OMB Control No: 2060-0656 Did any of the responses (individual cells) you entered in this tab contain CBI? 

Expiration Date: 2/28/2014 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.

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.

"Nominal daily throughput capacity" is defined as the typical operating rate for the emission unit.

Pulp and Paper sector facility data.

Instruction:

Provide for all entries. This should 

match NEI Site ID used in Part II of 

this survey (the NEI update).

If no NEI Site ID exists for your 

facility in Part II, use a temporary 

ID of "NEW_____" where the 

blank is your facility's zip code. Name of legal operator of facility Complete street address of facility (physical location) Provide mailing address if different than physical location Facility contact able to answer technical questions about the completed survey

Survey reference:

Field: NEI Site ID Legal operator Physical address Physical city

Physical 

state Physical zip

Physical 

county 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

Example entry: 99999 Gaint Corporation 1000 Plant Road Anytown VA 24553 Amherst PO Box 123 Fairspring VA 24554 Amherst Joe Smith Environmental Manager 999-999-9999 456 999-999-8888 joe.smith@anymillusa.com

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Mill 0900006480f7efd2.xls 1 of 5
OMB Control No:

Expiration Date:

UK = Unknown. NA = Not Applicable

"Nominal daily throughput capacity" is defined as the typical operating rate for the emission unit.

Pulp and Paper sector facility data.

Instruction:

Survey reference:

Field:

Example entry:

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If 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 in the survey 

overview document for notifying EPA 

to determine if you should complete 

this survey.

See the 40 CFR part 63 subpart A 

definition of "major source" in the 

survey overview document 

Attachment 1.

The primary NAICS code represents the line of business that generates the 

most income for the facility.

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 of 

facility 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 Attachment 2 of the Part I survey instructions.

Size of entity

Legal owner address Legal owner city

Legal 

owner 

state

Legal 

owner zip

Dun Bradstreet 

owner Dun Bradstreet mill HAP size classification Primary NAICS Worldwide employees Facility employees Small business

100 Corporate Blvd Green Bay WI 54304 9020777 149810921 major 322121-Paper (except Newsprint) Mills >1000 500-749 no

Mill 0900006480f7efd2.xls 2 of 5
OMB Control No:

Expiration Date:

UK = Unknown. NA = Not Applicable

"Nominal daily throughput capacity" is defined as the typical operating rate for the emission unit.

Pulp and Paper sector facility data.

Instruction:

Survey reference:

Field:

Example entry:

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Select yes/no Select the most relevant response Select yes/no Select yes/no

Select from menu. You may write in more than 

once choice. Enter number

Enter the 2009 

nominal daily 

production capacity 

total for all market 

pulp products. Select from menu

Federal rule coverage Pulps Pulp dryers Market pulp Bleaching (or brightening) systems

P&P 

NESHAP 

subpart S

Combustion 

Source NESHAP 

subpart MM

Paper/web 

coating 

NESHAP 

subpart 

JJJJ

Boiler NESHAP subpart 

DDDDD (or CISWI emission 

guidelines/NSPS) that are 

under development

Other NESHAP 

(list subparts)

Kraft NSPS 

subpart BB

Boiler 

NSPS

Other NSPS (list 

subparts)

Does the mill 

produce virgin 

pulp?

Does the mill produce pulp from 

secondary fiber?

Does the mill 

purchase virgin pulp?

Does the mill purchase 

secondary fiber pulp? Types of market pulp produced by the mill

Total number of pulp 

dryers used to 

produce market pulp

2009 nominal daily 

market pulp 

production capacity 

(short tons/day) Is bleaching or brightening 

performed at the mill?

Applies Applies Applies Applies DDDD Applies Db NA yes no no no NA NA NA yes-bleaching

Indicate "applies" for each federal NESHAP or NSPS that limits emissions or establishes requirements from any single piece of equipment at the mill. 

Mark "NA" if not applicable (or if the otherwise applicable Federal rule contains no specific requirements for the equipment types at your mill). For the 

other standards list the subparts that apply. If in doubt, check your operating permit for Federal air rule subparts that apply.

Mill 0900006480f7efd2.xls 3 of 5
OMB Control No:

Expiration Date:

UK = Unknown. NA = Not Applicable

"Nominal daily throughput capacity" is defined as the typical operating rate for the emission unit.

Pulp and Paper sector facility data.

Instruction:

Survey reference:

Field:

Example entry:

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Enter number of 

machines

Enter the 2009 total 

nominal daily 

production capacity 

for all 

paper/paperboard 

products.

Enter decimal percent 

for utilization (e.g., 0.7 

for 70% of capacity 

utilized). See survey 

instructions for an 

example.

Enter the typical decimal percent 

for utilization (e.g., 0.7 for 70% of 

capacity utilized) for the past 5 

years. One way to determine the 

5-year utilization would be to 

average the utilization 

percentages for 2005, 2006, 

2007, 2008, and 2009.

Select from menu the general paper 

grades manufactured by the paper mill 

in 2009 (noting the product produced in 

the greatest quantity as product 1, 

product produced in the 2nd greatest 

quantity as product 2, etc.) 

Use the paper grades most closely 

related to the paper grades produced at 

your mill if you do not find an exact 

match in the menu.

Specify other paper grade(s) if none of 

the grades in the menu reasonably 

match the grades produced at your mill

Paper or paperboard processes/products Paper capacity utilization Paper grades produced

Total number of paper 

machines

2009 nominal daily 

production capacity 

total for 

paper/paperboard 

(air dried short 

tons/day) 

2009 

paper/paperboard 

capacity utilization 

percentage

5-year average (2005-2009) 

paper/paperboard capacity 

utilization percentage

Paper grade 1 Paper grade 2 Paper grade 3 Paper grade 4 Paper grade 5 Paper grade 6 Paper grade 7

1 340000 0.8 0.95 uncoated free sheet linerboard other - specialty food-grade

Mill 0900006480f7efd2.xls 4 of 5
OMB Control No:

Expiration Date:

UK = Unknown. NA = Not Applicable

"Nominal daily throughput capacity" is defined as the typical operating rate for the emission unit.

Pulp and Paper sector facility data.

Instruction:

Survey reference:

Field:

Example entry:

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Optional. Enter any comments you have on the data supplied.

Paper grade 8 Paper grade 9 Paper grade 10 Comments

Mill 0900006480f7efd2.xls 5 of 5
OMB Control No: 2060-0656 Did any of the responses (individual cells) you entered in this tab contain CBI? 

Expiration Date: 2/28/2014 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.

You may find it helpful to use Excel's "freeze panes" or "split" features when viewing this spreadsheet. 

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms. "Nominal daily throughput capacity" is defined as the typical operating rate for the emission unit. For example, pulp mill production can be used to approximate pulp mill equipment throughput capacity. *You do not need to complete these columns for boilers if you included Boiler MACT survey codes. *You do not need to complete these columns for boilers if you included Boiler MACT surv

Instruction:

Provide for all 

entries. This should 

match NEI Site ID 

used in Part II.

Provide for all entries. Use the Emission Unit ID in the NEI data set for your mill (supplied for Part II) if the 

individual emission unit is listed there. If emission units are aggregated by collection system in the NEI, then 

you would list each emission unit separately with a new Emission Unit ID in this tab. See the survey 

instruction document for more information on matching Emission Unit IDs to the NEI.

Collection systems (identified with the Collection system ID), boilers, 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. 

Supply information for combustion units that burn NCGs or SOGs in this PI Equip detail tab.

OPTIONAL (for boilers). 

Instead of entering certain 

boiler details in this 

spreadsheet, you may specify 

the ID numbers included in the 

Boiler MACT survey for your 

boilers. Use the Boiler MACT 

Code Lookup.xls spreadsheet 

provided with Part I to 

determine your Boiler MACT 

codes.

Enter the Boiler MACT Facility 

ID

OPTIONAL (for boilers)

Enter the Boiler MACT 

Unit ID

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.)

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

Use this column for notes or if helpful to 

relate equipment and process lines to your 

permit, the NEI, or other information

Write in a description using the 

common equipment types listed in 

Attachment 1 of the survey instruction 

document.

(See boiler note*)

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 of 

the upgrade as "XXXXupgrade." 

(See boiler note*)

Enter 2009 operating 

hr/yr. 

Enter the exhaust flow rate from the emission unit (if known) in actual cubic feet per 

minute (acfm).

Leave blank for emission units not ducted through a conveyance (e.g., emission 

units not vented, vented into a building, or fugitive sources). 

Measured flow rates from stack tests are preferred (if available). Otherwise, 

provide an estimate or enter "UK" for unknown.

If the emission unit listed in this row has multiple vents, the please enter the total 

flow from all vents combined and note in column O "multiple vents combined". See 

instruction document for details.

If exhaust from the emission unit is combined with exhaust from other emission 

units, please indicate the emission units IDs in the next column with combined 

exhaust flow.

Enter the emission unit exhaust gas 

temperature in degrees Fahrenheit 

(if known)

Enter the emission unit exhaust gas 

moisture content (% H2O), if known. 

For example, enter "10" for 10%. 

Exhaust flow rate measurements may have been 

performed through stack testing at the emission point 

after multiple exhaust streams have been combined. If 

exhaust from the emission unit is combined with exhaust 

from other emission units, please indicate the emission 

units IDs with combined exhaust flow.

If the emission unit has multiple vents and the exhaust 

flow provided is the total from multiple combined vents, 

enter the "multiple vents combined" in this column.

Specify the location of the flow rate provided. 

Select from menu (or write in response):

List any combustion control measures 

installed/employed to reduce air 

pollution from combustion sources (e.g., 

thermal oxidizers, direct-fired dryers, or 

boilers) Select yes/no

Survey reference: Equipment identification Emission unit exhaust parameters (if emitted through a conveyance)* Combustion modifications or controls*

Field: NEI Site ID Emission Unit ID

Boiler MACT Survey Facility 

ID

Boiler MACT Survey 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 Process notes (optional) Emission unit description

Year emission unit 

installed

Emission unit 

operating hr/yr Emission unit exhaust flow rate, acfm (if known)

Exhaust gas temperature, F (if 

known)

Exhaust gas moisture content, % 

(if known)

Emission units IDs (or Collection System IDs) with 

combined exhaust flow Location of flow rate provided Combustion controls

Were these 

combustion controls 

added within the last 10 

years?

Example entry: 99999 DIG-1 LVHC-1 digester pre-1990 8400 2,000 175 45 multiple vents combined inlet to collection system

99999 DIG-2 LVHC-1 digester pre-1990 8430 1,200 200 50 multiple vents combined inlet to collection system

99999 STRIPPER NEI Emission Unit ID = 06 steam stripper system 2000 8430 14,000 UK UK stripper outlet (inlet to boiler)

LVHC-1 LVHC collection system 2000-upgrade 8370 14,000 UK UK collection system outlet (inlet to lime kiln)

99999 TO thermal oxidizer (backup) 2000 390 11,000 300 8 control device (scrubber) outlet

99999 Boiler EU55 VAGaintCorporationAnytown EU55 NEI Emission Unit ID = EU55 boiler 1985 8700 56,000 250 12 control device outlet overfire air No

99999 EVAP LVHC-1 evaporator UK 8430 UK UK UK NA

99999 GENERIC UNIT 0.85 NEI Emission Unit ID = GEN09 generic example row UK 8430 18,000 150 7 prior to atmospheric release

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PI Equip detail 0900006480f7efd2.xls 1 of 66
Field: NEI Site ID Emission Unit ID

Boiler MACT Survey Facility 

ID

Boiler MACT Survey 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 Process notes (optional) Emission unit description

Year emission unit 

installed

Emission unit 

operating hr/yr Emission unit exhaust flow rate, acfm (if known)

Exhaust gas temperature, F (if 

known)

Exhaust gas moisture content, % 

(if known)

Emission units IDs (or Collection System IDs) with 

combined exhaust flow Location of flow rate provided Combustion controls

Were these 

combustion controls 

added within the last 10 

years?

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PI Equip detail 0900006480f7efd2.xls 2 of 66
Field: NEI Site ID Emission Unit ID

Boiler MACT Survey Facility 

ID

Boiler MACT Survey 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 Process notes (optional) Emission unit description

Year emission unit 

installed

Emission unit 

operating hr/yr Emission unit exhaust flow rate, acfm (if known)

Exhaust gas temperature, F (if 

known)

Exhaust gas moisture content, % 

(if known)

Emission units IDs (or Collection System IDs) with 

combined exhaust flow Location of flow rate provided Combustion controls

Were these 

combustion controls 

added within the last 10 

years?

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PI Equip detail 0900006480f7efd2.xls 3 of 66
Field: NEI Site ID Emission Unit ID

Boiler MACT Survey Facility 

ID

Boiler MACT Survey 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 Process notes (optional) Emission unit description

Year emission unit 

installed

Emission unit 

operating hr/yr Emission unit exhaust flow rate, acfm (if known)

Exhaust gas temperature, F (if 

known)

Exhaust gas moisture content, % 

(if known)

Emission units IDs (or Collection System IDs) with 

combined exhaust flow Location of flow rate provided Combustion controls

Were these 

combustion controls 

added within the last 10 

years?

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PI Equip detail 0900006480f7efd2.xls 4 of 66
Field: NEI Site ID Emission Unit ID

Boiler MACT Survey Facility 

ID

Boiler MACT Survey 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 Process notes (optional) Emission unit description

Year emission unit 

installed

Emission unit 

operating hr/yr Emission unit exhaust flow rate, acfm (if known)

Exhaust gas temperature, F (if 

known)

Exhaust gas moisture content, % 

(if known)

Emission units IDs (or Collection System IDs) with 

combined exhaust flow Location of flow rate provided Combustion controls

Were these 

combustion controls 

added within the last 10 

years?

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PI Equip detail 0900006480f7efd2.xls 5 of 66
Field: NEI Site ID Emission Unit ID

Boiler MACT Survey Facility 

ID

Boiler MACT Survey 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 Process notes (optional) Emission unit description

Year emission unit 

installed

Emission unit 

operating hr/yr Emission unit exhaust flow rate, acfm (if known)

Exhaust gas temperature, F (if 

known)

Exhaust gas moisture content, % 

(if known)

Emission units IDs (or Collection System IDs) with 

combined exhaust flow Location of flow rate provided Combustion controls

Were these 

combustion controls 

added within the last 10 

years?

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PI Equip detail 0900006480f7efd2.xls 6 of 66
OMB Control No:

Expiration Date:

You may find it helpful to use Excel's "freeze panes" or "split" features when viewing this spreadsheet. 

UK = Unknown. NA = Not Applicable

Instruction:

Survey reference:

Field:

Example entry: 123456789

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eed to complete these columns for boilers if you included Boiler MACT survey codes. **You do not need to complete these columns for boilers if you included Boiler MACT survey codes (on rows where the Emission Unit ID is a boiler). However, boilers that control NCG/SOG must be listed (on rows for the Emission Unit IDs the boiler controls).

Enter percent 

reduction (if known) 

and indicate the 

basis for the value 

provided (e.g., 

CEMS data, beforeand-after testing, 

design value).

Enter percent 

reduction (if known) 

and indicate the 

basis for the value 

provided (e.g., 

CEMS data, beforeand-after testing, 

design value).

Enter percent 

reduction (if known) 

and indicate the 

basis for the value 

provided (e.g., 

CEMS data, beforeand-after testing, 

design value).

Describe any specific process control or 

pollution prevention measures used to reduce 

emissions 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.

Primary 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 

emissions, 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 

emissions, include any control devices 

used on the process equipment. 

Enter ID code 

for 4th APCD 

(to be used 

throughout the 

survey 

spreadsheets)

Process controls or pollution prevention Air pollution controls (primary method of control)**

Combustion 

control NOx %red 

(note basis)

Combustion 

control SO2 %red 

(note basis)

Combustion 

control CO% red 

(note basis)

Process controls or pollution prevention 

measures 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

20%-design WESP WESP 1

Uncontrolled

PI Equip detail 0900006480f7efd2.xls 7 of 66
Field:

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Combustion 

control NOx %red 

(note basis)

Combustion 

control SO2 %red 

(note basis)

Combustion 

control CO% red 

(note basis)

Process controls or pollution prevention 

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

PI Equip detail 0900006480f7efd2.xls 8 of 66
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Combustion 

control NOx %red 

(note basis)

Combustion 

control SO2 %red 

(note basis)

Combustion 

control CO% red 

(note basis)

Process controls or pollution prevention 

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

PI Equip detail 0900006480f7efd2.xls 9 of 66
Field:

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Combustion 

control NOx %red 

(note basis)

Combustion 

control SO2 %red 

(note basis)

Combustion 

control CO% red 

(note basis)

Process controls or pollution prevention 

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

PI Equip detail 0900006480f7efd2.xls 10 of 66
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Combustion 

control NOx %red 

(note basis)

Combustion 

control SO2 %red 

(note basis)

Combustion 

control CO% red 

(note basis)

Process controls or pollution prevention 

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

PI Equip detail 0900006480f7efd2.xls 11 of 66
Field:

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Combustion 

control NOx %red 

(note basis)

Combustion 

control SO2 %red 

(note basis)

Combustion 

control CO% red 

(note basis)

Process controls or pollution prevention 

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

PI Equip detail 0900006480f7efd2.xls 12 of 66
OMB Control No:

Expiration Date:

You may find it helpful to use Excel's "freeze panes" or "split" features when viewing this spreadsheet. 

UK = Unknown. NA = Not Applicable

Instruction:

Survey reference:

Field:

Example entry: 123456789

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ed (on rows for the Emission Unit IDs the boiler controls).

Complete for emission units (as 

shown in the Emission Unit ID 

column) with alternate/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**

Alternate method of control 

(specify APCD_ID or Emission 

Unit ID)

Conditions when alternate 

control is used

Approximate hr/yr when 

alternate 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

PI Equip detail 0900006480f7efd2.xls 13 of 66
Field:

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Alternate method of control 

(specify APCD_ID or Emission 

Unit ID)

Conditions when alternate 

control is used

Approximate hr/yr when 

alternate control is used to 

control emissions from the 

Emission Unit ID

PI Equip detail 0900006480f7efd2.xls 14 of 66
Field:

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Alternate method of control 

(specify APCD_ID or Emission 

Unit ID)

Conditions when alternate 

control is used

Approximate hr/yr when 

alternate control is used to 

control emissions from the 

Emission Unit ID

PI Equip detail 0900006480f7efd2.xls 15 of 66
Field:

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Alternate method of control 

(specify APCD_ID or Emission 

Unit ID)

Conditions when alternate 

control is used

Approximate hr/yr when 

alternate control is used to 

control emissions from the 

Emission Unit ID

PI Equip detail 0900006480f7efd2.xls 16 of 66
Field:

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Alternate method of control 

(specify APCD_ID or Emission 

Unit ID)

Conditions when alternate 

control is used

Approximate hr/yr when 

alternate control is used to 

control emissions from the 

Emission Unit ID

PI Equip detail 0900006480f7efd2.xls 17 of 66
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Alternate method of control 

(specify APCD_ID or Emission 

Unit ID)

Conditions when alternate 

control is used

Approximate hr/yr when 

alternate control is used to 

control emissions from the 

Emission Unit ID

PI Equip detail 0900006480f7efd2.xls 18 of 66
OMB Control No:

Expiration Date:

You may find it helpful to use Excel's "freeze panes" or "split" features when viewing this spreadsheet. 

UK = Unknown. NA = Not Applicable

Instruction:

Survey reference:

Field:

Example entry: 123456789

10

11

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Select yes/no. 

[Consider how the emission unit is permitted 

when specifying if it is subject to NSPS BB. For 

example, a boiler or thermal oxidizer controlling 

BB emission units is not necessarily an emission 

unit subject 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 approximate year 

(e.g., "pre-1990") Select from menu.

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. Leave blank if 

not applicable.] 

Indicate NSPS subpart BB TRS compliance option used to 

demonstrate compliance using backup method of control for the 

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

[Note: Leave blank if no backup control is specified in the columns 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

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 

emissions from 

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

no

no

yes pre-1990 new

no

PI Equip detail 0900006480f7efd2.xls 19 of 66
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Is emission unit subject to NSPS BB?

If yes, year became 

subject to BB (XXXX)

Reason subject 

to 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)

PI Equip detail 0900006480f7efd2.xls 20 of 66
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477

478

479

480

481

482

Is emission unit subject to NSPS BB?

If yes, year became 

subject to BB (XXXX)

Reason subject 

to 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)

PI Equip detail 0900006480f7efd2.xls 21 of 66
Field:

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Is emission unit subject to NSPS BB?

If yes, year became 

subject to BB (XXXX)

Reason subject 

to 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)

PI Equip detail 0900006480f7efd2.xls 22 of 66
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819

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821

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823

824

825

826

827

828

829

830

831

832

Is emission unit subject to NSPS BB?

If yes, year became 

subject to BB (XXXX)

Reason subject 

to 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)

PI Equip detail 0900006480f7efd2.xls 23 of 66
Field:

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Is emission unit subject to NSPS BB?

If yes, year became 

subject to BB (XXXX)

Reason subject 

to 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)

PI Equip detail 0900006480f7efd2.xls 24 of 66
OMB Control No:

Expiration Date:

You may find it helpful to use Excel's "freeze panes" or "split" features when viewing this spreadsheet. 

UK = Unknown. NA = Not Applicable

Instruction:

Survey reference:

Field:

Example entry:

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

17

18

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Select yes/no.

Synthetic area sources should select "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, along with a slection for synthetic area sources. You may write in other reasons. 

Complete for each digester source. 

This could include multiple emission 

units that are part of one emission 

source (as noted in the Part I 

survey instructions for "Multiple 

emission units ducted to a single 

release point").

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 hardwood and softwood. 

You may also select "Non-wood."

Complete for each 

pulp washing system 

(e.g., washing line).

Enter numeric value

Enter number of 

washers in series

Enter the types 

of washers 

used in series:

V=vacuum 

drum

D=diffusion

P=pressure

B=belt

O=other

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 milligrams per 

liter, if known. Use the average 

from 2009 or target value.

Subpart S NESHAP applicability Digesters Pulp washing systems

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 Batch or continuous

Digester 

nominal daily 

production 

capacity, 

ADTP/d Wood type (HW, SW, HW/SW swing)

Washing system 

nominal daily 

production 

capacity, ADTP/d

Total number of 

washers

Washer types 

and sequence

Source of vacuum drum 

washer final stage shower 

water

Vacuum drum washer final 

stage shower water methanol 

concentration, mg/l

yes Continuous 480 SW

yes Continuous 520 HW/SW swing

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

yes

no 1000 3 D-V-V

stripped digester and 

evaporator condensates

PI Equip detail 0900006480f7efd2.xls 25 of 66
Field:

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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 Batch or continuous

Digester 

nominal daily 

production 

capacity, 

ADTP/d Wood type (HW, SW, HW/SW swing)

Washing system 

nominal daily 

production 

capacity, ADTP/d

Total number of 

washers

Washer types 

and sequence

Source of vacuum drum 

washer final stage shower 

water

Vacuum drum washer final 

stage shower water methanol 

concentration, mg/l

PI Equip detail 0900006480f7efd2.xls 26 of 66
Field:

308

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481

482

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 Batch or continuous

Digester 

nominal daily 

production 

capacity, 

ADTP/d Wood type (HW, SW, HW/SW swing)

Washing system 

nominal daily 

production 

capacity, ADTP/d

Total number of 

washers

Washer types 

and sequence

Source of vacuum drum 

washer final stage shower 

water

Vacuum drum washer final 

stage shower water methanol 

concentration, mg/l

PI Equip detail 0900006480f7efd2.xls 27 of 66
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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 Batch or continuous

Digester 

nominal daily 

production 

capacity, 

ADTP/d Wood type (HW, SW, HW/SW swing)

Washing system 

nominal daily 

production 

capacity, ADTP/d

Total number of 

washers

Washer types 

and sequence

Source of vacuum drum 

washer final stage shower 

water

Vacuum drum washer final 

stage shower water methanol 

concentration, mg/l

PI Equip detail 0900006480f7efd2.xls 28 of 66
Field:

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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 Batch or continuous

Digester 

nominal daily 

production 

capacity, 

ADTP/d Wood type (HW, SW, HW/SW swing)

Washing system 

nominal daily 

production 

capacity, ADTP/d

Total number of 

washers

Washer types 

and sequence

Source of vacuum drum 

washer final stage shower 

water

Vacuum drum washer final 

stage shower water methanol 

concentration, mg/l

PI Equip detail 0900006480f7efd2.xls 29 of 66
Field:

833

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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 Batch or continuous

Digester 

nominal daily 

production 

capacity, 

ADTP/d Wood type (HW, SW, HW/SW swing)

Washing system 

nominal daily 

production 

capacity, ADTP/d

Total number of 

washers

Washer types 

and sequence

Source of vacuum drum 

washer final stage shower 

water

Vacuum drum washer final 

stage shower water methanol 

concentration, mg/l

PI Equip detail 0900006480f7efd2.xls 30 of 66
OMB Control No:

Expiration Date:

You may find it helpful to use Excel's "freeze panes" or "split" features when viewing this spreadsheet. 

UK = Unknown. NA = Not Applicable

Instruction:

Survey reference:

Field:

Example entry: 123456789

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Complete 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

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. Use the average 

from 2009 or target value.

Knotters, screens, and deckers Evaporators Oxygen delignification

Knotter, screen, or decker 

nominal daily production 

capacity, ADTP/d

Type of shower water used in 

decker

Evaporator nominal 

daily production 

capacity, gal/day of 

weak black liquor

Which pulp washer(s) are 

the source(s) of weak liquor 

for the evaporator set?

How many 

evaporator 

effects are 

there?

Nominal daily 

production 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 WASHER6

300 1100 WASHER 436

PI Equip detail 0900006480f7efd2.xls 31 of 66
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Knotter, screen, or decker 

nominal daily production 

capacity, ADTP/d

Type of shower water used in 

decker

Evaporator nominal 

daily production 

capacity, gal/day of 

weak black liquor

Which pulp washer(s) are 

the source(s) of weak liquor 

for the evaporator set?

How many 

evaporator 

effects are 

there?

Nominal daily 

production 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

PI Equip detail 0900006480f7efd2.xls 32 of 66
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Knotter, screen, or decker 

nominal daily production 

capacity, ADTP/d

Type of shower water used in 

decker

Evaporator nominal 

daily production 

capacity, gal/day of 

weak black liquor

Which pulp washer(s) are 

the source(s) of weak liquor 

for the evaporator set?

How many 

evaporator 

effects are 

there?

Nominal daily 

production 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

PI Equip detail 0900006480f7efd2.xls 33 of 66
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657

Knotter, screen, or decker 

nominal daily production 

capacity, ADTP/d

Type of shower water used in 

decker

Evaporator nominal 

daily production 

capacity, gal/day of 

weak black liquor

Which pulp washer(s) are 

the source(s) of weak liquor 

for the evaporator set?

How many 

evaporator 

effects are 

there?

Nominal daily 

production 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

PI Equip detail 0900006480f7efd2.xls 34 of 66
Field:

658

659

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811

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813

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815

816

817

818

819

820

821

822

823

824

825

826

827

828

829

830

831

832

Knotter, screen, or decker 

nominal daily production 

capacity, ADTP/d

Type of shower water used in 

decker

Evaporator nominal 

daily production 

capacity, gal/day of 

weak black liquor

Which pulp washer(s) are 

the source(s) of weak liquor 

for the evaporator set?

How many 

evaporator 

effects are 

there?

Nominal daily 

production 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

PI Equip detail 0900006480f7efd2.xls 35 of 66
Field:

833

834

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1000

Knotter, screen, or decker 

nominal daily production 

capacity, ADTP/d

Type of shower water used in 

decker

Evaporator nominal 

daily production 

capacity, gal/day of 

weak black liquor

Which pulp washer(s) are 

the source(s) of weak liquor 

for the evaporator set?

How many 

evaporator 

effects are 

there?

Nominal daily 

production 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

PI Equip detail 0900006480f7efd2.xls 36 of 66
OMB Control No:

Expiration Date:

You may find it helpful to use Excel's "freeze panes" or "split" features when viewing this spreadsheet. 

UK = Unknown. NA = Not Applicable

Instruction:

Survey reference:

Field:

Example entry: 123456789

10

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Complete 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 other process liquid streams that are stripped

Enter numeric value for 

total liquid flow to the 

stripper (design value)

Enter numeric value 

of the design 

parameter

Enter numeric value 

of the design 

parameter

Enter numeric 

value of the 

design parameter Select from menu or write in

Enter the methanol removal efficiency 

if it has been measured (e.g., enter 92 

for 92%). Use the average from 2009 

or target value.

If measured efficiency is not available, 

enter the design efficiency (e.g., enter 

"95-D" to reflect a design methanol 

removal efficiency of 95%) or "UK" for 

unknown.

Enter the total TRS removal 

efficiency if it has been measured 

(e.g., enter 92 for 92%). Use the 

average from 2009 or target value.

If measured efficiency is not 

available, enter the design 

efficiency (e.g., enter "95-D" to 

reflect a design TRS removal 

efficiency of 95%) or "UK" for 

unknown

Strippers

Type of stripper

Is the stripper 

integrated with 

the multiple 

effect 

evaporator 

system? List all liquid streams sent to the stripper

Design liquid flow to 

the stripper, gpm

Design steam 

application rate, 

lb/gal

Design liquid 

column feed 

temperature, F

For air stripper, 

design 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

PI Equip detail 0900006480f7efd2.xls 37 of 66
Field:

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Type of stripper

Is the stripper 

integrated with 

the multiple 

effect 

evaporator 

system? List all liquid streams sent to the stripper

Design liquid flow to 

the stripper, gpm

Design steam 

application rate, 

lb/gal

Design liquid 

column feed 

temperature, F

For air stripper, 

design air flow 

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

PI Equip detail 0900006480f7efd2.xls 38 of 66
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Type of stripper

Is the stripper 

integrated with 

the multiple 

effect 

evaporator 

system? List all liquid streams sent to the stripper

Design liquid flow to 

the stripper, gpm

Design steam 

application rate, 

lb/gal

Design liquid 

column feed 

temperature, F

For air stripper, 

design air flow 

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

PI Equip detail 0900006480f7efd2.xls 39 of 66
Field:

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Type of stripper

Is the stripper 

integrated with 

the multiple 

effect 

evaporator 

system? List all liquid streams sent to the stripper

Design liquid flow to 

the stripper, gpm

Design steam 

application rate, 

lb/gal

Design liquid 

column feed 

temperature, F

For air stripper, 

design air flow 

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

PI Equip detail 0900006480f7efd2.xls 40 of 66
Field:

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Type of stripper

Is the stripper 

integrated with 

the multiple 

effect 

evaporator 

system? List all liquid streams sent to the stripper

Design liquid flow to 

the stripper, gpm

Design steam 

application rate, 

lb/gal

Design liquid 

column feed 

temperature, F

For air stripper, 

design air flow 

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

PI Equip detail 0900006480f7efd2.xls 41 of 66
Field:

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Type of stripper

Is the stripper 

integrated with 

the multiple 

effect 

evaporator 

system? List all liquid streams sent to the stripper

Design liquid flow to 

the stripper, gpm

Design steam 

application rate, 

lb/gal

Design liquid 

column feed 

temperature, F

For air stripper, 

design air flow 

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

PI Equip detail 0900006480f7efd2.xls 42 of 66
OMB Control No:

Expiration Date:

You may find it helpful to use Excel's "freeze panes" or "split" features when viewing this spreadsheet. 

UK = Unknown. NA = Not Applicable

Instruction:

Survey reference:

Field:

Example entry: 123456789

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Complete the pulp and liquor storage questions for pulp storage 

tanks (e.g., high density storage), stock chests, strong and weak 

liquor storage tanks. 

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.

Select from menu or specify 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 reflected 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. 

Use the average from 

2009 or target value.

Pulp storage and Liquor storage Liquor storage ponds

Typical tank contents Tank capacity, gal 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 FR =fixed roof NA weak black liquor 26400 158400 2,300,000

PI Equip detail 0900006480f7efd2.xls 43 of 66
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Typical tank contents Tank capacity, gal 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

PI Equip detail 0900006480f7efd2.xls 44 of 66
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Typical tank contents Tank capacity, gal 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

PI Equip detail 0900006480f7efd2.xls 45 of 66
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Typical tank contents Tank capacity, gal 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

PI Equip detail 0900006480f7efd2.xls 46 of 66
Field:

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832

Typical tank contents Tank capacity, gal 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

PI Equip detail 0900006480f7efd2.xls 47 of 66
Field:

833

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Typical tank contents Tank capacity, gal 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

PI Equip detail 0900006480f7efd2.xls 48 of 66
OMB Control No:

Expiration Date:

You may find it helpful to use Excel's "freeze panes" or "split" features when viewing this spreadsheet. 

UK = Unknown. NA = Not Applicable

Instruction:

Survey reference:

Field:

Example entry:

1

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*You do not need to complete these columns for boilers if you included Boiler MACT survey codes.

Enter numeric value for lime 

kiln capacity in tons CaO/day.

Enter (repeat) value for each 

causticizing emission unit 

listed in this tab.

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 PI Controls tab. 

Select yes/no.

Answer this question with respect to each 

causticizing Emission Unit ID specified in 

column C.

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.

Complete for fuel-fired equipment such as 

such as boilers, thermal oxidizers controlling 

Part I emission sources, and direct-fired 

dryers.

Note that information for recovery furnaces 

(also known as "recovery boilers" or "black 

liquor boilers") and lime kilns is to be supplied 

under Part III of the pulp and paper survey 

(not Part I).

Enter numeric value in million Btu per hour 

(MMBtu/hr)

Complete for Emission Units such as boilers or thermal 

oxidizers that are used to incinerate NCG or SOG. 

Note that information for recovery furnaces (also known as 

"recovery boilers" or "black liquor boilers") and lime kilns is 

to be supplied under Part III of the pulp and paper survey 

(not Part I).

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 ...)

Complete for fuel-fired equipment such as 

boilers, thermal oxidizers controlling Part I 

emission sources, and direct-fired dryers. 

Enter the types of primary fuels fired 

(excluding NCG/SOGs). 

Note that information for recovery 

furnaces (also known as "recovery 

boilers" or "black liquor boilers") and lime 

kilns is to be supplied under Part III of the 

pulp and paper survey (not Part I).

Enter primary fuel type

Enter decimal percent (e.g., 1 = 100% or 

0.9 = 90%). Approximations based on 

the average from 2009 or a target value 

will suffice.

Optional. Enter the numeric higher 

heating value (HHV) for non-fossil fuels 

corresponding to the suggested units in 

next column.

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. Use 

Btu/gal for liquid fuels, 

MMBtu/ton (dry basis) for solid 

fuels, and 

Btu/MMscf for gaseous fuels.

Optional. If biomass is the 

primary fuel type, specify 

average moisture content as 

fired for biomass fuels only 

(decimal percent by weight, i.e., 

enter "0.2" for 20%) 

Causticizing equipment Fuel-fired equipment* Equipment incinerating NCG or SOG Primary fuels for fuel-fired equipment (except black or red liquor)*

Causticizing area nominal 

daily production capacity 

(use lime kiln tons CaO/day) 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 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 Primary fuel type

Approximate percent of annual heat 

input capacity (MMBtu/yr) supplied by 

primary fuel

Optional: Average HHV of non-fossil 

primary fuels

Optional: Primary fuel HHV 

units

Optional: Moisture content 

for biomass fuel (decimal % 

by weight)

20 STRIPPER, LVHC-1

435 STRIPPER hog fuel 0.95 12.6 MMBtu/ton 0.23

3942000 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.

PI Equip detail 0900006480f7efd2.xls 49 of 66
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Causticizing area nominal 

daily production capacity 

(use lime kiln tons CaO/day) 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 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 Primary fuel type

Approximate percent of annual heat 

input capacity (MMBtu/yr) supplied by 

primary fuel

Optional: Average HHV of non-fossil 

primary fuels

Optional: Primary fuel HHV 

units

Optional: Moisture content 

for biomass fuel (decimal % 

by weight)

PI Equip detail 0900006480f7efd2.xls 50 of 66
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Causticizing area nominal 

daily production capacity 

(use lime kiln tons CaO/day) 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 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 Primary fuel type

Approximate percent of annual heat 

input capacity (MMBtu/yr) supplied by 

primary fuel

Optional: Average HHV of non-fossil 

primary fuels

Optional: Primary fuel HHV 

units

Optional: Moisture content 

for biomass fuel (decimal % 

by weight)

PI Equip detail 0900006480f7efd2.xls 51 of 66
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Causticizing area nominal 

daily production capacity 

(use lime kiln tons CaO/day) 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 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 Primary fuel type

Approximate percent of annual heat 

input capacity (MMBtu/yr) supplied by 

primary fuel

Optional: Average HHV of non-fossil 

primary fuels

Optional: Primary fuel HHV 

units

Optional: Moisture content 

for biomass fuel (decimal % 

by weight)

PI Equip detail 0900006480f7efd2.xls 52 of 66
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Causticizing area nominal 

daily production capacity 

(use lime kiln tons CaO/day) 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 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 Primary fuel type

Approximate percent of annual heat 

input capacity (MMBtu/yr) supplied by 

primary fuel

Optional: Average HHV of non-fossil 

primary fuels

Optional: Primary fuel HHV 

units

Optional: Moisture content 

for biomass fuel (decimal % 

by weight)

PI Equip detail 0900006480f7efd2.xls 53 of 66
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Causticizing area nominal 

daily production capacity 

(use lime kiln tons CaO/day) 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 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 Primary fuel type

Approximate percent of annual heat 

input capacity (MMBtu/yr) supplied by 

primary fuel

Optional: Average HHV of non-fossil 

primary fuels

Optional: Primary fuel HHV 

units

Optional: Moisture content 

for biomass fuel (decimal % 

by weight)

PI Equip detail 0900006480f7efd2.xls 54 of 66
OMB Control No:

Expiration Date:

You may find it helpful to use Excel's "freeze panes" or "split" features when viewing this spreadsheet. 

UK = Unknown. NA = Not Applicable

Instruction:

Survey reference:

Field:

Example entry:

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*You do not need to complete these columns for boilers if you included Boiler MACT survey codes. Hidden columns: Additional supplemental fuel columns (for types 2-6) are hidden. Unhide and complete these columns if relevant.

Complete for fuel-fired equipment such as boilers, thermal 

oxidizers controlling Part I emission sources, and direct-fired 

dryers. Enter the types of supplemental or other fuels fired 

(excluding SOG or other NCGs). 

Note that information for recovery furnaces (also known as 

"recovery boilers" or "black liquor boilers") and lime kilns is to be 

supplied under Part III of the pulp and paper survey (not Part I).

Include secondary and additional fuels used routinely for multifuel fired equipment in these columns.

Enter decimal percent (e.g., 1 = 

100% or 0.9 = 90%). 

Approximations based on the 

average from 2009 or a target 

value will suffice.

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. Use 

Btu/gal for liquid fuels, 

MMBtu/ton (dry basis) for 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.

Supply startup/shutdown information for equipment (including collection systems or APCDs) that appear in the Emission Unit ID 

column (except thermal oxidizers). Enter startup/shutdown information for thermal oxidizers in the PI 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 

emission 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

Write 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 Emission Unit ID column.

Supplemental or other fuels for fuel-fired equipment* Emission Unit Startup and Shutdown

Supplemental fuel type 1

Approximate percent of annual 

heat input capacity (MMBtu/yr) 

supplied by supplemental fuel 1 Optional: Supplemental fuel type 1 HHV (if non-fossil) 

Optional: Supplemental fuel type 

1 HHV units

Conditions when supplemental fuel 

type 1 used 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)

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.

0.5 backup/alternate control When full pulp flow from the digester is obtained 1 continue routing emissions to LVHC-1 collection system and primary or backup control system Stop transfer of wood chips form the feed silo

Rule could require continued routing of emissions to LVHC-1 collection system and primary and/or 

backup control system during digester startup and shutdown.

0.5 backup/alternate control When full pulp flow from the digester is obtained 1 continue routing emissions to LVHC-1 collection system and primary or backup control system Stop transfer of wood chips form the feed silo

Rule could require continued routing of emissions to LVHC-1 collection system and primary and/or 

backup control system during digester startup and shutdown.

2 backup/alternate control

stripper steam application rate reaches target; and 

begin flow of process condensates from tank 1 stop routing process condensates to stripper before beginning 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.

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

natural gas 0.05 startup, backup 12 Operate WESP during boiler startup Steam pressure of 100 psig or greater achieved 12

emission unit and control device operates during emission unit startup (but not necessarily in compliance with 

all NSPS/NESHAP parameter limits) Stop charging hog fuel into boiler

18 backup/alternate control

Strong liquor flow of 600 gpm at evaporator exit (55% 

solids) 16 continue routing emissions to LVHC-1 collection system and primary or backup control system Steam flow to first effect reduced by 50%

Rule could require continued routing of emissions to LVHC-1 collection system and primary and/or 

backup control system during evaporator startup and shutdown.

12

emission unit and control device operates in compliance with NSPS and NESHAP 

parameter limits during emission unit startup Combustion temperature is reached 14 Temperature drops below 200F Cease flow of liquor through injection nozzles

PI Equip detail 0900006480f7efd2.xls 55 of 66
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Supplemental fuel type 1

Approximate percent of annual 

heat input capacity (MMBtu/yr) 

supplied by supplemental fuel 1 Optional: Supplemental fuel type 1 HHV (if non-fossil) 

Optional: Supplemental fuel type 

1 HHV units

Conditions when supplemental fuel 

type 1 used 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)

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.

PI Equip detail 0900006480f7efd2.xls 56 of 66
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482

Supplemental fuel type 1

Approximate percent of annual 

heat input capacity (MMBtu/yr) 

supplied by supplemental fuel 1 Optional: Supplemental fuel type 1 HHV (if non-fossil) 

Optional: Supplemental fuel type 

1 HHV units

Conditions when supplemental fuel 

type 1 used 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)

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.

PI Equip detail 0900006480f7efd2.xls 57 of 66
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Supplemental fuel type 1

Approximate percent of annual 

heat input capacity (MMBtu/yr) 

supplied by supplemental fuel 1 Optional: Supplemental fuel type 1 HHV (if non-fossil) 

Optional: Supplemental fuel type 

1 HHV units

Conditions when supplemental fuel 

type 1 used 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)

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.

PI Equip detail 0900006480f7efd2.xls 58 of 66
Field:

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Supplemental fuel type 1

Approximate percent of annual 

heat input capacity (MMBtu/yr) 

supplied by supplemental fuel 1 Optional: Supplemental fuel type 1 HHV (if non-fossil) 

Optional: Supplemental fuel type 

1 HHV units

Conditions when supplemental fuel 

type 1 used 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)

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.

PI Equip detail 0900006480f7efd2.xls 59 of 66
Field:

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Supplemental fuel type 1

Approximate percent of annual 

heat input capacity (MMBtu/yr) 

supplied by supplemental fuel 1 Optional: Supplemental fuel type 1 HHV (if non-fossil) 

Optional: Supplemental fuel type 

1 HHV units

Conditions when supplemental fuel 

type 1 used 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)

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.

PI Equip detail 0900006480f7efd2.xls 60 of 66
OMB Control No:

Expiration Date:

You may find it helpful to use Excel's "freeze panes" or "split" features when viewing this spreadsheet. 

UK = Unknown. NA = Not Applicable

Instruction:

Survey reference:

Field:

Example entry: 123456789

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Optional. Enter any comments you have on the data supplied.

Comments

PI Equip detail 0900006480f7efd2.xls 61 of 66
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Comments

PI Equip detail 0900006480f7efd2.xls 62 of 66
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Comments

PI Equip detail 0900006480f7efd2.xls 63 of 66
Field:

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Comments

PI Equip detail 0900006480f7efd2.xls 64 of 66
Field:

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Comments

PI Equip detail 0900006480f7efd2.xls 65 of 66
Field:

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Comments

PI Equip detail 0900006480f7efd2.xls 66 of 66
OMB Control No: 2060-0656

Expiration Date: 2/28/2014

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.

Pulp and Paper sector permit data You do not need to complete this tab for boilers.

Instruction:

Provide for all entries. 

This should match NEI 

Site ID used in Part II.

Provide for all entries. Use the Emission Unit ID in the PI 

Equip detail tab if the individual emission unit was listed 

there. If emission units are aggregated by a collection 

system then you may need to use the Collection system ID 

from the PI Equip detail tab.

OPTIONAL column useful for crosschecking permit data and when 

comparing permit to NEI. Select from menu or write in

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 selected. 

You do not have to provide 

every limit for pollutants with 

multiple limits in different units 

of measure.

See the survey instruction 

document for permit limit units 

of interest. Enter units for permit limit 

Survey reference: Equipment identification

Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

Example entry: 99999 EU30 EU30_1 PM - filterable 0.02 gr/dscf @ 8% O2

99999 EU30 EU30_1 Opacity 5 % opacity

1

2

3

4

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30

PI Permit limits 0900006480f7efd2.xls 1 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

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PI Permit limits 0900006480f7efd2.xls 2 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

87

88

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PI Permit limits 0900006480f7efd2.xls 3 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

143

144

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146

147

148

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152

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PI Permit limits 0900006480f7efd2.xls 4 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

199

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202

203

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PI Permit limits 0900006480f7efd2.xls 5 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

255

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PI Permit limits 0900006480f7efd2.xls 6 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

311

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331

332

333

334

335

336

337

338

339

340

341

342

343

344

345

346

347

348

349

350

351

352

353

354

355

356

357

358

359

360

361

362

363

364

365

366

PI Permit limits 0900006480f7efd2.xls 7 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

367

368

369

370

371

372

373

374

375

376

377

378

379

380

381

382

383

384

385

386

387

388

389

390

391

392

393

394

395

396

397

398

399

400

401

402

403

404

405

406

407

408

409

410

411

412

413

414

415

416

417

418

419

420

421

422

PI Permit limits 0900006480f7efd2.xls 8 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

423

424

425

426

427

428

429

430

431

432

433

434

435

436

437

438

439

440

441

442

443

444

445

446

447

448

449

450

451

452

453

454

455

456

457

458

459

460

461

462

463

464

465

466

467

468

469

470

471

472

473

474

475

476

477

478

PI Permit limits 0900006480f7efd2.xls 9 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

479

480

481

482

483

484

485

486

487

488

489

490

491

492

493

494

495

496

497

498

499

500

501

502

503

504

505

506

507

508

509

510

511

512

513

514

515

516

517

518

519

520

521

522

523

524

525

526

527

528

529

530

531

532

533

534

PI Permit limits 0900006480f7efd2.xls 10 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

535

536

537

538

539

540

541

542

543

544

545

546

547

548

549

550

551

552

553

554

555

556

557

558

559

560

561

562

563

564

565

566

567

568

569

570

571

572

573

574

575

576

577

578

579

580

581

582

583

584

585

586

587

588

589

590

PI Permit limits 0900006480f7efd2.xls 11 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

591

592

593

594

595

596

597

598

599

600

601

602

603

604

605

606

607

608

609

610

611

612

613

614

615

616

617

618

619

620

621

622

623

624

625

626

627

628

629

630

631

632

633

634

635

636

637

638

639

640

641

642

643

644

645

646

PI Permit limits 0900006480f7efd2.xls 12 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

647

648

649

650

651

652

653

654

655

656

657

658

659

660

661

662

663

664

665

666

667

668

669

670

671

672

673

674

675

676

677

678

679

680

681

682

683

684

685

686

687

688

689

690

691

692

693

694

695

696

697

698

699

700

701

702

PI Permit limits 0900006480f7efd2.xls 13 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

703

704

705

706

707

708

709

710

711

712

713

714

715

716

717

718

719

720

721

722

723

724

725

726

727

728

729

730

731

732

733

734

735

736

737

738

739

740

741

742

743

744

745

746

747

748

749

750

751

752

753

754

755

756

757

758

PI Permit limits 0900006480f7efd2.xls 14 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

759

760

761

762

763

764

765

766

767

768

769

770

771

772

773

774

775

776

777

778

779

780

781

782

783

784

785

786

787

788

789

790

791

792

793

794

795

796

797

798

799

800

801

802

803

804

805

806

807

808

809

810

811

812

813

814

PI Permit limits 0900006480f7efd2.xls 15 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

815

816

817

818

819

820

821

822

823

824

825

826

827

828

829

830

831

832

833

834

835

836

837

838

839

840

841

842

843

844

845

846

847

848

849

850

851

852

853

854

855

856

857

858

859

860

861

862

863

864

865

866

867

868

869

870

PI Permit limits 0900006480f7efd2.xls 16 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

871

872

873

874

875

876

877

878

879

880

881

882

883

884

885

886

887

888

889

890

891

892

893

894

895

896

897

898

899

900

901

902

903

904

905

906

907

908

909

910

911

912

913

914

915

916

917

918

919

920

921

922

923

924

925

926

PI Permit limits 0900006480f7efd2.xls 17 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

927

928

929

930

931

932

933

934

935

936

937

938

939

940

941

942

943

944

945

946

947

948

949

950

951

952

953

954

955

956

957

958

959

960

961

962

963

964

965

966

967

968

969

970

971

972

973

974

975

976

977

978

979

980

981

982

PI Permit limits 0900006480f7efd2.xls 18 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

983

984

985

986

987

988

989

990

991

992

993

994

995

996

997

998

999

1000

1001

1002

1003

1004

1005

1006

1007

1008

1009

1010

1011

1012

1013

1014

1015

1016

1017

1018

1019

1020

1021

1022

1023

1024

1025

1026

1027

1028

1029

1030

1031

1032

1033

1034

1035

1036

1037

1038

PI Permit limits 0900006480f7efd2.xls 19 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

1039

1040

1041

1042

1043

1044

1045

1046

1047

1048

1049

1050

1051

1052

1053

1054

1055

1056

1057

1058

1059

1060

1061

1062

1063

1064

1065

1066

1067

1068

1069

1070

1071

1072

1073

1074

1075

1076

1077

1078

1079

1080

1081

1082

1083

1084

1085

1086

1087

1088

1089

1090

1091

1092

1093

1094

PI Permit limits 0900006480f7efd2.xls 20 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

1095

1096

1097

1098

1099

1100

1101

1102

1103

1104

1105

1106

1107

1108

1109

1110

1111

1112

1113

1114

1115

1116

1117

1118

1119

1120

1121

1122

1123

1124

1125

1126

1127

1128

1129

1130

1131

1132

1133

1134

1135

1136

1137

1138

1139

1140

1141

1142

1143

1144

1145

1146

1147

1148

1149

1150

PI Permit limits 0900006480f7efd2.xls 21 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

1151

1152

1153

1154

1155

1156

1157

1158

1159

1160

1161

1162

1163

1164

1165

1166

1167

1168

1169

1170

1171

1172

1173

1174

1175

1176

1177

1178

1179

1180

1181

1182

1183

1184

1185

1186

1187

1188

1189

1190

1191

1192

1193

1194

1195

1196

1197

1198

1199

1200

1201

1202

1203

1204

1205

1206

PI Permit limits 0900006480f7efd2.xls 22 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

1207

1208

1209

1210

1211

1212

1213

1214

1215

1216

1217

1218

1219

1220

1221

1222

1223

1224

1225

1226

1227

1228

1229

1230

1231

1232

1233

1234

1235

1236

1237

1238

1239

1240

1241

1242

1243

1244

1245

1246

1247

1248

1249

1250

1251

1252

1253

1254

1255

1256

1257

1258

1259

1260

1261

1262

PI Permit limits 0900006480f7efd2.xls 23 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

1263

1264

1265

1266

1267

1268

1269

1270

1271

1272

1273

1274

1275

1276

1277

1278

1279

1280

1281

1282

1283

1284

1285

1286

1287

1288

1289

1290

1291

1292

1293

1294

1295

1296

1297

1298

1299

1300

1301

1302

1303

1304

1305

1306

1307

1308

1309

1310

1311

1312

1313

1314

1315

1316

1317

1318

PI Permit limits 0900006480f7efd2.xls 24 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

1319

1320

1321

1322

1323

1324

1325

1326

1327

1328

1329

1330

1331

1332

1333

1334

1335

1336

1337

1338

1339

1340

1341

1342

1343

1344

1345

1346

1347

1348

1349

1350

1351

1352

1353

1354

1355

1356

1357

1358

1359

1360

1361

1362

1363

1364

1365

1366

1367

1368

1369

1370

1371

1372

1373

1374

PI Permit limits 0900006480f7efd2.xls 25 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

1375

1376

1377

1378

1379

1380

1381

1382

1383

1384

1385

1386

1387

1388

1389

1390

1391

1392

1393

1394

1395

1396

1397

1398

1399

1400

1401

1402

1403

1404

1405

1406

1407

1408

1409

1410

1411

1412

1413

1414

1415

1416

1417

1418

1419

1420

1421

1422

1423

1424

1425

1426

1427

1428

1429

1430

PI Permit limits 0900006480f7efd2.xls 26 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

1431

1432

1433

1434

1435

1436

1437

1438

1439

1440

1441

1442

1443

1444

1445

1446

1447

1448

1449

1450

1451

1452

1453

1454

1455

1456

1457

1458

1459

1460

1461

1462

1463

1464

1465

1466

1467

1468

1469

1470

1471

1472

1473

1474

1475

1476

1477

1478

1479

1480

1481

1482

1483

1484

1485

1486

PI Permit limits 0900006480f7efd2.xls 27 of 84
Field: NEI Site ID Emission Unit ID or Collection System ID

Identifier used in permit (e.g., 

emission unit ID, stack ID, etc) - 

optional Pollutant

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)

1487

1488

1489

1490

1491

1492

1493

1494

1495

1496

1497

1498

1499

1500

PI Permit limits 0900006480f7efd2.xls 28 of 84
OMB Control No:

Expiration Date:

UK = Unknown. NA = Not Applicable

Pulp and Paper sector permit data

Instruction:

Survey reference:

Field:

Example entry:

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

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 selected. 

You do not have to provide 

every limit for pollutants with 

multiple limits in different units 

of measure.

See the survey instruction 

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 

selected. 

You do not have to provide every 

limit for pollutants with multiple 

limits in different units of 

measure.

See the survey instruction 

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 

selected. 

You do not have to provide every 

limit for pollutants with multiple 

limits in different units of 

measure.

See the survey instruction 

document for permit limit units of 

interest. Enter units for permit limit 

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

6-min avg 20 % opacity

Do not exceed 20% for more 

than three 6-min averages in a 

3-hour period determined by 

Method 9

PI Permit limits 0900006480f7efd2.xls 29 of 84
Field:

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

46

47

48

49

50

51

52

53

54

55

56

57

58

59

60

61

62

63

64

65

66

67

68

69

70

71

72

73

74

75

76

77

78

79

80

81

82

83

84

85

86

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 30 of 84
Field:

87

88

89

90

91

92

93

94

95

96

97

98

99

100

101

102

103

104

105

106

107

108

109

110

111

112

113

114

115

116

117

118

119

120

121

122

123

124

125

126

127

128

129

130

131

132

133

134

135

136

137

138

139

140

141

142

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 31 of 84
Field:

143

144

145

146

147

148

149

150

151

152

153

154

155

156

157

158

159

160

161

162

163

164

165

166

167

168

169

170

171

172

173

174

175

176

177

178

179

180

181

182

183

184

185

186

187

188

189

190

191

192

193

194

195

196

197

198

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 32 of 84
Field:

199

200

201

202

203

204

205

206

207

208

209

210

211

212

213

214

215

216

217

218

219

220

221

222

223

224

225

226

227

228

229

230

231

232

233

234

235

236

237

238

239

240

241

242

243

244

245

246

247

248

249

250

251

252

253

254

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 33 of 84
Field:

255

256

257

258

259

260

261

262

263

264

265

266

267

268

269

270

271

272

273

274

275

276

277

278

279

280

281

282

283

284

285

286

287

288

289

290

291

292

293

294

295

296

297

298

299

300

301

302

303

304

305

306

307

308

309

310

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 34 of 84
Field:

311

312

313

314

315

316

317

318

319

320

321

322

323

324

325

326

327

328

329

330

331

332

333

334

335

336

337

338

339

340

341

342

343

344

345

346

347

348

349

350

351

352

353

354

355

356

357

358

359

360

361

362

363

364

365

366

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 35 of 84
Field:

367

368

369

370

371

372

373

374

375

376

377

378

379

380

381

382

383

384

385

386

387

388

389

390

391

392

393

394

395

396

397

398

399

400

401

402

403

404

405

406

407

408

409

410

411

412

413

414

415

416

417

418

419

420

421

422

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 36 of 84
Field:

423

424

425

426

427

428

429

430

431

432

433

434

435

436

437

438

439

440

441

442

443

444

445

446

447

448

449

450

451

452

453

454

455

456

457

458

459

460

461

462

463

464

465

466

467

468

469

470

471

472

473

474

475

476

477

478

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 37 of 84
Field:

479

480

481

482

483

484

485

486

487

488

489

490

491

492

493

494

495

496

497

498

499

500

501

502

503

504

505

506

507

508

509

510

511

512

513

514

515

516

517

518

519

520

521

522

523

524

525

526

527

528

529

530

531

532

533

534

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 38 of 84
Field:

535

536

537

538

539

540

541

542

543

544

545

546

547

548

549

550

551

552

553

554

555

556

557

558

559

560

561

562

563

564

565

566

567

568

569

570

571

572

573

574

575

576

577

578

579

580

581

582

583

584

585

586

587

588

589

590

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 39 of 84
Field:

591

592

593

594

595

596

597

598

599

600

601

602

603

604

605

606

607

608

609

610

611

612

613

614

615

616

617

618

619

620

621

622

623

624

625

626

627

628

629

630

631

632

633

634

635

636

637

638

639

640

641

642

643

644

645

646

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 40 of 84
Field:

647

648

649

650

651

652

653

654

655

656

657

658

659

660

661

662

663

664

665

666

667

668

669

670

671

672

673

674

675

676

677

678

679

680

681

682

683

684

685

686

687

688

689

690

691

692

693

694

695

696

697

698

699

700

701

702

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 41 of 84
Field:

703

704

705

706

707

708

709

710

711

712

713

714

715

716

717

718

719

720

721

722

723

724

725

726

727

728

729

730

731

732

733

734

735

736

737

738

739

740

741

742

743

744

745

746

747

748

749

750

751

752

753

754

755

756

757

758

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 42 of 84
Field:

759

760

761

762

763

764

765

766

767

768

769

770

771

772

773

774

775

776

777

778

779

780

781

782

783

784

785

786

787

788

789

790

791

792

793

794

795

796

797

798

799

800

801

802

803

804

805

806

807

808

809

810

811

812

813

814

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 43 of 84
Field:

815

816

817

818

819

820

821

822

823

824

825

826

827

828

829

830

831

832

833

834

835

836

837

838

839

840

841

842

843

844

845

846

847

848

849

850

851

852

853

854

855

856

857

858

859

860

861

862

863

864

865

866

867

868

869

870

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 44 of 84
Field:

871

872

873

874

875

876

877

878

879

880

881

882

883

884

885

886

887

888

889

890

891

892

893

894

895

896

897

898

899

900

901

902

903

904

905

906

907

908

909

910

911

912

913

914

915

916

917

918

919

920

921

922

923

924

925

926

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 45 of 84
Field:

927

928

929

930

931

932

933

934

935

936

937

938

939

940

941

942

943

944

945

946

947

948

949

950

951

952

953

954

955

956

957

958

959

960

961

962

963

964

965

966

967

968

969

970

971

972

973

974

975

976

977

978

979

980

981

982

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 46 of 84
Field:

983

984

985

986

987

988

989

990

991

992

993

994

995

996

997

998

999

1000

1001

1002

1003

1004

1005

1006

1007

1008

1009

1010

1011

1012

1013

1014

1015

1016

1017

1018

1019

1020

1021

1022

1023

1024

1025

1026

1027

1028

1029

1030

1031

1032

1033

1034

1035

1036

1037

1038

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 47 of 84
Field:

1039

1040

1041

1042

1043

1044

1045

1046

1047

1048

1049

1050

1051

1052

1053

1054

1055

1056

1057

1058

1059

1060

1061

1062

1063

1064

1065

1066

1067

1068

1069

1070

1071

1072

1073

1074

1075

1076

1077

1078

1079

1080

1081

1082

1083

1084

1085

1086

1087

1088

1089

1090

1091

1092

1093

1094

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 48 of 84
Field:

1095

1096

1097

1098

1099

1100

1101

1102

1103

1104

1105

1106

1107

1108

1109

1110

1111

1112

1113

1114

1115

1116

1117

1118

1119

1120

1121

1122

1123

1124

1125

1126

1127

1128

1129

1130

1131

1132

1133

1134

1135

1136

1137

1138

1139

1140

1141

1142

1143

1144

1145

1146

1147

1148

1149

1150

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 49 of 84
Field:

1151

1152

1153

1154

1155

1156

1157

1158

1159

1160

1161

1162

1163

1164

1165

1166

1167

1168

1169

1170

1171

1172

1173

1174

1175

1176

1177

1178

1179

1180

1181

1182

1183

1184

1185

1186

1187

1188

1189

1190

1191

1192

1193

1194

1195

1196

1197

1198

1199

1200

1201

1202

1203

1204

1205

1206

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 50 of 84
Field:

1207

1208

1209

1210

1211

1212

1213

1214

1215

1216

1217

1218

1219

1220

1221

1222

1223

1224

1225

1226

1227

1228

1229

1230

1231

1232

1233

1234

1235

1236

1237

1238

1239

1240

1241

1242

1243

1244

1245

1246

1247

1248

1249

1250

1251

1252

1253

1254

1255

1256

1257

1258

1259

1260

1261

1262

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 51 of 84
Field:

1263

1264

1265

1266

1267

1268

1269

1270

1271

1272

1273

1274

1275

1276

1277

1278

1279

1280

1281

1282

1283

1284

1285

1286

1287

1288

1289

1290

1291

1292

1293

1294

1295

1296

1297

1298

1299

1300

1301

1302

1303

1304

1305

1306

1307

1308

1309

1310

1311

1312

1313

1314

1315

1316

1317

1318

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 52 of 84
Field:

1319

1320

1321

1322

1323

1324

1325

1326

1327

1328

1329

1330

1331

1332

1333

1334

1335

1336

1337

1338

1339

1340

1341

1342

1343

1344

1345

1346

1347

1348

1349

1350

1351

1352

1353

1354

1355

1356

1357

1358

1359

1360

1361

1362

1363

1364

1365

1366

1367

1368

1369

1370

1371

1372

1373

1374

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 53 of 84
Field:

1375

1376

1377

1378

1379

1380

1381

1382

1383

1384

1385

1386

1387

1388

1389

1390

1391

1392

1393

1394

1395

1396

1397

1398

1399

1400

1401

1402

1403

1404

1405

1406

1407

1408

1409

1410

1411

1412

1413

1414

1415

1416

1417

1418

1419

1420

1421

1422

1423

1424

1425

1426

1427

1428

1429

1430

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 54 of 84
Field:

1431

1432

1433

1434

1435

1436

1437

1438

1439

1440

1441

1442

1443

1444

1445

1446

1447

1448

1449

1450

1451

1452

1453

1454

1455

1456

1457

1458

1459

1460

1461

1462

1463

1464

1465

1466

1467

1468

1469

1470

1471

1472

1473

1474

1475

1476

1477

1478

1479

1480

1481

1482

1483

1484

1485

1486

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 55 of 84
Field:

1487

1488

1489

1490

1491

1492

1493

1494

1495

1496

1497

1498

1499

1500

Averaging time for permit 

limit 1 (if applicable) 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) Numeric permit limit 4

Units for permit limit 4 

(including any applicable 

%O2 or %CO2 correction 

factors)

PI Permit limits 0900006480f7efd2.xls 56 of 84
OMB Control No:

Expiration Date:

UK = Unknown. NA = Not Applicable

Pulp and Paper sector permit data

Instruction:

Survey reference:

Field:

Example entry:

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

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 

selected. 

You do not have to provide every 

limit for pollutants with multiple 

limits in different units of measure.

See the survey instruction 

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. Optional. Enter any comments you have on the data supplied.

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) Comments

PI Permit limits 0900006480f7efd2.xls 57 of 84
Field:

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

46

47

48

49

50

51

52

53

54

55

56

57

58

59

60

61

62

63

64

65

66

67

68

69

70

71

72

73

74

75

76

77

78

79

80

81

82

83

84

85

86

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) Comments

PI Permit limits 0900006480f7efd2.xls 58 of 84
Field:

87

88

89

90

91

92

93

94

95

96

97

98

99

100

101

102

103

104

105

106

107

108

109

110

111

112

113

114

115

116

117

118

119

120

121

122

123

124

125

126

127

128

129

130

131

132

133

134

135

136

137

138

139

140

141

142

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) Comments

PI Permit limits 0900006480f7efd2.xls 59 of 84
Field:

143

144

145

146

147

148

149

150

151

152

153

154

155

156

157

158

159

160

161

162

163

164

165

166

167

168

169

170

171

172

173

174

175

176

177

178

179

180

181

182

183

184

185

186

187

188

189

190

191

192

193

194

195

196

197

198

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) Comments

PI Permit limits 0900006480f7efd2.xls 60 of 84
Field:

199

200

201

202

203

204

205

206

207

208

209

210

211

212

213

214

215

216

217

218

219

220

221

222

223

224

225

226

227

228

229

230

231

232

233

234

235

236

237

238

239

240

241

242

243

244

245

246

247

248

249

250

251

252

253

254

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) Comments

PI Permit limits 0900006480f7efd2.xls 61 of 84
Field:

255

256

257

258

259

260

261

262

263

264

265

266

267

268

269

270

271

272

273

274

275

276

277

278

279

280

281

282

283

284

285

286

287

288

289

290

291

292

293

294

295

296

297

298

299

300

301

302

303

304

305

306

307

308

309

310

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) Comments

PI Permit limits 0900006480f7efd2.xls 62 of 84
Field:

311

312

313

314

315

316

317

318

319

320

321

322

323

324

325

326

327

328

329

330

331

332

333

334

335

336

337

338

339

340

341

342

343

344

345

346

347

348

349

350

351

352

353

354

355

356

357

358

359

360

361

362

363

364

365

366

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) Comments

PI Permit limits 0900006480f7efd2.xls 63 of 84
Field:

367

368

369

370

371

372

373

374

375

376

377

378

379

380

381

382

383

384

385

386

387

388

389

390

391

392

393

394

395

396

397

398

399

400

401

402

403

404

405

406

407

408

409

410

411

412

413

414

415

416

417

418

419

420

421

422

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) Comments

PI Permit limits 0900006480f7efd2.xls 64 of 84
Field:

423

424

425

426

427

428

429

430

431

432

433

434

435

436

437

438

439

440

441

442

443

444

445

446

447

448

449

450

451

452

453

454

455

456

457

458

459

460

461

462

463

464

465

466

467

468

469

470

471

472

473

474

475

476

477

478

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) Comments

PI Permit limits 0900006480f7efd2.xls 65 of 84
Field:

479

480

481

482

483

484

485

486

487

488

489

490

491

492

493

494

495

496

497

498

499

500

501

502

503

504

505

506

507

508

509

510

511

512

513

514

515

516

517

518

519

520

521

522

523

524

525

526

527

528

529

530

531

532

533

534

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) Comments

PI Permit limits 0900006480f7efd2.xls 66 of 84
Field:

535

536

537

538

539

540

541

542

543

544

545

546

547

548

549

550

551

552

553

554

555

556

557

558

559

560

561

562

563

564

565

566

567

568

569

570

571

572

573

574

575

576

577

578

579

580

581

582

583

584

585

586

587

588

589

590

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) Comments

PI Permit limits 0900006480f7efd2.xls 67 of 84
Field:

591

592

593

594

595

596

597

598

599

600

601

602

603

604

605

606

607

608

609

610

611

612

613

614

615

616

617

618

619

620

621

622

623

624

625

626

627

628

629

630

631

632

633

634

635

636

637

638

639

640

641

642

643

644

645

646

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) Comments

PI Permit limits 0900006480f7efd2.xls 68 of 84
Field:

647

648

649

650

651

652

653

654

655

656

657

658

659

660

661

662

663

664

665

666

667

668

669

670

671

672

673

674

675

676

677

678

679

680

681

682

683

684

685

686

687

688

689

690

691

692

693

694

695

696

697

698

699

700

701

702

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) Comments

PI Permit limits 0900006480f7efd2.xls 69 of 84
Field:

703

704

705

706

707

708

709

710

711

712

713

714

715

716

717

718

719

720

721

722

723

724

725

726

727

728

729

730

731

732

733

734

735

736

737

738

739

740

741

742

743

744

745

746

747

748

749

750

751

752

753

754

755

756

757

758

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) Comments

PI Permit limits 0900006480f7efd2.xls 70 of 84
Field:

759

760

761

762

763

764

765

766

767

768

769

770

771

772

773

774

775

776

777

778

779

780

781

782

783

784

785

786

787

788

789

790

791

792

793

794

795

796

797

798

799

800

801

802

803

804

805

806

807

808

809

810

811

812

813

814

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) Comments

PI Permit limits 0900006480f7efd2.xls 71 of 84
Field:

815

816

817

818

819

820

821

822

823

824

825

826

827

828

829

830

831

832

833

834

835

836

837

838

839

840

841

842

843

844

845

846

847

848

849

850

851

852

853

854

855

856

857

858

859

860

861

862

863

864

865

866

867

868

869

870

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) Comments

PI Permit limits 0900006480f7efd2.xls 72 of 84
Field:

871

872

873

874

875

876

877

878

879

880

881

882

883

884

885

886

887

888

889

890

891

892

893

894

895

896

897

898

899

900

901

902

903

904

905

906

907

908

909

910

911

912

913

914

915

916

917

918

919

920

921

922

923

924

925

926

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) Comments

PI Permit limits 0900006480f7efd2.xls 73 of 84
Field:

927

928

929

930

931

932

933

934

935

936

937

938

939

940

941

942

943

944

945

946

947

948

949

950

951

952

953

954

955

956

957

958

959

960

961

962

963

964

965

966

967

968

969

970

971

972

973

974

975

976

977

978

979

980

981

982

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) Comments

PI Permit limits 0900006480f7efd2.xls 74 of 84
Field:

983

984

985

986

987

988

989

990

991

992

993

994

995

996

997

998

999

1000

1001

1002

1003

1004

1005

1006

1007

1008

1009

1010

1011

1012

1013

1014

1015

1016

1017

1018

1019

1020

1021

1022

1023

1024

1025

1026

1027

1028

1029

1030

1031

1032

1033

1034

1035

1036

1037

1038

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) Comments

PI Permit limits 0900006480f7efd2.xls 75 of 84
Field:

1039

1040

1041

1042

1043

1044

1045

1046

1047

1048

1049

1050

1051

1052

1053

1054

1055

1056

1057

1058

1059

1060

1061

1062

1063

1064

1065

1066

1067

1068

1069

1070

1071

1072

1073

1074

1075

1076

1077

1078

1079

1080

1081

1082

1083

1084

1085

1086

1087

1088

1089

1090

1091

1092

1093

1094

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) Comments

PI Permit limits 0900006480f7efd2.xls 76 of 84
Field:

1095

1096

1097

1098

1099

1100

1101

1102

1103

1104

1105

1106

1107

1108

1109

1110

1111

1112

1113

1114

1115

1116

1117

1118

1119

1120

1121

1122

1123

1124

1125

1126

1127

1128

1129

1130

1131

1132

1133

1134

1135

1136

1137

1138

1139

1140

1141

1142

1143

1144

1145

1146

1147

1148

1149

1150

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) Comments

PI Permit limits 0900006480f7efd2.xls 77 of 84
Field:

1151

1152

1153

1154

1155

1156

1157

1158

1159

1160

1161

1162

1163

1164

1165

1166

1167

1168

1169

1170

1171

1172

1173

1174

1175

1176

1177

1178

1179

1180

1181

1182

1183

1184

1185

1186

1187

1188

1189

1190

1191

1192

1193

1194

1195

1196

1197

1198

1199

1200

1201

1202

1203

1204

1205

1206

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) Comments

PI Permit limits 0900006480f7efd2.xls 78 of 84
Field:

1207

1208

1209

1210

1211

1212

1213

1214

1215

1216

1217

1218

1219

1220

1221

1222

1223

1224

1225

1226

1227

1228

1229

1230

1231

1232

1233

1234

1235

1236

1237

1238

1239

1240

1241

1242

1243

1244

1245

1246

1247

1248

1249

1250

1251

1252

1253

1254

1255

1256

1257

1258

1259

1260

1261

1262

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) Comments

PI Permit limits 0900006480f7efd2.xls 79 of 84
Field:

1263

1264

1265

1266

1267

1268

1269

1270

1271

1272

1273

1274

1275

1276

1277

1278

1279

1280

1281

1282

1283

1284

1285

1286

1287

1288

1289

1290

1291

1292

1293

1294

1295

1296

1297

1298

1299

1300

1301

1302

1303

1304

1305

1306

1307

1308

1309

1310

1311

1312

1313

1314

1315

1316

1317

1318

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) Comments

PI Permit limits 0900006480f7efd2.xls 80 of 84
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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) Comments

PI Permit limits 0900006480f7efd2.xls 81 of 84
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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) Comments

PI Permit limits 0900006480f7efd2.xls 82 of 84
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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) Comments

PI Permit limits 0900006480f7efd2.xls 83 of 84
Field:

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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) Comments

PI Permit limits 0900006480f7efd2.xls 84 of 84
OMB Control No: 2060-0656 Did any of the responses (individual cells) you entered in this tab contain CBI? 

Expiration Date: 2/28/2014 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.

Complete this table for add-on air pollution controls. Questions regarding combustion controls and process changes are included elsewhere in other survey tabs.

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.

You do not need to complete this tab for boiler air pollution control devices.

Instruction:

Provide for all entries. This 

should match NEI Site ID 

used in Part II.

Enter APCD_ID 

matching the PI 

Equip detail tab

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 of 

the upgrade as "XXXXupgrade."

Enter the typical 

pressure drop 

across the 

control device 

in inches of 

water

Enter control efficiencies, if 

known (e.g., enter 99 for 

99%).

"Actual" control efficiency is 

a measured value obtained 

through inlet/outlet 

emissions testing. 

Leave blank if not known or 

not applicable.

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.

Complete for thermal oxidizers or 

incinerators used to control Part I 

emission sources.

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

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. Use the 

average from 2009 

or a target value.

Survey reference: APCD identification P-drop Control efficiency Thermal oxidizers/incinerators Sorbent injection

Field: NEI Site ID APCD_ID

Emission Unit ID(s) or 

Collection system ID(s) 

controlled Type of control device

APCD 

manufacturer (if 

known) Year installed (XXXX)

Pressure drop, 

in. H2O

Actual PM control 

efficiency (if known), %

Actual TRS control 

efficiency (if known), %

Actual HCl control 

efficiency (if known), %

Actual SO2 control 

efficiency (if known), %

Actual HAP control 

efficiency (if known), % Specify HAP 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? Sorbent type

List pollutants the sorbent 

injection was installed to 

control

Sorbent injection 

rate, lb/hr

Example entry: 99999 ANYCONTROL ANYUNIT ANYTYPE UK pre-1990 4 98 90 Methanol activated carbon Hg 100

99999 SCRB2 LK1, LVHC1 Scrubber Ducon 1985 6 95 92 82 50 Formaldehyde, Methanol

99999 TO

STRIPPER (backup); LVHC1 

(backup) Thermal oxidizer/incinerator Coen 1999 2 98 Single-stage combustion chamber NA 1300 1.8 no NA

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PI Controls 0900006480f7efd2.xls 1 of 4
OMB Control No:

Expiration Date:

Complete this table for add-on air pollution controls

UK = Unknown. NA = Not Applicable

You do not need to complete this tab for boiler air pollution control devices.

Instruction:

Survey reference:

Field:

Example entry:

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Complete for fabric filters (baghouses) used on 

significant pulp and paper processing 

equipment (e.g., combustion units). You do not 

need to provide these details for baghouses 

used solely for dust collection from 

wood/material handling operations.

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 

baghouse is not 

separated by different 

compartments.

Enter the design airto-cloth ratio (gas 

flow divided by the 

filter bag material 

area)

Complete 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 design 

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. Use the average 

from 2009 or a target value.

Complete 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 value 

for the scrubber design 

liquid-to-gas ratio (L/G) in 

gallons of liquid per 1000 

acfm of gas. Use the 

average from 2009 or a 

target value.

Enter numeric 

value for the target 

pH. Use the 

average from 2009 

or a target value.

Enter typical 

gallons per 

minute of 

scrubbing fluid 

(e.g., water) 

makeup added to 

the system. Use 

the average from 

2009 or a target 

value.

Select yes/no for scrubbers that 

control chemical recovery furnaces or 

Semichemical liquor combustion 

units. 

Leave blank for other scrubbers. 

Complete the 

scrubber 

questions and 

complete the 

additional 

questions 

below related 

to the packing 

material 

Enter 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 PI Equip detail tab). Select yes/no

Enter numeric 

value in gallons 

per minute 

(gpm). Use the 

average from 

2009 or a target 

value.

Enter the decimal percentage of 

recirculation gpm flow (e.g., 0.1 

for 10%) that is not recalculated 

back to the control device (i.e., 

the blowdown percentage). Use 

the average from 2009 or a 

target value.

Enter end use or disposal method for the 

blowdown

Fabric filters ESPs WESPs Scrubber Packed bed scrubbers/absorbers Water source and usage

Filter material and added coatings Bag cleaning method

Typical bag life 

(months)

Number of 

compartments

Air-to-cloth ratio 

(acfm/ft2)

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

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 recovery furnaces/combustion 

units: Does scrubber also serve as 

a direct contact evaporator?

Type of 

packing 

material

Packing 

material 

depth, ft

Scrubber/absorber 

cross-sectional area, 

ft2 Water source Is water recirculated?

Water 

recirculation 

rate, gpm Wastewater (blowdown) %

Wastewater (blowdown) reuse or disposal 

method

Polyester Shake 15 1 7 8 4 466 No No 275 8 130 No plastic packing 3 19.6 treated wastewater Yes 200 0.1 Treated in onsite wastewater treatment plant

Caustic 6 10 60 surface water and water from recirculation pond Yes 350 0.35 Treated in onsite wastewater treatment plant

PI Controls 0900006480f7efd2.xls 2 of 4
OMB Control No:

Expiration Date:

Complete this table for add-on air pollution controls

UK = Unknown. NA = Not Applicable

You do not need to complete this tab for boiler air pollution control devices.

Instruction:

Survey reference:

Field:

Example entry:

1

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Complete the solid material questions for 

control devices that collect or generate 

solid material to be handled or disposed. 

Do not include baghouses or cyclones 

used solely for wood/material handling 

operations.

Provide information for any solid material 

collected by the APCD (e.g., PM, sorbent, 

etc)

Explain how the solid material is 

used or disposed. Explain 

where the material re-enters the 

process if it is reused.

Enter the amount of solid 

material disposed annually 

(if known) in cubic yards 

per year (cu yd/yr). Use the 

average from 2009 or a 

target value.

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. 

Explain how the solid material is 

used or disposed. Explain 

where the material re-enters the 

process if it is reused.

Enter the amount of 

material that must be 

disposed in cubic yards (if 

known). Use the average 

from 2009 or a target value.

Select from list or write in.

List multiple parameters for the same 

control device separated by commas (as 

shown in the example below).

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

Supply 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.

Solid material handling and disposal Parameter monitoring Control Device Startup and Shutdown

Type of material collected

End use/method of disposal for 

solid material collected

Solid material disposed (if 

known), cu yd/yr 

Identify any other solid waste 

associated with the APCD

Frequency of material 

replacement/disposal

End use/method of disposal for 

solid material collected

Amount of material to be 

disposed (if known), cu yd

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) 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

carbon sorbent laden with PM landfill onsite 410 degraded packing material 5 yr landfill offsite 0.5 liquid flow, voltage carbon injection rate (100 lb/hr) 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

pressure drop, liquid flow rate 34500 2007 3

Control device cannot function as designed unless an air flow rate of 29,000 acfm from the emission 

unit is achieved. pressure drop

combustion chamber temperature 22000 1999 4 temperature set point

PI Controls 0900006480f7efd2.xls 3 of 4
OMB Control No:

Expiration Date:

Complete this table for add-on air pollution controls

UK = Unknown. NA = Not Applicable

You do not need to complete this tab for boiler air pollution control devices.

Instruction:

Survey reference:

Field:

Example entry:

1

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Write in response (if any).

Write 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. Select 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. Optional. Enter any comments you have on the data supplied.

Measures employed to reduce air emissions 

during control device startup (if any)

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

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. Comments

Ensure water is recirculated through control device 

throughout 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

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)

meet liquid flow parameter limit

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.

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)

bring TO temperature to 1400F before routing NCG 

or SOG to the TO 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 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)

PI Controls 0900006480f7efd2.xls 4 of 4
OMB Control No: 2060-0656 Did any of the responses (individual cells) you entered in this tab contain CBI? 

Expiration Date: 2/28/2014 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 this table for pulp produced onsite. Do not include pulp purchases in 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.

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.

Provide data for the 2009 operating year.

Instruction:

Provide for all entries. 

This should match NEI 

Site ID used in Part II.

Select from menu. Include additional rows in 

this table if your mill has more than one pulping 

line/process (e.g., two kraft lines or one kraft 

line and one TMP line).

Enter numeric 

value for 2009

Enter numeric value in air dried 

tons of pulp per day (ADTP/d). 

This value corresponds to pulp 

production exiting the pulping line 

and prior to any 

bleaching/brightening.

Enter decimal percent 

for utilization (e.g., 0.7 

for 70% of capacity 

utilized)

Enter the typical decimal percent 

for utilization (e.g., 0.7 for 70% of 

capacity utilized) for the past 5 

years. One way to determine the 

5-year utilization would be to 

average the utilization 

percentages for 2005, 2006, 

2007, 2008, and 2009.

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 

unbleached pulp it produces from 

virgin wood fiber? 

Determine the approximate 

decimal percentage requested 

based on annual unbleached pulp 

capacity (ADTP/yr).

This column represents the 

amount of unbleached pulp that 

typically goes to an onsite 

bleaching/brightening line.

This column represents the amount of 

unbleached pulp that is sold (or 

transferred to another mill within the 

same company) as unbleached market 

pulp. Decimal percent.

This column represents the 

amount of unbleached pulp 

that is used onsite to 

manufacture unbleached 

paper/paperboard. Decimal 

percent.

Survey reference: Pulping line identification Virgin wood fiber sources used for chemical or mechanical wood pulps

Field: NEI Site ID Pulping processes Operating hr/yr

Unbleached pulp nominal daily 

production capacity ADTP/d in 

2009

Unbleached pulp 

nominal capacity 

utilization percentage 

in 2009

5-year average (2005-2009) 

unbleached pulp capacity 

utilization percentage

Chips produced 

onsite

Chips produced 

offsite Sawmill residues

Virgin SW 

decimal% Virgin HW decimal%

Approximate percentage of 

virgin wood pulp that is 

bleached (or brightened) 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)

Example entry: 99999 kraft 8500 950 0.8 0.95 yes yes no 0.2 0.8 NA 0.25 0.75 1

1 0

2 0

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Pulp prod 0900006480f7efd2.xls 1 of 3
OMB Control No:

Expiration Date:

Use this table for pulp produced onsite. Do not include pulp purchases in 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.

UK = Unknown. NA = Not Applicable

Provide data for the 2009 operating year.

Instruction:

Survey reference:

Field:

Example entry:

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Select yes/no

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? 

Determine the approximate decimal 

percentage requested based on annual 

unbleached pulp capacity (ADTP/yr).

This column represents the amount of 

unbleached pulp that typically goes to an 

onsite bleaching/brightening line.

This column represents the amount of 

unbleached pulp that is sold (or 

transferred to another mill within the 

same company) as unbleached 

market pulp. Decimal percent.

This column represents the 

amount of unbleached pulp that is 

used onsite to manufacture 

unbleached paper/paperboard. 

Decimal percent.

Non-wood pulping material.

Select from list

How does the mill use the nonwood pulp it produces? 

Determine the approximate 

decimal percentage requested 

based on annual unbleached 

pulp capacity (ADTP/yr).

This column represents the 

amount of unbleached pulp that 

typically goes to an onsite 

bleaching/brightening line.

This column represents the 

amount of unbleached pulp 

that is sold (or transferred to 

another mill within the same 

company) as unbleached 

market pulp.

This column represents the amount 

of unbleached pulp that is used 

onsite to manufacture unbleached 

paper/paperboard.

Mechanical wood pulps Recycled/secondary fiber pulps Non-wood pulps

For TMP or pressurized 

groundwood systems, is a 

heat recovery system 

used?

Mixed paper 

decimal%

High grade deinked 

decimal% ONP decimal% OCC decimal%

Pulp substitute 

decimal%

Approximate percentage of secondary 

fiber pulp that is bleached (or 

brightened) onsite

Approximate percentage of 

secondary fiber pulp sold as 

unbleached market pulp

Approximate percentage of 

secondary fiber pulp used 

onsite to manufacture 

unbleached paper/paperboard?

Check 

(=1) Non-wood material

Approximate percentage of 

nonwood pulp that is 

bleached (or brightened) 

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 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0

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0 0

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Pulp prod 0900006480f7efd2.xls 2 of 3
OMB Control No:

Expiration Date:

Use this table for pulp produced onsite. Do not include pulp purchases in 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.

UK = Unknown. NA = Not Applicable

Provide data for the 2009 operating year.

Instruction:

Survey reference:

Field:

Example entry: 123456789

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Optional. Enter any comments you have on the data 

supplied.

Comments

Pulp prod 0900006480f7efd2.xls 3 of 3
OMB Control No: 2060-0656 Did any of the responses (individual cells) you entered in this tab contain CBI? 

Expiration Date: 2/28/2014 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.

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.

Each pulp mill producing turpentine and/or tall oil should have one row in this table.

Instruction:

Provide for all entries. This 

should match NEI Site ID used 

in Part II.

Enter numeric value based on 

nominal production capacity

Enter numeric value based on 

nominal production capacity Insert Emission Unit IDs separated by commas

Enter numeric value based on nominal 

production capacity Select from menu.

Survey reference: Turpentine Tall oil

Field: NEI Site ID Turpentine production, hr/yr Turpentine production, gal/yr

Digesters supplying turpentine production (insert 

Emission Unit IDs) Tall oil production, ton tall oil/yr

Evaporators supplying tall oil production (insert 

Emission Unit IDs)

Is tall oil acidulation reactor batch or 

continuous? 

Example entry: 99999 8500 700 DIG-1, DIG-2 220000 EVAP-1, EVAP-2 continuous

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Byproducts 0900006480f7efd2.xls 1 of 2
OMB Control No:

Expiration Date:

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.

Each pulp mill producing turpentine and/or tall oil should have one row in this table.

Instruction:

Survey reference:

Field:

Example entry:

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Enter numeric value (if batch) Enter numeric value (if batch)

Enter numeric value based on nominal production 

capacity (if continuous) Enter numeric value (if continuous)

Optional. Enter any comments you have on the data 

supplied.

Batch reactor cycle time (hr) Typical batch reactor cycles per day

Continuous or batch tall oil reactor operation, 

day/yr

Continuous tall oil reactor 

nominal production capacity, 

tons tall oil per hour Comments

365 25

Byproducts 0900006480f7efd2.xls 2 of 2
OMB Control No: 2060-0656 Did any of the responses (individual cells) you entered in this tab contain CBI? 

Expiration Date: 2/28/2014 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.

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms. This tab does not apply for synthetic area sources. 

Instruction:

Provide for all entries. This 

should match NEI Site ID 

used in Part II.

The kraft condensate streams covered under subpart S 

are "named" in §63.446(b). 

Select from menu the source of each "named" kraft 

condensate stream (digester, turpentine recovery, 

evaporator, HVLC, or LVHC systems). Select "Combined 

systems" if you wish to describe combined condensate 

streams from multiple "named" sources (e.g., combined 

digester and evaporator condensates). Select "Other 

systems" to describe condensate streams that are unnamed (i.e., not listed in §63.446(b)) but are controlled to 

meet subpart S as part of an innovative or equivalency-bypermit project. 

Enter Emission Unit ID(s) or 

Collection system ID(s) 

(matching the PI Equip 

detail tab) that are 

associated with the 

condensate stream

Select from menu (Yes, No, Partially).

-If "No" complete question II. 

-If "Yes" complete questions III-VII to 

specify the applicable method of 

condensate treatment.

-If "Partially" complete question II for the 

uncontrolled portion of the condensate 

stream; and complete questions III-VII for 

the controlled portion of the condensate 

stream.

Mills may either collect/control all "named" kraft pulping condensates, or employ one of the volume reduction 

options are specified in subpart S at §63.446(c)(2) or (3). Mills may also comply with subpart S through 

equivalency-by-permit. 

Select from the following codes to describe why certain "named" condensate streams (or portions of these 

streams) are uncollected/uncontrolled:

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.

C - Mills uses equivalency-by-permit or other means of compliance for the "named" streams. Specify Emission Unit ID(s)

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.

Select from menu. Control options 

are described in the survey 

instruction 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 WW tab to 

supply the results of the 

four quarterly tests 

conducted in calendar 

year 2009.

Write in condensate treatment method 

(e.g., wastewater thermal oxidizer)

Select from menu. Control options are 

described in the survey 

instructiondocument. 

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.

Complete this question if multiple methods 

are used to treat the condensate (for 

example, usually steam stripping but 

biological treatment when the steam 

stripper is down).

Pick from the menu and write in a 

description of how the different treatment 

methods are used.

Enter any comments that you may have 

regarding the data supplied in this table.

Survey reference: I II - uncollected/uncontrolled III - recycling IV - stripping V - biological treatment VI - other treatment methods VII - multiple treatment methods

Field: NEI Site ID Kraft condensate stream

Emission Unit IDs (or 

Collection System IDs for 

HVLC or LVHC systems)

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

Date of compliance 

demonstration(s)

Compliance test results (include 

units)

For condensates treated by 

biological treatment, specify the 

control option used

Date of compliance 

demonstration(s)

Compliance test 

results (include units)

Specify condensate treatment method 

(if other than steam stripping or 

biological treatment) Specify the control option used

Date of compliance 

demonstration(s)

Compliance test results 

(include units)

Please describe if multiple treatment 

methods used for this condensate Comments

Example entry: 99999 Digester systems DIG-1, DIG-2 N 2B

99999 Combined systems DIG-3, LVHC-1, HVLC Y 92% total HAP reduction (by weight) 6/30/2009 94%

99999 Evaporator systems EVAP-1 Y WASHER Remove 10.2 pounds/ton ODP (1) 3/29/2001; (2) 5/15/2007

(1) Removed 15.7 lb HAP/ton ODP; 

(2) Removed 12.3 lb HAP/ton ODP Remove 10.2 pounds/ton ODP NA NA

As backup: Biological treatment is used as 

a backup when the steam stripper is not 

performing as required

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Kraft condensates 0900006480f7efd2.xls 1 of 4
Field: NEI Site ID Kraft condensate stream

Emission Unit IDs (or 

Collection System IDs for 

HVLC or LVHC systems)

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

Date of compliance 

demonstration(s)

Compliance test results (include 

units)

For condensates treated by 

biological treatment, specify the 

control option used

Date of compliance 

demonstration(s)

Compliance test 

results (include units)

Specify condensate treatment method 

(if other than steam stripping or 

biological treatment) Specify the control option used

Date of compliance 

demonstration(s)

Compliance test results 

(include units)

Please describe if multiple treatment 

methods used for this condensate Comments

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Kraft condensates 0900006480f7efd2.xls 2 of 4
Field: NEI Site ID Kraft condensate stream

Emission Unit IDs (or 

Collection System IDs for 

HVLC or LVHC systems)

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

Date of compliance 

demonstration(s)

Compliance test results (include 

units)

For condensates treated by 

biological treatment, specify the 

control option used

Date of compliance 

demonstration(s)

Compliance test 

results (include units)

Specify condensate treatment method 

(if other than steam stripping or 

biological treatment) Specify the control option used

Date of compliance 

demonstration(s)

Compliance test results 

(include units)

Please describe if multiple treatment 

methods used for this condensate Comments

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Kraft condensates 0900006480f7efd2.xls 3 of 4
Field: NEI Site ID Kraft condensate stream

Emission Unit IDs (or 

Collection System IDs for 

HVLC or LVHC systems)

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

Date of compliance 

demonstration(s)

Compliance test results (include 

units)

For condensates treated by 

biological treatment, specify the 

control option used

Date of compliance 

demonstration(s)

Compliance test 

results (include units)

Specify condensate treatment method 

(if other than steam stripping or 

biological treatment) Specify the control option used

Date of compliance 

demonstration(s)

Compliance test results 

(include units)

Please describe if multiple treatment 

methods used for this condensate Comments

494

495

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498

499

500

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).

Kraft condensates 0900006480f7efd2.xls 4 of 4
OMB Control No: 2060-0656 Did any of the responses (individual cells) you entered in this tab contain CBI? 

Expiration Date: 2/28/2014 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.

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). This tab does not apply for synthetic area sources. 

Notes:

Sources eligible for inclusion in the CCA as credit generators include (but are not limited to): pulping systems, bleaching systems, causticizing systems, papermaking systems, and wastewater treatment 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). If equipment other than that listed above is included in your CCA calculations, please include that equipment in the tab.

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. 

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.

Emissions Balance Your response will consist of one row on this left side of the orange line. CCA Equipment List Your response will consist of multiple rows on this right side of the orange line.

Instruction:

Provide for all entries. This 

should match NEI Site ID 

used in Part II.

Baseline emissions are measured after compliance has 

been achieved with the kraft pulping process condensate 

standards, and the 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). Instruction:

Your response will be multiple 

rows on this side of the orange 

line

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

Optional. Enter any comments you have on the 

data supplied.

Survey reference: Survey reference:

Field: NEI Site ID Baseline emissions (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). Field: NEI Site ID Emission Unit ID

CCA debit or credit generating 

emission point?

Clean condensate alterative 

technology applied

Parameters monitored for clean 

condensate alterative technology Comments

Example entry: 99999 0.68 0.34 2007 once - 2007 Example entry: 99999 BSW1 debit (uncontrolled) NA-debit source

99999 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 save-all (SVT)

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CCA 0900006480f7efd2.xls 1 of 10
Field: NEI Site ID Baseline emissions (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). Field: NEI Site ID Emission Unit ID

CCA debit or credit generating 

emission point?

Clean condensate alterative 

technology applied

Parameters monitored for clean 

condensate alterative technology Comments

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181

182

183

184

185

186

187

CCA 0900006480f7efd2.xls 2 of 10
Field: NEI Site ID Baseline emissions (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). Field: NEI Site ID Emission Unit ID

CCA debit or credit generating 

emission point?

Clean condensate alterative 

technology applied

Parameters monitored for clean 

condensate alterative technology Comments

188

189

190

191

192

193

194

195

196

197

198

199

200

201

202

203

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286

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288

289

290

291

292

293

294

295

CCA 0900006480f7efd2.xls 3 of 10
Field: NEI Site ID Baseline emissions (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). Field: NEI Site ID Emission Unit ID

CCA debit or credit generating 

emission point?

Clean condensate alterative 

technology applied

Parameters monitored for clean 

condensate alterative technology Comments

296

297

298

299

300

301

302

303

304

305

306

307

308

309

310

311

312

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400

401

402

403

CCA 0900006480f7efd2.xls 4 of 10
Field: NEI Site ID Baseline emissions (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). Field: NEI Site ID Emission Unit ID

CCA debit or credit generating 

emission point?

Clean condensate alterative 

technology applied

Parameters monitored for clean 

condensate alterative technology Comments

404

405

406

407

408

409

410

411

412

413

414

415

416

417

418

419

420

421

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499

500

501

502

503

504

505

506

507

508

509

510

511

CCA 0900006480f7efd2.xls 5 of 10
Field: NEI Site ID Baseline emissions (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). Field: NEI Site ID Emission Unit ID

CCA debit or credit generating 

emission point?

Clean condensate alterative 

technology applied

Parameters monitored for clean 

condensate alterative technology Comments

512

513

514

515

516

517

518

519

520

521

522

523

524

525

526

527

528

529

530

531

532

533

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541

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608

609

610

611

612

613

614

615

616

617

618

619

CCA 0900006480f7efd2.xls 6 of 10
Field: NEI Site ID Baseline emissions (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). Field: NEI Site ID Emission Unit ID

CCA debit or credit generating 

emission point?

Clean condensate alterative 

technology applied

Parameters monitored for clean 

condensate alterative technology Comments

620

621

622

623

624

625

626

627

628

629

630

631

632

633

634

635

636

637

638

639

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711

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715

716

717

718

719

720

721

722

723

724

725

726

727

CCA 0900006480f7efd2.xls 7 of 10
Field: NEI Site ID Baseline emissions (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). Field: NEI Site ID Emission Unit ID

CCA debit or credit generating 

emission point?

Clean condensate alterative 

technology applied

Parameters monitored for clean 

condensate alterative technology Comments

728

729

730

731

732

733

734

735

736

737

738

739

740

741

742

743

744

745

746

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748

749

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811

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815

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818

819

820

821

822

823

824

825

826

827

828

829

830

831

832

833

834

835

CCA 0900006480f7efd2.xls 8 of 10
Field: NEI Site ID Baseline emissions (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). Field: NEI Site ID Emission Unit ID

CCA debit or credit generating 

emission point?

Clean condensate alterative 

technology applied

Parameters monitored for clean 

condensate alterative technology Comments

836

837

838

839

840

841

842

843

844

845

846

847

848

849

850

851

852

853

854

855

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864

865

866

867

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880

881

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890

891

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895

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899

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901

902

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904

905

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910

911

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913

914

915

916

917

918

919

920

921

922

923

924

925

926

927

928

929

930

931

932

933

934

935

936

937

938

939

940

941

942

943

CCA 0900006480f7efd2.xls 9 of 10
Field: NEI Site ID Baseline emissions (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). Field: NEI Site ID Emission Unit ID

CCA debit or credit generating 

emission point?

Clean condensate alterative 

technology applied

Parameters monitored for clean 

condensate alterative technology Comments

944

945

946

947

948

949

950

951

952

953

954

955

956

957

958

959

960

961

962

963

964

965

966

967

968

969

970

971

972

973

974

975

976

977

978

979

980

981

982

983

984

985

986

987

988

989

990

991

992

993

994

995

996

997

998

999

CCA 0900006480f7efd2.xls 10 of 10
OMB Control No: 2060-0656 Did any of the responses (individual cells) you entered in this tab contain CBI? 

Expiration Date: 2/28/2014 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.

Include one row for each bleaching or brightening line located at your mill. Some mills will have only one row, while other mills will have a few rows.

For example, a mill that produces bleached chemical pulp, bleached secondary fiber pulp, and brightened mechanical pulp could include three rows (one for each type of pulp that is bleached/brightened using separate bleaching/brightening processes).

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.

Note: The terms "bleaching" and "brightening" should be viewed as interchangeable in this tab (e.g., "Bleaching" can also be read as "Brightening").

Instruction:

Provide for all entries. This 

should match NEI Site ID 

used in Part II.

This section (to the left of the 

orange line) is to be 

completed by all mills that 

perform any type of bleaching 

or brightening. Select yes/no Select yes/no

Select from menu. Please 

explain if the bleaching process 

cannot be characterized as 

ECF, PCF, or TCF.

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)

 S-Sodium hydrosulfite (Na2S2O4)

 SO2-SO2

Add other notation for bleaching/brightening stages 

not represented above.

Enter numeric 

value

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 annual bleached pulp 

capacity (ADTBP/yr).

This column represents the 

amount of bleached pulp that is 

sold (or transferred to another 

mill within the same company) as 

bleached market pulp.

This column represents the 

amount of bleached pulp that 

is used onsite to manufacture 

bleached paper/paperboard.

This section (to the 

right of the orange line) 

is to be completed for 

bleaching systems that 

use any chlorine or 

chlorinated 

compounds.

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.

 

Enter the APCD_ID for the control method. 

In some cases the same control device (and 

the same APCD_ID) will apply for multiple 

stages.

Describe the control system (using any 

relevant APCD_IDs) if only portions of the 

bleaching stage vent gases are controlled.

Enter "NA" not applicable if no control is 

used. 

Survey reference:

Field: NEI Site ID

Bleaching line ID (if 

applicable)

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? Bleaching sequence

Bleach line 

operating 

hr/yr

2009 nominal daily 

bleached production 

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) Material type

Does stage 1 use 

chlorine or 

chlorinated 

compounds? Stage 1 control method

Example entry: 99999 B1 yes yes ECF - elemental chlorine free DED(DOP) 8500 16 0.15 0.85 1 mixture of HW and SW Yes SCBR_BL1

1 0

2 0

3 0

4 0

5 0

6 0

7 0

8 0

9 0

10 0

11 0

12 0

13 0

14 0

15 0

16 0

17 0

18 0

19 0

20 0

21 0

22 0

23 0

24 0

25 0

26 0

27 0

28 0

29 0

30 0

31 0

32 0

33 0

34 0

35 0

36 0

37 0

38 0

39 0

40 0

41 0

42 0

43 0

44 0

45 0

46 0

47 0

48 0

49 0

50 0

Bleaching 0900006480f7efd2.xls 1 of 3
OMB Control No:

Expiration Date:

Include one row for each bleaching or brightening line located at your mill. Some mills will have only one row, while other mills will have a few rows.

For example, a mill that produces bleached chemical pulp, bleached secondary fiber pulp, and brightened mechanical pulp could include three rows (one for each type of pulp that is bleached/brightened using separate bleaching/brightening processes).

UK = Unknown. NA = Not Applicable

Note: The terms "bleaching" and "brightening" should be viewed as interchangeable in this tab (e.g., "Bleaching" can also be read as "Brightening").

Instruction:

Survey reference:

Field:

Example entry:

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

46

47

48

49

50

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 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

Stage 1 chloroform control 

option(s) used to demonstrate 

subpart S compliance

Stage 1 chlorinated HAP control 

option used to demonstrate 

subpart S compliance

Does stage 2 use 

chlorine or 

chlorinated 

compounds?

Stage 2 control 

method

Stage 2 chloroform control 

option(s) used to demonstrate 

subpart S compliance

Stage 2 chlorinated HAP control 

option used to demonstrate 

subpart S compliance

Does stage 3 use 

chlorine or 

chlorinated 

compounds?

Stage 3 control 

method

Stage 3 chloroform control 

option(s) used to demonstrate 

subpart S compliance

Stage 3 chlorinated HAP 

control option used to 

demonstrate subpart S 

compliance

Does stage 4 use 

chlorine or 

chlorinated 

compounds?

Stage 4 control 

method

Stage 4 chloroform control 

option(s) used to demonstrate 

subpart S compliance

Stage 4 chlorinated HAP control 

option used to demonstrate 

subpart S compliance

Meet effluent guidelines/standards

99% reduction (by weight) 

measured as total chlorinated 

HAP 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 Yes SCBR_BL2 Meet effluent guidelines/standards

Outlet concentration < 10 ppmv 

measured as methanol

Bleaching 0900006480f7efd2.xls 2 of 3
OMB Control No:

Expiration Date:

Include one row for each bleaching or brightening line located at your mill. Some mills will have only one row, while other mills will have a few rows.

For example, a mill that produces bleached chemical pulp, bleached secondary fiber pulp, and brightened mechanical pulp could include three rows (one for each type of pulp that is bleached/brightened using separate bleaching/brightening processes).

UK = Unknown. NA = Not Applicable

Note: The terms "bleaching" and "brightening" should be viewed as interchangeable in this tab (e.g., "Bleaching" can also be read as "Brightening").

Instruction:

Survey reference:

Field:

Example entry:

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

46

47

48

49

50

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

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.

Optional. Enter any comments you have on the data 

supplied.

Does stage 5 use 

chlorine or 

chlorinated 

compounds?

Stage 5 control 

method

Stage 5 chloroform control 

option(s) used to demonstrate 

subpart S compliance

Stage 5 chlorinated HAP control 

option used to demonstrate subpart S 

compliance

Does stage 6 use 

chlorine or 

chlorinated 

compounds?

Stage 6 control 

method

Stage 6 chloroform 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. Comments

None (no CO control measure)

Bleaching 0900006480f7efd2.xls 3 of 3
OMB Control No: 2060-0656 Did any of the responses (individual cells) you entered in this tab contain CBI? 

Expiration Date: 2/28/2014 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.

Provide data for the 2009 operating year. Do not include pulp dryers in this tab. 

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.

Include one (or more) rows for each paper machine. You may include multiple rows for each paper machine if needed to reflect information that varies considerably by major paper grade, copying down information that does not vary (or remains adequately representative) from row to row.

Instruction:

Provide for all entries. 

This should match NEI 

Site ID used in Part II.

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

Specify the approximate fiber 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). 

You may specify a range (e.g., 0.6-0.7) if 

there is variation within a main paper grade.

Indicate the other pulp type(s) followed 

by its approximate decimal percentage 

(e.g., softwood semichem - 0.10)

Survey reference: Pulp types used

Field: NEI Site ID Paper machine Emission Unit ID

Type of paper 

machine as 

currently 

configured

Is furnish mixture 

bleached or unbleached? Hardwood kraft % Softwood kraft % Soda % Sulfite %

Dissolving/ 

specialty pulp %

Semichemical 

pulp %

Hardwood mechanical/ 

groundwood %

Softwood mechanical/ 

groundwood % Secondary fiber % Non-wood fiber % Other % (specify)

Example entry: 99999 PM1 Fourdrinier bleached 0.2 0.65 0.15

99999 PM1 Fourdrinier bleached 0.3-0.4 0.6-0.7

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

46

47

48

49

50

Paper prod 0900006480f7efd2.xls 1 of 3
OMB Control No:

Expiration Date:

Provide data for the 2009 operating year. Do not include pulp dryers in this tab. 

UK = Unknown. NA = Not Applicable

Include one (or more) rows for each paper machine. You may include multiple rows for each paper machine if needed to reflect information that varies considerably by major paper grade, copying down information that does not vary (or remains adequately representative) from row to row.

Instruction:

Survey reference:

Field:

Example entry:

1

2

3

4

5

6

7

8

9

10

11

12

13

14

15

16

17

18

19

20

21

22

23

24

25

26

27

28

29

30

31

32

33

34

35

36

37

38

39

40

41

42

43

44

45

46

47

48

49

50

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. 

Add rows for the major paper 

grades listed in the pull down 

menu only (not for every 

single minor variation within 

every major paper grade).

Enter paper machine 

nominal production 

capacity in air dried 

tons paper/day 

(ADT/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 (gal/ODTP). 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.

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 the PI 

Controls tab, if applicable (e.g., if 

an APCD is used on wet end vent 

gases).

Enter number of 

dryer steam 

cylinders

Paper machine details

Paper grade produced

Nominal production 

capacity, ADT/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)

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

coated free sheet 935 0.001 48,300 28 UK UK 16 456,000 50

uncoated free sheet 1050 0.001 48,300 28 UK UK 16 456,000 50

Paper prod 0900006480f7efd2.xls 2 of 3
OMB Control No:

Expiration Date:

Provide data for the 2009 operating year. Do not include pulp dryers in this tab. 

UK = Unknown. NA = Not Applicable

Include one (or more) rows for each paper machine. You may include multiple rows for each paper machine if needed to reflect information that varies considerably by major paper grade, copying down information that does not vary (or remains adequately representative) from row to row.

Instruction:

Survey reference:

Field:

Example entry:

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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.

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 the PI 

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).

Optional. Enter any comments you have on the data 

supplied.

Indicate firing method and fuel type if air drying is 

used 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 

dry end vents/stacks, acfm (if known)

Describe any process improvements 

used to reduce HAP emissions from 

the dry end Comments

steam-heated (indirect-fired) 4 90,000 2 40,000

steam-heated (indirect-fired) 4 90,000 2 40,000

Paper prod 0900006480f7efd2.xls 3 of 3
OMB Control No: 2060-0656 Did any of the responses (individual cells) you entered in this tab contain CBI? 

Expiration Date: 2/28/2014 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.

Complete the table for any stock preparation and paper machine additives that contain "measurable" amounts of the following HAP: formaldehyde, acetaldehyde, naphthalene, methylene chloride, acrylamide, or benzene.

For purposes of this survey, "measurable" is defined (consistent with OSHA MSDS reporting requirements) as amounts greater than 0.1% for carcinogens, and amounts greater than 1% for non-carcinogens. See the survey instructions for more information. 

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.

Instruction:

Provide for all entries. This should 

match NEI Site ID used in Part II. List additive type

Separate with commas if multiple HAP are 

present (e.g., formaldeyde-5%, 

acetaldehyde-2%). Attach additional 

information to your survey response if 

necessary.

Enter numeric value 

of additive amount 

used (not the 

amount of the 

additive ingredient 

used). Select from list or write in

Enter description of any 

substitute additives.

Enter "UK" if unknown Enter description

Optional. Enter any comments you have on the data 

supplied.

Survey reference:

Field: NEI Site ID Additive

HAP content (% by volume or ppmv for 

liquids; % by weight or ppmw for solids)

Amount of additive 

used in 2009 Units for amount

Is the mill aware of any 

substitutes for this additive 

that do not contain the 

listed HAP? If so, please 

describe.

Indicate if the additive 

substitute(s) listed in the 

previous column contain other 

compounds that may not be 

desirable from a worker safety 

perspective Comments

Example entry: 99999 Wet strength resin Formaldehyde - 5% 8,000 lb/day UK UK 123456789

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HAP additives 0900006480f7efd2.xls 1 of 1
OMB Control No: 2060-0656 Did any of the responses (individual cells) you entered in this tab contain CBI? 

Expiration Date: 2/28/2014 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.

WWTP = wastewater treatment plant

Provide a flow diagram of each WWTP showing each wastewater handling/treatment unit.

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.

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.

Instruction:

Provide for all entries. This should 

match NEI Site ID used in Part II.

Select yes or no. 

If yes, please continue with completion of the WW tab. 

If no, see the instruction document. Select from menu or write in.

Select from menu: 

Yes - Biological treatment occurring at the wastewater treatment entity 

(POTW or private company) is used to comply with the subpart S 

standards for kraft condensates.

OR

No - The mill uses a methods other than biological treatment to comply 

with the kraft condensate standards. 

If you answer yes, then EPA requests that you complete the remainder of 

this WW tab to the extent that information is available for the WWTP. 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.

Select yes or no.

If yes, submit documentation of the most 

recent modeled emission estimates as a 

separate file attachment to your survey 

response.

If no fenceline monitoring, measurements (e.g., ambient measurements), or 

estimates of emissions from the wastewater treatment system have been 

conducted, please explain how wastewater treatment system emissions are 

accounted for in your air operating permit. In you explanation, list the specific 

wastewater treatment system air pollutants for which limits are specified in your air 

permit.

Select not applicable "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.

Enter the 2009 average daily 

throughput of the wastewater 

treatment plant (million gallons 

per day)

If known, enter the 

approximate volume 

percentage of water entering 

the WWTP from each general 

mill location. Use decimal 

percentages (e.g., enter 0.75 

for 75%).

See the instruction document 

for joint WWTP's shared by 

multiple mills.

Survey reference:

Field: NEI Site ID

Does the mill perform onsite wastewater treatment beyond operation of a 

clarifier for suspended solids removal? 

If mill wastewater treatment is 

outsourced to a POTW or private 

entity, indicate pre-treatment steps 

occuring onsite at the mill.

For kraft pulp mills outsourcing wastewater treatment, is 

biological treatment performed at the WWTP used to demonstrate 

compliance with the subpart S kraft condensate standards? 

Does the mill have permit limits (including 

occupational health limits) related to air pollutants 

specifically 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 since the 

mill came into compliance with the 

cluster rules (NESHAP subpart S and 

the pulp and paper effluent limitations)?

Have air emissions associated with 

the WWTP been measured?

Have air emissions associated with the 

WWTP been estimated (e.g., with 40 CFR 

part 63 Appendix C and 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 throughput, 

MMgal/day

Approximate volume 

percentage of WWTP 

capacity from kraft 

condensate streams hard 

piped for biological 

treatment in the WWTP (per 

subpart S) (if known)

Approximate volume 

percentage of WWTP 

capacity from chemical 

pulping and chemical 

recovery processes (other 

than subpart S hard-piped 

kraft condensates) (if 

known)

Approximate volume percentage of WWTP 

capacity from non-chemical pulping 

processes (e.g., mechanical, secondary 

fiber, or non-wood pulping) (if known)

Approximate volume percentage of WWTP 

capacity from the power and steam 

generation area(s) (e.g., boiler blowdown, 

wet ash handling systems) (if known)

Example entry: 99999 yes yes 

We have OSHA limits for H2S and other 

compounds. See WWTP attachment with our 

survey response for a tabular summary. no no

yes (see separate WWTP attachment with 

modeling input and output) NA 18.5 0.05 0.25 NA 0.05

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WW 0900006480f7efd2.xls 1 of 3
OMB Control No:

Expiration Date:

WWTP = wastewater treatment plant

Provide a flow diagram of each WWTP showing each wastewater handling/treatment unit.

UK = Unknown. NA = Not Applicable

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.

Instruction:

Survey reference:

Field:

Example entry:

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Biological treatment system performance data (required for biological treatment systems controlling kraft pulping condensates):

Select the general type of WWTP used by your 

mill. Select from menu or write in a description.

Select from list or write in description. 

Include systems installed for the purpose of 

reducing emissions from the WWTP, or 

systems that were not installed for this purpose 

but coincidentally lead to substantially reduced 

emissions from the WWTP.

Enter short description

Include practices/measures implemented for the 

purpose of reducing emissions from the 

WWTP, or practices/measures that were not 

implemented for this purpose but coincidentally 

lead to substantially reduced emissions from the 

WWTP.

Select from list or write in description

Include practices/measures implemented for the purpose of 

reducing emissions from the WWTP, or practices/measures 

that were not implemented for this purpose but coincidentally 

lead to substantially reduced emissions from the WWTP.

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, activatedsludge 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.

Do not include steam or air strippers, or effluent cooling towers.

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 PI Equip detail and 

PI Control tabs and indicate the APCD information 

in those tabs. 

This question applies for nonthoroughly mixed biological 

treatment units. Specify the 

number of zones used to 

characterize the biological 

treatment system (e.g., under 

40 CFR part 63, Appendix C). 

Enter "NA" if not applicable.

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 

percent 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.

Approximate volume 

percentage of WWTP 

capacity from bleaching 

processes (if known)

Approximate volume 

percentage of WWTP 

capacity from papermaking 

processes (if known)

Approximate volume 

percentage of WWTP 

capacity from other 

processes (if known) Check (=1)

General type of wastewater treatment 

system

Identify upstream process wastewater 

treatment systems 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 

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.

Number of zones used to 

characterize the biological 

treatment system

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)

0.2 0.35 0.1 1

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 4 11.5 0.35 0.03 0.97 94

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WW 0900006480f7efd2.xls 2 of 3
OMB Control No:

Expiration Date:

WWTP = wastewater treatment plant

Provide a flow diagram of each WWTP showing each wastewater handling/treatment unit.

UK = Unknown. NA = Not Applicable

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.

Instruction:

Survey reference:

Field:

Example entry:

1

2

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16

Second quarter (Q2) compliance Third quarter (Q3) compliance Fourth quarter (Q4) compliance Optional. Enter any comments you have on the data supplied.

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)

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) Comments

5.9 0.92 5.3 9.8 0.98 95 12.3 0.95 92

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WW 0900006480f7efd2.xls 3 of 3
OMB Control No: 2060-0656 Did any of the responses (individual cells) you entered in this tab contain CBI? 

Expiration Date: 2/28/2014 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 you are required to submit a Part III response, are you deferring until Part III submittal of any of the test data required in Attachment 1 to the Part I survey instructions? 

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. 

UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.

See Attachment 3 of the Part I survey instruction document for a list of emissions test reports to be submitted.

Instruction:

Provide for all entries. This should 

match NEI Site ID used in Part II.

Provide for all entries. Emission Unit IDs should 

match those used in other tabs such as the PI 

Equip detail tab.

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 PI Equip detail tab.

Provide the APCD used during the emissions test.

APCD_IDs should match those used in other tabs 

such as the PI Equip detail tab (unless equipment 

configuration has changed).

Enter combustion controls used during the 

emission test (e.g., combustion 

modifications/controls specified in the PI Equip 

detail 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)

Survey reference:

Field: NEI Site ID Emission Unit ID(s) Collection system ID(s) APCD_ID(s)

Combustion modifications or controls used to 

reduce air pollution (from combustion 

sources) Process testing notes (optional)

Test report year 

(XXXX)

Example entry: 99999 DIG-1, DIG-2, EVAP LVHC-1 LK1/SCBR2 2006

99999 LK1 SCBR2 2006

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PI Emissions test data 0900006480f7efd2.xls 1 of 4
Field: NEI Site ID Emission Unit ID(s) Collection system ID(s) APCD_ID(s)

Combustion modifications or controls used to 

reduce air pollution (from combustion 

sources) Process testing notes (optional)

Test report year 

(XXXX)

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PI Emissions test data 0900006480f7efd2.xls 2 of 4
OMB Control No:

Expiration Date:

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. 

UK = Unknown. NA = Not Applicable

See Attachment 3 of the Part I survey instruction document for a list of emissions test reports to be submitted.

Instruction:

Survey reference:

Field:

Example entry:

1

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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 Optional. Enter any comments you have on the data supplied.

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, 

$ Comments

methanol M308 inlet and outlet no one-time test only 12000

PM M5 outlet no annually 6000

PI Emissions test data 0900006480f7efd2.xls 3 of 4
Field:

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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, 

$ Comments

PI Emissions test data 0900006480f7efd2.xls 4 of 4