OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

Data to the left of the orange column in this tab are NEI inventory data to be updated according to the instructions in section D2 of the survey overview document. EPA will use the NEI data to determine residual risk for the pulp and paper source category. Do not over-write gray shaded NEI data. Facility data from the NEI to be reviewed and revised. Follow instructions in section D2 of the survey overview document to populate this table to the right of the orange column.

Instruction: Email address for person providing comments A general descriptive comment on the revision Name of person providing comments Commenter's affiliation - state/local/agency, trade association, company, etc. Phone number for person providing comments Survey overview reference:

Field: Commenter Email Address Commenter General Comment Commenter Name Commenter Organization Commenter Phone Number

Example entry: jane.doe@amymillusa.com Jane Doe Anymill USA 999-999-9999

Facility EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 1 of 101Yes/No If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.

Data to the left of the orange column in this tab are NEI inventory data to be updated according to the instructions in section D2 of the survey overview document. EPA will use the NEI data to determine residual risk for the pulp and paper source category.

See State and County FIPS tab in Lookups for P&P Survey.xls See Tribal Code tab in Lookups for P&P Survey.xls See Tribal Code tab

in Lookups for P&P Survey.xls Enter revised Tribal

Code here Two-character

alphabetical code for state County name for

MACT facility Enter revised county

name here See State and

County FIPS tab in Lookups for P&P Survey.xls Unique identifier

assigned by EPA to NEI Facility The ID number

assigned by the EPA Facility Registry System. FRS IDs can be found at: http://w ww.epa.gov/envi ro/html/facility.html. Enter revised Facility Registry Identifier here 01 - MAJOR (HAP

emitting facility) 02 - Area (HAP emitting facility) Definition

associated with Facility Category Code For the facility code

us one of the following: 01 - MAJOR (HAP emitting facility) 02 - Area (HAP emitting facility)

EPA Region Tribal Code Tribe Name REVISED Tribal Code State Abbreviation County Name REVISED County Name State County FIPs NEI Site ID Facility Registry Identifier REVISED Facility Registry Identifier Facility Category Facility Category Description REVISED Facility

Category Code

3 000 Non-Tribal Area VA Amherst County 51009 99999 110020689999 01 MAJOR (HAP emitting facility)

Facility EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 2 of 101The name of the facility of the MACT facility Enter revised Facility Name here Physical street address

for MACT facility City where the MACT facility is located State where MACT

facility is located Zip Code for the

MACT facility Enter revised

Location Address here Enter revised city

name here Enter revised State

here Enter revised Zip

Code here Indicate the year

closed if the facility is no longer in operation (permanently closed)

Facility Name REVISED Facility Name Location Address City State Zip Code REVISED Location Address REVISED City REVISED State REVISED Zip Code Closed Year

Anymill USA 1000 Plant Road Anytown VA 24553

Facility EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 3 of 101Pulp and Paper sector facility data. Follow instructions in section D3 of the survey overview document to populate this table to the right of the orange column.

Instruction: Name of legal operator of facility Complete street address of facility (physical location) Survey overview reference:

Field: Legal operator Physical address Physical city Physical state Physical zip Physical county

Example entry: Gaint Corporation 1000 Plant Road Anytown VA 24553 Amherst Pull down menu text located below this line

Facility EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 4 of 101Provide mailing address if different than physical location Facility contact able to answer technical questions about the completed survey

Mail address Mail city Mail state Mail zip Mail county Facility contact name Facility contact title Facility contact phone Facility contact ext Facility

contact fax Facility contact email

PO Box 123 Fairspring VA 24554 Amherst Joe Smith Environmental Manager 999-999-9999 456 999-999-8888 joe.smith@anymillusa.com

Facility EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 5 of 101If not the same as legal operator, provide name and address of legal owner of this facility Dun and Bradstreet Number for the legal

owner of this mill (see TRI Form R) (Optional) Dun and Bradstreet Number for this mill (if the mill has its own Dun and Bradstreet Number) If you operate a non-major source, follow the instructions for notifying EPA to determine if you should complete this survey.

See subpart A definition of "major source" in survey attachment 2. "Area" is not major without controls. "Synthetic minor" is not major considering controls. The primary NAICS code represents the line of business that generates the most income for the facility.

Legal owner address Legal owner city Legal

owner state Legal

owner zip Dun Bradstreet

owner Dun Bradstreet mill HAP size classification Primary NAICS

100 Corporate Blvd Green Bay WI 54304 9020777 149810921 major 322121-Paper (except New sprint) Mills major 322110-Pulp Mills area (true) 322121-Paper (except New sprint) Mills synthetic minor 322122-New sprint Mills not known 322130-Paperboard Mills 322211-Corrugated and Solid Fiber Box Manufacturing 322212-Folding Paperboard Box Manufacturing 322213-Setup Paperboard Box Manufacturing 322214-Fiber Can, Tube, Drum, and Similar Products Manufacturing 322215-Non-Folding Sanitary Food Container Manufacturing 322221-Coated and Laminated Packaging Paper Manufacturing 322222-Coated and Laminated Paper Manufacturing 322223-Coated Paper Bag and Pouch Manufacturing 322224-Uncoated Paper and Multiwall Bag Manufacturing 322225-Laminated Aluminum Foil Manufacturing for Flexible Packaging Uses 322226-Surface-Coated Paperboard Manufacturing 322231-Die-Cut Paper and Paperboard Office Supplies Manufacturing 322232-Envelope Manufacturing 322233-Stationery, Tablet, and Related Product Manufacturing 322291-Sanitary Paper Product Manufacturing 322299-All Other Converted Paper Product Manufacturing

Facility EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 6 of 101Size of entity. Enter the approximate number of employees (worldwide) of the business enterprise that owns this facility, including where applicable, the parent company and all subsidiaries, branches, and unrelated establishments owned by the parent company. Please count full-time, part-time, and temporary employees equally. Enter the number offacility employees (fulltime, part-time, and temporary employees should be counted equally) The small business size standards for NAICS 322 are based on number of employees of the parent company: 750 employees for NAICS 322110- 322130, 322212, and 322215; and 500 employees for all other 322xxx NAICS. See also survey Attachment 3.

Worldwide employees Facility employees Small business P&P NESHAP subpart S Combustion

Source NESHAP subpart MM Paper/web

coating NESHAP subpart JJJJ Boiler

NESHAP subpart DDDDD Other

NESHAP (list subparts) Kraft NSPS

subpart BB Boiler

NSPS Other NSPS (list

subparts)

>1000 500-749 no Applies Applies Applies Applies N/A Applies Db N/A <50 <50 yes Applies Applies Applies Applies Applies D 50-99 50-99 no N/A N/A N/A N/A N/A N/A Da N/A 100-499 100-499 don’t know Db 500-749 500-749 Dc 750-999 750-999 >1000 >1000 Federal rule coverage. Indicate "applies" for each federal NESHAP and NSPS that apply at the mill. Mark "N/A" if not applicable. For the others list as such "Subpart __"

Facility EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 7 of 101Pulps

Select yes/no Select yes/no Select yes/no Select yes/no Select from menu. You may write in more than once choice. Bleaching systems

Does the mill produce virgin pulp? Does the mill produce

pulp from secondary post consumer fiber? Does the mill purchase virgin pulp? Does the mill purchase secondary fiber pulp? Types of market pulp produced by the mill Is bleaching performed at the mill?

yes no no no N/A yes yes yes yes yes Dissolving pulp yes
no no no no Softw ood chemical market pulp no Hardw ood chemical market pulp Mechanical market pulp Market pulp from secondary (recycled) fiber N/A can be more than one

Facility EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 8 of 101Natural gas supply Paper or paperboard processes/products Enter decimal percent for utilization (e.g., 0.7 for 70% of capacity utilized) Enter decimal percent for utilization (e.g., 0.7 for 70% of capacity utilized) for the past 5 years. To determine the 5-year utilization, average the utilization percentages for 2005, 2006, 2007, 2008, and 2009.

Type of natural gas supply available to the mill Total number of paper machines 2009 total

paper/paperboard capacity (short tons/year) 2009

paper/paperboard capacity utilization percentage 5-year average (2005- 2009) paper/paperboard capacity utilization percentage Table 1 totals

should match column I.14. This column provides a check.

pipeline 1 340000 0.8 0.95 340000 pipeline local distribution company (e.g., truck delivery) none (natural gas is currently unavailable)

Facility EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 9 of 101Enter 2009 total mill capacity of each paper grade below

for all paper machines including idle machines in 2009 (st/yr - short tons per year). Use the paper grades most closely related to the paper grades produced at your mill if you do not find an exact match. Specify other paper grade(s) if none of the grades to the left reasonably match the grades produced at your mill Enter capacity for

"other" paper grade(s)

newsprint (short tons/year) coated free sheet (short tons/year) uncoated free sheet (short tons/year) coated

groundwood (short tons/year) uncoated

groundwood (short tons/year) tissue &

sanitary (short tons/year) specialty

packaging & industrial (short tons/year) kraft packaging

(short tons/year) linerboard

(short tons/year) corrugating

medium (short tons/year) solid bleached

board (short tons/year) recycled board

(short tons/year) construction

paper and board (short tons/year) other (specify

type) other (short

tons/year)

340000

Facility EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 10 of 101

### OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

Data to the left of the orange column in this tab are NEI inventory data to be updated according to the instructions in section D2 of the survey overview document. EPA will use the NEI data to determine residual risk for the pulp and paper source category. Do not over-write gray shaded NEI data. Inventory data from the NEI to be reviewed and revised.

Instruction: OPTIONAL. Use this column for comments related to emissions. OPTIONAL. Use this

column for comments related to the process. OPTIONAL. Use this

column for comments related to stack configuration. Unique ID number used

by a state/local/tribal agency to identify a facility Unique identifier assigned by EPA to NEI Facility The name of the

facility of the MACT facility See the SIC tab in

Lookups for P&P Survey.xls See the SIC tab in

Lookups for P&P Survey.xls Survey overview reference:

Field: CommentEmissions Comment-Process Comment-Stack State Facility Identifier NEI Site ID Facility Name SIC Code SIC Code Description

Example entry: 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631 00022 99999 Anymill USA 2631

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 11 of 101

### Yes/No If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.

Data to the left of the orange column in this tab are NEI inventory data to be updated according to the instructions in section D2 of the survey overview document. EPA will use the NEI data to determine residual risk for the pulp and paper source category.

North American Industry Classification Code. An industry classification system, NAICS is erected on a production-oriented conceptual framework that groups establishments into industries according to similarity in the process used to produce goods or services.

See Lookups for P&P survey.xls or Attachment 3 to the P&P survey instructions. Unique ID reported consistently over time by state/local/tribal agency Enter description of the emission unit. Use this field to identify emission units for which SCCs are not available or areassigned generic or "not-elsewhereclassified" SCCs. See the survey overview document for additional instructions. Indicate the general type of emission process associated with the specified emission point (e.g., Kraft Pulping, Causticizing, Semichemical Pulping, etc). See the "P&P Att 1 with SCC" and "All 11575 SCC" tabs in Lookups for P&P survey.xls for a listing of Emission Process Groups crosswalked with the SCCs.

NAICS Code Emission Unit ID Emission Unit Description REVISED Emission Unit Description Emission Process Group

322130 1 BLR01 B&W(NORTH) BOILER Residual Oil 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER 322130 1 BLR01 B&W(NORTH) BOILER

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 12 of 101

### Unique ID reported consistently over time by state/local/ tribal agency Source Classification

Code.

See Lookups for P&P survey.xls and the pulp and paper survey instructions. Enter revised SCC

Code here.

See Lookups for P&P survey.xls and the pulp and paper survey instructions. Descriptive text

associated with SCC code State/local/tribal ID for

point/location where emissions are released to ambient air The code for physical configuration of the release point: 1 - Fugitive 2 - Vertical 3 - Horizontal 4 - Goose Neck 5 - Vertical with Rain Cap 6 - Downward-facing Vent 99 - Unknown Descriptive text for EmissionReleasePointTyp e code: 1 - Fugitive 2 - Vertical 3 - Horizontal 4 - Goose Neck 5 - Vertical with Rain Cap 6 - Downward-facing Vent 99 - Unknown This column is included for informational purposes to reflect what is included in prior versions of the inventory. Emission unit descriptions should be entered into the "REVISED Emission Unit Description" column.

Process ID SCC REVISED SCC SCC Description Emission Release Point ID Emission Release Point Type Emission Release Point Type Description EMISSION_RELEASE_PT_DESCRIPT

1 10200401 1 02 BOILERS-NORTH AND SOUTH 1 10200401 1 02 BOILERS-NORTH AND SOUTH 1 10200401 1 02 BOILERS-NORTH AND SOUTH 1 10200401 1 02 BOILERS-NORTH AND SOUTH 1 10200401 1 02 BOILERS-NORTH AND SOUTH 1 10200401 1 02 BOILERS-NORTH AND SOUTH 1 10200401 1 02 BOILERS-NORTH AND SOUTH 1 10200401 1 02 BOILERS-NORTH AND SOUTH 1 10200401 1 02 BOILERS-NORTH AND SOUTH 1 10200401 1 02 BOILERS-NORTH AND SOUTH 1 10200401 1 02 BOILERS-NORTH AND SOUTH 1 10200401 1 02 BOILERS-NORTH AND SOUTH 1 10200401 1 02 BOILERS-NORTH AND SOUTH 2 10200601 1 02 BOILERS-NORTH AND SOUTH 2 10200601 1 02 BOILERS-NORTH AND SOUTH 2 10200601 1 02 BOILERS-NORTH AND SOUTH 2 10200601 1 02 BOILERS-NORTH AND SOUTH 2 10200601 1 02 BOILERS-NORTH AND SOUTH 2 10200601 1 02 BOILERS-NORTH AND SOUTH 2 10200601 1 02 BOILERS-NORTH AND SOUTH 2 10200601 1 02 BOILERS-NORTH AND SOUTH 2 10200601 1 02 BOILERS-NORTH AND SOUTH 2 10200601 1 02 BOILERS-NORTH AND SOUTH 2 10200601 1 02 BOILERS-NORTH AND SOUTH K 30700199 KR-1 02 K 30700199 KR-1 02

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 13 of 101

### Start date of the period in which reported emissions occur, e.g., 20050101 = January 1, 2005 End date of the

period in which reported emissions occur, e.g., 20051231 = December 31, 2005 Enter revised Start

Date here Enter revised End

Date here Code assigned by EPA to

individual pollutants. See The Pollutant tab in Lookups for P&P Survey.xls Enter revised Pollutant Code here Descriptive text associated with pollutant code. See The Pollutant

tab in Lookups for P&P Survey.xls

Start Date End Date REVISED Start Date REVISED End Date Pollutant Code REVISED Pollutant Code Pollutant_Code_Desc

20020101 20021231 20090101 20091231 PM10-FIL Primary PM10, Filterable Portion Only 20020101 20021231 CO Carbon Monoxide 20020101 20021231 NH3 Ammonia 20020101 20021231 NOX Nitrogen Oxides 20020101 20021231 PM10-FIL Primary PM10, Filterable Portion Only 20020101 20021231 PM10-PRI Primary PM10 (Includes Filterables + Condensibles) 20020101 20021231 PM25-FIL Primary PM2.5, Filterable Portion Only 20020101 20021231 PM25-PRI Primary PM2.5 (Includes Filterables + Condensibles) 20020101 20021231 PM-CON Primary PM Condensible Portion Only (All Less Than 1 Micron) 20020101 20021231 SO2 Sulfur Dioxide 20020101 20021231 VOC Volatile Organic Compounds 20050101 20051231 226 Nickel & Compounds 20050101 20051231 7439921 Lead 20020101 20021231 CO Carbon Monoxide 20020101 20021231 NH3 Ammonia 20020101 20021231 NOX Nitrogen Oxides 20020101 20021231 PM10-FIL Primary PM10, Filterable Portion Only 20020101 20021231 PM10-PRI Primary PM10 (Includes Filterables + Condensibles) 20020101 20021231 PM25-FIL Primary PM2.5, Filterable Portion Only 20020101 20021231 PM25-PRI Primary PM2.5 (Includes Filterables + Condensibles) 20020101 20021231 PM-CON Primary PM Condensible Portion Only (All Less Than 1 Micron) 20020101 20021231 SO2 Sulfur Dioxide 20020101 20021231 VOC Volatile Organic Compounds 20050101 20051231 50000 Formaldehyde 20050101 20051231 7439976 Mercury 20050101 20051231 7440439 Cadmium

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 14 of 101

### Broader grouping to which an individual chemical compound is assigned to by EPA. For example, “lead and compounds” contains all pollutants containing lead. Numeric value of routine emissions in tons/year Enter revised routine emissions value here Use one of the following Emission Calculation Method Codes:

01 - CEMS - CONTINUOUS EMISSION MONITORING SYSTEM 02 - ENGINEERING JUDGMENT 03 - MATERIAL BALANCE 04 - STACK TEST 05 - EPA SPECIATION PROFILE 06 - STATE/LOCAL SPECIATION PROFILE 07 - MANUFACTURER SPECIFICATION 08 - EPA EMISSION FACTOR 09 - STATE/LOCAL EMISSION FACTOR 10 - SITE-SPECIFIC EMISSION FACTOR 11 - VENDER EMISSION FACTOR 12 - TRADE GROUP EMISSION FACTOR Maximum hourly emission rate for routine emissions. Emissions that occurred during startup periods. Maximum hourly

emission rate for startup period emissions.

HAP_CATEGORY_NAME Emissions (TPY) Routine Emissions (TPY) Emission Calculation Method Code For Revised Emissions Routine Emissions Max Hourly

Rate (lbs per hour) Startup Emissions (TPY) Startup Emissions

Max Hourly

Rate (lbs per hour)

PM 0.314416647 8.56 04 0.51 8.5 CO 0.9375 NH3 0.15 NOX 8.813 PM 0.314416647 PM 2.156 PM 0.314416647 PM 2.156 PM 1.841583252 SO2 32.381 VOC 0.0525 Nickel Compounds 0.116568 Lead Compounds 0.002083 CO 41.916 NH3 1.597 NOX 139.72 PM 0.947999954 PM 1.108910486 PM 0.947999954 PM 1.108910486 PM 0.160910532 SO2 0.2994 VOC 2.745 Formaldehyde 0.0000375 Mercury Compounds 0.00014016 Cadmium Compounds 0.00063072

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 15 of 101

### Emissions that occurred during shutdown periods. Maximum hourly

emission rate for shutdown period emissions. Emissions that

occurred during periods of malfunction. Maximum hourly

emission rate for emissions that occurred during periods of malfunction. See the MACT Code

tab in Lookups for P&P Survey.xls. Use the MACT Code listed with the MACT Source Category description. Enter revised MACT Code here.

See the MACT Code tab in Lookups for P&P Survey.xls. See the MACT Code

tab in Lookups for P&P Survey.xls. Use the MACT Source Category description listed with the MACT Code The height (in feet) of

a stack The temperature of

an exit gas stream (degree Fahrenheit) The diameter (in

feet) of a stack

Shutdown Emissions (TPY) Shutdown

Emissions Max Hourly Rate (lbs per hour) Malfunction

Emissions (TPY) Malfunction

Emissions Max Hourly Rate (lbs per hour) MACT Code REVISED MACT Code MACT Source

Category Stack Height Exit Gas Temperature Stack Diameter

0.23 3.8 1.6 26.7 0107-3 100 400 9 0107-3 100 400 9 0107-3 100 400 9 0107-3 100 400 9 0107-3 100 400 9 0107-3 100 400 9 0107-3 100 400 9 0107-3 100 400 9 0107-3 100 400 9 0107-3 100 400 9 0107-3 100 400 9 0107-3 100 400 9 0107-3 100 400 9 0107-2 100 400 9 0107-2 100 400 9 0107-2 100 400 9 0107-2 100 400 9 0107-2 100 400 9 0107-2 100 400 9 0107-2 100 400 9 0107-2 100 400 9 0107-2 100 400 9 0107-2 100 400 9 0107-2 100 400 9 1626-1 127.1208115 224.3161621 5.395833492 1626-1 127.1208115 224.3161621 5.395833492

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 16 of 101

### The velocity of an exit gas stream (feet per second) Numeric value of

stack gas flow rate in actual cubic feet per second The stack default code is a 5-digit code that indicates if and how the

stack parameters were defaulted. Each digit represents a stack parameter in the following order: stack height, exit gas temperature, stack diameter, exit gas velocity, and exit gas flowrate. The individual digits in the string indicate the source of the defaulted parameters: 0= Original Value, 1 = SCC Default, 2 = SIC Default, 3 = National Default, 4 = Calculated Value, 5 = MACT Default, 6 = State Revision, 8 = CAMD Value. Thus, 22222 means all 5 parameters were defaulted using SIC Default List. Descriptive text associated with StackDefaultFlag Dimension of the

source in the eastwest (x-) direction, commonly

referred to as length Dimension of the

source in the northsouth (y-) direction, commonly

referred to as width Release angle (clockwise

from true North); orientation of the y-dimension relative to true North, measured positive for clockwise starting at 0 degrees (maximum 89 degrees); will assume 0 degrees if it is not provided in data submittal Enter revised Stack Height here

Exit Gas Velocity Exit Gas Flow Rate Stack Default Flag Stack Default Flag Description Fugitive Length (EW) (ft) Fugitive Width (N-S)

(ft) Fugitive Angle (degrees) REVISED Stack Height (ft)

19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 19.42000008 1235.199951 00000 38.29502869 875.6871948 00000 38.29502869 875.6871948 00000

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 17 of 101

### Enter revised Exit Gas Temperature here Enter revised Stack Diameter

here Enter revised Exit Gas Velocity here Enter revised Exit

Gas Flowrate here Enter revised

dimension of thesource in the eastwest (x-) direction, commonly

referred to as length Enter revised

dimension of thesource in the northsouth (y-) direction, commonly

referred to as width Enter revised release

angle (clockwise from true North);orientation of the ydimension relative to true North, measured positive for clockwise starting at 0 degrees (maximum 89 degrees); will assume 0 degrees if it is not provided in data submittal Code indicating

source of emissions estimate (state, EPA, TRI, etc.).

See Lookups for P&P survey.xls

Specify "RTR09" for new rows that you add. Code that represents

the performance level, or operating scenario, for the HAP emissions reported. 01 - Actual 02 - Allowable 03 - Maximum 04 - Potential Descriptive text

associated with code for HAP Performance Level

REVISED Exit Gas Temperature (F) REVISED Stack Diameter

(ft) REVISED Exit Gas Velocity (ft/sec) REVISED Exit Gas

Flow Rate (cuft/sec) REVISED Fugitive

Length (E-W) (ft) REVISED Fugitive

Width (N-S) (ft) REVISED Fugitive

Angle (degrees) Data Source Code HAP Emissions Performance Level HAP Emissions

Performance Level Description

440 22.6 1437 R R R R R R R R R R R S 01 S 01 R R R R AUGPM10FIL R AUGPM25FIL R R R S 01 R 01 R 01

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 18 of 101

### Longitude measured in decimal degrees of the angular distance on a meridian east or west of the prime meridian. Negative (-) data point for N America. Include (-) sign, Ex. - 123.234561. For point sources this represents the center of the source; for fugitive sources this is the southwest corner if the fugitive angle is zero, or the western most corner if the fugitive angle is greater than

zero. Latitude measured in decimal degrees of the angular distance on a meridian north or south of the equator. Positive (+) data point for N America. Include (+) sign, Ex. +78.123456. For point sources this represents the center of the source; for fugitive sources this is the southwest corner if the fugitive angle is zero, or the western most corner if the fugitive angle is greater than

zero. Code that indicates source of locational coordinates. See Location Default tab in Lookups for P&P Survey.xls Enter revised code

that represents the performance level, or operating scenario, for the HAP emissions reported. 01 - Actual 02 - Allowable 03 - Maximum 04 - Potential North American

Datum (NAD) for longitude and latitude coordinates (NAD27 or NAD83). If left blank NAD83 is assumed. Enter revised

Longitude here. Specify decimal degrees to 6 digits to the right of the decimal point. Enter revised

Latitude here. Specify decimal degrees to 6 digits to the right of the decimal point. Select the most representative control

measure code from Lookups for P&P Survey.xls.

Codes for some common controls are as follows: 127 - Fabric Filter 128 - Electrostatic Precipitator 131 - Thermal oxidizer 141 - Wet scrubber 146 - Wet Electrostatic Precipitator 150 - Mechanical Collector

Longitude (decimal degrees) Latitude (decimal degrees) Location Default Flag REVISED HAP

Emissions Performance Level North American

Datum REVISED Longitude

(decimal degrees) REVISED Latitude

(decimal degrees) Control measure code

-78.9104538 37.51063156 01 NAD83 -78.90139008 37.51305771 128, 129 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.9104538 37.51063156 -78.90139008 37.51305771 -78.90139008 37.51305771

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 19 of 101

### Provide control measure description from Lookups for P&P Survey.xls.

If you cannot find a representative control measure code from Lookups for P&P Survey.xls, then write in a description of the control measure in this column. Optional: Use this column if you need to describe a control that is not identified in the codes list and/or to indicate backup controls. Indicate here (with an "X") if the record should be deleted Describes the reason

for deletion Indicate here (with an "OK")

if the facility or record is correct with no changes.

Control Measure Code Description Control Measure Comment Delete Delete Comment Is Reviewed With No Changes

Electrostatic Precipitator, Scrubber ESP is followed by a scrubber

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 20 of 101

### Copied from left for convenience (DO NOT OVER-WRITE GREEN). You may find it helpful to use Excel's "freeze panes" or "split panes" feature when completing your permit information so you can see emission units and pollutants entered to the left.

Pollutant Code REVISED Pollutant Code Pollutant_Code_Desc

PM10-FIL Primary PM10, Filterable Portion Only CO Carbon Monoxide NH3 Ammonia NOX Nitrogen Oxides PM10-FIL Primary PM10, Filterable Portion Only PM10-PRI Primary PM10 (Includes Filterables + Condensibles) PM25-FIL Primary PM2.5, Filterable Portion Only PM25-PRI Primary PM2.5 (Includes Filterables + Condensibles) PM-CON Primary PM Condensible Portion Only (All Less Than 1 Micron) SO2 Sulfur Dioxide VOC Volatile Organic Compounds 226 Nickel & Compounds 7439921 Lead CO Carbon Monoxide NH3 Ammonia NOX Nitrogen Oxides PM10-FIL Primary PM10, Filterable Portion Only PM10-PRI Primary PM10 (Includes Filterables + Condensibles) PM25-FIL Primary PM2.5, Filterable Portion Only PM25-PRI Primary PM2.5 (Includes Filterables + Condensibles) PM-CON Primary PM Condensible Portion Only (All Less Than 1 Micron) SO2 Sulfur Dioxide VOC Volatile Organic Compounds 50000 Formaldehyde 7439976 Mercury 7440439 Cadmium

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 21 of 101

### Pulp and Paper sector permit data. Follow instructions in section D3 of the survey overview document to populate this permit information table to the right of the orange column.

Instruction: Optional column useful for crosschecking permit data and when comparing permit to NEI. Optional. Complete this column to avoid restating Federal permit limits in the columns to the right. Enter numeric value of permit limit coinciding with the pollutant listed in the POLLUTANT_DESCRIPTION column in the NEI data to the left of the orange line.

See Table 2 of survey overview document for permit limit units of interest. Enter units for permit limit Supply averaging time for permit limit if an averaging time is specified in the permit. Averaging times are commonly

specified for pollutants measured with continuous monitors (e.g., 3- hour block average, daily average, etc).

Leave blank if no averaging time is specified in your permit.

Survey overview reference:

Field: Identifier used in permit (e.g., emission unit ID, stack ID, etc) - optional If the permit limit is identical to the Federal NESHAP or NSPS limit, you may enter the NESHAP/NSPS subpart here rather than restating the Federal limit in the columns to the right Numeric permit limit 1 Units for permit limit 1 (including any applicable %O2 or %CO2 correction factors) Averaging time for permit limit 1 (if applicable)

Example PM entry: BLR01 0.02 gr/dscf @ 8% O2 Pull down menu text located below this line Subpart S (P&P NESHAP) gr/dscf @ 8% O2 3-hour Subpart MM (P&P combustion source NESHAP) gr/dscf @ 10% O2 12-hour Subpart BB (Kraft NSPS) lb/ton BLS daily Subpart Db (Boiler NSPS) ppmdv @ 8% O2 test Subpart Dc (Small Boiler NSPS) ppmdv @ 10% O2 allow others allow others lb/ton BLS (as H2S) lb/MMBtu ppmdv % reduction % opacity

allow others

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 22 of 101

### Enter numeric value of permit limit coinciding with the pollutant listed in the POLLUTANT_DESCRIPTION column in the NEI data to the left of the orange line.

See Table 2 of survey overview document for permit limit units of interest. Enter units for permit limit Supply averaging time for permit limit if an averaging time is specified in the permit. Averaging times are commonly specified for pollutants measured with continuous monitors (e.g., 3-hour block average, daily average, etc).

Leave blank if no averaging time is specified in your permit. Enter numeric value of permit limit coinciding with the pollutant listed in the POLLUTANT_DESCRIPTION column in the NEI data to the left of the orange line.

See Table 2 of survey overview document for permit limit units of interest. Enter units for permit limit Supply averaging time for permit limit if an averaging time is specified in the permit. Averaging times are commonly specified for pollutants measured with continuous monitors (e.g., 3-hour block average, daily average, etc).

Leave blank if no averaging time is specified in your permit.

Numeric permit limit 2 Units for permit limit 2 (including any applicable %O2 or %CO2 correction factors) Averaging time for permit limit 2 (if applicable) Numeric permit limit 3 Units for permit limit 3 (including any applicable %O2 or %CO2 correction factors) Averaging time for permit limit 3 (if applicable)

5 % opacity 20 % opacity Do not exceed 20% for more than three 6-min averages in a 3-hour period determined by Method 9 3-hour 3-hour 12-hour 12-hour daily daily test test allow others allow others

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 23 of 101

### Enter numeric value of permit limit coinciding with the pollutant listed in the POLLUTANT_DESCRIPTION column in the NEI data to the left of the orange line.

See Table 2 of survey overview document for permit limit units of interest. Enter units for permit limit Supply averaging time for permit limit if an averaging time is specified in the permit. Averaging times are commonly

specified for pollutants measured with continuous monitors (e.g., 3- hour block average, daily average, etc).

Leave blank if no averaging time is specified in your permit. Enter numeric value of permit limit coinciding with the pollutant listed in the POLLUTANT_DESCRIPTION column in the NEI data to the left of the orange line.

See Table 2 of survey overview document for permit limit units of interest. Enter units for permit limit Supply averaging time for permit limit if an averaging time is specified in the permit. Averaging times are commonly specified for pollutants measured with continuous monitors (e.g., 3-hour block average, daily average, etc).

Leave blank if no averaging time is specified in your permit.

Numeric permit limit 4 Units for permit limit 4 (including any applicable %O2 or %CO2 correction factors) Averaging time for permit limit 4 (if applicable) Numeric permit limit 5 Units for permit limit 5 (including any applicable %O2 or %CO2 correction factors) Averaging time for permit limit 5 (if applicable)

3-hour 3-hour 12-hour 12-hour daily daily test test allow others allow others

Inventory EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 24 of 101OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Yes/No

Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

Follow instructions in section D3 of the survey overview document to populate this table. You may find it helpful to use Excel's "freeze panes" or "split" features when viewing this spreadsheet.

Instruction: Provide for all entries. This should match NEI Site ID used in other tabs. Provide for all entries. Line IDs should match those used in other tabs. Enter Pulping line ID for pulp mill equipment, Bleaching line ID for bleach plant equipment, or Emission Unit ID of paper machine with which paper mill equipment are affiliated. If equipment is shared between 2 lines (e.g., chemical recovery equipment serving 2 pulping lines) then indicate both Line IDs separated by an underscore "_." See subpart S definitions of "pulping line" and "bleaching line" if needed. Provide for all entries. Use the Emission Unit ID in the Inventory tab if the individual

em ission unit was listed there. If emission units were aggregated by collection system in the inventory tab, then you would list each emission unit separately with a new Emission Unit ID in this tab. Collection systems (identified with the Collection system ID), boilers/combustion units, strippers, and thermal oxidizers must also be included in this column so air pollution controls and equipment details can be specified separately for these equipment.

Note that in some cases the Emission Unit ID will be the same as a Collection system ID or APCD_ID. Leave columns that do not apply for a given

em ission unit blank.

Specify the collection system if applicable. (Examples of collection systems include closed vent systems, LVHC, and HVLC systems.) Enter the decimal value for control capture efficiency, if available (e.g., 0.90 = 90% capture).

Blank entries for emission units with control devices will be considered as having 100% capture. Enter the following codes for emission units that are not emitted through a conveyance such as a collection system or stack: NV = not vented; BLDG = vented into a building; FUGITIVE = fugitive emission source

Survey overview reference: Equipment identification

Field: NEI Site ID Line ID (Pulping line ID, Bleaching line ID, or paper machine Emission Unit ID) Emission Unit ID Collection system ID (for collection systems that collect gases from multiple process units prior to air pollution control). Control Capture Efficiency (%) Configuration if not emitted through a conveyance

Example entry: 99999 Kraft1 DIG-1 LVHC-1

99999 Kraft1 DIG-2 LVHC-1

99999 Kraft1 STRIPPER

LVHC-1 99999 Kraft1 TO

99999 Kraft1 LK1

99999 Kraft1_TMP1 Boiler EU55

99999 Kraft1 EVAP LVHC-1

99999 Kraft1 GENERIC UNIT 0.85

NV

BLDG

FUGITIVE

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 25 of 101Use this column for notes or

if helpful to relate equipment and process lines to permit or other information Write in a description using the common equipment types listed in Attachment 1 of the survey overview document, and/or refer to EMISSION_UNIT_DESCRIPTION or "Emission Process Group" columns in the Inventory tab. Enter "UK" if unknown; or "pre-1990" if more than 20 years old and the install date is unknown. if the emission unit was substantially upgraded, enter the year ofthe upgrade as XXXXupgrade. Enter manufacturer ONLY for chemical recovery combustion sources (recovery furnaces, black liquor oxidizers, chemical recovery combustion units, lime kilns, black liquor oxidizers) and boilers. Enter "UK" for unknown. Enter "shop-built" for equipment designed by the mill. Enter 2009 operating hr/yr Enter any combustion control

measures installed/employed to reduce air pollution from combustion sources (e.g., boilers, recovery furnaces, lime kilns) Select yes/no Enter percent reduction (if known) and specify if

measured or design. Enter percent

reduction (if known) and specify if

measured or design. Enter percent

reduction (if known) and specify if

measured or design. Describe any specific process control or

pollution prevention measures used to reduce

em issions from the Emission Unit ID (other then the use of combustion controls or an air pollution control device). Use this column to describe control measures that are not otherwise reflected elsewhere in this survey response spreadsheet.

Combustion controls Process controls or pollution prevention

Process notes (optional) Emission unit description Year emission unit installed Emission unit manufacturer Emission unit operating hr/yr Combustion controls Were these combustion controls added within the last 10 years? Combustion control NOx %red Combustion

control SO2 %red Combustion

control CO%red Process controls or pollution prevention

measures

digester pre-1990 8400

digester pre-1990 8430

steam stripper system 2000 8430

LVHC collection system 2000-upgrade 8370 thermal oxidizer (backup) 2000 390

lime kiln 1983 Chanderpur Works 8400 use fresh mill water for lime mud washing to reduce TRS from the lime kiln

boiler 1985 Wellons 8700 overfire air No 20%-design

evaporator UK 8430

generic example row UK 8430

UK UK low NOx burners Y/N

pre-1990 shop-built quarternary air

other {specify}

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 26 of 101Primary method of control. Use these "APCD" columns to

describe the primary method of control. (Backup controls are to be entered in the next series of columns to the right).

Enter controls in sequence in which they are used to control each emission unit.

Enter controls for collection systems only in the row where the collection system ID appears in the Emission Unit ID column. Enter ID code for first APCD (to be used throughout the survey spreadsheets) Enter 2nd control device if multiple

controls used.

If process equipment such as a boiler or lime kiln) is used to control emissions, include any control devices used on the process equipment. Enter ID code for 2nd APCD (to be used throughout the survey spreadsheets) Enter 3rd control device if multiple

controls used.

If process equipment such as a boiler or lime kiln) is used to control

em issions, include any control devices used on the process equipment. Enter ID code for 3rd APCD (to be used throughout the survey spreadsheets ) Enter 4th control device if multiple

controls used.

If process equipment such as a boiler or lime kiln) is used to control

em issions, include any control devices used on the process equipment. Enter ID code for 4th APCD (to be used throughout the survey spreadsheets )

Air pollution controls

APCD1 type APCD1_ID APCD2 type APCD2_ID APCD3 type APCD3_ID APCD4 type APCD4_ID

Boiler EU55 Boiler EU55 WESP WESP 1

Lime kiln 1 LK1 Scrubber SCBR2 Scrubber SCBR6

Scrubber SCBR2

WESP WESP 1

Uncontrolled

Recovery furnace ESP (dry bottom) same pull-down as APCD1 same pull-down as APCD1 same pull-down as APCD1

Recovery furnace ESP (wet bottom)

ESP (dry)

Wet ESP (WESP)

Scrubber - venturi

Scrubber - quench

Scrubber - packed bed

Scrubber

Absorber

Mist eliminator Thermal oxidizer/incinerator Regenerative thermal oxidizer Multicyclone Cyclone (excluding product recovery cyclones) Fabric filter (baghouse) Condenser Gravel bed Dry sorbent injection Carbon adsorber Selective noncatalytic reduction Selective catalytic reduction Boiler (specify Emission Unit ID) Lime kiln (specify Emission Unit ID) Recovery furnace (specify Emission Unit ID) Other - specify type (and Emission Unit ID if applicable) Uncontrolled

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 27 of 101Complete for emission units (as

shown in the Emission Unit ID column) with backup controls used only during certain times. (Primary controls for the collection system were identified in the APCD columns to the left). Specify conditions Specify

Backup controls

Back-up method of control (specify APCD_ID or Emission Unit ID) Conditions when backup control is used Approximate hr/yr when backup control is used to control emissions from the Emission Unit ID

TO When Boiler EU55 is not operating 330

TO When LK1 is not operating 390

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 28 of 101Select yes/no.

[Consider how the emission unit is permitted when specifying if it is subject to NSPS BB. For

exam ple, a boiler or thermal oxidizer controlling BB emission units is not necessarily an em ission unitsubject to BB. If your permit indicates the unit is subject to BB then indicate "yes" in the column below.] Provide year. If not known, enter approximation year (e.g., "pre-1990") Select from menu. Select from menu for recovery furnaces subject to subpart BB (straignt or cross). Indicate NSPS BB TRS compliance option used to demonstrate NSPS compliance with primary method of control.

[Note: You may enter the compliance option for each emission unit or for the relevant collection system if listed separately.] Indicate NSPS subpart BB TRS compliance option used to demonstrate compliance using backup method of control for the

em ission unit (if a backup method of control is used).

[Note: Leave blank if no backup control is specified in columns AB-AD to the left for this emission unit.]

Subpart BB NSPS applicability

Is emission unit subject to NSPS BB? If yes, year became subject to BB (XXXX) Reason subject to BB Type of recovery furnace subject to

subpart BB Specify TRS compliance option used to demonstrate NSPS subpart BB compliance (if applicable) Specify TRS compliance option used for backup method of control (if applicable)

yes pre-1990 new

yes pre-1990 new

no

yes pre-1990 collects

em issions from BB emisison units combust gases in lime kiln or recovery furnace subject to subpart BB 5 ppmdv @ 10% O2 (combustion control)

no

yes 1983 new 8 ppmdv @ 10% O2 (lime kilns)

no

yes pre-1990 new

no

Y/N new straight 5 ppmdv @ 10% O2 (combustion control) 5 ppmdv @ 10% O2 (combustion control)

modified cross 5 ppmdv, uncorrected for O2 (control other than combustion) 5 ppmdv, uncorrected for O2 (control other than combustion)

reconstructed combust gases in lime kiln or recovery furnace subject to subpart BB combust gases in lime kiln or recovery furnace subject to subpart BB modified or reconstructed (not sure) combust gases at 1200oF for at least 0.5 sec combust gases at 1200oF for at least 0.5 sec

collects

em issions from BB emisison units incinerating brown stock washer gases is not feasible incinerating brown stock washer gases is not feasible

uncontrolled digester gases contain <0.01 lb TRS/ton ADP uncontrolled digester gases contain <0.01 lb TRS/ton ADP

8 ppmdv @ 10% O2 (lime kilns) 8 ppmdv @ 10% O2 (lime kilns)

0.033 lb/ton BLS as H2S (SDTs) 0.033 lb/ton BLS as H2S (SDTs)

5 ppmdv @ 8% O2 (striaght recovery furnace) 5 ppmdv @ 8% O2 (striaght recovery furnace)

25 ppmdv @ 8% O2 (cross recovery furnace) 25 ppmdv @ 8% O2 (cross recovery furnace) Meet permit limit more stringent than NSPS Meet permit limit more stringent than NSPS

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 29 of 101Select yes/no.

[Consider how the emission unit is permitted when specifying if it is subject to subpart S. For example, a boiler or TO controlling subpart S emission units is not necessarily an emission unit subject to subpart S. If your permit indicates the unit is subject to subpart S then indicate "yes" in the column below.] Indicate compliance option met using primary

method of control for the emission unit.

If the clean condensate alternative (CCA) is used, be sure to complete the CCA tab. Indicate compliance option met using backup

method of control for the emission unit (if a backup

method of control is used).

If the CCA is used, be sure to complete the CCA tab. See pull down menu for potential reasons some vent gas streams may not be covered under subpart S. Some rule exceptions are listed in the menu. You may write in other reasons. Leave blank for emission units emission units outside of the subpart S source category (e.g., boilers, lime kilns, recovery furnaces, etc)

Subpart S NESHAP applicability

Is emission unit subject to NESHAP subpart S? Subpart S compliance option used (for primary method of control) Subpart S compliance option used (for backup method of control, if applicable) Provide reason if not controlled to meet subpart S

yes

yes

yes Use a boiler, LK, or RF in which the HAP gas stream in introduced with the primary fuel into the flame zone Reduce total HAP concentration at the outlet of thermal oxidizer to <20 ppmv @ 10% O2 (dry basis)

yes Use a boiler, LK, or RF in which the HAP gas stream in introduced with the primary fuel into the flame zone Reduce total HAP concentration at the outlet of thermal oxidizer to <20 ppmv @ 10% O2 (dry basis)

no

no

no

yes

no

Y/N Reduce total HAP emissions by 98 wt% Reduce total HAP emissions by 98 wt% Systems of this type at existing sources are not subject to subpart S

Reduce total HAP concentration at the outlet of thermal oxidizer to <20 ppmv @ 10% O2 (dry basis) Reduce total HAP concentration at the outlet of thermal oxidizer to <20 ppmv @ 10% O2 (dry basis) The system does not match the definitions for controlled systems in subpart S. Provide reason (e.g., due to specific location of the system in the process line). Reduce total HAP emissions using a thermal oxidizer operating >1600F and >.75 secs residence time Reduce total HAP emissions using a thermal oxidizer operating >1600F and >.75 secs residence time Exception 63.443(a)(ii)(A): knotter system with HAP emissions <0.1 lb/ton ODP Use a boiler, LK, or RF in which the HAP gas stream in introduced with the primary fuel into the flame zone Use a boiler, LK, or RF in which the HAP gas stream in introduced with the primary fuel into the flame

zone Exception 63.443(a)(ii)(B): screen system with <0.2 lb/ton ODP,

Use a boiler or RF with a heat input capacity >150 MMBtu/hr (44 MW) in which the HAP gas stream is introduced with the combustion air Use a boiler or RF with a heat input capacity >150 MMBtu/hr (44 MW) in which the HAP gas stream is introduced with the combustion air Exception 63.443(a)(ii)(C): knotter and screen system with combined emissions <0.3 lb/ton ODP

Clean condensate alternative (§63.447) for kraft HVLC systems. Clean condensate alternative (§63.447) for kraft HVLC systems. Exception 63.443(a)(iv)(A): decker uses only fresh water or paper machine white water 0.89 lb/ton ODP (for Ca- or Na-based sulfite pulping) 0.89 lb/ton ODP (for Ca- or Na-based sulfite pulping) Exception 63.443(a)(iv)(B): decker uses process water with < 400 ppmw 92% reduction by weight (for Ca- or Na-based sulfite pulping) 92% reduction by weight (for Ca- or Na-based sulfite pulping) Mill received equivalency by permit approval 2.2 lb/ton ODP (for Mg-based or NH3-based sulfite pulping) 2.2 lb/ton ODP (for Mg-based or NH3-based sulfite pulping) Mill undertook innovations project 87% reduction by weight (for Mg-based or NH3- based sulfite pulping) 87% reduction by weight (for Mg-based or NH3- based sulfite pulping) Emissions from this unit were offset using CCA Other - specify

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 30 of 101Select yes/no

[Consider how the emission unit is permitted when specifying if it is subject to subpart MM. For

exam ple, an LVHC stream controlled by a lime kiln is not necessarily a subpart MM emission unit. If your permit indicates the unit is subject to MM then indicate "yes" in the column below.] Provide description for emission units subject to subpart MM. If no physical equipment changes or operational changes were required to achieve subpart MM compliance, then enter "no changes required." If yes, submit PM bubble calculations per instructions. Complete for each

digester.

Select from menu Enter

numeric value Select from menu. In the menu, "HW/SW

swing" refers to digesters that process hardwood (HW) some of the time and softwood (SW) at other times. "HW and SW" refers to digesters that process a mixture of hardwoodand softwood. You may also select "Nonwood." Complete for each pulp washer.

Enter numeric value Select from

menu Enter numeric value Write in the source of the wash water for the final stage of the vacuum drum washer (if vacuum drum washer used) If you have vacuum drum washers, enter the final washing stage shower water methanol concentration in millograms per liter, if known

Subpart MM NESHAP applicability Digesters Pulp washers

Is emission unit subject to NESHAP MM? Describe any physical or operational changes made to the emisison unit in order to achieve subpart MM compliance Is this emission unit involved in a subpart MM PM bubble calculation? Batch or

continuous Digester

capacity, ADTP/d Wood type (HW, SW, HW/SW swing) Washer capacity, ADTP/d Washer type If the washing line has rotary drum vacuum washers, how many washing stages are there? Source of vacuum drum washer final stage shower water Vacuum drum washer final stage shower water methanol concentration, mg/l

no Continuous 480 SW

no Continuous 520 HW/SWswing

no

no
no

yes no changes required no

no

no

no 1000 vacuum drum 3 stripped digester and evaporator condensates

Y/N Y/N Batch HW vacuum drum

Continuous SW diffusion

HW/SWswing pressure

HWand SW belt

Non-wood

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 31 of 101Complete for each, knotter, screen,

and decker.

Enter numeric value Enter type of shower water used in decker (if applicable) Complete for each evaporator system

Enter numeric value Enter Emission Unit ID(s) for

pulp washers supplying weak liquor Enter numeric value Select from menu Complete for oxygen delignification systems.

Enter numeric value Enter Emission Unit ID(s) for pulp washers supplying the brownstock Enter the numeric value for

methanol concentration, if known

Knotters, screens, and deckers Evaporators Oxygen delignification

Knotter, screen, or decker capacity, ADTP/d Type of shower water used in decker Evaporator capacity, ADTP/d Which pulp washer(s) are

the source(s) of weak liquor for the evaporator set? How many evaporator effects are there? Does last effect serve

as DCE or NDCE? (specify which) Design capacity, ADTP/d (inlet stock) From which washer lines is the brownstock coming from? Methanol concentration in post-O2 delignification washer shower water, mg/l

1000 WASHER 6 No

300 1100 WASHER 436

contaminated condensates No

clean condensates Yes - DCE

white water Yes - NDCE

other (specify)

NA

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 32 of 101Complete for steam

strippers and air strippers used to remove compounds from condensates, wastewater, or other process liquids.

Select air/steam Select yes/no Enter description of the condensate streams (e.g., evaporator condensates, digester condensates, turpentine recovery system condensates, LVHC system condensates, HVLC system condensates), wastewater streams, or othe process liquid streams that are stripped Enter numeric value for total liquid flow to the stripper Enter numeric value Enter numeric value Enter numeric value Select from menu or write in Enter the methanol removal efficiency if it has been measured (e.g., enter 92 for 92%).

If measured efficiency is not available, enter the design efficiency (e.g., enter "95-D" to reflect a design methanol removal efficiency of 95%) Enter the total TRS removal efficiency if it has been measured (e.g., enter 92 for 92%).

If measured efficiency is not available, enter the design efficiency (e.g., enter "95-D" to reflect a design methanol removal efficiency of 95%)

Strippers

Type of stripper Is the stripper integrated with the multiple effect evaporator system? List all liquid streams sent to the stripper Liquid flow to the stripper, gpm Steam application rate, lb/gal Liquid column

feed temperature, F For air stripper,

air flow rate, cfm/gpm Primary reason for installation of the stripper Methanol removal efficiency, % TRS removal efficiency, %

steam no DIG-1 and DIG-2 condensates, EVAP condensates (effects 1-3), LVHC-1 condensates, Turpentine decanter underflow 315 1.5 130 water conservation; and subpart S kraft pulping condensate standards 92 94

steam Y/N TRS control

air BOD reduction

water conservation

subpart S kraft pulping condensate standards

nonchlorinated organic HAP control

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 33 of 101Complete the pulp and liquor

storage questions for pulp storage tanks (e.g., high density storage), stock chests, strong and weak liquor storage tanks.

Select from menu or specify Do not include tanks that are defined as part of the bleaching, decker, evaporator, pulp washing, O2 delignification, steam stripper, process wastewater treatment, or turpentine recovery systems under Subpart S. Do not include acid condensate storage tanks.

Enter numeric value Enter numeric value Select from menu. If tank emissions are routed to a collection system and control device or to a process, then the collection system, APCD, or process Emission Unit ID should be relfected in the appropriate columns to the left of this worksheet. Select from menu Complete for liquor storage ponds

Select from menu or write in Enter numeric value Enter numeric value Enter numeric value

Pulp storage and Liquor storage Liquor storage ponds

Tank contents Tank capacity, gal Annual throughput, gal/yr Tank control technique If floating roof is used, type of seal Pond contents Pond surface area, ft2 Pond capacity, gal Annual pond throughput, gal/yr

strong black liquor 14365 1,304,230 FR =fixed roof Not applicable weak black liquor 26400 158400 2,300,000

weak black liquor Open tank Not applicable weak black liquor

strong black liquor FR =fixed roof Mechanical shoe primary seal (MS1) strong black liquor

high density pulp EFR = external floating roof MS1 with shoe mounted secondary (MESA) white liquor

white liquor IFR = internal floating roof MS1 with rim mounted secondary (MESA) green liquor

green liquor Collection system and control device liquid mounted primary seal (LM1)

Emissions routed to process (enter Emission Unit ID) LM1 with rim mounted secondary (LM2)

vapor mounted primary seal (VM1)

M1 with rim mounted secondary (VM2)

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 34 of 101Enter numeric value for lime kiln

throughput in tons CaO/yr.

Enter (repeat) value for each causticizing emission unit listed in this tab, except for slakers. Enter numeric value Complete this question for lime mud washers and lime mud pre-coat filters.Select the source(s) of makeup water added to the mud washer or precoat filter from the list. You may write in more than one source. Untreated process condensates refers to process condensates that have received no treatment (such as steam stripping or biological treatment).See description of the other menu choices in the survey overview document instructions for the Select yes/no.

Answer this question with respect to each causticizing Emission Unit ID specified in column D. Enter description if answer to previous question was "yes."

Emission reductions achieved may apply to the Emission Unit ID specified (for which the process change was made) or to down stream emission units in the causticizing loop. Indicate the Emission Unit ID for any down stream emission units affected. If black liquor gasification is used, provide a diagram and description of the system including any combustion controls or add-on controls used to reduce air pollutants. Complete for each black liquor oxidation (BLO) system. Select from

menu Select from menu Enter number Enter

numeric value Enter

numeric value (e.g., enter "45" for 45%)

Causticizing equipment Black liquor gasification Black liquor oxidation systems

Causticizing area throughput (use lime kiln tons CaO/yr) Slaker capacity, tph Source(s) of makeup water added to mud washer or precoat filter Has the mill taken steps within the last 10 years to control makeup water quality for the causticizing emission unit such that air emissions from any equipment would be reduced? If yes, please describe these changes and the reduction in emissions achieved Black liquor gasifier capacity (million ton BLS/yr) Emission Unit ID(s) of recovery furnace(s) downstream of BLO Type of liquor oxidized BLO type No. of air oxidation stages Liquor

flow rate, gpm Liquor

solids content, %

3942000 450 treated wastewater, and partially treated wastewater - CLARIFIER1 water yes Replaced half of the lime mud wash water volume (from CLARIFIER1) with treated wastewater from STRIPPER in order to reduce methanol emissions from the lime mud washer and LK1. 1.9 RF1 strong air 1 364 49

Untreated process condensates from {specify process - e.g., evaporator, blow heat recovery} yes strong air

surface water no weak molecular oxygen

fresh water

process water {specify source}

treated wastewater

partially treated wastewater {specify last wastewater treatment unit water passed through}

mixture {specify sources}

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 35 of 101Complete for each

recovery furnace at kraft, soda, sulfite, and co-located kraft/semi-chemical pulp mills.

Select from menu If you operate an NDCE recovery furnace, indicate if it was previously a DCE recovery furnace that underwent a DCE furnace conversion (e.g., a low odor conversion).

Select yes/no

Leave blank if not applicable. Enter year (e.g., 2000) when DCE furnace was converted to an NDCE furnace (if applicable).

Leave blank if not applicable. Select from menu or write in Enter numeric

value for black liquor solids (BLS) or red liquor solids (RLS) for sulfite Enter numeric

value (e.g., enter "45" for 45%) Enter % sulfur,

chloride, or nitrogen if known. Input site-specific higher heating value (HHV) of the pulping liquor, if measured. Complete the recovery furnace ESP questions if applicable. If not applicable leave blank.

Indicate the type of liquor used in the wet bottom ESP The particulate matter (PM) return system returns PM collected in the ESP to the process.

Select wet or dry from menu Select from menu Enter year (e.g., 2000) if an ESP was converted.

Recovery furnaces Recovery furnace ESPs

Recovery furnace type Was NDCE formerly a DCE (i.e., has the unit undergone a low odor conversion)? DCE furnace conversion year (XXXX), if applicable Type of liquor Spent liquor solids feed rate, million lb BLS/yr (or million lb RLS/yr for sulfite) Liquor solids %

by weight Liquor sulfur

% by weight Liquor chloride

% by weight Liquor nitrogen

% by weight Liquor HHV Btu/lb

dry solids Oxidized or unoxidized black liquor (for wet bottom recovery furnace ESPs) Wet or dry PM return system (for recovery furnace ESPs) For wet PM return system, specify liquid Indicate year (XXXX) recovery furnace ESP was converted from a wet bottom/wet PM return system to a dry bottom/dry PM return system, if applicable

DCE no black 1.9 65 4.3 0.71 5940 Oxidized black liquor wet Oxidized black liquor

DCE yes black Oxidized black liquor wet Oxidized black liquor

NDCE no red Unoxidized black liquor dry Unoxidized black liquor

mixture of kraft black liquor and semi hem green liquor NA-wet bottom ESP not used

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 36 of 101Complete for each

chemical recovery combustion unit at astand-alone semichemical pulp mill.

Select from menu Select from

menu Select from menu Select from menu or write in Enter numeric value Input site-specific higher heating value (HHV) of the pulping liquor, if

measured. Enter numeric value Complete for each kraft,

soda, sulfite, and semichemical smelt (or ash) dissolving tank. Select from

menu Enter numeric value Select from menu or write in. Enter "SDT scrubber water" if the SDT scrubber water drains into the SDT (as if often the case). See description of the other menu choices in the survey overview document instructions for the Controls tab. Enter numeric value in millograms per liter. Enter numeric value in millograms per liter.

Enter NA if TRS emissions would not be expected (e.g., for nonsulfur semichemical pulp mills)

Sem i-chemical combustion units Smelt/ash dissolving tanks

Type of combustor Liquor

evaporation equipment Type of DCE Type of liquor Spent liquor solids feed rate, million lb/yr Liquor HHV Btu/lb dry solids Combustion unit hottest temperature, F EMISISON_UNIT_ID of

RF or combustion unit supplying SDT Type Smelt or ash production rate, lb/day Type and source of water used in tank Methanol concentration of water used to dissolve smelt/ash in tank (if known), mg/l TRS concentration of water used to dissolve smelt/ash in tank (if known), mg/l

fluidized bed reactor DCE Venturi scrubber black 75 5420 1400 RF1 smelt 690000 process water {weak wash} 45

fluidized bed reactor Concentrator Cyclone black smelt SDT scrubber water

recovery furnace DCE Cascade ash surface water

smelter None Venturi scrubber fresh water

rotary liquor kiln process water {specify source}

pyrolysis reactor treated wastewater partially treated wastewater {specify last wastewater treatment unit water passed through}

mixture {specify sources}

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 37 of 101Complete Table 8

for each kraft or soda lime kiln.

Select from menu Enter numeric value Enter numeric value (i.e., "30" = 30%) Enter numeric

value for kiln hot end operating temperature (F) Enter numeric

value for kiln cold end operating temperature (F) Select from menu Select yes/no Select from menu Complete for boiles, thermal oxidizers, or incinerators.

Enter numeric value in million Btu per hour (MMBtu/hr) Complete for lime kilns, recovery furnaces, chemical

recovery combustion units, boilers, thermal oxidizers, etc that are used to incinerate NCG or SOG.

List all sources of NCG or SOG, identified by their Collection System IDs or Emission Unit IDs separated by commas, for which the emission unit serves as primary control (e.g., LVHC1, SOG, TALLOIL, ...) List all sources of NCG or SOG, identified by their Collection System IDs or Emission Unit IDs separated by commas, for which the emission unit serves as backup control (e.g., LVHC2, HVLC1 ...)

Lime kilns (including rotary lime kilns and fluidized bed calciners) Boilers and thermal oxidixers/incinerator

s Equipment incinerating NCG or SOG

Type of kiln Lime production rate, ton/d Moisture content of lime mud, % Kiln hot end

temperature (F) Kiln cold end

temperature (F) NCG introduction method Are SOG introduced with NCG? If no, SOG introduction method Design heat input capacity, MMBtu/hr NCG/SOG for which the emission unit provides

primary control NCG/SOG for which the emission unit provides backup control

20 STRIPPER, LVHC-1

rotary 200 29 2000 450 with primary fuel no NA - SOG are not burned in lime kiln LVHC-1

435 STRIPPER

rotary with primary fuel Y/N with primary fuel

fluidized bed with primary combustion air with primary combustion air

dedicated nozzle located near burner dedicated nozzle located near burner

NA - SOG are not burned in lime kiln

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 38 of 101Complete for fuel-fired equipment such

as boilers, lime kilns, thermal oxidizers, and direct-fired dryers. Enter the types of primary fuels fired (excluding black liquor, red liquor, SOG, or other NCGs).

Enter primary fuel type Enter numeric value for amount of fuel used in 2009. Use the list of preferred units in the next column. Enter units of measure for fuel usage amount: Use gal/yr

for liquid fuels (#2 distillate fuel oil, #6 residual fuel oil, turpentine, tall oil). Use tons/yr

for solid fuels such as bituminous/subbitumnius/lignite coal, tirederived fuel, or petroleum coke. Use tons/yr (as fired)for solid fuels such as bark, hog fuel, and sludge. Use MMscf/yr for gaseous fuels. Enter the numeric higher heating value (HHV) for non-fossil fuels corresponding to the suggested units in next column.

Optional. EPA can assume default HHVs for fossil fuels, or you may opt to enter the HHV for your fossil fuel (e.g., if the fuel is relatively uncommon) Specify units corresponding to the HHV as fired. Use Btu/galfor liquid fuels, MMBtu/tonfor solid fuels, and Btu/MMscf

for gaseous fuels. Specify average

moisture content as fired for biomass fuels only (decimal percent by weight, i.e., enter "0.2" for 20%)

Primary fuels for fuel-fired equipment (except black or red liquor)

Primary fuel type Primary fuel amount Primary fuel amount units Average HHV of non-fossil primary fuels Primary fuel HHV units Moisture content for biomass fuel (decimal % by weight)

natural gas 12297.6 MMscf/yr 1020000000 Btu/MMscf

hog fuel 416700 tons/yr 12.6 MMBtu/ton 23

natural gas gal/yr Btu/gal

#2 distillate oil tons/yr MMBtu/ton

#6 residual oil tons/yr (as fired) Btu/MMscf

bark MMscf/yr

hog fuel

bituminous coal

subbitumnius coal

lignite coal

allow others

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 39 of 101Hidden columns:

Complete for fuel-fired equipment such as boilers, recovery furnaces, chemical recovery combustion units, lime kilns, thermal oxidizers, and direct-fired dryers. Enter the types of supplemental or other fuels fired (excluding SOG or other NCGs).

Include secondary and additional fuels used routinely for multi-fuel fired equipment in these columns. Enter numeric value for amount of fuel used in 2009. Use the list of preferred units in the next column. Enter units of measure for fuel usage amount: Use gal/yr

for liquid fuels (#2 distillate fuel oil, #6 residual fuel oil, turpentine, tall oil). Use tons/yr

for solid fuels such as bituminous/subbitumnius/lignite coal, tirederived fuel, or petroleum coke. Use tons/yr (as fired)for solid fuels such as bark, hog fuel, and sludge. Use MMscf/yr for gaseous fuels. Enter the numeric higher heating value (HHV) for nonfossil fuels corresponding to the suggested units in next column.

Optional. EPA can assume default HHVs for fossil fuels, or you may opt to enter the HHV for your fossil fuel (e.g., if the fuel is relatively uncommon) Specify units corresponding to the HHV as fired. Use Btu/galfor liquid fuels, MMBtu/tonfor solid fuels, and Btu/MMscf

for gaseous fuels. Select from menu or write in. You may write in more than one condition.

Multi-fuel fired units can select "routine use (multi-fuel fired unit)" from the

menu. Approximate hours per year fuel used in 2009

Supplemental or other fuels for fuel-fired equipment

Supplemental fuel type 1 Supplemental fuel type 1 amount Supplemental fuel type 1 amount units Supplemental fuel type 1 HHV (if non-fossil) Supplemental fuel type 1 HHV units Conditions when supplemental fuel type 1 used hr/yr supplemental fuel type 1 used

#6 residual oil 153360 gal/yr 150000 Btu/gal backup 360

natural gas 155 MMscf/yr startup, backup 800

natural gas gal/yr Btu/gal routine use (multi-fuel fired unit)

#2 distillate oil tons/yr MMBtu/ton startup

#6 residual oil tons/yr (as fired) Btu/MMscf backup

turpentine MMscf/yr during upset conditions

tall oil seasonally during curtailments or peak prices

peteroleum coke when tall oil prices low

tire-derived fuel

wastewater treatment plant sludge

allow others

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 40 of 101Additional supplemental fuel columns (for types 2-6) are hidden. Unhide and complete these columns if relevant.

Supply startup/shutdown information for equipment (including collection systems or APCDs) that appear in the EMSISION_UNIT_ID column (except thermal oxidizers). Enter startup/shutdown information for thermal oxidizers in the Controls tab.

Enter approximately how long it takes for the emission unit to startup. Use decimals if less than one hour (e.g., 18 minutes = 0.3 hr).

Supply information for routine startup and shutdown events such as events associated with planned mill downtime. (Do not provide information for startup/shutdown events associated with control device or emission unit malfunctions).

"Startup" means the setting in operation of an affected source or portion of an affected source for any purpose. Select from menu or write in Write in response specifying when startup ends and normal operation begins (e.g., Startup ends when the auxiliary burners switch off and material throughput begins to flow.) Enter approximately how long it takes for the

em ission unit to shutdown. Use decimals if less than one hour (e.g., 18 minutes = 0.3 hr).

"Shutdown" means the cessation of operation of an affected source or portion of an affected source for any purpose. Select from menu or write in

Emission Unit Startup and Shutdown

Approximate duration of emission unit startup (hours) Measures employed to reduce air emissions during emission unit startup (if any) What marks the end of emission unit startup and beginning of normal operating conditions? Approximate duration of emission unit shutdown (hours) Measures employed to reduce air emissions during shutdown (if any)

0.5 backup control When full pulp flow from the digester is obtained 1 continue routing emisisons to LVHC-1 collection system and primary or backup control system

0.5 backup control When full pulp flow from the digester is obtained 1 continue routing emisisons to LVHC-1 collection system and primary or backup control system

2 backup control stripper steam application rate reaches target; and begin flow of process condenstes from tank 1 stop routing process condensates to stripper before beginning shutdown

0.1 backup control flow through bypass ceases 0.2 NA - applicable emission and parameter limits not expected to be exceeded during shutdown

24 Ensure scrubber liquid is flowing during startup once LK1 temperature reaches 200F LK1 hot end temperature reaches 2000F 18 Continue operatign scrubber until temperature in LK1 drops to 200F

12 Operate WESP during boiler startup Steam pressure of 100 psig or greater achieved 12 em ission unit and control device operates during emission unit startup (but not necessarily in compliance with all NSPS/NESHAP parameter limits)

18 backup control Strong liquor flow of 600 gpm at evaporator exit (55% solids) 16 continue routing emisisons to LVHC-1 collection system and primary or backup control system

12 em ission unit and control device operates in compliance with NSPS and NESHAP parameter limits during emission unit startup Combustion temperature is reached 14 Tem perature drops below 200F

em ission unit and control device operates in compliance with NSPS and NESHAP parameter limits during emission unit startup em ission unit and control device operates in compliance with NSPS and NESHAP parameter limits during emission unit shutdown

em ission unit and control device operates during emission unit startup (but not necessarily in compliance with all NSPS/NESHAP parameter limits) em ission unit and control device operates during emission unit startup (but not necessarily in compliance with all NSPS/NESHAP parameter limits)

backup control backup controls

NA - applicable emission and parameter limits not expected to be exceeded during startup NA - applicable emission and parameter limits not expected to be exceeded during shutdown

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 41 of 101Write in response specifying when shutdown

begins and normal operation ends (e.g., Shutdown begins when material throughput ceases to flow.) OPTIONAL QUESTION. Input on appropriate standards that would be reasonable for your pulp and paper source category emission units is requested. Supply recommendations for the specific equipment (including collection systems or APCDs) appearing in the EMSISION_UNIT_ID column.

What marks the end of normal operating conditions and beginning of emission unit shutdown? Optional: Do you wish to recommend a standard that would apply during startup or shutdown of this emission unit? If so, please describe the event to which the standard would apply; the recommended standard (this could be an emission limitation, work practice, or operational standard) that would apply during the period; the basis for the recommended standard; why and how the standard would minimize emissions during the event; and how would compliance be determined and/or monitored. Supply as a separate attachment to your survey response if necessary.

Stop transfer of wood chips form the feed silo Rule could require continued routing of emisisons to LVHC-1 collection system and primary and/or backup control system during digester startup and shutdown.

Stop transfer of wood chips form the feed silo Rule could require continued routing of emisisons to LVHC-1 collection system and primary and/or backup control system during digester startup and shutdown.

shut off steam supply to the stripper Rule could require continued routing of SOG to existing primary and/or backup control system during stripper startup and shutdown.

flow through bypass begins

Turn down gas burner to 50% flow Require compliance with scrubber liquid flow parameter monitoring limit, but not pressure drop parameter monitoring limit (since the pressure drop cannot be maintained without sufficient exhaust flow from the lime kiln.

Stop charging hog fuel into boiler

Steam flow to first effect reduced by 50% Rule could require continued routing of emisisons to LVHC-1 collection system and primary and/or backup control system during evaporator startup and shutdown.

Cease flow of liquor through injecction nozzles

Equip detail EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 42 of 101OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Yes/No Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

Complete this table for add-on air pollution controls. Questions regarding combustion controls and process changes are included elsewhere in other survey tabs. Follow instructions in section D3 of the survey overview document to populate this table

Instruction: Provide for all entries. This should match NEI Site ID used in other tabs. Line IDs should match those used in other tabs such as the Equip detailtab. Enter APCD_ID matching the Equip detailtab Enter Emission Unit ID or

Collection system ID matching the Equip detail tab.

Note if control device serves as a backup control. Select from menu or write in Enter the manufacturer of the APCD, if known. Enter "UK" for unknown. Enter "shop-built" for equipment designed by the mill. Enter the year installed, if

known. Enter "UK" if unknown; or "pre-1990" if more than 20 years old and the install date is unknown. If the APCD was substantially upgraded, enter the year ofthe upgrade as XXXXupgrade. Survey overview reference: APCD identification

Field: NEI Site ID Line ID (Pulping line ID, Bleaching line ID, or paper machine Emission Unit ID) APCD_ID Emission Unit ID(s) or Collection system ID(s) controlled Type of control device APCD manufacturer (if known) Year installed (XXXX)

Example entry: 99999 Kraft1 ANYCONTROL ANYUNIT ANYTYPE UK pre-1990

99999 Kraft1 SCRB2 LK1, LVHC1 Scrubber Ducon 1985

99999 Kraft1 TO STRIPPER (backup); LVHC1 (backup) Thermal oxidizer/incinerator Coen 1999

Recovery furnace ESP (dry bottom)

Recovery furnace ESP (wet bottom)

ESP (dry)

Wet ESP (WESP)

Scrubber - venturi Scrubber - quench Scrubber - packed bed Scrubber Absorber Mist eliminator Thermal oxidizer/incinerator Regenerative thermal oxidizer Multicyclone Cyclone (excluding product recovery cyclones) Fabric filter (baghouse) Condenser Gravel bed Dry sorbent injection Carbon adsorber Selective noncatalytic reduction Selective catalytic reduction Other - specify type

Controls EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 43 of 101Enter the gas flow rate in actual cubit feet per minute (acfm) at the inlet of the APCD if known. Enter the gas

temperature in degrees Fahrenheit at the inlet of the APCD if known. Enter the gas

moisture content (% H2O) at the inlet of the APCD if known. For example, enter "10" for 10%. Enter the gas

flow rate in actual cubit feet per minute (acfm) exiting the APCD Enter the gas

temperature in degrees Fahrenheit exiting the APCD Enter the gas

moisture content (% H2O) exiting the APCD. For example, enter "10" for 10%. Enter the

typical/design pressure drop across the control device in inches of water Complete for

PM control devices.

Enter particle size in micrometers (um) if known Stack gas flow P-drop

Inlet gas flow rate, acfm (if known) Inlet gas

temperature, F (if known) Inlet gas

moisture content, %

(if known) Exit gas flow

rate, acfm Exit gas

temperature, F Exit gas

moisture content, % Pressure drop,

in. H2O Range of

particle size entering control device (um)

20000 240 10 195 220 11 4 2 to 10

32000 450 25 25000 170 30 6 0.1 to 50

600 200 6 610 220 8 2

Controls EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 44 of 101Enter control efficiencies , if known (e.g., enter 99 for 99%). Leave blank if

not known or not applicable. "Actual" control

efficiency is a measured value. "Design" control

efficiency reflects the efficiency the APCD was designed to achieve. Include control efficiency for specific HAP that you identify. This may be HAPs used as surrogates in a rule (e.g., methanol, chlorine) or other HAP. You may attach a separate listing of HAPs and control efficiencies if this information is available for a number of compounds. Control efficiency

Actual PM control efficiency, % Design PM

control efficiency, % Actual TRS

control efficiency, % Design TRS

control efficiency, % Actual HCl

control efficiency, % Design HCl

control efficiency, % Actual SO2

control efficiency, % Design SO2

control efficiency, % Actual HAP control

efficiency, % Specify HAP for actual % Design HAP control efficiency, % Specify HAP for design %

98 99.5 90 Methanol 95 Methanol

95 92 90 82 75 50 Methanol 85 Hg

98 95 Formaldehyde, methanol

Controls EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 45 of 101Complete for thermal oxidizers or incinerators

Select from list Enter number of canisters (media beds) for a regenerative thermal oxidizer (RTO) Enter target firebox combustion/operating temperature (F) Enter time stack gases are exposed to the target temperature (actual or design value) Select yes/no Select from list or write in

Incinerator type If RTO, number of canisters Target firebox temperature (F) Residence time at operating temperature (sec) Heat recovery What is the recovered heat from the incinerator exhaust used for?

Single-stage combustion chamber NA 1300 1.8 no NA

Single-stage combustion chamber yes preheat incoming emission stream

Two-stage combustion chamber no produce steam

Regenerative thermal oxidizer (RTO) produce hot water

Controls EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 46 of 101Complete for mechanical collectors. Do not include product collection cyclones in this table.

Enter number Complete the sorbent injection questions for sorbents injected into the gas stream prior to collection by a fabric filter or other control device for which information is being provided. For example, complete the sorbent injection questions for a dry injection fabric filter system in the same row where you enter information for the fabric filter. Select from list or write in Enter pounds per hour (lb/hr) of sorbent injected into the exhaust gas stream Complete for fabric filters

(baghouses).

Indicate the filter material and note if coatings are added to the filter material (e.g., polyester with PTFE coating). If no coating is indicated (e.g., polyester), the it will be assumed that the filter material is uncoated. Select from list Enter typical bag life (or expected bag life), months Enter number of fabric filter compartments. Enter "1" if the bagouse is not separated by different compartments. Enter air-to-cloth ratio (gas flow divided by the filter bag material area) Mechanical collectors Sorbent injection Fabric filters

Number of tubes Sorbent type List pollutants the sorbent injection was installed to control Sorbent injection rate, lb/hr Filter material and added

coatings Bag cleaning method Typical bag life (months) Number of compartments Air-to-cloth ratio (acfm/ft2)

8 activated carbon Hg 100 Polyester Shake 15 1 7

activated carbon acid gases (HCl, SO2, HF) Shake

lime SO2 Reverse air

other (specify) Hg Pulse jet

dioxins

Controls EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 47 of 101Complete the ESP questions for dry ESPs and WESPs

Enter number of fields Enter number of

fields used during normal operation. This may be the same as the total number of fields unless some fields are offline (e.g., for cleaning). Enter the specific collection area (area of the plates divided by gas flow rate). Describe any ESP upgrades made within the last 10 years, such as addition of fields or other upgrades to increase ESP efficiency. If no upgrades, leave blank. Complete these additional ESP questions for WESPs.

If a quench is used prior to the ESP, complete the scrubber questions for the quench. Include water flow through the WESP ESPs WESPs

Total number of fields Number of fields

used during normal operation Specific collection area, ft2/1,000 acfm Have fields/chambers been added to expand the ESP within the last 10 years? Is WESP preceded by a quench chamber WESP water flow, gpm

8 4 466 No No 275

Y/N Y/N

Controls EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 48 of 101Complete for all types of wet scrubbers (venturi, tray, plate, injection, quench, etc)

Enter type of alkali added (e.g., NaOH/caustic, KOH, KMNO4). Leave blank if no alkali added. Enter the numeric valuefor the scrubber liquid-togas ratio (L/G) in gallons of liquid per 1000 acfm of gas. Enter numeric value for pH Enter gallons per

minute of scrubbing fluid (e.g., water) makeup added to the system Select yes/no for scrubbers that

control chemical recovery furnaces or combustion units.

Leave blank for other scrubbers. Complete the scrubber questions and complete the additional questions below related to the packing material Scrubber Packed bed scrubbers/absorbers

Type of alkali added, if any Liquid-to-gas ratio (gal/1000 acfm) Inlet pH of scrubbing liquid Scrubbing fluid

make-up rate, gpm For chemical recovery

furnaces/combustors: Does scrubber also serve as a direct contact evaporator? Type of packing material Packing

material depth, ft Scrubber/absorber

cross-sectional area, ft2

8 130 No plastic packing 3 19.6

Caustic 6 10 60

Controls EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 49 of 101Enter water source and usage information for wet control devices such as wet scrubbers, WESP, mist eliminators, absorbers, etc.

Do not include spent pulping liquor used in recovery furnace wet bottom ESPs here (as information for wet bottom ESPs is requested in the Equip detailtab). Select yes/no Enter numeric value in gallons per minute (gpm) Enter numeric

value in gallons per minute (gpm) of the water that is not recirculated back to the control device (i.e., blowdown) Enter end use or disposal method for the

blowdown Water source and usage

Water source Is water recirculated? Water recirculation rate, gpm Wastewater

(blowdown) generated, gpm Wastewater (blowdown) reuse or disposal

method

treated wastewater Yes 200 10 Treated in onsite wastewater treatment plant

surface water and water from recirculation pond Yes 350 35 Treated in onsite wastewater treatment plant

surface water Y/N Treated in onsite wastewater treatment plant

fresh water Recycled to mud washer(s)

process water {specify source} Recycled to SDT

treated wastewater Recycled to process: {specify equipment receiving water using Emission Unit ID OR APCD_ID} partially treated wastewater {specify last wastewater treatment unit water passed through} POTW mixture {specify sources} Other {specify}

Controls EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 50 of 101Complete the solid material questions for control devices that collect or generate solid material to be handled or disposed.

Provide information for any solid material collected by the APCD (e.g., PM, sorbent, etc) Enter the amount of solid material collected annually. Explain how the solid material is used or disposed. Explain where the material re-enters the process if it is reused. Identify any other solid waste associated with the APCD that must be replaced/disposed periodically (e.g., packing material, ceramic saddles) Enter the frequency in which the material must be replaced/disposed, etc. Enter the amount of material that must be replaced/disposed. Explain how the solid material is used or disposed. Explain where the material re-enters the process if it is reused. Solid material handling and disposal

Type of material collected Solid material collected, ton/yr End use/method of disposal for solid material collected Identify any other solid waste associated with the APCD Frequency of material replacement/disposal Amount of material, tons End use/method of disposal for solid material collected

carbon sorbent laden with PM 410 landfilled onsite degraded packing material 5 yr 0.5 landfill offsite

PM landfill

PM and sorbent reuse {specify}

Sorbent

Controls EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 51 of 101Select from list or write in List any operating parameters not included in the previous column OPTIONAL: Supply approximate capital costs of the parameter monitoring system equipment installed within the past 10 years for this control device. Include in the equipment costs the analyzer and data acquisition system (DAS), if known. OPTIONAL: Enter year for parameter monitoring system costs Parameter monitoring

List continuous parameter monitoring systems used for this control device (e.g., pressure drop, liquid flow) Please list below any additional operating parameters that are either monitored or that are important for proper operation of the APCD, and include average values and units. Capital costs of parameter monitoring system, $ Base year for parameter monitoring system capital cost (e.g., 2005)

liquid flow, voltage carbon injection rate (100 lb/hr)

pressure drop, liquid flow rate 34500 2007

combustion chamber temperature 22000 1999

pressure drop

liquid flow rate

voltage

current

temperature (specify if inlet, outlet, bed, or other temperature) pH percent solids in recycle water other (specify)

Controls EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 52 of 101Supply startup/shutdown information for the equipment that appears in the APCD_ID column.

Enter approximately how long it takes for the control device to startup. Use decimals if less than one hour (e.g., 18 minutes = 0.3 hr).

Supply information for routine startup and shutdown events such as events associated with planned mill downtime. (Do not provide information for startup/shutdown events associated with control device or emission unit malfunctions).

"Startup" means the setting in operation of an affected source or portion of an affected source for any purpose. Select from menu, expand on menu response, and/or write in.

For example, is a certain gas flow rate from the emission unit required before the control device operating parameter limits can be met? Is a certain heating value from the emission unit exhaust gas required to achieve control device temperature? List any control device parameter limits that cannot be met during control device startup. Certain parameters may be "instant on" while others are more transient in nature. Examples could include control device temperature that must heat up to a set point, or pressure drop that cannot be achieved due to low exhaust gas flow from the emission unit.

The EPA is particularly interested in emission limits or parameter limits originating from the pulp and paper NSPS or NESHAP that cannot be met during control device startup or shutdown.

Select from menu if the applicable emission and parameter limits are expected to be met during startup

. Write in response (if any). Control Device Startup and Shutdown

Approximate duration of control device startup (hours) Explain how control device startup is integrated with (dependent upon) emission unit startup/operation List any control device continuous emissions monitoring or operating parameter limits that cannot be met during control device startup Measures employed to reduce air emissions during control device startup (if any)

0.4 Need airflow from emission unit of at least 10,000 acfm in order for injected carbon to properly mix and become entrained in gas stream carbon injection rate Ensure water is recirculated through control device throughout startup

3 Control device cannot function as designed unless an air flow rate of 29,000 acfm from the emission unit is achieved. pressure drop meet liquid flow parameter limit

4 temperature set point bring TO temperature to 1400F before routing NCG or SOG to the TO

Control device is started up and meets required operating parameter limits before emission unit is started up. The applicable emission and parameter limits are expected to be met during startup Control device cannot be started prior to emission unit starting up due to safety issue or risk of property damage. {Explain} Control device cannot function as designed unless an air flow rate of {specify} acfm from the emission unit is achieved.

Controls EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 53 of 101Write in response specifying when control device startup ends and normal operation begins (e.g., Startup ends when oxidizer temperature set point of 1200F is reached.) Enter approximately how long it takes for the control device to shutdown. Use decimals if less than one hour (e.g., 18 minutes = 0.3 hr).

"Shutdown" means the cessation of operation of an affected source or portion of an affected source for any purpose. Select from menu, expand on menu response, and/or write in. For example, is a certain gas flow rate from the emission unit required for the control device operating parameter limits to be met? Is a certain heating value from the emission unit exhaust gas required to achieve control device temperature? List any control device parameter limits that cannot be met during control device shutdown. Certain parameters may be "instant off" while others are more transient in nature. Examples could include control device temperature that decreases from the set point as shutdown progresses, or pressure drop that cannot be achieved due to low exhaust gas flow from the emission unit.

The EPA is particularly interested in emission limits or parameter limits originating from the pulp and paper NSPS or NESHAP that cannot be met during control device startup or shutdown.

Select from menu if the applicable emission and parameter limits are expected to be met during shutdown

.

What marks the end of control device startup and beginning of normal operating conditions? Approximate duration of control device shutdown (hours) Explain how control device shutdown is integrated with (dependent upon) emission unit shutdown List any control device continuous emissions monitoring or operating parameter limits that cannot be met during control device startup

route emission unit exhaust damper to control device and switch on carbon injection once process exhaust gas reaches 10,000 acfm 0.4 Need airflow from emission unit of at least 10,000 acfm in order for injected carbon to properly mix and become entrained in gas stream carbon injection rate

Startup ends when the pressure drop parameter limit range is achieved 0.5 Control device cannot function as designed unless an air flow rate of 29,000 acfm from the emission unit is achieved.

Combustion temperature reaches 1400F 4 Control device continues to operate and meets required operating limits while emission unit is shut down or re-routed. temperature set point Control device continues to operate and meets required operating limits while emission unit is shut down. The applicable emission and parameter limits are expected to be met during shutdown Control device cannot operate during emission unit shut down due to safety issue or risk of property damage. {Explain} Control device cannot function as designed unless an air flow rate of {specify} acfm from the emission unit is achieved.

Controls EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 54 of 101Select from menu or write in Write in response specifying when shutdown begins and normal operation ends (e.g., Shutdown begins when the burners are shut off.) OPTIONAL QUESTION. Input on appropriate standards that would be reasonable for your pulp and paper source category control system is requested. Supply recommendations for the specific APCD appearing in the APCD_ID column. Enter the amount of control device downtime (hr/yr). Include downtime when the process would otherwise be operating, including time when the process currently continues to operate (e.g., under an excess emissions allowance) and time when the process is shut down because the control device is down.

This question does not apply for backup controls (simply enter "Backup control")

Measures employed to reduce air emissions during control device shutdown (if any) What marks the end of normal operating conditions and beginning of control device shutdown? Optional: Do you wish to recommend a standard that would apply during startup or shutdown of this control device? If so, please describe the event to which the standard would apply; the recommended standard (this could be an emission limitation, work practice, or operational standard) that would apply during the period; the basis for the recommended standard; why and how the standard would minimize emissions during the event; and how would compliance be determined and/or monitored. Supply as a separate attachment to your survey response if necessary. Annual control device downtime (when process controlled would otherwise be operating), hr/yr

Continue injection of carbon until process gas flow drops to 10,000 acfm; continue water recirculation unit emission unit switched off When process gas flow drops to 10,000 acfm and carbon injection is shut off Require compliance with liquid flow parameter limit during startup and shutdown (but not carbon injection rate limit) 100

Wait until LK is cooled to 200F before switching off liquid flow. Shut off liquid flow Meet liquid flow parameter limits during startup and shutdown (but not the pressure drop drop parameter limit because it can only be achieved during normal operation) 40

Route NCG and/or SOG back to primary control NCG/SOG re-routed to primary control device Cease firing NCG or SOG during TO shutdown (route NCG and SOG to primary control device) Backup control

Backup control

Controls EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 55 of 101

### OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

Follow instructions in section D3 of the survey overview document to populate this table. Your response may consist of one or more rows.

Instruction: Provide for all entries. This should match NEI Site ID used in other tabs. Provide for all entries. Line IDs should match those used in other tabs such as the Equip detail tab. Select yes/no Survey overview reference: New equipment

Field: NEI Site ID Pulping line ID Does the mill plan to commence construction of any new affected facilities that could potentially become subject to NSPS subpart BB or NESHAP subpart MM within the next 8 years (e.g., between 2009 and 2017) If yes, please indicate the approximate year that the construction will commence If yes, please specify the type of NSPS or NESHAP subpart MM affected facilities that might be constructed Example entry: 99999 P1 yes 2011 add new lime kiln yes
no

Potential changes EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 56 of 101

### Yes/No If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.

Select yes/no Select yes/no Modified/reconstructed equipment Black liquor gasification

Does the mill plan to commence modification or reconstruction of any equipment within the next 8 years (e.g., between 2009 and 2017) that could potentially for the first time become subject to NSPS subpart BB? If yes, please specify the affected facilities to be modified or reconstructed and describe the changes that might be made Does the mill plan to construct a new black liquor gasification system with the next 8 years (e.g., between 2009 and 2017)? If yes, indicate Emission Unit IDs of existing boilers, lime kilns, or other equipment that will burn the syngas produced by the black liquor gasifier/pyrolysis system (either before or after production of liquid fuels) If yes, indicate Emission Unit IDs of existing recovery furnaces that may be retired and replaced with the black liquor gasification system Will the black liquor gasifier be used to supply heat and electric power; or be used to generate liquid fuels (or both)

no yes new lime kiln RF-1 heat/electric power yes yes heat/electric power

no no liquid fuels heat/electric power and liquid fuels

Potential changes EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 57 of 101

### Select yes/no. Select yes/no. Value prior to pulping (VPP) technology Woody biomass gasification

Does the mill plan to install value prior to pulping (VPP) technology for recovery of ethanol or other chemicals within the next 8 years? If yes, please describe the VPP technology planned to be installed. Does the mill plan to install woody biomass gasification or pyrolysis technology within the next 8 years? If yes, indicate Emission Unit IDs of existing boilers, lime kilns, or other equipment that will burn the syngas produced by the biomass gasifier/pyrolysis system (either before or after production of liquid fuels) If yes, indicate Emission Unit IDs of existing boilers (or other equipment) that may be retired and replaced with the biomass gasification/pyrolysis system

no no yes yes
no no

Potential changes EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 58 of 101

### Select yes/no Select yes/no Retiring equipment Low-odor conversions (DCE-->NDCE)

Does the mill plan to retire any equipment subject to NESHAP subpart MM within the next 8 years (e.g., between 2009 and 2017)? If yes, specify Emission Unit IDs to be retired Does the mill plan any lowodor conversions of recovery furnaces in the next 8 years (e.g., between 2009 and 2017)? If yes, specify Emission Unit IDs that might be converted: yes RF-1 no yes yes
no no

Potential changes EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 59 of 101

### Select yes/no Select yes/no ESP conversions New control measures

Does the mill plan to change any recovery furnace ESP systems from a wet bottom ESP to a dry bottom ESP in the next 8 years (e.g., between 2009 and 2017)? If yes, specify APCD_IDs that might be converted: Does the mill plan to install any additional or new PM, HAP, TRS, NOx, SO2, or CO control devices/measures on equipment subject to NSPS subpart BB or NESHAP subpart MM within the next 8 years (e.g., between 2009 and 2017)? If yes, specify Emission Unit IDs to be controlled and control devices/measures that might be installed

no no yes yes
no no

Potential changes EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 60 of 101

### Select yes/no PCC plants

Does the mill plan to begin routing boiler or lime kiln exhaust to an onsite PCC plant within the next 8 years? If yes, Emission Unit IDs likely to be routed to the PCC plant yes LK1 yes
no

Potential changes EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 61 of 101

## OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

Use this table for pulp produced onsite. Do not include pulp purchases in this table. Follow instructions in section D3 of the survey overview document to populate this table Mills can have one or more rows in this table depending on the number of pulping processes/lines at the mill. Complete the columns that are applicable for each pulp type, leaving the inapplicable columns blank. Provide data for the 2009 operating year.

Instruction: Provide for all entries. This should match NEI Site ID used in other tabs. Select from menu Provide for all entries. Line IDs should match those used in other tabs such as the Equip detail tab. Survey overview reference: Pulping line identification

Field: NEI Site ID Pulping processes Pulping line ID Example entry: 99999 kraft P1 kraft soda semi-chemical sulfite-Na sulfite-Mg sulfite-NH3 sulfite-Ca stone groundwood (SGW) pressurized groundwood (PGW) thermo-mechanical pulping (TMP) refiner mechanical pulping (RMP) secondary fiber

non-wood

Pulp prod EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 62 of 101

## Do any of the responses (individual cells) you entered in this tab contain CBI? Yes/No If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.

Enter numeric value for 2009 Enter numeric value

for 2009 Enter numeric value in air dried tons of pulp per year (ADTP/yr) Enter numeric

value in air dried tons of pulp per day (ADTP/d) Enter decimal

percent for utilization (e.g., 0.7 for 70% of capacity utilized) Enter decimal percent for

utilization (e.g., 0.7 for 70% of capacity utilized) for the past 5 years. To determine the 5-year utilization, average the utilization percentages for 2005, 2006, 2007, 2008, and 2009.

Operating hr/yr Operating hr/d Pulp capacity ADTP/yr in 2009 Pulp capacity

ADTP/d in 2009 Pulp capacity

utilization percentage in 2009 5-year average (2005-2009) pulp

capacity utilization percentage 8500 24 340000 950 0.8 0.95

Pulp prod EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 63 of 101

## Virgin wood fiber

sources. Select yes/no to

indicate virgin fiber source(s) used Virgin wood fiber (approximate decimal percent across all virgin

wood fiber sources) How does the mill use the pulp it produces from virgin wood fiber?

Enter approximate decimal percentage of the pulp capacity in (ADTP/yr supplied to the left). Enter approximate decimal percentages of the pulp capacity in (ADTP/yr supplied to the left). Virgin wood fiber sources

Chips produced onsite Chips produced

offsite Sawmill residues Virgin SW % Virgin HW % Approximate percentage of virgin wood pulp that is bleached onsite Approximate percentage of virgin wood pulp sold as unbleached market pulp Approximate percentage of virgin wood pulp used onsite to manufacture unbleached paper/paperboard? Check (=1) yes yes no 20 80 1 0.25 0.75 1 yes yes yes 0

no no no

Pulp prod EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 64 of 101

## Complete for mechanical

wood pulps produced onsite.

Select yes/no Select yes/no Select yes/no Mechanical wood pulps

Is the mechanical pulp brightened? If yes, indicate the chemicals used for brightening For TMP or pressurized groundwood systems, is a heat recovery system used?

no no no yes yes yes
no no no

Pulp prod EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 65 of 101

## Specify the recycled material used for secondary fiber pulping. Provide approximate

decimal percentages of secondary fiber capacity (ADTP/yr supplied to the left). How does the mill use the pulp it produces from secondary fiber?

Enter approximate decimal percentage of the pulp capacity in (ADTP/yr supplied to the left). Enter approximate decimal percentages of the pulp capacity in (ADTP/yr supplied to the left). Recycled/secondary fiber pulps

Mixed paper % High grade deinked % ONP % OCC % Pulp substitute % Approximate percentage of secondary fiber pulp sold as unbleached market pulp Approximate percentage of secondary fiber pulp used onsite to manufacture unbleached paper/paperboard? Other (specify use and approximate percentage) Check (=1) 0 manufacture paper/paperboard products 0 sell as market pulp NA - not producing pulp from secondary fiber

Pulp prod EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 66 of 101

## Non-wood pulping material.

Select from list How does the mill use the

non-wood pulp it produces?

Enter approximate decimal percentage of the pulp capacity in (ADTP/yr supplied to the left). Enter approximate decimal percentages of the pulp capacity in (ADTP/yr supplied to the left). Non-wood pulps

Non-wood material Approximate percentage of nonwood pulp that is bleached onsite Approximate percentage of nonwood pulp sold as unbleached market pulp Approximate percentage of nonwood pulp used onsite to manufacture unbleached paper/paperboard? Check (=1) 0 bagasse 0 kenaf cotton other {specify}

Pulp prod EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 67 of 101

### OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

Each pulp mill producing turpentine and/or tall oil should have one row in this table. Follow instructions in section D3 of the survey overview document to populate this table.

Instruction: Provide for all entries. This should match NEI Site ID used in other tabs. Enter numeric value Enter numeric value Insert Emission Unit IDs separated by commas Survey overview reference: Turpentine

Field: NEI Site ID Turpentine production, hr/yr Turpentine production, gal/day Pulping lines supplying turpentine production (insert Pulping line IDs) Digesters supplying turpentine production (insert Emission Unit IDs) Example entry: 99999 8500 700 P1 DIG-1, DIG-2

Byproducts EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 68 of 101

### Yes/No If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.

Enter numeric value Select from menu. Enter numeric value (if batch) Tall oil

Tall oil production, ton tall oil/yr Pulping lines supplying tall oil production (insert Pulping line IDs) Digesters supplying tall oil production (insert Emission Unit IDs) Is tall oil acidulation reactor batch or continous? Batch reactor cycle time (hr) 220000 P1 DIG-1, DIG-2 continuous batch continuous

Byproducts EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 69 of 101

### Enter numeric value (if batch) Enter numeric value (if continuous) Enter numeric value (if continuous)

Batch reactor cycles per day Continuous or batch tall oil reactor operation, day/yr Continuous tall oil reactor tons tall oil per hour 365 25

Byproducts EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 70 of 101

### OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

Follow instructions in section D3 of the survey overview document to populate this table

Instruction: Provide for all entries. This should match NEI Site ID used in other tabs. Common condensate sources are listed below. You may add rows for additional condensate sources or delete rows as needed. Line IDs should match those used in other tabs such as the Equip detail tab. Enter Emission Unit ID or Collection system ID matching the Equip detail tab

Survey overview reference:

Field: NEI Site ID Kraft condensate streams Pulping line ID Emission Unit IDs (or Collection System IDs for HVLC or LVHC systems) Example entry: 99999 Digester systems P1 DIG-1, DIG-2

99999 P1 DIG-3 99999 Evaporator systems P1 EVAP-1 Digester systems

Turpentine recovery systems

Evaporator systems

HVLC collection systems

LVHC collection systems

Pull down menu text:

Kraft condensates EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 71 of 101

### Do any of the responses (individual cells) you entered in this tab contain CBI? Yes/No If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.

If no, complete column B. If yes, complete columns C-F to specify the applicable method of condensate treatment. The volume reduction options are specified in subpart S at §63.446(c)(2) or (3). Select from the following codes: NA - system does not exist at mill 1 - Mill collects/controls pulping process condensate streams containing a combined total of at least 65 percent of the total HAP mass from each digester system, turpentine recovery system, and evaporator system according to 63.446(c)(2). 2A - Mill collects/controls pulping process condensate streams containing a combined total of at least 7.2 lb total HAP/ton ODP, according to 63.446(c)(3), for mills that DO NOT perform bleaching. 2B-Mill collects/controls pulping process condensate streams containing a combined total of at least 11.1 lb total HAP/ton ODP, according to 63.446(c)(3), for mills that perform bleaching. Specify Emission Unit ID(s) Select from menu. Control options are described in the survey overview document.

A B C

Is condensate stream collected and treated according to subpart S? Indicate volume reduction option being used, or other reason why condensate stream is not collected and controlled For condensates treated by recycling to equipment meeting the kraft pulping system vent standards, specify the equipment Emission Unit ID receiving recycled condensates. For condensates treated by steam stripping, specify the control option used N 2B

Y WASHER Remove 10.2 pounds/ton ODP Y

Y/N NA-system does not exist at mill 92% total HAP reduction (by weight) 1 Remove 6.6 pounds/ton ODP

2A 210 ppmw at the outlet of the control device 2B Remove 10.2 pounds/ton ODP 330 ppmw at the outlet of the control device Remove prorated mass of ___ pounds/ton ODP {specify limit}

Kraft condensates EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 72 of 101

### Include the date/result from your most recent compliance demonstration. You may enter the date/results from more than one compliance demonstration (e.g., initial and subsequent demonstrations as shown in the example). If necessary, submit results for multiple compliance demonstrations in a separate attachment. Select from menu. Control options are described in the survey overview document. Include the date/result from your most recent compliance demonstration. You may enter the date/results from more than one compliance demonstration (e.g., initial and subsequent demonstrations as shown in the example). If necessary, submit results for multiple compliance demonstrations in a separate attachment. Note: If an onsite wastewater treatment plant is used for biological treatment of kraft condensates, then in addition to the question below, you are asked in the WWtab to supply the results of the four quartlerly tests conducted in calendar year 2009.

D E

Date of compliance demonstration(s) Emission limit achieved (include units of measure) For condensates treated by biological treatment, specify the control option used Date of compliance demonstration(s) Emission limit achieved (include units of measure)

(1) 3/29/2001; (2) 5/15/2007 (1) Removed 15.7 lb HAP/ton ODP; (2) Removed 12.3 lb HAP/ton ODP 92% total HAP reduction (by weight) 6/30/2009 94%

92% total HAP reduction (by weight) Remove 6.6 pounds/ton ODP 210 ppmw at the outlet of the control device Remove 10.2 pounds/ton ODP 330 ppmw at the outlet of the control device Remove prorated mass of ___ pounds/ton ODP {specify limit}

Kraft condensates EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 73 of 101

### Write in condensate treatment method (e.g., wastewater thermal oxidizer) Select from menu. Control options are described in the survey overview document. Include the date/result from your most recent compliance demonstration. You may enter the date/results from more than one compliance demonstration (e.g., initial and subsequent demonstrations as shown in the example). If necessary, submit results for multiple compliance demonstration in a separate attachment.

F

Specify condensate treatment method (if other than steam stripping or biological treatment) Specify the control option used Date of compliance demonstration(s) Emission limit achieved (include units of measure)

92% total HAP reduction (by weight) Remove 6.6 pounds/ton ODP 210 ppmw at the outlet of the control device Remove 10.2 pounds/ton ODP 330 ppmw at the outlet of the control device Remove prorated mass of ___ pounds/ton ODP {specify limit}

Kraft condensates EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 74 of 101

## OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

Follow instructions in section D3 of the survey overview document to populate this table

Instruction: Provide for all entries. This should match NEI Site ID used in other tabs. Enter the pulping line ID associated with the Emission Unit ID routing exhaust to the PCC plant Enter Emission Unit ID routing exhaust to the PCC plant. This should match the Emission Unit ID in the Equip detail tab. Select yes/no Survey overview reference:

Field: NEI Site ID Pulping line ID Emission Unit ID routing exhaust to a PCC plant Does exhaust pass through the emission unit air pollution control device(s) prior to being routed to PCC plant? Example entry: 99999 P1 LK1 yes yes
no

PCC EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 75 of 101

## Do any of the responses (individual cells) you entered in this tab contain CBI? Yes/No If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.

If answer to the previous question is no, please explain if exhaust does not pass through the full emission control system prior to being routed to the PCC plant. Enter numeric value This will be 1 (for 100%), unless if the exhaust stream in split such that only a portion of the volume goes to the PCC plant.

Enter decimal percent (e.g., enter "0.15" for 15%) Specify Select yes/no If the PCC plant is NOT located on mill property, please enter physical street address for PCC plant PCC_LOCATION_ADDRESS

If no, explain control configuration relevant to the exhaust stream routed to the PCC plant hr/yr exhaust routed to PCC plant Volume percent of exhaust stream routed to PCC plant Owner of PCC plant Is PCC plant located on P&P mill property PCC Facility Street A

ddress 1500 0.15 Carbonate Minerals, Inc no 1400 Plant Road yes
no

PCC EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 76 of 101

## If the PCC plant is NOT located on mill property, please enter city for PCC plant If the PCC plant is NOT located on mill property, please enter state for PCC plant If the PCC plant is NOT located on mill property, please enter zip code for PCC plant Longitude measured in decimal degrees of the angular distance on a meridian east or west of the prime meridian. Negative (-) data point for N America. Include (-) sign, Ex. - 123.234561. For point sources this represents the center of the source. Enter PCC longitude here. Specify decimal degrees to at least 6 digits to the right of the decimal point. Latitude measured in decimal degrees of the angular distance on a meridian north or south of the equator. Positive (+) data point for N America. Include (+) sign, Ex. +78.123456. For point sources this represents the center of the source. Enter PCC latitude here. Specify decimal degrees to at least 6 digits to the right of the decimal point. Answer "no" unless the PCC plant is included in your title V permit PCC_CITY PCC_STATE PCC_ZIPCODE PCC_Longitude (decimal PCC Latitude (decimal degrees)

PCC Facility

City PCC Facility State PCC Facility Zip Code PCC Facility Longitude (decimal degrees) Latitude (decimal degrees) Does the PCC plant have a separate air permit from the P&P mill? Anytown VA 24553 -78.9104538 37.51063156 no yes
no

PCC EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 77 of 101OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Yes/No Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft Follow instructions in section D3 of the survey overview document to populate this table Complete this spreadsheet tab once for each set of CCA compliance calculations used by a mill. As an alternative to completing this tab, you may submit documentation of your CCA calculations used for purposes of showing compliance. You will have 1 row of data in the left-hand table of this tab (emission balance), and multiple rows in the right-hand table in this tab (CCA equipment list)

Notes: Sources eligible for inclusion in the CCA as credit generators include: pulping systems, bleaching systems, causticizing systems, and papermaking systems. Debit generating sources can include equipment from the kraft mill HVLC system, including: pulp washing systems, knotter systems, screen systems, decker systems, O2 delignification systems, and weak liquor storage tanks. Refer to the system definitions in subpart S at §§63.441 and 63.447(a). EPA is not requesting detailed calculations used to show compliance with the CCA at this time. However, EPA reserves the right to request additional detail if needed as a follow-up to this survey.

Emissions Balance Your response will consist of one row on this left side of the orange line.

Instruction: Provide for all entries. This should match NEI Site ID used in other tabs. Baseline emissions are measured after compliance has been achieved with the kraft pulping process condensate standards, and to revised effluent limitations guidelines and standards in 40 CFR 430 subpart B. The baseline HAP emissions are determined according to §63.447(d). HAP emission reductions from baseline are required to be determined in §63.447(e). Survey overview reference:

Field: NEI Site ID Baseline emissions (kg total HAP/Mg ODP) Emission reductions expected through compliance with the kraft pulping system standards (kg total HAP/Mg ODP) Emission reductions expected through compliance with the CCA (kg total HAP/Mg ODP) Year compliance last demonstrated using CCA How many times has the mill changed the CCA compliance strategy (e.g., changed debit or credit emission points) since first demonstrating compliance with the CCA? Please indicate the year(s) of the change(s). Example entry: 99999 0.68 0.22 0.34 2007 once - 2007

CCA EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 78 of 101CCA Equipment List Your response will consist of miltuple rows on this right side of the orange line.

Instruction: Your response will be multiple rows on this side of the orange line You may add rows to this table to accommodate additional emission units Complete for each emissions unit involved in a CCA calculation. List each emission unit on a separate row and indicate whether it generates debits or credits in the CCA calculation. Select from menu List control technology for creditgenerating emission units. If applicable, list technology applied for under-controlled debit-generating units as well. List parameters

Survey overview reference:

Field: NEI Site ID Line ID (Pulping line ID, Bleaching line ID, or paper machine Emission Unit ID) Emission Unit ID CCA debit or credit generating emission point? Clean condensate alterative technology applied Parameters monitored for clean condensate alterative technology Example entry: 99999 Kraft1 BSW1 debit (uncontrolled) NA-debit source

99999 PM2 PM2 credit other - maintain paper machine white water methanol concentration below 20 mg/l by draining a portion of the methanol-concentrated liquid from the pulp stock and replacing it with cleaner water paper machine throughput; and methanol concentration (mg/l) in the stock blend tanks (SBT3), machine chest (PM2MC), and saveall (SVT) debit (uncontrolled) NA-debit source debit (under controlled) stand-alone biological treatment unit credit steam stripper other - specify

CCA EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 79 of 101

### OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

Follow instructions in section D3 of the survey overview document to populate this table

Instruction: Provide for all entries. This should match NEI Site ID used in other tabs. This section (to the left of the orange line) is to be completed by all mills that perform any type of bleaching.

Line IDs should match those used in other tabs such as the Equip detail tab. Select yes/no Select yes/no Select from menu. Please explain if the bleaching process cannot be characterized as ECF, PCF, or TCF.

Survey overview reference:

Field: NEI Site ID Bleaching line ID Are chlorine or chlorinated compounds used in any stage of the bleaching line? Is the bleaching line preceded by O2 delignification? Is the process ECF, PCF or TCF?

Example entry: 99999 B1 yes yes ECF - elemental chlorine free

yes yes ECF - elemental chlorine free

no no PCF - processed chlorine free

TCF - totally chlorine free

Bleaching EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 80 of 101

### Yes/No If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.

Use the following bleaching sequence notation: C-Chlorine (Cl2) D-Chlorine dioxide (ClO2) E-Alkaline extraction (NaOH etc) P-Hydrogen Peroxide (H2O2) O-Oxygen (O2) H-Hypochlorite (NaClO) Z-Ozone (O3) M-Monox-L X-Enzyme (xylanase) SO2-SO2 Add other notation for bleaching stages not represented above. Enter the decimal percent chlorine dioxide substitution (e.g., enter 0.90 for 90%; enter 1 for 100%) Enter numeric value Enter numeric

value for air dried tons of bleached pulp per year (ADTBP/yr) Enter numeric

value for air dried tons of bleached pulp per day (ADTBP/d) How does the mill use the

bleached pulp produced?

Determine the approximate decimal percentage requested based on bleached pulp capacity in ADTBP/yr.

Bleaching sequence Percent chlorine dioxide substitution Bleach plant operating hr/yr 2009 bleached

capacity, ADTBP/yr 2009

bleached capacity, ADTBP/d Approximate decimal

percentage of bleaching line capacity sold as bleached market pulp Approximate decimal percentage of bleaching line capacity used to manufacture paper or paperboard onsite Check (=1)

DED(DOP) 1 8500 6500 16 0.15 0.85 1

0

Bleaching EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 81 of 101

### This section (to the

right of the orange line) is to be completed for bleaching systems that use any chlorine or chlorinated compounds.

Enter numeric value in oven dried tons per year (ODT/yr) Enter numeric value in

oven dried tons per day(ODT/d) Select from list Select yes/no Each bleaching stage includes the tower vent, washer hood, seal tank vent, chemical and steam mixers, and vacuum pumps Select from list Select from list

Design capacity, ODT/yr Design capacity,

ODT/d Material type Bleaching stage 1 use chlorine or chlorinated compounds? Stage 1 control method Stage 1 chlorofrom control option(s) used to demonstrate subpart S compliance Stage 1 chlorinated HAP control option used to demonstrate subpart S compliance

5475 15 mixture of HWand SW Yes SCBR_BL1 Meet effluent guidelines/standards 99% reduction (by weight) measured as total chlorinated HAP

HW only Y/N NA NA (no chlorine or chlorinated compounds used in this stage) NA (no chlorine or chlorinated compounds used in this stage)

SW only scrubber {enter APCD_ID} NA (mechanical, non-wood, or secondary fiber mill) 99% reduction (by weight) measured as total chlorinated HAP

mixture of HWand SW Use no chlorine or hypochlorite AND meet effluent guidelines/standards 99% reduction (by weight) measured as methanol

secondary fiber Use no chlorine or hypochlorite Outlet concentration < 10 ppmv measured as total chlorinated HAP

non-wood fiber Meet effluent guidelines/standards Outlet concentration < 10 ppmv measured as methanol Total outlet mass emission levels for all subject stages < 0.002 lb/ton ODP

Bleaching EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 82 of 101

### Select yes/no Each bleaching stage includes the tower vent, washer hood, seal tank vent, chemical and steam mixers, and vacuum pumps Select from list Select from list Select yes/no Each bleaching stage includes the tower vent, washer hood, seal tank vent, chemical and steam mixers, and vacuum pumps Select from list Select from list

Bleaching stage 2 use chlorine or chlorinated compounds? Stage 2 control method Stage 2 chlorofrom control option(s) used to demonstrate subpart S compliance Stage 2 chlorinated HAP control option used to demonstrate subpart S compliance Bleaching stage 3 use chlorine or chlorinated compounds? Stage 3 control method Stage 3 chlorofrom control option(s) used to demonstrate subpart S compliance Stage 3 chlorinated HAP control option used to demonstrate subpart S compliance

No SCBR_BL2 NA (no chlorine or chlorinated compounds used in this stage) NA (no chlorine or chlorinated compounds used in this stage) Yes SCBR_BL1 Meet effluent guidelines/standards 99% reduction (by weight) measured as total chlorinated HAP

Y/N NA NA (no chlorine or chlorinated compounds used in this stage) NA (no chlorine or chlorinated compounds used in this stage) Y/N NA NA (no chlorine or chlorinated compounds used in this stage) NA (no chlorine or chlorinated compounds used in this stage)

scrubber {enter APCD_ID} NA (mechanical, non-wood, or secondary fiber mill) 99% reduction (by weight) measured as total chlorinated HAP scrubber {enter APCD_ID} NA (mechanical, non-wood, or secondary fiber mill) 99% reduction (by weight) measured as total chlorinated HAP

Use no chlorine or hypochlorite AND meet effluent guidelines/standards 99% reduction (by weight) measured as methanol Use no chlorine or hypochlorite AND meet effluent guidelines/standards 99% reduction (by weight) measured as methanol

Use no chlorine or hypochlorite Outlet concentration < 10 ppmv measured as total chlorinated HAP Use no chlorine or hypochlorite Outlet concentration < 10 ppmv measured as total chlorinated HAP

Meet effluent guidelines/standards Outlet concentration < 10 ppmv measured as methanol Meet effluent guidelines/standards Outlet concentration < 10 ppmv measured as methanol

Total outlet mass emission levels for all subject stages < 0.002 lb/ton ODP Total outlet mass emission levels for all subject stages < 0.002 lb/ton ODP

Bleaching EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 83 of 101

### Select yes/no Each bleaching stage includes the tower vent, washer hood, seal tank vent, chemical and steam mixers, and vacuum pumps Select from list Select from list Select yes/no Each bleaching stage includes the tower vent, washer hood, seal tank vent, chemical and steam mixers, and vacuum pumps Select from list Select from list

Bleaching stage 4 use chlorine or chlorinated compounds? Stage 4 control method Stage 4 chlorofrom control option(s) used to demonstrate subpart S compliance Stage 4 chlorinated HAP control option used to demonstrate subpart S compliance Bleaching stage 5 use chlorine or chlorinated compounds? Stage 5 control method Stage 5 chlorofrom control option(s) used to demonstrate subpart S compliance Stage 5 chlorinated HAP control option used to demonstrate subpart S compliance

Yes SCBR_BL2 Meet effluent guidelines/standards Outlet concentration < 10 ppmv measured as methanol

Y/N NA NA (no chlorine or chlorinated compounds used in this stage) NA (no chlorine or chlorinated compounds used in this stage) Y/N NA NA (no chlorine or chlorinated compounds used in this stage) NA (no chlorine or chlorinated compounds used in this stage)

scrubber {enter APCD_ID} NA (mechanical, non-wood, or secondary fiber mill) 99% reduction (by weight) measured as total chlorinated HAP scrubber {enter APCD_ID} NA (mechanical, non-wood, or secondary fiber mill) 99% reduction (by weight) measured as total chlorinated HAP

Use no chlorine or hypochlorite AND meet effluent guidelines/standards 99% reduction (by weight) measured as methanol Use no chlorine or hypochlorite AND meet effluent guidelines/standards 99% reduction (by weight) measured as methanol

Use no chlorine or hypochlorite Outlet concentration < 10 ppmv measured as total chlorinated HAP Use no chlorine or hypochlorite Outlet concentration < 10 ppmv measured as total chlorinated HAP

Meet effluent guidelines/standards Outlet concentration < 10 ppmv measured as methanol Meet effluent guidelines/standards Outlet concentration < 10 ppmv measured as methanol Total outlet mass emission levels for all subject stages < 0.002 lb/ton ODP Total outlet mass emission levels for all subject stages < 0.002 lb/ton ODP

Bleaching EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 84 of 101

### Select yes/no Each bleaching stage includes the tower vent, washer hood, seal tank vent, chemical and steam mixers, and vacuum pumps Select from list Select from list Select from list or write in description. Select "NA" if ClO2 bleaching is not performed at the mill. Select "None" if ClO2 bleaching is performed but no measures are employed to reduce CO emissions. Otherwise, describe process or control measure used to reduce CO emissions.

Bleaching stage 6 use chlorine or chlorinated compounds? Stage 6 control method Stage 6 chlorofrom control option(s) used to demonstrate subpart S compliance Stage 6 chlorinated HAP control option used to demonstrate subpart S compliance For mills that use chlorine dioxide (ClO2) bleaching, describe any process or control measures used to reduce emissions of carbon monoxide (CO) from bleaching processes.

None (no CO control measure)

Y/N NA NA (no chlorine or chlorinated compounds used in this stage) NA (no chlorine or chlorinated compounds used in this stage) NA - ClO2 bleaching is not performed

scrubber {enter APCD_ID} NA (mechanical, non-wood, or secondary fiber mill) 99% reduction (by weight) measured as total chlorinated HAP None (no CO control measure)

Use no chlorine or hypochlorite AND meet effluent guidelines/standards 99% reduction (by weight) measured as methanol

Use no chlorine or hypochlorite Outlet concentration < 10 ppmv measured as total chlorinated HAP

Meet effluent guidelines/standards Outlet concentration < 10 ppmv measured as methanol

Total outlet mass emission levels for all subject stages < 0.002 lb/ton ODP

Bleaching EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 85 of 101

### OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

Follow instructions in section D3 of the survey overview document to populate this table Provide data for the 2009 operating year.

Instruction: Provide for all entries. This should match NEI Site ID used in other tabs. Complete table for operable paper machines located at any type of mill. You may need to specify the same paper machine in multiple rows if the machine produces multiple grades of paper at different times (see instructions). Select paper machine configuration from the menu or write in Select from menu Survey overview reference:

Field: NEI Site ID Paper machine Emission Unit ID Type of paper machine as currently configured Is furnish mixture bleached

or unbleached? Example entry: 99999 PM1 Fourdrinier bleached Fourdrinier bleached cylinder unbleached

twin-wire mixture of bleached and

unbleached (please specify)

Paper prod EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 86 of 101

### Do any of the responses (individual cells) you entered in this tab contain CBI? Yes/No If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.

Specify the approximate makeup of each paper machine furnish. Indicate the makeup by showing an approximate percentage in decimal form (e.g., enter 0.65 for 65% softwood kraft) Indicate the other pulp type(s) followed by its approximate decimal percentage (e.g., softwood semichem - 0.10)

Pulp types used

Hardwood kraft % Softwood kraft % Soda % Sulfite % Dissolving/ specialty pulp % Semichemical

pulp % Hardwood mechanical/

groundwood % Softwood mechanical/ groundwood % Secondary fiber % Non-wood fiber % Other % (specify) 0.2 0.65 0.15

Paper prod EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 87 of 101

### Select from menu the most closely related paper grade(s) produced by the paper machine. If multiple paper grades are produced on the same machine, add the additional paper grade(s) in separate rows for the paper machine. Enter paper machine capacity in air dried tons of finished paper/day (ADTFP/d) Specify high density pulp storage (stock chest) consistency in decimal form (e.g., enter 0.15 for 15%).

Leave blank for bleached pulp. Select yes/no. If yes, please include an explanation.

Leave blank for bleached pulp. Specify the headbox consistency in decimal form (e.g., enter 0.001 for 0.1%) Enter the numeric value for the white water recirculation rate in gallons per oven dried ton of pulp. This is the amount of recirculated white water added to the pulp stock prior to the paper machine headbox/wet end. Provide typical white water methanol concentration in milligrams per liter (mg/l) if it has been measured.

HAP concentrations at the paper machine wet end are of interest. Provide typical white water acetaldehyde concentration in milligrams per liter (mg/l) if it has been measured Specify HAPs and concentrations if known. You may provide documentation of typical white water HAP concentrations (if measured) as a separate attachment to your survey response.

Paper machine details

Paper grade produced Capacity, ADTFP/d For unbleached pulps, what is the consistency of pulp in high density storage (%)? For unbleached pulps, has the mill taken steps (e.g., installed a screw press) to raise the consistency of the pulp in high density storage in order to reduce emissions associated with the fluid in the unbleached pulp? What is the consistency of pulp entering the paper machine (%)? White water recirculation rate, gal/ODTP White water methanol concentration, mg/l (if known) White water acetaldehyde concentration, mg/l (if known) White water other HAP concentration, mg/l (if known) coated free sheet 935 0.001 48,300 28 UK UK coated free sheet no uncoated free sheet yes {please explain}

coated groundwood uncoated groundwood tissue & sanitary specialty packaging & industrial kraft packaging linerboard corrugating medium solid bleached board recycled board construction paper and board other (specify type)

Paper prod EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 88 of 101

### Enter description. Examples may include: measures to reduce organics in the pulp stock liquid or white water (e.g., use of clean condensates in final stage of pulp washing); or switching to non-HAP or reduced-HAP additives.

Note Emission Unit ID of stripper if used to strip organics from the paper machine white water (or pulping liquid). Strippers should be included in the Equip detail tab. Enter the number of vents/stacks on the paper machine wet end (e.g., forming and press sections, and other portions of paper machine prior to first dryer) that vent to the atmosphere. Count vents ducted together prior to release to the atmosphere as one vent (e.g., count 4 vacuum system vents ducted together prior to release to the atmosphere as one vent stack). Enter the total exhaust gas flow rate from the wet end vents/stacks in actual cubic feet per minute (if known) Specify APCD_ID from Controls tab, if applicable (e.g., if an APCD is used on wet end vent gases). Enter number of dryer steam cylinders Select air dryer firing method from menu or write in.

Air dryers are direct fired or indirect-fired (use steam-toair heat exchangers to produce a hot air stream that is forced over the surface of the paper). Hoods are used to contain and route the air flow. Air dryers tend to be used on lighter weights of paper, such as tissues, and to supplement the drying of steam cylinders.

Describe any process improvements used to reduce HAP emissions from the wet end Number of vents/stacks on the wet end Total exhaust gas flow rate from the wet end vents/stacks, acfm (if known) Add-on air pollution controls used to reduce HAP emissions from the wet end (insert APCD_IDs) Number of dryer steam cylinders Indicate firing method and fuel type if air drying is

used 16 456,000 50 steam-heated (indirect-fired) steam-heated (indirect-fired) direct fired (natural gas)

direct-fired {specify fuel}

Paper prod EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 89 of 101

### Enter the number of vents/stacks on the paper machine associated with the paper machine dryer(s). Count vents ducted together prior to release to the atmosphere as one vent (e.g., count 4 dryer system vents ducted together prior to release to the atmosphere as one vent stack). Enter the total exhaust gas flow rate from the dryer vents/stacks in actual cubic feet per minute (if known) Specify APCD_ID from Controls tab if applicable (e.g., if an APCD is used on dry end vent gases) Enter the number of vents/stacks on the paper machine dry end following the dryers (e.g., vents around the calendering and winding areas) that vent to the atmosphere. Count vents ducted together prior to release to the atmosphere as one vent. Enter the total exhaust gas flow rate from dry end vents/stacks not associated with the paper machine dryer(s) in actual cubic feet per minute (if known) Enter description of any process improvements that might reduce HAP emissions from the paper machine dry end (dryers or other vents/stacks following the dryers).

Number of dryer vents/stacks Total exhaust gas flow rate from the dryer vents/stacks, acfm (if known) Add-on air pollution controls used to reduce HAP emissions from the dryers (insert APCD_IDs) Number of vents/stacks following the dryer Total exhaust gas flow rate from the dryer vents/stacks, acfm (if known) Describe any process improvements used to reduce HAP emissions from the dry end 4 90,000 2 40,000

Paper prod EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 90 of 101OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Yes/No Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

Complete the table for any stock preparation and paper machine additives that contain measurable amounts of the following HAP: formaldehyde, acetaldehyde, napthalene, methylene chloride, acrylamide, or benzene. Follow instructions in section D3 of the survey overview document to populate this table.

Instruction: Provide for all entries. This should match NEI Site ID used in other tabs. Enter Emission Unit ID List additive type Separate with commas if multiple HAP arepresent (e.g., formaldeyde-5%, acetladehyde2%). Attach additional information to your survey resposne if necessary. Enter numeric value Select from list or write in Survey overview reference:

Field: NEI Site ID Paper machine Emission Unit ID Additive HAP content (% by volume or ppmv for liquids; %

by weight or ppmw for solids) Amount used Units for amount Example entry: 99999 PM1 Wet strength resin Formaldehyde – 5% 8,000 lb/day gal/day lb/day lb/ton paper

HAP additives EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 91 of 101OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

WWTP = wastewater treatment plant Provide a flow diagram of each WWTP showing each wastewater handling/treatment unit. [See survey overview section D1] Use this table to specify any Federal/State/local requirements, permit limits, fenceline monitoring, measurement methods, or modeling methods that apply for measurement or estimation of air emissions (HAP, TRS – including H2S) associated with the WWTP. Follow instructions in section D3 of the survey overview document to populate this table

Instruction: Provide for all entries. This should match NEI Site ID used in other tabs. Specify yes/no. Select yes or no.

If yes, submit the most recent measurement methods and results as a separate file attachment to your survey response. Select yes or no.

If yes, submit the most recent measurement methods (e.g., ambient measurements) and results as a separate file attachment to your survey response. Survey overview reference:

Field: NEI Site ID Does the mill have specific permit limits (including occupational health limits) related to air pollutants from wastewater sources? If yes, please specify the limits (and applicable units) and explain how compliance is demonstrated with these limits. Has fenceline monitoring for air emissions (including WWTP air emissions) been performed? Have air emissions associated with the WWTP been measured?

Example entry: 99999 yes Wehave OSHA limits for H2S and other compounds. See WWTP attachment with our

survey response for a tabular summary. no no

yes yes yes
no no no

WW EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 92 of 101Yes/No If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.

Select yes or no.

If yes, submit documentation of the most recent modeling as a separate file attachment to your survey response. If no fenceline monitoring, measurements (e.g., ambient measurements), or modeling of the wastewater treatment system has been conducted, please explain how wastewater treatment system emissions are accounted for in your air operating permit.

Select "NA" from menu if you answered yes to one of the previous 3 questions.

Select from menu if air emissions associated with wastewater treatment are not addressed in your air permit. Capacity of the wastewater treatment plant (million gallons per day) Enter the approximate volume percentage (decimal percent) of water entering the WWTP from each general mill location

Have air emissions associated with the WWTP been modeled (e.g., with WATER9 or another model)? Explain how wastewater treatment system emissions are accounted for in your air permit if you answered "no" to the previous 3 questions WWTP capacity, MMgal/day Approximate volume percentage of WWTP capacity from kraft condensate streams hard piped for biological treatment in the WWTP (per subpart S) Approximate volume percentage of WWTP capacity from chemical pulping processes (other than subpart S hard-piped kraft condensates) Approximate volume percentage of WWTP capacity from non-chemical pulping processes (e.g., mechanical, secondary fiber, or non-wood pulping) Approximate volume percentage of WWTP capacity from bleaching processes Approximate volume percentage of WWTP capacity from papermaking processes Approximate volume percentage of WWTP capacity from other processes or stormwater runoff Check (=1)

yes (see separate WWTP attachment with modeling input and output) NA 18.5 0.05 0.3 NA 0.2 0.35 0.1 1

yes Air emissions associated with wastewater treatment are not addressed in the air operating permit. 0

no NA

WW EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 93 of 101Select the general type of WWTP used by your mill. Select from menu or write in a description. Select from list or write in description Enter short description Select from list or write in description List the wastewater treatment units in your WWTP (separated by commas) in the general sequence in which wastewater flows through the units. Include any primary and/or secondary clarifiers, oil-water separators, equalization basins, neutralization, activated-sludge biological treatment units, aerated or non-aerated surface impoundments, anaerobic digesters, other biological treatment units (trickling filters, rotating biological contactors), wastewater storage tanks, and any other wastewater treatment units.

Provide a flow diagram showing each wastewater handling/treatment unit. If any wastewater treatment units are equipped with a closed vent collection system and air pollution control device (APCD), then you should also include the wastewater treatment unit in the Emission Unit ID column of the Equip detailand Controltabs and indicate the APCD information in those tabs.

General type of wastewater treatment system Identify upstream process wastewater treatment systems used to reduce wastewater treatment unit air emissions of nonchlorinated organic HAP and TRS (including H2S). Describe any upstream practices or pollution prevention measures that reduce wastewater treatment unit air emissions of nonchlorinated organic HAP and TRS (including H2S). Describe any upstream practices or pollution prevention measures that reduce wastewater treatment unit air emissions of chlorinated HAP. List the wastewater treatment units in your WWTP in the general sequence in which they are used Identify any wastewater treatment units from the list in the previous column that are closed systems. Indicate controls if the unit is equipped with a closed vent collection system and APCD.

Aerated stabilization basin (aerated surface impoundment) steam stripper (STRIPPER) Use ClO2 bleaching (instead of chlorine or hypochlorite) Clarifiers 1-3 (in parallel), aeration basins 1 and 2, activated sludge basin, and secondary clarifiers 4-6 (in parallel) NA

Aerated stabilization basin (aerated surface impoundment) steam stripper (enter Emission Unit ID) Use only nonchlorinated bleaching compounds Activated-sludge biological treatment biological treatment unit Use ClO2 bleaching (instead of chlorine or hypochlorite)

Packaged system (specify e.g., UNOX system)wastewater thermal oxidizer (enter Emission Unit ID) Other (specify) Other (specify) Other (specify)

WW EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 94 of 101Biological treatment system performance data (required for biological treatment systems controlling kraft pulping condensates):

First quarter (Q1) compliance determination for 2009 See equation in §63.457(l) of subpart S for calculation of "r" The value of Fbio(MeOH) is used in the equations in §63.457(l) of subpart S for purposes of determining percent reduction or mass removal of total HAP in a biological treatment system Enter the percent reduction of total HAP if percent reduction is used to demonstrate compliance with subpart S. For example, enter "92" for a 92 percent reduction. Leave blank if the precent reduction compliance option is not used.

"Total HAP" includes acetaldehyde, methanol, MEK, and propionaldehyde. Enter the mass removal of total HAP if

mass removal is used to demonstrate compliance with subpart S. Leave blank if the mass removal compliance option is not used.

Q1 mass flow rate of methanol entering the system (kg/Mg ODP) Q1 mass flow rate of acetaldehyde, MEK, and propionaldehyde entering the system (kg/Mg ODP) Mass flow ratio of non-methanol total HAP to methanol (value of "r") Q1 value of Fbio(MeOH) determined according to 40 CFR 63 Appendix C Q1 percent reduction in "total HAP" (%) Q1 mass removal of "total HAP" (kg/Mg ODP)

11.5 0.35 0.03 0.97 94

WW EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 95 of 101Second quarter (Q2) compliance Third quarter (Q3) compliance

Q2 mass flow rate of methanol entering the system (kg/Mg ODP) Q2 value of Fbio(MeOH) determined according to 40 CFR 63 Appendix C Q2 percent reduction in total HAP (calculated using the quarterly methanol measurement and value of "r" as specified in subpart S), % Q2 mass removal of "total HAP" calculated as specified in subpart S (kg/Mg ODP) Q3 mass flow rate of methanol entering the system (kg/Mg ODP) Q3 value of Fbio(MeOH) determined according to 40 CFR 63 Appendix C Q3 percent reduction in total HAP (calculated using the quarterly methanol measurement and value of "r" as specified in subpart S), % Q3 mass removal of "total HAP" calculated as specified in subpart S (kg/Mg ODP)

5.9 0.92 5.3 9.8 0.98 95

WW EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 96 of 101Fourth quarter (Q4) compliance

Q4 mass flow rate of methanol entering the system (kg/Mg ODP) Q4 value of Fbio(MeOH) determined according to 40 CFR 63 Appendix C Q4 percent reduction in total HAP (calculated using the quarterly methanol measurement and value of "r" as specified in subpart S), % Q4 mass removal of "total HAP" calculated as specified in subpart S (kg/Mg ODP)

12.3 0.95 92

WW EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 97 of 101

## OMB Control No: xxxx-xxxx Do any of the responses (individual cells) you entered in this tab contain CBI? Expiration Date: xx/xx/xxxx If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI. Review Draft

Follow instructions in section D4 of the survey overview document to populate this table. Use this table to identify the specific emission units for which emission test reports are being submitted. EPA will extract the test data from the emission test reports. See Attachment 6 of the survey overview document for a list of emissions test reports to be submitted.

Instruction: Provide for all entries. This should match NEI Site ID used in other tabs. Provide for all entries. Line IDs should match those used in other tabs such as the Equip detailtab. Provide for all entries. Emission Unit IDs should match those used in other tabs such as the Equip detail tab. Survey overview reference:

Field: NEI Site ID Line ID (Pulping line ID, Bleaching line ID, or paper machine Emission Unit ID) Emission Unit ID(s) Example entry: 99999 Kraft1 DIG-1, DIG-2, EVAP 99999 Kraft1 LK1

Emissions test data EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 98 of 101

## Do any of the responses (individual cells) you entered in this tab contain CBI? Yes/No If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.

Leave columns that do not apply for a given emission unit blank.

Specify the collection system if applicable. (Examples of collection systems include closed vent systems, LVHC, and HVLC systems.) Collection system IDs should match those used in other tabs such as the Equip detail tab. Provide the APCD used during the emissions test.

APCD_IDs should match those used in other tabs such as theEquip detailtab (unless equipment configuration has changed). Enter combustion controls used during the emission test (see also the Controls tab) Use this column for notes or if helpful to specify the emission points tested (e.g., for equipment with multiple emission points, where only selected emission points/vents were tested) Enter year testing was conducted (i.e., the test date year)

Collection system ID(s) APCD_ID(s) Combustion controls used to reduce air pollution (from combustion sources) Process testing notes (optional) Test report year (XXXX) LVHC-1 LK1/SCBR2 2006 SCBR2 2006

Emissions test data EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 99 of 101

## List the pollutants tested. Separate multiple pollutants by

commas. Enter the EPA test method number (e.g., M5, M7E). Be very specific if the method used was not an EPA method. Specify if APCD

inlet or outlet data are provided (or both) This question will be used in

determining whether the test data remain representative of your current operations. Explain any changes in equipment configuration as they relate to representativeness of the emissions test data supplied. OPTIONAL: Data regarding frequency and cost of testing would help EPA more accurately estimate testing costs associated with the pulp and paper NESHAP and NSPS. OPTIONAL

Pollutants tested Test method(s) used Are inlet or

outlet data provided? Has the configuration of the

emission unit, combustion controls, collection system, or APCD changed since the test was conducted? If yes, please explain How often are you required to perform testing of this emission unit for the pollutants listed? Approximate cost per test, $ methanol M308 inlet and outlet no one-time test only 12000 PM M5 outlet no annually 6000 PM outlet yes annually PM2.5-filterable inlet no every 2 years PM2.5-cond. inlet and outlet every 5 years NOx one-time test only SO2 as requested by the permitting authority CO methanol THC chlorine CDD/CDF POM/PAH Speciated HAP metals HCl TRS

Emissions test data EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 100 of 101

### Review of this draft spreadsheet is being requested for general structure and content (e.g., column headings, menu choices, etc).

Customized spreadsheets containing each mill's NEI data set can be supplied for each mill on a disk or flash drive.

Brief instructions for each column are provided where needed in an "Instructions" row as well as in a descriptive column heading. More lengthy instructions appear in the survey overview document (as needed).

The final spreadsheet will contain pull down menus (convenient for users, and leading to consistency in the final data base). Pull down menu text is currently located in the draft tabs for reviewer convenience, but will be moved to its own locked and hidden tab in the final draft (so that it only appears when the cell containing the menu is selected). Some pull down menus will be limited to the list provided, while others will allow for "write-in" answers (depending on the survey question).

Cells outside the range where data are to be entered can be locked (to prevent data being written in outside cells and eventually getting pulled into Access) Shading may be used to indicate where data are not to be entered. Cells formats and print areas will be set in the final version.

QA would be conducted upon receipt of completed spreadsheets from respondents to:

ensure all non-CBI check completeness check mill and equipment coding for consistency check the data for import issues etc

Following QA and followup with the mill (if needed), a Macro can be run to replace instruction rows and long column headings with short Access headings and to otherwise format the data for import into Access. This spreadsheet is being set up so that data can be read into Access with a computer program (to be written).

Draft Notes EPA-HQ-OAR-2007-0544-DRAFT-0003.xls 101 of 101