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 WESP RTO acetaldehyde NICM lb/ hr 1.24594 0.471457 0.47146 0.18018 0.069 85.3 all outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 WESP RTO acrolein NICM lb/ hr 0.11986 0.057732 0.05773 0.11811 0.058  0.1 all inlet and outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 WESP RTO benzene NICM lb/ hr 0.03743 0.024773 0.02477 0.03914 0.027  9.1 2 inlet runs and 1 outlet run BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 WESP RTO cumene NICM lb/ hr 0.74566 0.772714 0.77271 0.7667 0.803  3.9 all inlet and outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 WESP RTO formaldehyde NICM lb/ hr 1.06017 0.275196 0.2752 0.10622 0.028 89.8 2 outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 1 WESP RTO m, p xylene NICM lb/ hr 0.06568 0.059258 0.05926 0.03914 0.037 38.0 1 inlet and 1 outlet run BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 WESP RTO methanol NICM lb/ hr 4.47411 1.235988 1.23599 0.35166 0.099 92.0 2 outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 WESP RTO methyl ethyl ketone NICM lb/ hr 0.11719 0.072593 0.07259 0.11516 0.072 0.2 all inlet and outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 WESP RTO methyl isobutyl ketone NICM lb/ hr 0.07807 0.067057 0.06706 0.07185 0.063 6.3 all inlet and outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 WESP RTO methylene chloride NICM lb/ hr 0.03743 0.026939 0.02694 0.03914 0.029  9.1 2 inlet runs and 1 outlet run BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 WESP RTO o xylene NICM lb/ hr 0.03743 0.03367 0.03367 0.03914 0.037  9.1 2 inlet runs and 1 outlet run BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 WESP RTO phenol NICM lb/ hr 0.14744 0.119303 0.1193 0.14865 0.122  2.3 all inlet and outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 WESP RTO propionaldehyde NICM lb/ hr 0.13182 0.065806 0.06581 0.13136 0.067  1.2 all inlet and outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 WESP RTO styrene NICM lb/ hr 0.03743 0.033035 0.03304 0.03914 0.036  9.1 2 inlet runs and 1 outlet run BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 0 WESP RTO THC as carbon M25A lb/ hr 488.493 50.41784 50.4178 6.43446 0.673 98.7 CH4 subtracted from inlet & outlet R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 1 WESP RTO toluene NICM lb/ hr 0.08247 0.064641 0.06464 0.03914 0.032 50.7 1 inlet and 1 outlet run BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 NONE WESP/ RTO acetaldehyde NICM lb/ hr 1.20706 0.36108 0.36108 0.18018 0.069 80.8 3 outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 NONE WESP/ RTO acrolein NICM lb/ hr 0.14465 0.054953 0.05495 0.11811 0.058  5.1 all inlet and outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 NONE WESP/ RTO benzene NICM lb/ hr 0.03865 0.020468 0.02047 0.03914 0.027  32.0 3 inlet and 1 outlet run BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 NONE WESP/ RTO cumene NICM lb/ hr 0.77308 0.629907 0.62991 0.7667 0.803  27.4 all inlet and outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 NONE WESP/ RTO formaldehyde NICM lb/ hr 0.99953 0.202858 0.20286 0.10622 0.028 86.2 2 outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 NONE WESP/ RTO m, p xylene NICM lb/ hr 0.05223 0.037675 0.03768 0.03914 0.037 2.5 2 inlet and 1 outlet run BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 NONE WESP/ RTO methanol NICM lb/ hr 3.97445 0.859329 0.85933 0.35166 0.099 88.5 2 outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 NONE WESP/ RTO methyl ethyl ketone NICM lb/ hr 0.14168 0.069222 0.06922 0.11516 0.072  4.7 all inlet and outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 NONE WESP/ RTO methyl isobutyl ketone NICM lb/ hr 0.09798 0.066509 0.06651 0.07185 0.063 5.5 all inlet and outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 NONE WESP/ RTO methylene chloride NICM lb/ hr 0.03865 0.022258 0.02226 0.03914 0.029  32.0 all inlet and 1 outlet run BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 NONE WESP/ RTO o xylene NICM lb/ hr 0.03865 0.027819 0.02782 0.03914 0.037  32.0 3 inlet and 1 outlet run BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 NONE WESP/ RTO phenol NICM lb/ hr 0.17546 0.111897 0.1119 0.14865 0.122  9.1 all inlet and outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 NONE WESP/ RTO propionaldehyde NICM lb/ hr 0.15802 0.062193 0.06219 0.13136 0.067  7.0 all inlet and outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 NONE WESP/ RTO styrene NICM lb/ hr 0.03865 0.027295 0.02729 0.03914 0.036  32.0 3 inlet and 1 outlet run BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 0 NONE WESP/ RTO THC as carbon M25A lb/ hr 488.493 50.41784 50.4178 6.43446 0.673 98.7 CH4 subtracted from inlet & outlet R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 NONE WESP/ RTO toluene NICM lb/ hr 0.06121 0.038357 0.03836 0.03914 0.032 16.9 2 inlet and 1 outlet run BDL Page 2 of 7 Unit Test No. of No. of Pre Test Inlet1, Inlet1, Inlet2, Inlet2, Total inlet, Outlet, Outlet, Cont. effic.,

code date Product runs runs BDL treatmen t APCD Pollutant method Units ppm lb/ unit ppm lb/ unit lb/ unit ppm lb/ unit % Comment F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO acetaldehyde NICM lb/ hr 11.7403 2.61133 2.61133 0.20281 0.051 98.0 all outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO acrolein NICM lb/ hr 3.3895 0.95692 0.95692 0.14201 0.046 95.2 all outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO benzene NICM lb/ hr 0.03541 0.013988 0.01399 0.03911 0.018  25.6 all inlet and outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO cumene NICM lb/ hr 0.7082 0.430467 0.43047 0.78221 0.541  25.6 all inlet and outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 2 NONE RTO formaldehyde NICM lb/ hr 4.39499 0.661082 0.66108 0.11196 0.019 97.1 2 outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO m, p xylene NICM lb/ hr 0.03541 0.019011 0.01901 0.03911 0.024  25.6 all inlet and outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO methanol NICM lb/ hr 9.34398 1.520261 1.52026 0.26445 0.049 96.8 all outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO methyl ethyl ketone NICM lb/ hr 0.1339 0.04891 0.04891 0.13912 0.058  18.1 all inlet and outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO methyl isobutyl ketone NICM lb/ hr 0.09213 0.046735 0.04674 0.09671 0.056  19.4 all inlet and outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO o xylene NICM lb/ hr 0.03541 0.019011 0.01901 0.03911 0.024  25.6 all inlet and outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 2 NONE RTO phenol NICM lb/ hr 0.1662 0.07925 0.07925 0.23959 0.131  64.8 all inlet runs BDL; 2 outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO propionaldehyde NICM lb/ hr 11.7729 3.431402 3.4314 0.15499 0.052 98.5 all outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO styrene NICM lb/ hr 0.03541 0.018653 0.01865 0.03911 0.023  25.6 all inlet and outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 0 NONE RTO THC as carbon M25A lb/ hr 352.185 21.41545 21.4155 4.67233 0.32 98.5 CH4 not subtracted ( not measured)

F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO toluene NICM lb/ hr 0.03541 0.016502 0.0165 0.03911 0.021  25.6 all inlet and outlet runs BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 3 NONE RTO acetaldehyde NICM lb/ hr 0.43672 0.184293 0.18429 0.2078 0.098 46.7 1 inlet and 3 outlet runs BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 3 NONE RTO acrolein NICM lb/ hr 0.14098 0.075816 0.07582 0.14541 0.087  15.4 all inlet and outlet runs BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 3 NONE RTO benzene NICM lb/ hr 0.03887 0.029122 0.02912 0.0398 0.033  14.5 all inlet and outlet runs BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 3 NONE RTO cumene NICM lb/ hr 0.77733 0.896218 0.89622 0.79608 1.026  14.5 all inlet and outlet runs BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 0 NONE RTO formaldehyde NICM lb/ hr 5.62712 1.62473 1.62473 0.54175 0.175 89.2 B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 3 NONE RTO m, p xylene NICM lb/ hr 0.03887 0.03958 0.03958 0.0398 0.045  14.5 all inlet and outlet runs BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 1 NONE RTO methanol NICM lb/ hr 17.7308 5.441179 5.44118 0.83214 0.285 94.8 1 outlet run BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 3 NONE RTO methyl ethyl ketone NICM lb/ hr 0.13811 0.095524 0.09552 0.14244 0.11  15.3 all inlet and outlet runs BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 3 NONE RTO methyl isobutyl ketone NICM lb/ hr 0.09602 0.092258 0.09226 0.09891 0.106  15.2 all inlet and outlet runs BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 2 NONE RTO phenol NICM lb/ hr 0.89745 0.810979 0.81098 0.3779 0.383 52.7 2 outlet runs BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 3 NONE RTO propionaldehyde NICM lb/ hr 0.15385 0.085721 0.08572 0.15872 0.099  15.4 all inlet and outlet runs BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 3 NONE RTO styrene NICM lb/ hr 0.03887 0.038834 0.03883 0.0398 0.044  14.5 all inlet and outlet runs BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 0 NONE RTO THC as carbon M25A lb/ hr 51.3821 5.913199 5.9132 3.306 0.426 92.8 CH4 not subtracted ( not measured) B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 3 NONE RTO toluene NICM lb/ hr 0.03887 0.034357 0.03436 0.0398 0.039  14.5 all inlet and outlet runs BDL R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO acetaldehyde NICM lb/ hr 33.5545 12.18942 12.1894 5.18795 2.211 81.9 R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO acrolein NICM lb/ hr 8.47441 3.90733 3.90733 1.13352 0.614 84.3 R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO benzene NICM lb/ hr 0.58265 0.376021 0.37602 0.23681 0.179 52.4 R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 3 WESP RTO cumene NICM lb/ hr 0.76617 0.762083 0.76208 0.77639 0.903  18.6 all inlet and outlet runs BDL R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO formaldehyde NICM lb/ hr 45.2337 11.22791 11.2279 13.1172 3.815 66.0 R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 3 WESP RTO m, p xylene NICM lb/ hr 0.03831 0.033656 0.03366 0.03882 0.04  18.6 all inlet and outlet runs BDL R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO methanol NICM lb/ hr 24.0545 6.372851 6.37285 4.57033 1.416 77.8 R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 3 WESP RTO methyl ethyl ketone NICM lb/ hr 0.23546 0.139938 0.13994 0.13925 0.097 30.5 1 inlet and 3 outlet runs BDL R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 3 WESP RTO methyl isobutyl ketone NICM lb/ hr 0.09341 0.077429 0.07743 0.09665 0.094  21.0 all inlet and outlet runs BDL R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO phenol NICM lb/ hr 0.68283 0.534002 0.534 0.40188 0.366 31.5 R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 1 WESP RTO propionaldehyde NICM lb/ hr 1.41241 0.676412 0.67641 0.26402 0.148 78.1 1 outlet run BDL R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 3 WESP RTO styrene NICM lb/ hr 0.07777 0.066835 0.06683 0.03882 0.039 41.4 1 inlet and 3 outlet runs BDL R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO THC as carbon M25A lb/ hr 390.034 38.56629 38.5663 57.191 6.628 82.8 CH4 not subtracted ( not measured)

R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 3 WESP RTO toluene NICM lb/ hr 0.33005 0.25076 0.25076 0.03882 0.035 86.2 3 outlet runs BDL Page 3 of 7 Unit Test No. of No. of Pre Test Inlet1, Inlet1, Inlet2, Inlet2, Total inlet, Outlet, Outlet, Cont. effic.,

code date Product runs runs BDL treatmen t APCD Pollutant method Units ppm lb/ unit ppm lb/ unit lb/ unit ppm lb/ unit % Comment B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO acetaldehyde NICM lb/ hr 0.69324 0.64712 0.64712 0.19776 0.166 74.3 nat. gas injection mode; 1 inlet and 3 outlet runs B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO acrolein NICM lb/ hr 0.1579 0.18575 0.18575 0.13871 0.149 20.0 nat. gas injection mode; all inlet and outlet runs B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO benzene NICM lb/ hr 0.03853 0.063176 0.06318 0.03877 0.058 8.4 nat. gas injection mode; all inlet and outlet runs B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO cumene NICM lb/ hr 0.77064 1.944221 1.94422 0.77534 1.78 8.4 nat. gas injection mode; all inlet and outlet runs B1 OSB hot press 1/ 18/ 1998 OSB 3 2 NONE RTO formaldehyde NICM lb/ hr 3.44725 2.168481 2.16848 0.18984 0.11 94.9 nat. gas injection mode; 2 outlet runs BDL B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO m, p xylene NICM lb/ hr 0.03853 0.085863 0.08586 0.03877 0.079 8.4 nat. gas injection mode; all inlet and outlet runs B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO methanol NICM lb/ hr 25.4525 17.03734 17.0373 0.25763 0.157 99.1 nat. gas injection mode; 3 outlet runs BDL B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO methyl ethyl ketone NICM lb/ hr 0.15455 0.233826 0.23383 0.1359 0.187 20.0 nat. gas injection mode; all inlet and outlet runs B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO methyl isobutyl ketone NICM lb/ hr 0.10534 0.221419 0.22142 0.09471 0.181 18.2 nat. gas injection mode; all inlet and outlet runs B1 OSB hot press 1/ 18/ 1998 OSB 3 2 NONE RTO phenol NICM lb/ hr 0.50408 0.993354 0.99335 0.22458 0.404 59.3 nat gas injection mode; 2 outlet runs BDL B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO propionaldehyde NICM lb/ hr 0.17295 0.210786 0.21079 0.15131 0.168 20.4 nat. gas injection mode; all inlet and outlet runs B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO styrene NICM lb/ hr 0.03853 0.084246 0.08425 0.03877 0.077 8.4 nat. gas injection mode; all inlet and outlet runs B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO THC as carbon M25A lb/ hr 255.324 64.32727 64.3273 0.5 0.115 99.8 nat. gas injection mode; all outlet runs BDL; CH subtracted ( not measured)

B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO toluene NICM lb/ hr 0.03853 0.074532 0.07453 0.03877 0.068 8.4 nat. gas injection mode; all inlet and outlet runs R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO acetaldehyde NICM lb/ hr 4.63534 4.093543 4.09354 0.19402 0.239 94.2 nat. gas injection mode; all outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO acrolein NICM lb/ hr 2.53329 2.845826 2.84583 0.13626 0.214 92.5 nat. gas injection mode; all outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO benzene NICM lb/ hr 0.15845 0.247967 0.24797 0.03848 0.084 66.0 nat. gas injection mode; all outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO cumene NICM lb/ hr 0.74323 1.789863 1.78986 0.76964 2.592  44.8 nat. gas injection mode; all inlet and outlet runs R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 4 WESP RTO formaldehyde NICM lb/ hr 19.0781 11.49902 11.499 0.13634 0.114 99.0 nat. gas injection mode; 4 outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO m, p xylene NICM lb/ hr 0.15135 0.321979 0.32198 0.03848 0.114 64.4 nat. gas injection mode; all outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO methanol NICM lb/ hr 6.85387 4.399032 4.39903 0.25259 0.226 94.9 nat. gas injection mode; all outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO methyl ethyl ketone NICM lb/ hr 0.25732 0.371997 0.372 0.13351 0.27 27.5 nat. gas injection mode; 1 inlet and all outlet run R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO methyl isobutyl ketone NICM lb/ hr 0.24273 0.487206 0.48721 0.09321 0.262 46.3 nat. gas injection mode; all outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 2 WESP RTO phenol NICM lb/ hr 0.29702 0.559844 0.55984 0.40066 1.055  88.4 nat. gas injection mode; 2 inlet runs and 1 outlet BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO propionaldehyde NICM lb/ hr 0.32756 0.381538 0.38154 0.14858 0.242 36.6 nat. gas injection mode; 1 inlet and all outlet run R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO styrene NICM lb/ hr 0.03716 0.077557 0.07756 0.03848 0.112  44.8 nat. gas injection mode; all inlet and outlet runs R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 0 WESP RTO THC as carbon M25A lb/ hr 1190 286.0403 286.04 43.8125 14.74 94.8 nat. gas injection mode; CH4 subtracted from in outlet R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO toluene NICM lb/ hr 0.31279 0.57752 0.57752 0.03848 0.099 82.8 nat. gas injection mode; all outlet runs BDL Page 4 of 7 Unit Test No. of No. of Pre Test Inlet1, Inlet1, Inlet2, Inlet2, Total inlet, Outlet, Outlet, Cont. effic.,

code date Product runs runs BDL treatmen t APCD Pollutant method Units ppm lb/ unit ppm lb/ unit lb/ unit ppm lb/ unit % Comment T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO acetaldehyde NICM lb/ hr 31.7964 2.57904 2.57904 0.2011 0.022 99.2 all outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO acrolein NICM lb/ hr 7.78131 0.803204 0.8032 0.14073 0.019 97.6 all outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO benzene NICM lb/ hr 0.0393 0.005652 0.00565 0.03855 0.007  31.4 all inlet and outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO cumene NICM lb/ hr 0.78605 0.17395 0.17395 0.77091 0.229  31.4 all inlet and outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO formaldehyde NICM lb/ hr 2.62 0.145166 0.14517 0.06714 0.005 96.6 all outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO m, p xylene NICM lb/ hr 0.0393 0.007682 0.00768 0.03855 0.01  31.4 all inlet and outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 2 NONE RTO methanol NICM lb/ hr 8.45039 0.497676 0.49768 0.38103 0.03 94.0 2 outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO methyl ethyl ketone NICM lb/ hr 0.19283 0.025866 0.02587 0.13786 0.025 5.2 2 inlet runs and 3 outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO methyl isobutyl ketone NICM lb/ hr 0.84149 0.155454 0.15545 0.09574 0.024 84.8 all outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO o xylene NICM lb/ hr 0.0393 0.007682 0.00768 0.03855 0.01  31.4 all inlet and outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 1 NONE RTO phenol NICM lb/ hr 0.36623 0.06332 0.06332 0.28817 0.067  5.8 1 outlet run BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO propionaldehyde NICM lb/ hr 31.5247 3.372796 3.3728 0.15361 0.022 99.3 all outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO styrene NICM lb/ hr 0.0393 0.007538 0.00754 0.03855 0.01  31.4 all inlet and outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO THC as carbon M25A lb/ hr 763.837 16.87325 16.8733 0.5 0.015 99.9 all outlet runs BDL; CH4 subtracted from inlet b outlet ( all outlet THC = CH4)

T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO toluene NICM lb/ hr 0.0393 0.006668 0.00667 0.03855 0.009  31.4 all inlet and outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO acetaldehyde NICM lb/ hr 0.62819 0.369673 0.19796 0.04315 0.41282 0.20345 0.164 60.3 all press and outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO acrolein NICM lb/ hr 0.13111 0.098053 0.139683 0.03875 0.1368 0.14249 0.146  6.7 all inlet and outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO benzene NICM lb/ hr 0.03899 0.040623 0.041043 0.01587 0.05649 0.0393 0.056 0.7 all inlet and outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO cumene NICM lb/ hr 0.77974 1.25015 0.820867 0.48836 1.73851 0.78599 1.727 0.7 all inlet and outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 2 RBP RTO formaldehyde NICM lb/ hr 16.2976 6.553666 7.692813 1.14699 7.70065 0.18413 0.101 98.7 2 outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO m, p xylene NICM lb/ hr 0.03899 0.055211 0.041043 0.02157 0.07678 0.0393 0.076 0.7 all inlet and outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO methanol NICM lb/ hr 28.6029 12.25112 8.896868 1.40955 13.6607 0.26527 0.155 98.9 all outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO methyl ethyl ketone NICM lb/ hr 0.12852 0.123619 0.136913 0.04885 0.17247 0.13959 0.184  6.7 all inlet and outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO methyl isobutyl ketone NICM lb/ hr 0.09055 0.120988 0.144952 0.0719 0.19288 0.09706 0.178 7.9 all dryer and outlet runs BDL; 2 press runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO methylene chloride NICM lb/ hr 0.03899 0.044175 0.041043 0.01726 0.06143 0.0393 0.061 0.7 all inlet and outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO o xylene NICM lb/ hr 0.03899 0.055211 0.041043 0.02157 0.07678 0.0393 0.076 0.7 all inlet and outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 2 RBP RTO phenol NICM lb/ hr 0.27929 0.348447 0.228859 0.10608 0.45453 0.25696 0.441 3.1 2 press and outlet runs BDL; 1 dryer run BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO propionaldehyde NICM lb/ hr 0.14273 0.110586 0.152121 0.04372 0.15431 0.1555 0.165  7.0 all inlet and outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO styrene NICM lb/ hr 0.03899 0.054171 0.041043 0.02116 0.07533 0.0393 0.075 0.7 all inlet and outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 2 0 RBP RTO THC as carbon M25A lb/ hr 201.149 32.22919 20.33499 1.2081 33.4373 9.58696 2.085 93.8 CH4 not subtracted ( not measured)

M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO toluene NICM lb/ hr 0.03899 0.047925 0.041043 0.01872 0.06665 0.0393 0.066 0.7 all inlet and outlet runs BDL B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO acetaldehyde NICM lb/ hr 0.46774 0.246413 0.24641 0.20974 0.152 38.1 2 inlet and 3 outlet runs BDL; nat. gas injection B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO acrolein NICM lb/ hr 0.13883 0.097305 0.09731 0.14691 0.136  39.7 all inlet and outlet runs BDL; nat. gas injection m B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO benzene NICM lb/ hr 0.04043 0.039426 0.03943 0.04055 0.052  32.6 all inlet and outlet runs BDL; nat. gas injection m B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO cumene NICM lb/ hr 0.80863 1.213313 1.21331 0.81109 1.609  32.6 all inlet and outlet runs BDL; nat. gas injection m B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO formaldehyde NICM lb/ hr 2.42042 0.892949 0.89295 0.07391 0.037 95.9 all outlet runs BDL; nat. gas injection mode B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO m, p xylene NICM lb/ hr 0.04043 0.053584 0.05358 0.04055 0.071  32.6 all inlet and outlet runs BDL; nat. gas injection m B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO methanol NICM lb/ hr 19.6742 7.913139 7.91314 0.27345 0.144 98.2 all outlet runs BDL; nat. gas injection mode B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO methyl ethyl ketone NICM lb/ hr 0.13607 0.122654 0.12265 0.14392 0.171  39.6 all inlet and outlet runs BDL; nat. gas injection m B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO methyl isobutyl ketone NICM lb/ hr 0.09551 0.119565 0.11956 0.10008 0.165  38.4 all inlet and outlet runs BDL; nat. gas injection m B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO phenol NICM lb/ hr 0.16743 0.197022 0.19702 0.17782 0.276  40.2 all inlet and outlet runs BDL; nat. gas injection m B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO propionaldehyde NICM lb/ hr 0.15124 0.109826 0.10983 0.16032 0.154  39.9 all inlet and outlet runs BDL; nat. gas injection m B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO styrene NICM lb/ hr 0.04043 0.052575 0.05257 0.04055 0.07  32.6 all inlet and outlet runs BDL; nat. gas injection m B1 OSB hot press 4/ 3/ 1998 OSB 3 0 NONE RTO THC as carbon M25A lb/ hr 218.748 32.65834 32.6583 4.36404 0.864 97.4 CH4 not subtracted ( not measured); nat. gas inj mode B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO toluene NICM lb/ hr 0.04043 0.046513 0.04651 0.04055 0.062  32.6 all inlet and outlet runs BDL; nat. gas injection m Page 5 of 7 Unit Test No. of No. of Pre Test Inlet1, Inlet1, Inlet2, Inlet2, Total inlet, Outlet, Outlet, Cont. effic.,

code date Product runs runs BDL treatmen t APCD Pollutant method Units ppm lb/ unit ppm lb/ unit lb/ unit ppm lb/ unit % Comment R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 0 NONE RTO acetaldehyde NICM lb/ hr 6.49437 5.302698 5.3027 0.7489 0.628 88.2 burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO acrolein NICM lb/ hr 3.24896 3.376787 3.37679 0.18193 0.195 94.2 all outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO benzene NICM lb/ hr 0.27958 0.404575 0.40457 0.05044 0.075 81.4 all outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO cumene NICM lb/ hr 0.97392 2.164732 2.16473 1.00871 2.318  7.1 all inlet and outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 1 NONE RTO formaldehyde NICM lb/ hr 22.9191 12.75396 12.754 2.12947 1.268 90.1 1 outlet run BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO m, p xylene NICM lb/ hr 0.20745 0.408414 0.40841 0.05044 0.102 74.9 all outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 2 NONE RTO methanol NICM lb/ hr 8.5945 5.094153 5.09415 0.71303 0.434 91.5 2 outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO methyl ethyl ketone NICM lb/ hr 0.1862 0.248517 0.24852 0.17824 0.246 1.2 all inlet and outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO methyl isobutyl ketone NICM lb/ hr 0.12788 0.237069 0.23707 0.12404 0.237  0.2 all inlet and outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 5 NONE RTO phenol NICM lb/ hr 0.2313 0.40297 0.40297 0.34227 0.62  53.9 all inlet and 5 outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO propionaldehyde NICM lb/ hr 0.51269 0.552495 0.5525 0.19851 0.22 60.1 1 inlet and all outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO styrene NICM lb/ hr 0.0487 0.093801 0.0938 0.05044 0.1  7.1 all inlet and outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 4 0 NONE RTO THC as carbon M25A lb/ hr 766.275 169.8813 169.881 29.3996 6.933 95.9 CH4 not subtracted ( not measured); burner mod R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO toluene NICM lb/ hr 0.41571 0.710179 0.71018 0.05044 0.089 87.5 all outlet runs BDL; burner mode V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 2 NONE RTO acetaldehyde NICM lb/ hr 1.22305 0.376651 0.37665 0.26785 0.09 76.0 2 outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 3 NONE RTO acrolein NICM lb/ hr 0.13418 0.053946 0.05395 0.13302 0.058  7.1 2 inlet and 3 outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 3 NONE RTO benzene NICM lb/ hr 0.03802 0.020804 0.0208 0.03575 0.022  4.1 all inlet and outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 2 NONE RTO formaldehyde NICM lb/ hr 4.38435 0.910997 0.911 0.12438 0.029 96.8 2 outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 3 NONE RTO m, p xylene NICM lb/ hr 0.03802 0.028275 0.02827 0.03575 0.029  4.1 all inlet and outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 2 NONE RTO methanol NICM lb/ hr 5.50852 1.233799 1.2338 0.40357 0.101 91.8 2 outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 3 NONE RTO methyl ethyl ketone ( MEK) NICM lb/ hr 0.12812 0.064735 0.06474 0.13029 0.073  12.4 all inlet and outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 3 NONE RTO methyl isobutyl ketone NICM lb/ hr 0.08991 0.063102 0.0631 0.0902 0.07  10.9 all inlet and outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 3 NONE RTO o xylene NICM lb/ hr 0.03802 0.028275 0.02827 0.03575 0.029  4.1 all inlet and outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 2 NONE RTO phenol NICM lb/ hr 0.21899 0.142386 0.14239 0.235 0.172  21.1 2 inlet and 2 outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 3 NONE RTO propionaldehyde NICM lb/ hr 0.14241 0.057966 0.05797 0.14529 0.065  12.8 all inlet and outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 3 NONE RTO styrene NICM lb/ hr 0.03802 0.027742 0.02774 0.03575 0.029  4.1 all inlet and outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 3 NONE RTO toluene NICM lb/ hr 0.03802 0.024543 0.02454 0.03575 0.026  4.1 all inlet and outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 0 NONE RTO THC as carbon M25A lb/ hr 1814.16 151.151 151.151 87.112 8.1 94.6 CH4 subtracted from inlet and outlet V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 0 NONE RTO acetaldehyde NICM lb/ hr 5.78019 0.868799 0.8688 0.6621 0.107 87.7 V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 3 NONE RTO acrolein NICM lb/ hr 0.13616 0.026373 0.02637 0.13198 0.027  2.4 all inlet and outlet runs BDL V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 3 NONE RTO benzene NICM lb/ hr 0.03741 0.010085 0.01008 0.08223 0.024  134.4 3 inlet and 2 outlet runs BDL V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 0 NONE RTO formaldehyde NICM lb/ hr 4.52957 0.47006 0.47006 2.11837 0.231 50.8 V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 3 NONE RTO m, p xylene NICM lb/ hr 0.03741 0.013706 0.01371 0.03861 0.015  9.2 all inlet and outlet runs BDL V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 0 NONE RTO methanol NICM lb/ hr 21.7145 2.366071 2.36607 1.17621 0.138 94.2 V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 3 NONE RTO methyl ethyl ketone ( MEK) NICM lb/ hr 0.13339 0.033228 0.03323 0.12936 0.034  2.5 all inlet and outlet runs BDL V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 3 NONE RTO methyl isobutyl ketone NICM lb/ hr 0.09268 0.032067 0.03207 0.09087 0.033  3.6 all inlet and outlet runs BDL V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 3 NONE RTO o xylene NICM lb/ hr 0.03741 0.013706 0.01371 0.03861 0.015  9.2 all inlet and outlet runs BDL V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 2 NONE RTO phenol NICM lb/ hr 0.27001 0.085685 0.08569 1.05467 0.36  319.9 2 inlet and 1 outlet run BDL V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 3 NONE RTO propionaldehyde NICM lb/ hr 0.14861 0.029823 0.02982 0.14376 0.03  2.2 all inlet and outlet runs BDL V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 3 NONE RTO styrene NICM lb/ hr 0.03741 0.013448 0.01345 0.03861 0.015  9.2 all inlet and outlet runs BDL V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 3 NONE RTO toluene NICM lb/ hr 0.03741 0.011898 0.0119 0.03861 0.013  9.2 all inlet and outlet runs BDL V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 0 NONE RTO THC as carbon M25A lb/ hr 5090.2 213.0387 213.039 130.063 5.693 97.3 not corrected for CH4 ( corrected value is 98%) Page 6 of 7 Unit Test No. of No. of Pre Test Inlet1, Inlet1, Inlet2, Inlet2, Total inlet, Outlet, Outlet, Cont. effic.,

code date Product runs runs BDL treatmen t APCD Pollutant method Units ppm lb/ unit ppm lb/ unit lb/ unit ppm lb/ unit % Comment B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 3 NONE RCO acetaldehyde NICM lb/ hr 0.80617 0.33195 0.33195 0.20453 0.094 71.7 1 inlet and 3 outlet runs BDL B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 3 NONE RCO acrolein NICM lb/ hr 0.14746 0.077131 0.07713 0.14342 0.084  8.5 all inlet and outlet runs BDL B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 3 NONE RCO benzene NICM lb/ hr 0.04183 0.030486 0.03049 0.03999 0.033  6.7 all inlet and outlet runs BDL B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 3 NONE RCO cumene NICM lb/ hr 0.83664 0.938189 0.93819 0.79985 1.001  6.7 all inlet and outlet runs BDL B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 0 NONE RCO formaldehyde NICM lb/ hr 3.54315 0.992828 0.99283 2.59282 0.81 18.4 B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 3 NONE RCO m, p xylene NICM lb/ hr 0.04183 0.041434 0.04143 0.03999 0.044  6.7 all inlet and outlet runs BDL B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 0 NONE RCO methanol NICM lb/ hr 13.3222 3.977665 3.97767 3.9016 1.299 67.4 B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 3 NONE RCO methyl ethyl ketone NICM lb/ hr 0.14449 0.097204 0.0972 0.14052 0.105  8.5 all inlet and outlet runs BDL B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 3 NONE RCO methyl isobutyl ketone NICM lb/ hr 0.10095 0.094343 0.09434 0.09788 0.102  8.2 all inlet and outlet runs BDL B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 2 NONE RCO phenol NICM lb/ hr 0.75926 0.666977 0.66698 0.23541 0.23 65.5 2 outlet runs BDL B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 3 NONE RCO propionaldehyde NICM lb/ hr 0.16078 0.087128 0.08713 0.15646 0.095  8.6 all inlet and outlet runs BDL B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 3 NONE RCO styrene NICM lb/ hr 0.04183 0.040653 0.04065 0.03999 0.043  6.7 all inlet and outlet runs BDL B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 0 NONE RCO THC as carbon M25A lb/ hr 43.5641 4.87725 4.87725 14.679 1.833 62.4 CH4 not subtracted ( not measured)

B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 3 NONE RCO toluene NICM lb/ hr 0.04183 0.035966 0.03597 0.03999 0.038  6.7 all inlet and outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 0 NONE RCO acetaldehyde NICM lb/ hr 15.4492 2.305014 2.30501 8.57686 1.653 28.3 V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO acrolein NICM lb/ hr 0.92452 0.172285 0.17229 0.14518 0.036 79.4 all outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO benzene NICM lb/ hr 0.36511 0.096476 0.09648 0.04194 0.014 85.2 all outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 0 NONE RCO formaldehyde NICM lb/ hr 20.8234 2.114501 2.1145 7.88849 1.035 51.0 V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO m, p xylene NICM lb/ hr 0.29721 0.107072 0.10707 0.04194 0.019 81.8 all outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 0 NONE RCO methanol NICM lb/ hr 9.26046 0.982028 0.98203 0.93658 0.131 86.7 V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO methyl ethyl ketone ( MEK) NICM lb/ hr 0.29858 0.074157 0.07416 0.14228 0.045 39.6 1 inlet and 3 outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO methyl isobutyl ketone NICM lb/ hr 0.14057 0.048371 0.04837 0.09972 0.044 9.8 2 inlet and 3 outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO o xylene NICM lb/ hr 0.04287 0.015418 0.01542 0.04194 0.019  26.1 all inlet and outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 0 NONE RCO phenol NICM lb/ hr 0.65176 0.20954 0.20954 0.35714 0.147 29.9 V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO propionaldehyde NICM lb/ hr 0.30244 0.05876 0.05876 0.15819 0.04 31.7 1 inlet and 3 outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO styrene NICM lb/ hr 0.14344 0.050678 0.05068 0.04194 0.019 62.3 3 outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO toluene NICM lb/ hr 0.49295 0.153765 0.15377 0.04194 0.017 89.0 3 outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 0 NONE RCO THC as carbon M25A lb/ hr 1831.21 74.82071 74.8207 152.855 8.009 89.3 not corrected for CH4 ( corrected value is 92%) Page 7 of 7 Unit Test No. of No. of Pre Test Inlet1, Inlet1, Inlet2, Inlet2, Total inlet, Outlet, Outlet, Cont. effic.,

code date Product runs runs BDL treatmen t APCD Pollutant method Units ppm lb/ unit ppm lb/ unit lb/ unit ppm lb/ unit % Comment B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO acetaldehyde NICM lb/ hr 0.66465 0.285666 0.28567 0.20392 0.098 65.7 1 inlet and 3 outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO acrolein NICM lb/ hr 0.1491 0.08189 0.08189 0.14304 0.088  6.9 all inlet and outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO benzene NICM lb/ hr 0.04264 0.03263 0.03263 0.03998 0.034  4.4 all inlet and outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO cumene NICM lb/ hr 0.85287 1.004158 1.00416 0.79965 1.049  4.4 all inlet and outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO formaldehyde NICM lb/ hr 2.90441 0.856085 0.85609 0.07461 0.024 97.1 all outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO m, p xylene NICM lb/ hr 0.04264 0.044347 0.04435 0.03998 0.046  4.4 all inlet and outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 0 NONE BIO methanol NICM lb/ hr 90.2856 28.29377 28.2938 17.532 6.086 78.5 B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO methyl ethyl ketone NICM lb/ hr 0.14611 0.103208 0.10321 0.14014 0.11  6.9 all inlet and outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO methyl isobutyl ketone NICM lb/ hr 0.10223 0.100312 0.10031 0.09766 0.107  6.4 all inlet and outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO phenol NICM lb/ hr 4.38731 4.04789 4.04789 0.17299 0.178 95.6 all outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO propionaldehyde NICM lb/ hr 0.16252 0.092479 0.09248 0.15603 0.099  7.0 all inlet and outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO styrene NICM lb/ hr 0.04264 0.043512 0.04351 0.03998 0.045  4.4 all inlet and outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 0 NONE BIO THC as carbon M25A lb/ hr 128.928 15.15461 15.1546 23.0166 3.014 80.1 CH4 not subtracted ( not measured)

B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO toluene NICM lb/ hr 0.04264 0.038495 0.03849 0.03998 0.04  4.4 all inlet and outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 4 NONE BIO acetaldehyde NICM lb/ hr 0.44445 0.303803 0.3038 0.33811 0.267 12.1 2 inlet and 4 outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 6 NONE BIO acrolein NICM lb/ hr 0.18108 0.160815 0.16082 0.13842 0.14 12.8 4 inlet and all outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 6 NONE BIO benzene NICM lb/ hr 0.09785 0.122633 0.12263 0.02539 0.036 70.8 5 inlet and all outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 3 3 NONE BIO cumene NICM lb/ hr 0.50783 0.93177 0.93177 0.50783 1.084  16.4 all inlet and outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 3 NONE BIO formaldehyde NICM lb/ hr 13.4303 6.247704 6.2477 0.21742 0.117 98.1 3 outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 6 NONE BIO m, p xylene NICM lb/ hr 0.02539 0.042088 0.04209 0.02539 0.049  15.5 all inlet and outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 5 NONE BIO methanol NICM lb/ hr 18.8447 9.310108 9.31011 0.31992 0.185 98.0 5 outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 5 NONE BIO methyl ethyl ketone NICM lb/ hr 0.13854 0.157198 0.1572 0.15756 0.205  30.3 5 inlet and 5 outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 5 NONE BIO methyl isobutyl ketone NICM lb/ hr 0.13261 0.211218 0.21122 0.1208 0.218  3.1 5 inlet and 4 outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 6 NONE BIO methylene chloride NICM lb/ hr 0.02539 0.033675 0.03367 0.02539 0.039  15.5 all inlet and outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 6 NONE BIO o xylene NICM lb/ hr 0.02539 0.042088 0.04209 0.02539 0.049  15.5 all inlet and outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 6 NONE BIO phenol NICM lb/ hr 0.13452 0.19759 0.19759 0.15857 0.269  36.3 all inlet and outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 6 NONE BIO propionaldehyde NICM lb/ hr 0.13169 0.119599 0.1196 0.15267 0.16  33.9 all inlet and outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 6 NONE BIO styrene NICM lb/ hr 0.02539 0.041295 0.04129 0.02539 0.048  15.5 all inlet and outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 3 0 NONE BIO THC as carbon M25A lb/ hr 116.757 21.30187 21.3019 27.4422 5.824 72.7 C1 PB press and cooler 4/ 29/ 1997 PB 6 6 NONE BIO toluene NICM lb/ hr 0.02539 0.036533 0.03653 0.02539 0.042  15.5 all inlet and outlet runs BDL Note: Shaded control efficiencies are not meaningful because either all inlet and outlet runs are non detect, or at least 2 inlet runs were non detect. ATTACHMENT 3b Culled HAP Control Efficiency Data Page 1 of 3 Unit Test No. of No. of Pre Test Inlet1, Inlet1, Inlet2, Inlet2, Total inlet, Outlet, Outlet, Cont. effic.,

code date Product runs runs BDL treatmen t APCD Pollutant method Units ppm lb/ unit ppm lb/ unit lb/ unit ppm lb/ unit % Comment B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO formaldehyde NICM lb/ hr 43.2413 7.777488 7.77749 0.09376 0.018 99.8 all outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO methanol NICM lb/ hr 108.6 20.75225 20.7523 0.33786 0.07 99.7 all outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 3 NONE RTO methyl isobutyl ketone NICM lb/ hr 0.56457 0.338532 0.33853 0.11658 0.076 77.6 all outlet runs BDL B1 PB batch press 10/ 23/ 1997 PB 3 0 NONE RTO THC as carbon M25A lb/ hr 555.985 39.84825 39.8483 4.9284 0.383 99.0 CH4 not subtracted ( not measured)

R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 WESP RTO acetaldehyde NICM lb/ hr 1.24594 0.471457 0.47146 0.18018 0.069 85.3 all outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 WESP RTO formaldehyde NICM lb/ hr 1.06017 0.275196 0.2752 0.10622 0.028 89.8 2 outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 1 WESP RTO m, p xylene NICM lb/ hr 0.06568 0.059258 0.05926 0.03914 0.037 38.0 1 inlet and 1 outlet run BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 WESP RTO methanol NICM lb/ hr 4.47411 1.235988 1.23599 0.35166 0.099 92.0 2 outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 0 WESP RTO THC as carbon M25A lb/ hr 488.493 50.41784 50.4178 6.43446 0.673 98.7 CH4 subtracted from inlet & outlet R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 1 WESP RTO toluene NICM lb/ hr 0.08247 0.064641 0.06464 0.03914 0.032 50.7 1 inlet and 1 outlet run BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 3 NONE WESP/ RTO acetaldehyde NICM lb/ hr 1.20706 0.36108 0.36108 0.18018 0.069 80.8 3 outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 NONE WESP/ RTO formaldehyde NICM lb/ hr 0.99953 0.202858 0.20286 0.10622 0.028 86.2 2 outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 2 NONE WESP/ RTO methanol NICM lb/ hr 3.97445 0.859329 0.85933 0.35166 0.099 88.5 2 outlet runs BDL R1 PB rotary pre dryer 6/ 3/ 1998 PB 3 0 NONE WESP/ RTO THC as carbon M25A lb/ hr 488.493 50.41784 50.4178 6.43446 0.673 98.7 CH4 subtracted from inlet & outlet F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO acetaldehyde NICM lb/ hr 11.7403 2.61133 2.61133 0.20281 0.051 98.0 all outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO acrolein NICM lb/ hr 3.3895 0.95692 0.95692 0.14201 0.046 95.2 all outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 2 NONE RTO formaldehyde NICM lb/ hr 4.39499 0.661082 0.66108 0.11196 0.019 97.1 2 outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO methanol NICM lb/ hr 9.34398 1.520261 1.52026 0.26445 0.049 96.8 all outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 3 NONE RTO propionaldehyde NICM lb/ hr 11.7729 3.431402 3.4314 0.15499 0.052 98.5 all outlet runs BDL F1 FB dryer and HB press preheater 10/ 30/ 1997 FB 3 0 NONE RTO THC as carbon M25A lb/ hr 352.185 21.41545 21.4155 4.67233 0.32 98.5 CH4 not subtracted ( not measured)

B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 3 NONE RTO acetaldehyde NICM lb/ hr 0.43672 0.184293 0.18429 0.2078 0.098 46.7 1 inlet and 3 outlet runs BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 0 NONE RTO formaldehyde NICM lb/ hr 5.62712 1.62473 1.62473 0.54175 0.175 89.2 B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 1 NONE RTO methanol NICM lb/ hr 17.7308 5.441179 5.44118 0.83214 0.285 94.8 1 outlet run BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 2 NONE RTO phenol NICM lb/ hr 0.89745 0.810979 0.81098 0.3779 0.383 52.7 2 outlet runs BDL B1 OSB hot press, No. 2 5/ 5/ 1998 OSB 3 0 NONE RTO THC as carbon M25A lb/ hr 51.3821 5.913199 5.9132 3.306 0.426 92.8 CH4 not subtracted ( not measured)

R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO acetaldehyde NICM lb/ hr 33.5545 12.18942 12.1894 5.18795 2.211 81.9 R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO acrolein NICM lb/ hr 8.47441 3.90733 3.90733 1.13352 0.614 84.3 R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO benzene NICM lb/ hr 0.58265 0.376021 0.37602 0.23681 0.179 52.4 R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO formaldehyde NICM lb/ hr 45.2337 11.22791 11.2279 13.1172 3.815 66.0 R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO methanol NICM lb/ hr 24.0545 6.372851 6.37285 4.57033 1.416 77.8 R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 3 WESP RTO methyl ethyl ketone NICM lb/ hr 0.23546 0.139938 0.13994 0.13925 0.097 30.5 1 inlet and 3 outlet runs BDL R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO phenol NICM lb/ hr 0.68283 0.534002 0.534 0.40188 0.366 31.5 R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 1 WESP RTO propionaldehyde NICM lb/ hr 1.41241 0.676412 0.67641 0.26402 0.148 78.1 1 outlet run BDL R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 3 WESP RTO styrene NICM lb/ hr 0.07777 0.066835 0.06683 0.03882 0.039 41.4 1 inlet and 3 outlet runs BDL R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 0 WESP RTO THC as carbon M25A lb/ hr 390.034 38.56629 38.5663 57.191 6.628 82.8 CH4 not subtracted ( not measured)

R1 OSB rotary dryers ( 2) 5/ 7/ 1998 OSB 3 3 WESP RTO toluene NICM lb/ hr 0.33005 0.25076 0.25076 0.03882 0.035 86.2 3 outlet runs BDL B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO acetaldehyde NICM lb/ hr 0.69324 0.64712 0.64712 0.19776 0.166 74.3 nat. gas injection mode; 1 inlet and 3 outlet runs BD B1 OSB hot press 1/ 18/ 1998 OSB 3 2 NONE RTO formaldehyde NICM lb/ hr 3.44725 2.168481 2.16848 0.18984 0.11 94.9 nat. gas injection mode; 2 outlet runs BDL B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO methanol NICM lb/ hr 25.4525 17.03734 17.0373 0.25763 0.157 99.1 nat. gas injection mode; 3 outlet runs BDL B1 OSB hot press 1/ 18/ 1998 OSB 3 2 NONE RTO phenol NICM lb/ hr 0.50408 0.993354 0.99335 0.22458 0.404 59.3 nat gas injection mode; 2 outlet runs BDL B1 OSB hot press 1/ 18/ 1998 OSB 3 3 NONE RTO THC as carbon M25A lb/ hr 255.324 64.32727 64.3273 0.5 0.115 99.8 nat. gas injection mode; all outlet runs BDL; CH4 no subtracted ( not measured) Page 2 of 3 Unit Test No. of No. of Pre Test Inlet1, Inlet1, Inlet2, Inlet2, Total inlet, Outlet, Outlet, Cont. effic.,

code date Product runs runs BDL treatment APCD Pollutant method Units ppm lb/ unit ppm lb/ unit lb/ unit ppm lb/ unit % Comment R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO acetaldehyde NICM lb/ hr 4.63534 4.093543 4.09354 0.19402 0.239 94.2 nat. gas injection mode; all outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO acrolein NICM lb/ hr 2.53329 2.845826 2.84583 0.13626 0.214 92.5 nat. gas injection mode; all outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO benzene NICM lb/ hr 0.15845 0.247967 0.24797 0.03848 0.084 66.0 nat. gas injection mode; all outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 4 WESP RTO formaldehyde NICM lb/ hr 19.0781 11.49902 11.499 0.13634 0.114 99.0 nat. gas injection mode; 4 outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO m, p xylene NICM lb/ hr 0.15135 0.321979 0.32198 0.03848 0.114 64.4 nat. gas injection mode; all outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO methanol NICM lb/ hr 6.85387 4.399032 4.39903 0.25259 0.226 94.9 nat. gas injection mode; all outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO methyl ethyl ketone NICM lb/ hr 0.25732 0.371997 0.372 0.13351 0.27 27.5 nat. gas injection mode; 1 inlet and all outlet runs BD R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO methyl isobutyl ketone NICM lb/ hr 0.24273 0.487206 0.48721 0.09321 0.262 46.3 nat. gas injection mode; all outlet runs BDL R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO propionaldehyde NICM lb/ hr 0.32756 0.381538 0.38154 0.14858 0.242 36.6 nat. gas injection mode; 1 inlet and all outlet runs BD R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 0 WESP RTO THC as carbon M25A lb/ hr 1190 286.0403 286.04 43.8125 14.74 94.8 nat. gas injection mode; CH4 subtracted from inlet &

R2 OSB rotary dryers ( 5) 1/ 15/ 1998 OSB 6 6 WESP RTO toluene NICM lb/ hr 0.31279 0.57752 0.57752 0.03848 0.099 82.8 nat. gas injection mode; all outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO acetaldehyde NICM lb/ hr 31.7964 2.57904 2.57904 0.2011 0.022 99.2 all outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO acrolein NICM lb/ hr 7.78131 0.803204 0.8032 0.14073 0.019 97.6 all outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO formaldehyde NICM lb/ hr 2.62 0.145166 0.14517 0.06714 0.005 96.6 all outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 2 NONE RTO methanol NICM lb/ hr 8.45039 0.497676 0.49768 0.38103 0.03 94.0 2 outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO methyl isobutyl ketone NICM lb/ hr 0.84149 0.155454 0.15545 0.09574 0.024 84.8 all outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 1 NONE RTO phenol NICM lb/ hr 0.36623 0.06332 0.06332 0.28817 0.067  5.8 1 outlet run BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO propionaldehyde NICM lb/ hr 31.5247 3.372796 3.3728 0.15361 0.022 99.3 all outlet runs BDL T1 HB tempering oven 6/ 26/ 1998 HB 3 3 NONE RTO THC as carbon M25A lb/ hr 763.837 16.87325 16.8733 0.5 0.015 99.9 all outlet runs BDL; CH4 subtracted from inlet but no ( all outlet THC = CH4)

M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO acetaldehyde NICM lb/ hr 0.62819 0.369673 0.19796 0.04315 0.41282 0.20345 0.164 60.3 all press and outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 2 RBP RTO formaldehyde NICM lb/ hr 16.2976 6.553666 7.692813 1.14699 7.70065 0.18413 0.101 98.7 2 outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 3 3 RBP RTO methanol NICM lb/ hr 28.6029 12.25112 8.896868 1.40955 13.6607 0.26527 0.155 98.9 all outlet runs BDL M1 Dryer/ continuous press 1/ 13/ 1998 MDF 2 0 RBP RTO THC as carbon M25A lb/ hr 201.149 32.22919 20.33499 1.2081 33.4373 9.58696 2.085 93.8 CH4 not subtracted ( not measured)

B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO formaldehyde NICM lb/ hr 2.42042 0.892949 0.89295 0.07391 0.037 95.9 all outlet runs BDL; nat. gas injection mode B1 OSB hot press 4/ 3/ 1998 OSB 3 3 NONE RTO methanol NICM lb/ hr 19.6742 7.913139 7.91314 0.27345 0.144 98.2 all outlet runs BDL; nat. gas injection mode B1 OSB hot press 4/ 3/ 1998 OSB 3 0 NONE RTO THC as carbon M25A lb/ hr 218.748 32.65834 32.6583 4.36404 0.864 97.4 CH4 not subtracted ( not measured); nat. gas injectio R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 0 NONE RTO acetaldehyde NICM lb/ hr 6.49437 5.302698 5.3027 0.7489 0.628 88.2 burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO acrolein NICM lb/ hr 3.24896 3.376787 3.37679 0.18193 0.195 94.2 all outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO benzene NICM lb/ hr 0.27958 0.404575 0.40457 0.05044 0.075 81.4 all outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 1 NONE RTO formaldehyde NICM lb/ hr 22.9191 12.75396 12.754 2.12947 1.268 90.1 1 outlet run BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO m, p xylene NICM lb/ hr 0.20745 0.408414 0.40841 0.05044 0.102 74.9 all outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 2 NONE RTO methanol NICM lb/ hr 8.5945 5.094153 5.09415 0.71303 0.434 91.5 2 outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO propionaldehyde NICM lb/ hr 0.51269 0.552495 0.5525 0.19851 0.22 60.1 1 inlet and all outlet runs BDL; burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 4 0 NONE RTO THC as carbon M25A lb/ hr 766.275 169.8813 169.881 29.3996 6.933 95.9 CH4 not subtracted ( not measured); burner mode R2 OSB rotary dryer ( 5) 4/ 1/ 1998 OSB 6 6 NONE RTO toluene NICM lb/ hr 0.41571 0.710179 0.71018 0.05044 0.089 87.5 all outlet runs BDL; burner mode V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 2 NONE RTO acetaldehyde NICM lb/ hr 1.22305 0.376651 0.37665 0.26785 0.09 76.0 2 outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 2 NONE RTO formaldehyde NICM lb/ hr 4.38435 0.910997 0.911 0.12438 0.029 96.8 2 outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 2 NONE RTO methanol NICM lb/ hr 5.50852 1.233799 1.2338 0.40357 0.101 91.8 2 outlet runs BDL V1 Dryer 1,2,3,4 heated zones 11/ 17/ 1997 SPW 3 0 NONE RTO THC as carbon M25A lb/ hr 1814.16 151.151 151.151 87.112 8.1 94.6 CH4 subtracted from inlet and outlet V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 0 NONE RTO acetaldehyde NICM lb/ hr 5.78019 0.868799 0.8688 0.6621 0.107 87.7 V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 0 NONE RTO formaldehyde NICM lb/ hr 4.52957 0.47006 0.47006 2.11837 0.231 50.8 V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 0 NONE RTO methanol NICM lb/ hr 21.7145 2.366071 2.36607 1.17621 0.138 94.2 V1 Dryer No. 1,2,3 heated zones 12/ 9/ 1997 SPW 3 0 NONE RTO THC as carbon M25A lb/ hr 5090.2 213.0387 213.039 130.063 5.693 97.3 not corrected for CH4 ( corrected value is 98%) Page 3 of 3 Unit Test No. of No. of Pre Test Inlet1, Inlet1, Inlet2, Inlet2, Total inlet, Outlet, Outlet, Cont. effic.,

code date Product runs runs BDL treatmen t APCD Pollutant method Units ppm lb/ unit ppm lb/ unit lb/ unit ppm lb/ unit % Comment B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 3 NONE RCO acetaldehyde NICM lb/ hr 0.80617 0.33195 0.33195 0.20453 0.094 71.7 1 inlet and 3 outlet runs BDL B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 0 NONE RCO formaldehyde NICM lb/ hr 3.54315 0.992828 0.99283 2.59282 0.81 18.4 B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 0 NONE RCO methanol NICM lb/ hr 13.3222 3.977665 3.97767 3.9016 1.299 67.4 B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 2 NONE RCO phenol NICM lb/ hr 0.75926 0.666977 0.66698 0.23541 0.23 65.5 2 outlet runs BDL B1 OSB hot press, No. 1 5/ 6/ 1998 OSB 3 0 NONE RCO THC as carbon M25A lb/ hr 43.5641 4.87725 4.87725 14.679 1.833 62.4 CH4 not subtracted ( not measured)

V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 0 NONE RCO acetaldehyde NICM lb/ hr 15.4492 2.305014 2.30501 8.57686 1.653 28.3 V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO acrolein NICM lb/ hr 0.92452 0.172285 0.17229 0.14518 0.036 79.4 all outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO benzene NICM lb/ hr 0.36511 0.096476 0.09648 0.04194 0.014 85.2 all outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 0 NONE RCO formaldehyde NICM lb/ hr 20.8234 2.114501 2.1145 7.88849 1.035 51.0 V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO m, p xylene NICM lb/ hr 0.29721 0.107072 0.10707 0.04194 0.019 81.8 all outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 0 NONE RCO methanol NICM lb/ hr 9.26046 0.982028 0.98203 0.93658 0.131 86.7 V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO methyl ethyl ketone ( MEK) NICM lb/ hr 0.29858 0.074157 0.07416 0.14228 0.045 39.6 1 inlet and 3 outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 0 NONE RCO phenol NICM lb/ hr 0.65176 0.20954 0.20954 0.35714 0.147 29.9 V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO propionaldehyde NICM lb/ hr 0.30244 0.05876 0.05876 0.15819 0.04 31.7 1 inlet and 3 outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO styrene NICM lb/ hr 0.14344 0.050678 0.05068 0.04194 0.019 62.3 3 outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 3 NONE RCO toluene NICM lb/ hr 0.49295 0.153765 0.15377 0.04194 0.017 89.0 3 outlet runs BDL V1 Dryer No. 1 and 2 heated zones 7/ 15/ 1998 SPW 3 0 NONE RCO THC as carbon M25A lb/ hr 1831.21 74.82071 74.8207 152.855 8.009 89.3 not corrected for CH4 ( corrected value is 92%)

B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO acetaldehyde NICM lb/ hr 0.66465 0.285666 0.28567 0.20392 0.098 65.7 1 inlet and 3 outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO formaldehyde NICM lb/ hr 2.90441 0.856085 0.85609 0.07461 0.024 97.1 all outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 0 NONE BIO methanol NICM lb/ hr 90.2856 28.29377 28.2938 17.532 6.086 78.5 B1 OSB hot press 6/ 9/ 1998 OSB 3 3 NONE BIO phenol NICM lb/ hr 4.38731 4.04789 4.04789 0.17299 0.178 95.6 all outlet runs BDL B1 OSB hot press 6/ 9/ 1998 OSB 3 0 NONE BIO THC as carbon M25A lb/ hr 128.928 15.15461 15.1546 23.0166 3.014 80.1 CH4 not subtracted ( not measured)

C1 PB press and cooler 4/ 29/ 1997 PB 6 3 NONE BIO formaldehyde NICM lb/ hr 13.4303 6.247704 6.2477 0.21742 0.117 98.1 3 outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 6 5 NONE BIO methanol NICM lb/ hr 18.8447 9.310108 9.31011 0.31992 0.185 98.0 5 outlet runs BDL C1 PB press and cooler 4/ 29/ 1997 PB 3 0 NONE BIO THC as carbon M25A lb/ hr 116.757 21.30187 21.3019 27.4422 5.824 72.7 ATTACHMENT 4 Physical Properties of Organic HAP Physical Properties of Organic HAP Organic HAP Melting Point, ° C ( ° F) Boiling Point,

° C ( ° F) Autoignition ( A)

or Ignition ( I)

Temp, ° C ( ° F) a Lower Flammable/

Explosive Limit,

% b Upper Flammable/

Explosive Limit,

% b Acetaldehyde  123.6 ( 190.5) 20.5 ( 68.9) 185 ( 365) ( A) 4 ( E) 57 ( v/ v)  66 ( E)

Acetophenone 20.5 ( 68.9) 202.3 ( 396.1) 571 ( 1060) ( A)

Acrolein  87.9 ( 126.2) 52.5 ( 126.5) 234 ( 453) ( A) 2.8 ( v/ v, E) 31 ( v/ v, E)

Benzene 5.5 ( 41.9) 80.1 ( 176.2) 530 ( 986) ( A) 1.2 ( v/ v, E) 8.0 ( v/ v, E)

Biphenyl 70 ( 158) 254.7 ( 490.5) 540 ( 1004) ( A) 0.6 ( v/ v, E, at 111

C) 5.8 ( v/ v, E, at 166

C)

Bis( 2 ethylhexyl) phthalate  50 ( 58) 385 ( 545) 350 ( 662) ( A)

Carbon disulfide  110.2 ( 166.4) 46.3 ( 115.3) 100 ( 212) ( I)

90 ( 194) ( A) 1.1 ( v/ v, E) 50 ( v/ v, E)

Carbon tetrachloride  22.8 ( 9.0) 76.8 ( 170.2) Nonflammable Chloroform  63.6 ( 82.5) 61.2 ( 142.2) Nonflammable m Cresol 11.2 ( 52.2) 202.4 ( 396.32) 626 ( 1159) ( A) 1.1 ( v/ v, E) ? ( v/ v, E)

o Cresol 30.4 ( 86.7) 191.2 ( 376.16) 599 ( 1110) ( A) 1.4 ( v/ v, E) ? ( v/ v, E)

p Cresol 35.5 ( 95.9) 201.9 ( 395.4) 559 ( 1038) ( A) 1.1 ( v/ v, E, at 150

C ? ( v/ v, E)

Cumene  96.9 ( 142.4) 152.5 ( 306.5) 420 ( 788) ( A) 0.9 ( v/ v, E) 6.5 ( v/ v, E)

Dibutylphthalate ( di n butyl phthalate)  35 ( 31) 340 ( 644) 402 ( 756) 0.5 ( v/ v, E, at 235

C) ~ 2.5 ( v/ v, E)

Ethyl benzene  94.7 ( 138.5) 136.2 ( 277.2) 432 ( 810) 1.0 ( v/ v, E) 6.7 ( v/ v, E) Organic HAP Melting Point, ° C ( ° F) Boiling Point,

° C ( ° F) Autoignition ( A)

or Ignition ( I)

Temp, ° C ( ° F) a Lower Flammable/

Explosive Limit,

% b Upper Flammable/

Explosive Limit,

% b Ethyl chloride ( Chloroethane)  138.7 ( 217.7) 12.8 ( 55.0) 519 ( 966) ( A) 3.6 ( v/ v, E) 14.8 ( v/ v, E)

Formaldehyde  92 ( 134)  20 ( 4) 430 ( 806) ( A) 7 ( v/ v, E) 73 ( v/ v, E)

n Hexane  95.6 ( 140.1) 68.9 ( 156.0) 225 ( 437) ( A) 1.1 ( v/ v, E) 7.5 ( v/ v, E)

Hydroquinone 170.4 ( 338.7) 285.5 ( 545.9) 515 ( 959) ( A)

Methanol  97.9 ( 144.2) 64.7 ( 148.5) 470 ( 878) ( I)

( 725 867) ( A) 5.5  6.0 ( v/ v, E) 36.5  44 ( v/ v, E)

Methyl bromide ( Bromomethane)  93.3 ( 135.9) 4.0 ( 39) 537 ( 999) ( A) 10 ( v/ v, E) 16 ( v/ v, E)

Methyl chloride ( Chloromethane)  97.5 ( 143.5)  23.9 ( 11.0) 632 ( 1170) ( A) 8.1 ( v/ v, E) 17.3 ( v/ v, E)

Methyl ethyl ketone  86.3 ( 123.3) 78.9 ( 174.0) 510 ( 950) ( A) 1.9 ( v/ v, E) 11.3 ( v/ v, E)

Methyl isobutyl ketone ( MIBK)

( 4 methyl 2 pentanone)  84.7 ( 120.5) 117.5 ( 243.5) 460 ( 860) ( A) 1.4 ( v/ v, E) 7.5 ( v/ v, E)

Methylene chloride  95.9 ( 140.6) 40.1 ( 104.2) 556 ( 1033) ( A) 12 ( v/ v, E) 25 ( v/ v, E)

Methylene diphenyl diisocyanate ( MDI) ( Methylene bisphenyl isocyanate) 37 ( 99) 314 ( 597)

( at 100 kPa) 240 ( 464) ( A)

Phenol 41.5 ( 106.7) 182 ( 360) 715 ( 1319) 1.36 ( v/ v, E) 10 ( v/ v, E)

Propionaldehyde  81 ( 114) 49.3 ( 120.7) 207 ( 405) ( A) 2.6 ( v/ v, E) 17.0 ( v/ v, E)

Styrene  30.8 ( 23.4) 145.5 ( 293.9) 490 ( 914) ( A) 0.9 ( v/ v, E) 6.8 ( v/ v, E)

Toluene  95 ( 139) 110.7 ( 231.3) 480 ( 896) ( A) 1.3 ( v/ v, E) 6.9 ( v/ v, E)

1,1,1 Trichloroethane  301.3 ( 510.3) 74.1 ( 165.4) 537 ( 999) ( A) 8 ( v/ v, E) 16 ( v/ v, E) Organic HAP Melting Point, ° C ( ° F) Boiling Point,

° C ( ° F) Autoignition ( A)

or Ignition ( I)

Temp, ° C ( ° F) a Lower Flammable/

Explosive Limit,

% b Upper Flammable/

Explosive Limit,

% b m Xylene  47.6 ( 53.7) 139.2 ( 282.6) 527 ( 981) ( A) 1.1 ( v/ v, E) 7.0 ( v/ v, E)

o Xylene  25.1 ( 13.2) 144.2 ( 291.6) 463 ( 865) ( A) 0.9 ( v/ v, E) 6.7 ( v/ v, E)

p Xylene 13.3 ( 55.9) 138.1 ( 280.6) 528 ( 982) ( A) 1.1 ( v/ v, E) 7.0 ( v/ v, E)

a The autoignition temperature is the lower limit of the ignition temperature and is a constant, regardless of conditions. The ignition temperature varies depending on fuel to air ratio, total pressure inside the reactor ( or APCD), reactor ( or APCD) geometry, etc.

b The upper flammability limit ( UFL) and the lower flammability limit ( LFL) are the concentrations of a pure substance in air for which the mixture is capable of ignition. If the concentration of a compound in air is above the UFL or below the LFL, the mixture will not ignite, even if exposed to a spark or flame.

References:

Melting and Boiling points Budavari, S., ed. The Merck Index. Eleventh Edition. Rahway, New Jersey: Merck & Co., Inc, 1989.

Felder, R. M. and R. W. Rousseau. Elementary Principles of Chemical Processes. Third Edition. New York: John Wiley & Sons, Inc., 2000.

Perry, R. H., ed. Perry's Chemical Engineers' Handbook. Sixth Edition. New York: McGraw Hill Book Company, 1984.

Autoignition temperatures, Flammability limits Budavari, S., ed. The Merck Index. Eleventh Edition. Rahway, New Jersey: Merck & Co., Inc, 1989.

Howard Hughes Medical Institute Laboratory Chemical Safety Summaries. Reprinted with permission from Prudent Practices in the Laboratory: Handling and Disposal of Chemicals. Copyright 1995 by the National Academy of Sciences. Courtesy of the National Academy Press, Washington, D. C.

http:// www. hhmi. org/ research/ labsafe/ lcss/

International Programme on Chemical Safety ( IPCS) International Chemical Safety Cards ( ICSCs).

http:// www. inchem. org/ pages/ icsc. html


[Federal Register Volume 76, Number 235 (Wednesday, December 7, 2011)]
[Rules and Regulations]
[Pages 76299-76300]
[FR Doc No: 2011-31218]

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DEPARTMENT OF HOMELAND SECURITY

Coast Guard

33 CFR Part 155

[Docket No. USCG-2011-0576]
RIN 1625-AB75

Higher Volume Port Area--State of Washington

AGENCY: Coast Guard, DHS.

ACTION: Notice of intent.

-----------------------------------------------------------------------

SUMMARY: The Coast Guard announces that it intends to comply with
recent legislation that would expand an existing higher volume port
area (HVPA) for Puget Sound and the Strait of Juan de Fuca. The
expansion would add Pacific Ocean waters, under U.S. jurisdiction and
within a 50-mile arc measured from Cape Flattery, Washington, to the
HVPA. Higher volume port areas require certain tankers to plan for
faster response times following a spill of the tanker's cargo.

The expansion could require a tanker's owner or operator to review and
modify the tanker's existing vessel response plan (VRP) accordingly,
and to receive Coast Guard approval for the modified VRP by October 15,
2015.

ADDRESSES: The docket for this notice of intent is available for
inspection or copying at the Docket Management Facility (M-30), U.S.
Department of Transportation, West Building Ground Floor, Room W12-140,
1200 New Jersey Avenue SE., Washington, DC 20590, between 9 a.m. and 5
p.m., Monday through Friday, except Federal holidays. You may also find
this docket on the Internet by going to http://www.regulations.gov,
inserting USCG-2011-0576 in the ``Keyword'' box, and then clicking
``Search.''

FOR FURTHER INFORMATION CONTACT: If you have questions about this
notice of intent, call or email LT Evelynn Samms, U.S. Coast Guard
Office of Vessel Activities; telephone<PHONE_NUMBER>, email
<EMAIL_ADDRESS>If you have questions on viewing the material
in the docket, call Ms. Renee V. Wright, Program Manager, Docket
Operations, telephone<PHONE_NUMBER>.

SUPPLEMENTARY INFORMATION: A tanker is required by U.S. law and Coast
Guard regulations to have a vessel response plan (VRP) if its cargo
consists of petroleum or non-petroleum oil, animal fat, and/or
vegetable oil. A VRP describes how the tanker prevents, mitigates, or
responds to spills of its cargo. See 33 CFR 155.1010, 33 CFR 155.1110,
and 33 CFR 155.1210. In describing how the tanker would respond to a
spill, the VRP must demonstrate the tanker's ability to deploy specific
response resources within one of three different timeframes (Tiers 1
through 3). 33 CFR 155.1020. Those response resources typically include
the services of nearby response vessels under a contract between the
tanker's owner or operator and an oil spill response organization that
owns the response vessel. In 14 higher volume port areas (HVPAs)
defined in 33 CFR 155.1020, the risk of a cargo spill is considered
higher than normal because of a higher volume of shipping activity in
these HVPAs. To offset the increased risk, these HVPAs require faster
response times for each Tier.
    The Coast Guard Authorization Act of 2010 (``the Act''), Pub. L.
111-281, 124 Stat. 2905, was enacted on October 15, 2010, and provides
the authority for issuing this notice of intent. Section 710 of the Act
requires the Coast Guard to undertake action that will lead to the
expansion of the HVPA in the Strait of Juan de Fuca and Puget Sound,
Washington. Expansion would be achieved by moving the seaward boundary
of the HVPA, currently a 50-mile arc centered on the entrance to Port
Angeles, Washington, westward to Cape Flattery, Washington. Moving the
seaward boundary would add Pacific Ocean waters that are under U.S.
jurisdiction and within a 50-mile arc measured from Cape Flattery to
the Strait of Juan de Fuca and Puget Sound. We added an excerpt from
navigation chart 18480, ``Approaches to Strait of Juan de Fuca--
Destruction Island to Amphitrite Point,'' showing the revised HVPA, to
the docket.
    A currently valid VRP attests to a tanker's ability to comply with
HVPA response time requirements within the more sheltered waters of the
current HVPA, but the same tanker may need to revise its VRP to account
for spill response in the open ocean waters of the future expanded
HVPA. There may also be some tankers that do not operate within the
current boundaries of the HVPA, but that do operate in the open ocean
offshore of those boundaries, and these tankers may need to revise
their VRPs to show how they will comply with HVPA requirements once
those ocean waters become part of the HVPA.
    The Act further requires that, if a VRP needs to be revised in
light of the boundary change, the Coast Guard must approve the revision
not later than October 15, 2015. Our purpose in issuing this document
is to announce our intent to comply with the Act. The HVPA has not yet
been expanded; therefore, we cannot require tanker owners and operators
to revise VRPs in preparation for expansion at this time. However, if
you would be affected by the future expansion of the HVPA and would
need a VRP covering the expanded area, we advise you to begin
developing a VRP now so that you can submit it in time for Coast Guard
review and approval before the mandatory October 15, 2015, deadline.

    Dated: November 23, 2011.
Paul F. Thomas,
Captain, U.S. Coast Guard, Acting Director of Prevention Policy.
[FR Doc. 2011-31218 Filed 12-6-11; 8:45 am]
BILLING CODE 9110-04-P


[Federal Register Volume 77, Number 208 (Friday, October 26, 2012)]
[Notices]
[Pages 65375-65376]
[FR Doc No: 2012-26356]

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DEPARTMENT OF ENERGY

Federal Energy Regulatory Commission

Combined Notice of Filings

    Take notice that the Commission has received the following Natural
Gas Pipeline Rate and Refund Report filings:

Filings Instituting Proceedings

    Docket Numbers: RP13-166-000.
    Applicants: Centra Pipelines Minnesota Inc.
    Description: Revised Index of Shippers to be effective 12/1/2012.
    Filed Date: 10/18/12.
    Accession Number: 20121018-5059.
    Comments Due: 5 p.m. ET 10/30/12.

    Docket Numbers: RP13-167-000.
    Applicants: TC Offshore LLC.
    Description: NAESB 2.0 to be effective 12/1/2012.
    Filed Date: 10/18/12.
    Accession Number: 20121018-5108.
    Comments Due: 5 p.m. ET 10/30/12.

    Docket Numbers: RP13-168-000.
    Applicants: Central New York Oil And Gas, L.L.C.
    Description: MARC I Interim FTSA Filing to be effective 12/31/9998.
    Filed Date: 10/19/12.
    Accession Number: 20121019-5104.
    Comments Due: 5 p.m. ET 10/31/12.

    Docket Numbers: RP13-169-000.
    Applicants: El Paso Natural Gas Company, L.L.C.
    Description: Atmos Energy Non-Conforming TSA to be effective 10/25/
2012.
    Filed Date: 10/19/12.
    Accession Number: 20121019-5143.
    Comments Due: 5 p.m. ET 10/31/12.

    Docket Numbers: RP13-170-000.
    Applicants: Columbia Gulf Transmission Company.
    Description: Columbia Gulf Transmission Company submits tariff
filing per 154.601: Negotiated Rate Svc Agreements--NJR, Vitol,
Tenaska, LD to be effective 11/1/2012.
    Filed Date: 10/19/12.
    Accession Number: 20121019-5167.
    Comments Due: 5 p.m. ET 10/31/12.

    Docket Numbers: RP13-171-000.
    Applicants: Texas Eastern Transmission, LP.
    Description: PCB TETLP DEC 2012 FILING to be effective 12/1/2012.
    Filed Date: 10/22/12.
    Accession Number: 20121022-5000.
    Comments Due: 5 p.m. ET 11/5/12.

    Any person desiring to intervene or protest in any of the above
proceedings must file in accordance with Rules 211 and 214 of the
Commission's Regulations (18 CFR 385.211 and 385.214) on or before 5:00
p.m. Eastern time on the specified comment date. Protests may be
considered, but intervention is necessary to become a party to the
proceeding.

Filings in Existing Proceedings

    Docket Numbers: RP13-156-001.
    Applicants: Central New York Oil And Gas, L.L.C.
    Description: MARC I FTSA Compliance Filing--Correction2 to be
effective 12/31/9998.

    Filed Date: 10/19/12.
    Accession Number: 20121019-5035.
    Comments Due: 5 p.m. ET 10/31/12.

    Docket Numbers: RP13-60-001.
    Applicants: Tennessee Gas Pipeline Company, L.L.C.
    Description: NAESB V 2.0 Minor Corrections to 10/1/12. Compliance
Order No. 587-V Filing to be effective 12/1/2012.
    Filed Date: 10/19/12.
    Accession Number: 20121019-5043.
    Comments Due: 5 p.m. ET 10/31/12.

    Any person desiring to protest in any the above proceedings must
file in accordance with Rule 211 of the Commission's Regulations (18
CFR 385.211) on or before 5:00 p.m. Eastern time on the specified
comment date.
    The filings are accessible in the Commission's eLibrary system by
clicking on the links or querying the docket number.
    eFiling is encouraged. More detailed information relating to filing
requirements, interventions, protests, and service can be found at:
http://www.ferc.gov/docs-filing/efiling/filing-req.pdf. For other
information, call<PHONE_NUMBER> (toll free). For TTY, call (202) 502-
8659.

    Dated October 22, 2012.
Nathaniel J. Davis, Sr.,
Deputy Secretary.
[FR Doc. 2012-26356 Filed 10-25-12; 8:45 am]
BILLING CODE 6717-01-P