1 P&P Survey

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Overview

Mill
PI Equip detail
PI Permit limits
PI Controls
Pulp prod
Byproducts
Kraft condensates
CCA
Bleaching
Paper prod
HAP additives
WW
PI Emissions test data
Drop Down Menus(Ranges)

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Sheet 1: Mill

OMB Control No:

xxxx-xxxx

Did any of the responses (individual cells) you entered in this tab contain CBI?

Expiration Date:

xx/xx/xxxx

If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.

Review Draft

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

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 (full-time, 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.

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.

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

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

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

Survey reference:

Size of entity

Federal rule coverage

Pulps

Pulp dryers

Market pulp

Bleaching (or brightening) systems

Paper or paperboard processes/products

Paper capacity utilization

Paper grades produced

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

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

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?

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

Paper grade 8

Paper grade 9

Paper grade 10

Comments

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

[email protected]

100 Corporate Blvd

Green Bay

WI

54304

9020777

149810921

major

322121-Paper (except Newsprint) Mills

>1000

500-749

no

Applies

Applies

Applies

Applies

DDDD

Applies

Db

NA

yes

no

no

no

NA

NA

NA

yes-bleaching

1

340000

0.8

0.95

uncoated free sheet

linerboard

other - specialty food-grade

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

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Sheet 2: PI Equip detail

OMB Control No:	xxxx-xxxx				Did any of the responses (individual cells) you entered in this tab contain CBI?
Expiration Date:	xx/xx/xxxx				If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.
Review Draft
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 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).																																																													*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 survey codes.				Hidden columns:	Additional supplemental fuel columns (for types 2-6) are hidden. Unhide and complete these columns if relevant.
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 "XXXX-upgrade."	(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	Enter percent reduction (if known) and indicate the basis for the value provided (e.g., CEMS data, before-and-after testing, design value).	Enter percent reduction (if known) and indicate the basis for the value provided (e.g., CEMS data, before-and-after testing, design value).	Enter percent reduction (if known) and indicate the basis for the value provided (e.g., CEMS data, before-and-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)	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	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.]	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.	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.	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	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.	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%)	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 multi-fuel 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 non-fossil fuels corresponding to the suggested units in next column. Optional. EPA can assume default HHVs for fossil fuels, or you may opt to enter the HHV for your fossil fuel (e.g., if the fuel is relatively uncommon)	Specify units corresponding to the HHV. 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.	Optional. Enter any comments you have on the data supplied.
Survey reference:	Equipment identification											Emission unit exhaust parameters (if emitted through a conveyance)*					Combustion modifications or controls*					Process controls or pollution prevention	Air pollution controls (primary method of control)**								Backup controls**			Subpart BB NSPS applicability					Subpart S NESHAP applicability				Digesters			Pulp washing systems					Knotters, screens, and deckers		Evaporators			Oxygen delignification			Strippers										Pulp storage and Liquor storage				Liquor storage ponds				Causticizing equipment				Fuel-fired equipment*	Equipment incinerating NCG or SOG		Primary fuels for fuel-fired equipment (except black or red liquor)*					Supplemental or other fuels for fuel-fired equipment*					Emission Unit Startup and Shutdown
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?	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	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	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)	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	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	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, %	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	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)	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.	Comments
Example entry:	99999	DIG-1			LVHC-1				digester	pre-1990	8400	2,000	175	45	multiple vents combined	inlet to collection system																		yes	pre-1990	new			yes				Continuous	480	SW																																																	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.
	99999	DIG-2			LVHC-1				digester	pre-1990	8430	1,200	200	50	multiple vents combined	inlet to collection system																		yes	pre-1990	new			yes				Continuous	520	HW/SW swing																																																	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.
	99999	STRIPPER						NEI Emission Unit ID = 06	steam stripper system	2000	8430	14,000	UK	UK		stripper outlet (inlet to boiler)							Boiler EU55	Boiler EU55	WESP	WESP 1					TO	When Boiler EU55 is not operating	330	no					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)																		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																										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.
		LVHC-1							LVHC collection system	2000-upgrade	8370	14,000	UK	UK		collection system outlet (inlet to lime kiln)							Lime kiln 1	LK1	Scrubber	SCBR2					TO	When LK1 is not operating	390	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)	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)																																																					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
	99999	TO							thermal oxidizer (backup)	2000	390	11,000	300	8		control device (scrubber) outlet							Scrubber	SCBR6										no					no																																										20		STRIPPER, LVHC-1
	99999	Boiler EU55	VAGaintCorporationAnytown	EU55				NEI Emission Unit ID = EU55	boiler	1985	8700	56,000	250	12		control device outlet	overfire air	No	20%-design				WESP	WESP 1										no					no																																										435	STRIPPER		hog fuel	0.95	12.6	MMBtu/ton	0.23	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
	99999	EVAP			LVHC-1				evaporator	UK	8430	UK	UK	UK		NA																		yes	pre-1990	new			yes														1000	WASHER	6																																							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.
	99999	GENERIC UNIT				0.85		NEI Emission Unit ID = GEN09	generic example row	UK	8430	18,000	150	7		prior to atmospheric release							Uncontrolled											no					no							1000	3	D-V-V	stripped digester and evaporator condensates		300					1100	WASHER	436											strong black liquor	14365	FR =fixed roof	NA	weak black liquor	26400	158400	2,300,000	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.														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
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Sheet 3: PI Permit limits

OMB Control No:	xxxx-xxxx
Expiration Date:	xx/xx/xxxx
Review Draft
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 cross-checking 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	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	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.
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)	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)	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
Example entry:	99999	EU30	EU30_1	PM - filterable		0.02	gr/dscf @ 8% O2
	99999	EU30	EU30_1	Opacity		5	% opacity	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
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793
794
795
796
797
798
799
800
801
802
803
804
805
806
807
808
809
810
811
812
813
814
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
871
872
873
874
875
876
877
878
879
880
881
882
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884
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886
887
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890
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895
896
897
898
899
900
901
902
903
904
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906
907
908
909
910
911
912
913
914
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916
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920
921
922
923
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925
926
927
928
929
930
931
932
933
934
935
936
937
938
939
940
941
942
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961
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963
964
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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
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
1039
1040
1041
1042
1043
1044
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1046
1047
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1049
1050
1051
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1053
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1060
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1062
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1064
1065
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1067
1068
1069
1070
1071
1072
1073
1074
1075
1076
1077
1078
1079
1080
1081
1082
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1084
1085
1086
1087
1088
1089
1090
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1092
1093
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1095
1096
1097
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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
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1146
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1148
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1160
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1162
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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
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1206
1207
1208
1209
1210
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1213
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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
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
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1295
1296
1297
1298
1299
1300
1301
1302
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1304
1305
1306
1307
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1309
1310
1311
1312
1313
1314
1315
1316
1317
1318
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
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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
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
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1428
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1430
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
1487
1488
1489
1490
1491
1492
1493
1494
1495
1496
1497
1498
1499
1500

---

Sheet 4: PI Controls

OMB Control No:

xxxx-xxxx

Did any of the responses (individual cells) you entered in this tab contain CBI?

Expiration Date:

xx/xx/xxxx

If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.

Review Draft

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 "XXXX-upgrade."

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.

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 air-to-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

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.

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.

Survey reference:

APCD identification

P-drop

Control efficiency

Thermal oxidizers/incinerators

Sorbent injection

Fabric filters

ESPs

WESPs

Scrubber

Packed bed scrubbers/absorbers

Water source and usage

Solid material handling and disposal

Parameter monitoring

Control Device Startup and Shutdown

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

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

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

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

Example entry:

99999

ANYCONTROL

ANYUNIT

ANYTYPE

UK

pre-1990

4

98

90

Methanol

activated carbon

Hg

100

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

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

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)

99999

SCRB2

LK1, LVHC1

Scrubber

Ducon

1985

6

95

92

82

50

Formaldehyde, Methanol

Caustic

6

10

60

surface water and water from recirculation pond

Yes

350

0.35

Treated in onsite wastewater treatment plant

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

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)

99999

TO

STRIPPER (backup); LVHC1 (backup)

Thermal oxidizer/incinerator

Coen

1999

2

98

Single-stage combustion chamber

NA

1300

1.8

no

NA

combustion chamber temperature

22000

1999

4

temperature set point

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)

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

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

87

88

89

90

91

92

93

94

95

96

97

98

99

100

---

Sheet 5: Pulp prod

OMB Control No:	xxxx-xxxx		Did any of the responses (individual cells) you entered in this tab contain CBI?
Expiration Date:	xx/xx/xxxx		If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.
Review Draft
Use this table for pulp produced onsite. Do not include pulp purchases in this table.
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.		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 non-wood 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.		Optional. Enter any comments you have on the data supplied.
Survey reference:	Pulping line identification						Virgin wood fiber sources used for chemical or mechanical wood pulps									Mechanical wood pulps	Recycled/secondary fiber pulps									Non-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)	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)	Comments
Example entry:	99999	kraft	8500	950	0.8	0.95	yes	yes	no	0.2	0.8	NA	0.25	0.75	1										0					0
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Sheet 6: Byproducts

OMB Control No:	xxxx-xxxx		Did any of the responses (individual cells) you entered in this tab contain CBI?
Expiration Date:	xx/xx/xxxx		If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.
Review Draft
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.	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.
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?	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
Example entry:	99999	8500	700	DIG-1, DIG-2	220000	EVAP-1, EVAP-2	continuous			365	25
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Sheet 7: Kraft condensates

OMB Control No:	xxxx-xxxx		Did any of the responses (individual cells) you entered in this tab contain CBI?
Expiration Date:	xx/xx/xxxx		If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.
Review Draft
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 un-named (i.e., not listed in §63.446(b)) but are controlled to meet subpart S as part of an innovative or equivalency-by-permit 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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																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.

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Sheet 8: CCA

OMB Control No:	xxxx-xxxx		Did any of the responses (individual cells) you entered in this tab contain CBI?
Expiration Date:	xx/xx/xxxx		If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.
Review Draft
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 credit-generating 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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Sheet 9: Bleaching

OMB Control No:	xxxx-xxxx		Did any of the responses (individual cells) you entered in this tab contain CBI?
Expiration Date:	xx/xx/xxxx		If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.
Review Draft
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.	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	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.
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	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	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
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	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									None (no CO control measure)
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Sheet 10: Paper prod

OMB Control No:	xxxx-xxxx		Did any of the responses (individual cells) you entered in this tab contain CBI?
Expiration Date:	xx/xx/xxxx		If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.
Review Draft
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)	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	Select air dryer firing method from menu or write in. Air dryers are direct fired or indirect-fired (use steam-to-air 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.
Survey reference:					Pulp types used											Paper machine details
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)	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	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
Example entry:	99999	PM1	Fourdrinier	bleached	0.2	0.65							0.15			coated free sheet	935			0.001	48,300	28	UK	UK		16	456,000		50	steam-heated (indirect-fired)	4	90,000		2	40,000
	99999	PM1	Fourdrinier	bleached	0.3-0.4	0.6-0.7										uncoated free sheet	1050			0.001	48,300	28	UK	UK		16	456,000		50	steam-heated (indirect-fired)	4	90,000		2	40,000
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Sheet 11: HAP additives

OMB Control No:	xxxx-xxxx		Did any of the responses (individual cells) you entered in this tab contain CBI?
Expiration Date:	xx/xx/xxxx		If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.
Review Draft
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
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Sheet 12: WW

OMB Control No:	xxxx-xxxx		Did any of the responses (individual cells) you entered in this tab contain CBI?
Expiration Date:	xx/xx/xxxx		If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.
Review Draft
WWTP = wastewater treatment plant
Provide a flow diagram of each WWTP showing each wastewater handling/treatment unit.
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.																											Biological treatment system performance data (required for biological treatment systems controlling kraft pulping condensates):
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.								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, activated-sludge biological treatment units, aerated or non-aerated surface impoundments, anaerobic digesters, other biological treatment units (trickling filters, rotating biological contactors), wastewater storage tanks, and any other wastewater treatment units. 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 non-thoroughly 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.	Second quarter (Q2) compliance				Third quarter (Q3) compliance				Fourth quarter (Q4) compliance				Optional. Enter any comments you have on the data supplied.
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)	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)	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
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	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		5.9	0.92		5.3	9.8	0.98	95		12.3	0.95	92
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Sheet 13: PI Emissions test data

OMB Control No:	xxxx-xxxx		Did any of the responses (individual cells) you entered in this tab contain CBI?
Expiration Date:	xx/xx/xxxx		If yes, be sure to shade the CBI-containing cells red and follow the instructions in section C of the survey overview document for submitting CBI.
Review Draft
			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)	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.
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)	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
Example entry:	99999	DIG-1, DIG-2, EVAP	LVHC-1	LK1/SCBR2			2006	methanol	M308	inlet and outlet	no		one-time test only	12000
	99999	LK1		SCBR2			2006	PM	M5	outlet	no		annually	6000
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Sheet 14: Drop Down Menus(Ranges)

Drop Down List	Field	NOTE
Frequently Used Drop Downs
	CBI Box	All tabs but Permit Limits
Yes	All tabs but Permit Limits
No
	Small business	Mill
yes
no
UK
	P&P NESHAP subpart S	Mill
	Combustion Source NESHAP subpart MM	Mill
Applies	Paper/web coating NESHAP subpart JJJJ	Mill
NA	Other NESHAP (list subparts)
NA-Synthetic Area Source
Applies	Kraft NSPS subpart BB	Mill
NA
	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?	equip
	Is the stripper integrated with the multiple effect evaporator system?	equip
	Is emission unit subject to NESHAP subpart S?	equip
	Is emission unit subject to NSPS BB?	Mill
	Does the mill purchase secondary fiber pulp?	Mill
	Is natural gas supply currently available to the mill (e.g., truck delivery or pipeline)?	Mill
	Does the mill purchase virgin pulp?	Mill
	Does the mill produce virgin pulp?	controls
	Heat recovery	controls
	Is WESP preceded by a quench chamber	controls
	Have fields/chambers been added to expand the ESP within the last 10 years?	controls
	Is water recirculated?	pulp
	Sawmill residues	pulp
	Chips produced offsite	pulp
	Chips produced onsite	pulp
	For TMP or pressurized groundwood systems, is a heat recovery system used?	bleaching
	Is the bleaching line preceded by O2 delignification?	bleaching
	Are chlorine or chlorinated compounds used in any stage of the bleaching line?	bleaching
	Does stage 6 use chlorine or chlorinated compounds?	bleaching
	Does stage 5 use chlorine or chlorinated compounds?	bleaching
	Does stage 4 use chlorine or chlorinated compounds?	bleaching
	Does stage 3 use chlorine or chlorinated compounds?	bleaching
	Does stage 2 use chlorine or chlorinated compounds?	bleaching
	Does stage 1 use chlorine or chlorinated compounds?	WW
	Have air emissions associated with the WWTP been estimated (e.g., with 40 CFR part 63 Appendix C and WATER9 or another model)?	WW
	Have air emissions associated with the WWTP been measured?	WW
	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)?	WW
	Does the mill have permit limits (including occupational health limits) related to air pollutants specifically from wastewater sources?	Emission
Yes	Has the configuration of the emission unit, combustion controls, collection system, or APCD changed since the test was conducted?	Emission
No	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?
Mill Tab
	HAP size classification
major
area (true)
synthetic minor
UK
	Primary NAICS
322110-Pulp Mills
322121-Paper (except Newsprint) Mills
322122-Newsprint Mills
322130-Paperboard Mills
322211-Corrugated and Solid Fiber Box Manufacturing
322212-Folding Paperboard Box Manufacturing
322213-Setup Paperboard Box Manufacturing
322214-Fiber Can, Tube, Drum, and Similar Products Manufacturing
322215-Non-Folding Sanitary Food Container Manufacturing
322221-Coated and Laminated Packaging Paper Manufacturing
322222-Coated and Laminated Paper Manufacturing
322223-Coated Paper Bag and Pouch Manufacturing
322224-Uncoated Paper and Multiwall Bag Manufacturing
322225-Laminated Aluminum Foil Manufacturing for Flexible Packaging Uses
322226-Surface-Coated Paperboard Manufacturing
322231-Die-Cut Paper and Paperboard Office Supplies Manufacturing
322232-Envelope Manufacturing
322233-Stationery, Tablet, and Related Product Manufacturing
322291-Sanitary Paper Product Manufacturing
322299-All Other Converted Paper Product Manufacturing
	Worldwide employees
<50	Facility employees
50-99
100-499
500-749
750-999
>1000
	Boiler NESHAP subpart DDDDD (or CISWI emission guidelines/NSPS) that are under development
Expect DDDDD to apply
Expect CISWI to apply
Expect DDDDD and/or CISWI to apply (to be determined based on final applicability of these rules)
NA
	Boiler NSPS
D
Da
Db
Dc
	Other NSPS (list subparts)
K
Ka
Kb
GG
Other (enter 40 CFR part 60 subpart)
NA
	Does the mill produce pulp from secondary fiber?
yes
yes - use pre-consumer fiber
yes - use post-consumer fiber
yes - use pre- and post-consumer fiber
no
	Types of market pulp produced by the mill
Dissolving pulp
Softwood chemical market pulp
Hardwood chemical market pulp
Mechanical market pulp
Market pulp from secondary (recycled) fiber
NA (market pulp not produced)
	Is bleaching or brightening performed at the mill?
yes-bleaching
yes-brightening
yes-bleaching and brightening
yes-other {specify}
no
	Paper grade 1
newsprint	Paper grade 2
coated free sheet	Paper grade 3
uncoated free sheet	Paper grade 4
coated groundwood	Paper grade 5
uncoated groundwood	Paper grade 6
tissue & sanitary	Paper grade 7
specialty packaging & industrial	Paper grade 8
kraft packaging	Paper grade 9
linerboard	Paper grade 10
corrugating medium
solid bleached board
recycled board
construction paper and board
other (specify type)
PI Equip detail Tab
	Configuration if not emitted through a conveyance
NV
BLDG
FUGITIVE
	Year emission unit installed
UK
pre-1990
	Location of flow rate provided
inlet to collection system
collection system outlet prior to control device,
inlet to control device,
control device outlet
prior to atmospheric release
	Combustion controls
low NOx burners
quarternary air
other {specify}
	APCD1 type
Recovery furnace ESP (dry bottom)	APCD2 type
Recovery furnace ESP (wet bottom)	APCD3 type
ESP (dry)	APCD4 type
Wet ESP (WESP)
Scrubber - venturi
Scrubber - quench
Scrubber - packed bed
Scrubber
Absorber
Mist eliminator
Thermal oxidizer/incinerator
Regenerative thermal oxidizer
Multicyclone
Cyclone (excluding product recovery cyclones)
Fabric filter (baghouse)
Condenser
Gravel bed
Dry sorbent injection
Carbon absorber
Selective noncatalytic reduction
Selective catalytic reduction
Boiler (specify Emission Unit ID)
Lime kiln (specify Emission Unit ID)
Recovery furnace (specify Emission Unit ID)
Other - specify type (and Emission Unit ID if applicable)
Uncontrolled
	Reason subject to BB
new
modified
reconstructed
modified or reconstructed (not sure)
collects emissions from BB emission units
	Specify TRS compliance option used to demonstrate NSPS subpart BB compliance (if applicable)
5 ppmdv @ 10% O2 (combustion control)	Specify TRS compliance option used for backup method of control (if applicable)
5 ppmdv, uncorrected for O2 (control other than combustion)
combust gases in lime kiln or recovery furnace subject to subpart BB
combust gases at 1200oF for at least 0.5 sec
incinerating brown stock washer gases is not feasible
uncontrolled digester gases contain <0.01 lb TRS/ton ADP
8 ppmdv @ 10% O2 (lime kilns)
0.033 lb/ton BLS as H2S (SDTs)
5 ppmdv @ 8% O2 (straight recovery furnace)
25 ppmdv @ 8% O2 (cross recovery furnace)
Meet permit limit more stringent than NSPS
	Subpart S compliance option used (for primary method of control)
Reduce total HAP emissions by 98 wt%	Subpart S compliance option used (for backup method of control, if applicable)
Reduce total HAP concentration at the outlet of thermal oxidizer to <20 ppmv @ 10% O2 (dry basis)
Reduce total HAP emissions using a thermal oxidizer operating >1600F and >.75 secs residence time
Use a boiler, LK, or RF in which the HAP gas stream in introduced with the primary fuel into the flame zone
Use a boiler or RF with a heat input capacity >150 MMBtu/hr (44 MW) in which the HAP gas stream is introduced with the combustion air
Clean condensate alternative (§63.447).
0.89 lb/ton ODP (for Ca- or Na-based sulfite pulping)
92% reduction by weight (for Ca- or Na-based sulfite pulping)
2.2 lb/ton ODP (for Mg-based or NH3-based sulfite pulping)
87% reduction by weight (for Mg-based or NH3-based sulfite pulping)
	Provide reason if not controlled to meet subpart S
Systems of this type at existing sources are not subject to subpart S
Mill is a synthetic area source
The system does not match the definitions for controlled systems in subpart S. Provide reason (e.g., due to specific location of the system in the process line).
Exception 63.443(a)(ii)(A): knotter system with HAP emissions <0.1 lb/ton ODP
Exception 63.443(a)(ii)(B): screen system with <0.2 lb/ton ODP,
Exception 63.443(a)(ii)(C): knotter and screen system with combined emissions <0.3 lb/ton ODP
Exception 63.443(a)(iv)(A): decker uses only fresh water or paper machine white water
Exception 63.443(a)(iv)(B): decker uses process water with < 400 ppmw
Mill received equivalency by permit approval
Mill undertook innovations project
Emissions from this unit were offset using CCA
Other - specify
	Batch or continuous
Batch
Continuous
	Wood type (HW, SW, HW/SW swing)
HW
SW
HW/SW swing
HW and SW
Non-wood
	Washer types and sequence
vacuum drum
diffusion
pressure
belt
	Type of shower water used in decker
contaminated condensates
clean condensates
white water
other (specify)
NA
	Type of stripper
steam
air
	Primary reason for installation of the stripper
TRS control
BOD reduction
water conservation
subpart S kraft pulping condensate standards
nonchlorinated organic HAP control
	Tank contents
weak black liquor
strong black liquor
high density pulp
white liquor
green liquor
	Tank control technique
Open tank
FR =fixed roof
EFR = external floating roof
IFR = internal floating roof
Collection system and control device
Emissions routed to process (enter Emission Unit ID)
	If floating roof is used, type of seal
NA
Mechanical shoe primary seal (MS1)
MS1 with shoe mounted secondary (MESA)
MS1 with rim mounted secondary (MESA)
liquid mounted primary seal (LM1)
LM1 with rim mounted secondary (LM2)
vapor mounted primary seal (VM1)
M1 with rim mounted secondary (VM2)
	Pond contents
weak black liquor
strong black liquor
white liquor
green liquor
	Source(s) of makeup water added to mud washer or precoat filter
Untreated process condensates from {specify process - e.g., evaporator, blow heat recovery}
surface water
fresh water
process water {specify source}
treated wastewater
partially treated wastewater {specify last wastewater treatment unit water passed through}
mixture {specify sources}
	Primary fuel type
natural gas	Supplemental fuel type 1
#2 distillate oil
#6 residual oil
bark
hog fuel
turpentine
tall oil
petroleum coke
tire-derived fuel
wastewater treatment plant residuals
OCC rejects
	Optional: Primary fuel HHV units
Btu/gal	Optional: Supplemental fuel type 1 HHV units
MMBtu/ton
Btu/MMscf
	Conditions when supplemental fuel type 1 used
routine use (multi-fuel fired unit)
startup
backup
shutdown
pilot light
during upset conditions
seasonally during curtailments or peak prices
when turpentine prices are low
when tall oil prices are low
	Measures employed to reduce air emissions during emission unit startup (if any)
emission unit and control device operates in compliance with NSPS and NESHAP parameter limits during emission unit startup
emission unit and control device operates during emission unit startup (but not necessarily in compliance with all NSPS/NESHAP parameter limits)
backup/alternate control
NA - applicable emission and parameter limits not expected to be exceeded during startup
	Measures employed to reduce air emissions during shutdown (if any)
continue routing emissions to LVHC-1 collection system and primary or backup control system
continue routing emissions to LVHC-1 collection system and primary or backup control system
stop routing process condensates to stripper before beginning shutdown
NA - applicable emission and parameter limits not expected to be exceeded during shutdown
emission unit and control device operates during emission unit startup (but not necessarily in compliance with all NSPS/NESHAP parameter limits)
continue routing emissions to LVHC-1 collection system and primary or backup control system
Temperature drops below 200F
PI Permit limits
	Pollutant
TRS
SO2
sulfuric acid mist
NOx
CO
Pb or other HAP metals
VOC
THC
HCl
Methanol and gaseous organic HAP
Chlorine and chlorinated HAP
Opacity
PM
PM - filterable
PM - condensable
PM10
PM10 - filterable
PM10 - condensable
PM2.5
PM2.5 - filterable
PM2.5 - condensable
	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
Subpart S (P&P NESHAP)
Subpart MM (P&P combustion source NESHAP)
Subpart BB (Kraft NSPS)
Subpart BB (Kraft NSPS) - 1978
Subpart BB (Kraft NSPS) - 1986 revision
	Units for permit limit 1 (including any applicable %O2 or %CO2 correction factors)
gr/dscf @ 8% O2
gr/dscf @ 10% O2
lb/ton BLS
ppmdv @ 8% O2
ppmdv @ 10% O2
lb/ton BLS (as H2S)
lb/MMBtu
ppmdv
% reduction
% opacity
	Averaging time for permit limit 1 (if applicable)
3-hour	Averaging time for permit limit 2 (if applicable)
12-hour	Averaging time for permit limit 3 (if applicable)
daily	Averaging time for permit limit 4 (if applicable)
test	Averaging time for permit limit 5 (if applicable)
PI Controls
	Type of control device
Recovery furnace ESP (dry bottom)
Recovery furnace ESP (wet bottom)
ESP (dry)
Wet ESP (WESP)
Scrubber - venturi
Scrubber - quench
Scrubber - packed bed
Scrubber
Absorber
Mist eliminator
Thermal oxidizer/incinerator
Regenerative thermal oxidizer
Multicyclone
Cyclone (excluding product recovery cyclones)
Fabric filter (baghouse)
Condenser
Gravel bed
Dry sorbent injection
Carbon absorber
Selective noncatalytic reduction
Selective catalytic reduction
Other - specify type
	Incinerator type
Single-stage combustion chamber
Two-stage combustion chamber
Regenerative thermal oxidizer (RTO)
	What is the recovered heat from the incinerator exhaust used for?
preheat incoming emission stream
produce steam
produce hot water
	Sorbent type
activated carbon
lime
other (specify)
	List pollutants the sorbent injection was installed to control
acid gases (HCl, SO2, HF)
SO2
Hg
dioxins
	Bag cleaning method
Shake
Reverse air
Pulse jet
	Water source
surface water
fresh water
process water {specify source}
treated wastewater
partially treated wastewater {specify last wastewater treatment unit water passed through}
mixture {specify sources}
	Wastewater (blowdown) reuse or disposal method
Treated in onsite wastewater treatment plant
Recycled to mud washer(s)
Recycled to SDT
Recycled to process: {specify equipment receiving water using Emission Unit ID OR APCD_ID}
POTW
Other {specify}
	Type of material collected
PM
PM and sorbent
Sorbent
	End use/method of disposal for solid material collected
landfill onsite
lanffill offsite
recycle to causticizing system
sent to salt cake mix tank
reuse {specify}
	List continuous parameter monitoring systems used for this control device (e.g., pressure drop, liquid flow)
pressure drop
liquid flow rate
voltage
current
temperature (specify if inlet, outlet, bed, or other temperature)
pH
percent solids in recycle water
other (specify)
	Explain how control device startup is integrated with (dependent upon) emission unit startup/operation
Control device is started up and meets required operating parameter limits before emission unit is started up.
Control device cannot be started prior to emission unit starting up due to safety issue or risk of property damage. {Explain}
Control device cannot function as designed unless an air flow rate of {specify} acfm from the emission unit is achieved.
	List any control device continuous emissions monitoring or operating parameter limits that cannot be met during control device startup
The applicable emission and parameter limits are expected to be met during startup
	Explain how control device shutdown is integrated with (dependent upon) emission unit shutdown
Control device continues to operate and meets required operating limits while emission unit is shut down.
Control device cannot operate during emission unit shut down due to safety issue or risk of property damage. {Explain}
Control device cannot function as designed unless an air flow rate of {specify} acfm from the emission unit is achieved.
Pulp prod
	Pulping processes
kraft
soda
semi-chemical
sulfite-NH3
sulfite-Ca
Chemi-themo-mechanical pulp (CTMP)
stone groundwood (SGW)
pressurized groundwood (PGW)
thermo-mechanical pulping (TMP)
refiner mechanical pulping (RMP)
secondary fiber
non-wood
	Non-wood material
cotton
bagasse
kenaf
other {specify}
Byproducts
	Is tall oil acidulation reactor batch or continuous?
batch
continuous
Kraft condensates
	Kraft condensate stream
Digester systems
Turpentine recovery systems
Evaporator systems
HVLC collection systems
LVHC collection systems
Combined systems
Other systems {describe}
	Is condensate stream collected and treated according to subpart S?
Yes
No
Partially
	Indicate volume reduction option being used, or other reason why condensate stream is not collected and controlled
NA-system does not exist at mill
1
2A
2B
	For condensates treated by steam stripping, specify the control option used
92% total HAP reduction (by weight)	For condensates treated by biological treatment, specify the control option used
Remove 6.6 pounds/ton ODP	Specify condensate treatment method (if other than steam stripping or biological treatment)
210 ppmw at the outlet of the control device
Remove 10.2 pounds/ton ODP
330 ppmw at the outlet of the control device
Remove prorated mass of ___ pounds/ton ODP {specify limit}
	Please describe if multiple treatment methods used for this condensate
In series:
As backup:
Other:
CCA
	CCA debit or credit generating emission point?
debit (uncontrolled)
debit (under controlled)
credit
	Clean condensate alterative technology applied
NA-debit source
stand-alone biological treatment unit
steam stripper
other - specify
Bleaching
	Is the process ECF, PCF or TCF?
ECF - elemental chlorine free
PCF - processed chlorine free
TCF - totally chlorine free
	Material type
HW only
SW only
mixture of HW and SW
secondary fiber
non-wood fiber
	Stage 1 control method
	Stage 2 control method
	Stage 3 control method
NA	Stage 4 control method
scrubber {enter APCD_ID}	Stage 5 control method
other {describe}	Stage 6 control method
	Stage 1 chloroform control option(s) used to demonstrate subpart S compliance
NA (no chlorine or chlorinated compounds used in this stage)	Stage 2 chloroform control option(s) used to demonstrate subpart S compliance
NA (mechanical, non-wood, or secondary fiber mill)	Stage 3 chloroform control option(s) used to demonstrate subpart S compliance
NA (synthetic area source)
Use no chlorine or hypochlorite AND meet effluent guidelines/standards	Stage 4 chloroform control option(s) used to demonstrate subpart S compliance
Use no chlorine or hypochlorite	Stage 5 chloroform control option(s) used to demonstrate subpart S compliance
Meet effluent guidelines/standards	Stage 6 chloroform control option(s) used to demonstrate subpart S compliance
NA (no chlorine or chlorinated compounds used in this stage)	Stage 1 chlorinated HAP control option used to demonstrate subpart S compliance
NA (synthetic area source)
99% reduction (by weight) measured as total chlorinated HAP	Stage 2 chlorinated HAP control option used to demonstrate subpart S compliance
99% reduction (by weight) measured as methanol	Stage 3 chlorinated HAP control option used to demonstrate subpart S compliance
Outlet concentration < 10 ppmv measured as total chlorinated HAP	Stage 4 chlorinated HAP control option used to demonstrate subpart S compliance
Outlet concentration < 10 ppmv measured as methanol	Stage 5 chlorinated HAP control option used to demonstrate subpart S compliance
Total outlet mass emission levels for all subject stages < 0.002 lb/ton ODP	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.
NA - ClO2 bleaching is not performed
None (no CO control measure)
Paper prod
	Type of paper machine as currently configured
Fourdrinier
cylinder
twin-wire
other {specify}
	Is furnish mixture bleached or unbleached?
bleached
unbleached
mixture of bleached and unbleached (please specify)
	Paper grade produced
coated free sheet
uncoated free sheet
coated groundwood
uncoated groundwood
tissue & sanitary
specialty packaging & industrial
kraft packaging
linerboard
corrugating medium
solid bleached board
recycled board
construction paper and board
other (specify type)
	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?
no
yes {please explain}
	Indicate firing method and fuel type if air drying is used
steam-heated (indirect-fired)
direct fired (natural gas)
direct-fired {specify fuel}
HAP additives
	Units for amount
gal/day
lb/day
lb/ton paper
gal/year
lb/year
WW
	Does the mill perform onsite wastewater treatment beyond operation of a clarifier for suspended solids removal?
Yes
No - Mill wastewater treatment is outsourced to a POTW
No - Mill wastewater treatment is outsourced to a separate wastewater treatment plant owned/operated by {enter company name}.
No - Other {please explain}
	If mill wastewater treatment is outsourced to a POTW or private entity, indicate pre-treatment steps occuring onsite at the mill.
Primary clarification
Secondary clarification
Primary and secondary clarification
Other: {specify}
	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?
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.
No – The mill uses a methods other than biological treatment to comply with the kraft condensate standards.
	Explain how wastewater treatment system emissions are accounted for in your air permit if you answered "no" to the previous 3 questions
Air emissions associated with wastewater treatment are not addressed in the air operating permit.
NA
	General type of wastewater treatment system
Aerated stabilization basin (aerated surface impoundment)
Activated-sludge biological treatment
Anaerobic treatment
Packaged system (specify e.g., UNOX system)
Other (specify)
	Identify upstream process wastewater treatment systems that reduce wastewater treatment unit air emissions of nonchlorinated organic HAP and TRS (including H2S).
steam stripper (enter Emission Unit ID)
biological treatment unit
wastewater thermal oxidizer (enter Emission Unit ID)
Other (specify)
	Describe any upstream practices or pollution prevention measures that reduce wastewater treatment unit air emissions of chlorinated HAP.
Use only nonchlorinated bleaching compounds
Use ClO2 bleaching (instead of chlorine or hypochlorite)
Other (specify)
PI Emissions test data
	Pollutants tested
PM
PM2.5-filterable
PM2.5-cond.
NOx
SO2
CO
methanol
THC
chlorine
CDD/CDF
POM/PAH
Speciated HAP metals
HCl
TRS
	Are inlet or outlet data provided?
outlet
inlet
inlet and outlet
	How often are you required to perform testing of this emission unit for the pollutants listed?
annually
every 2 years
every 5 years
one-time test only
as requested by the permitting authority