3 Part 3 P&P Survey

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Overview

PIII Equip detail
PIII Permit limits
PIII Controls
PCC
PIII Emissions test data

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Sheet 1: PIII 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
UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.
You may find it helpful to use Excel's "freeze panes" or "split" features when viewing this spreadsheet.																																																																																											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. Note that in some cases the Emission Unit ID will be the same as a Collection system ID or APCD_ID.	Leave columns that do not apply for a given 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.	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."	Enter manufacturer ONLY for chemical recovery combustion sources (recovery furnaces, black liquor oxidizers, chemical recovery combustion units, lime kilns, black liquor oxidizers) and boilers. Enter "UK" for unknown. Enter "shop-built" for equipment designed by the mill.	Enter 2009 operating hr/yr	Enter 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 P "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):	Enter any combustion control measures installed/employed to reduce air pollution from combustion sources (e.g., recovery furnaces, lime kilns)	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.	Use these "APCD" columns to describe the primary method of control. 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.	Enter ID code for 2nd APCD (to be used throughout the survey spreadsheets)	Enter 3rd control device if multiple controls used.	Enter ID code for 3rd APCD (to be used throughout the survey spreadsheets)	Enter 4th control device if multiple controls used.	Enter ID code for 4th APCD (to be used throughout the survey spreadsheets)	Select yes/no.	Provide year. If not known, enter approximate year (e.g., "pre-1990")	Select from menu.	Select from menu for recovery furnaces subject to subpart BB (straight or cross).	Indicate NSPS BB TRS compliance option used to demonstrate NSPS compliance with primary method of control. [Note: You may enter the compliance option for each emission unit or for the relevant collection system if listed separately.]	Select yes/no	Provide description for emission units subject to subpart MM. If no physical equipment changes or operational changes were required to achieve subpart MM compliance, then enter "no changes required."	If yes, submit PM bubble calculations per instructions for "Mills using the PM bubble compliance option."	If black liquor gasification is used, a diagram and description of the system including any combustion controls or add-on controls used to reduce air pollutants would be helpful.	Complete for each black liquor oxidation (BLO) system.	Select from menu	Select from menu	Enter number	Enter numeric value. Use the average from 2009 or target value.	Enter numeric value (e.g., enter "45" for 45%). Use the average from 2009 or target value.	Complete for each recovery furnace at kraft, soda, sulfite, and co-located kraft/Semichemical pulp mills. "Recovery furnaces" may also be referred to as "black liquor boilers" or "recovery boilers." Select from menu	If you operate an NDCE recovery furnace, indicate if it was previously a DCE recovery furnace that underwent a DCE furnace conversion (e.g., a low odor conversion). Select yes/no/NA	Enter year (e.g., 2000) when DCE furnace was converted to an NDCE furnace (if applicable). Enter pre-1990 if conversion was not within the last 20 years.	Select from menu or write in	Enter numeric capacity value for black liquor solids (BLS) feed rate or red liquor solids (RLS) for sulfite	Enter numeric value (e.g., enter "45" for 45%). Use the average from 2009 or target value.	Enter % sulfur, chloride, or nitrogen if known. Use the average from 2009 or target value.			Input site-specific higher heating value (HHV) of the pulping liquor, if measured. Use the average from 2009 or target value	Complete the recovery furnace ESP questions if applicable. If not applicable leave blank. Indicate the type of liquid used in the wet bottom ESP	The particulate matter (PM) return system returns PM collected in the ESP to the process. Select wet or dry from menu	Select from menu	Enter year (e.g., 2000) if an ESP was converted.	Complete for each chemical recovery combustion unit at a stand-alone Semichemical pulp mill. This pertains to equipment following the evaporator set. Select from menu	Select from menu	Select from menu	Enter numeric capacity value	Input site-specific higher heating value (HHV) of the pulping liquor, if measured.	Enter numeric value	Complete for each kraft, soda, sulfite, and semichemical smelt (or ash) dissolving tank (as applicable).	Select from menu	Enter numeric value. For example, capacity is usually the same as recovery furnace capacity (e.g., lb BLS/day), except when there are two smelt tanks for one recovery furnace.	Select from menu or write in. Enter "SDT scrubber water" if the SDT scrubber water drains into the SDT (as if often the case). See description of the other menu choices in the survey overview document instructions for the Controls tab. If a mixture of water sources are used, please specify the sources.	Enter numeric value in milligrams per liter. Use the average from 2009 or target value.	Enter numeric value in milligrams per liter. Use the average from 2009 or target value. Enter NA if TRS emissions would not be expected (e.g., for nonsulfur Semichemical pulp mills)	Complete Table 8 for each kraft or soda lime kiln. Select from menu	Enter numeric value	Enter numeric value (i.e., "70" = 70%). Use the average from 2009 or target value.	Enter numeric value for kiln hot end operating temperature (F). Use the average from 2009 or target value.	Enter numeric value for kiln cold end operating temperature (F). Use the average from 2009 or target value.	Select from menu	Select yes/no	Select from menu	Complete for recovery furnaces, semichemical combustion units, and lime kilns. Do not enter thermal oxidizer information in this column. Thermal oxidizers controlling Part III emission units are addressed in the PIII Controls tab. Enter numeric value in million Btu per hour (MMBtu/hr) representing the total heat input for all fuels including spent pulping liquor.	Complete for lime kilns, recovery furnaces and chemical recovery combustion units that are used to incinerate NCG or SOG. List all sources of NCG or SOG, identified by their Collection System IDs or Emission Unit IDs separated by commas, for which the emission unit serves as primary control (e.g., LVHC1, SOG, TALLOIL, ...). Many of these IDs will come from your Part I response.	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 having a primary fuel type other than spent pulping liquor (e.g., complete for lime kilns). Do not enter thermal oxidizer information in this column. Thermal oxidizers controlling Part III emission units are addressed in the PIII Controls tab. 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. Biomass or black liquor syngas is an example of a non-fossil fuel that could be used in lime kilns. 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 recovery furnaces, semichemical combustion units, and lime kilns. Do not enter thermal oxidizer information in this column. Thermal oxidizers controlling Part III emission units are addressed in the PIII Controls tab. 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. 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)								Subpart BB NSPS applicability					Subpart MM NESHAP applicability			Black liquor gasification	Black liquor oxidation systems						Recovery furnaces										Recovery furnace ESPs				Semichemical combustion units						Smelt/ash dissolving tanks						Lime kilns (including rotary lime kilns and fluidized bed calciners)								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	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 manufacturer	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	Is emission unit subject to NSPS BB?	If yes, year became subject to BB (XXXX)	Reason subject to BB	Type of recovery furnace subject to subpart BB	Specify TRS compliance option used to demonstrate NSPS subpart BB compliance (if applicable)	Is emission unit subject to NESHAP MM?	Describe any physical or operational changes made to the emission unit in order to achieve subpart MM compliance	Is this emission unit involved in a subpart MM PM bubble calculation?	Black liquor gasifier capacity (million lb BLS/day)	Emission Unit ID(s) of recovery furnace(s) downstream of BLO	Type of liquor oxidized	BLO type	No. of air oxidation stages	Liquor flow rate, gpm	Liquor solids content, %	Recovery furnace type	Was NDCE formerly a DCE (i.e., has the unit undergone a low odor conversion)?	DCE furnace conversion year (XXXX), if applicable	Type of liquor	Spent liquor solids nominal daily throughput capacity, million lb BLS/day (or million lb RLS/day for sulfite)	Liquor solids % by weight	Liquor solids sulfur % by weight	Liquor solids chloride % by weight	Liquor solids nitrogen % by weight	Liquor HHV Btu/lb dry solids	Type of liquid used in the ESP	Wet or dry PM return system (for recovery furnace ESPs)	For wet PM return system, specify liquid	Indicate year (XXXX) recovery furnace ESP was converted from a wet bottom/wet PM return system to a dry bottom/dry PM return system, if applicable	Type of combustor	Liquor evaporation equipment	Type of DCE	Spent liquor solids nominal daily production capacity, million lb/day	Liquor HHV Btu/lb dry solids	Combustion unit hottest temperature, F	Emission Unit ID of RF or combustion unit supplying SDT/ADT	Type	Smelt or ash nominal daily production rate, lb liquor solids/day	Type and source of water used in tank	Methanol concentration of water used to dissolve smelt/ash in tank (if known), mg/l	TRS concentration of water used to dissolve smelt/ash in tank (if known), mg/l	Type of kiln	Lime nominal daily production capacity, ton CaO/d	Lime mud percent solids, %	Kiln hot end temperature (F)	Kiln cold end temperature (F)	NCG introduction method	Are SOGs combined with NCGs before being introduced into the kiln?	If no, SOG introduction method	Design heat input capacity, MMBtu/hr	NCG/SOG for which the emission unit provides primary control	NCG/SOG for which the emission unit provides backup control	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	LK1					lime kiln	1983	Chanderpur Works	8400	45,000	290	8		control device outlet						use fresh mill water for lime mud washing to reduce TRS from the lime kiln	Scrubber	SCBR2							yes	1983	new		8 ppmdv @ 10% O2 (lime kilns)	yes	no changes required	no																																		rotary	200	71	2000	450	with primary fuel	no	NA - SOG are not burned in lime kiln		LVHC-1		natural gas		1020000000	Btu/MMscf		#6 residual oil	1	150000	Btu/gal	backup	24	Ensure scrubber liquid is flowing during startup once LK1 temperature reaches 200F	LK1 hot end temperature reaches 2000F	18	Continue operating scrubber until temperature in LK1 drops to 200F	Turn down gas burner to 50% flow	Require compliance with scrubber liquid flow parameter monitoring limit, but not pressure drop parameter monitoring limit (since the pressure drop cannot be maintained without sufficient exhaust flow from the lime kiln.
	99999	GENERIC UNIT		0.85		NEI Emission Unit ID = GEN09	generic example row	UK	Wellons	8430	18,000	150	7		control device outlet	overfire air	No	20%-design				WESP	WESP 1							no					no			1.9	RF1	strong	air	1	364	49	DCE	no		black	1.9	65	4.3	0.71		5940	Oxidized black liquor	wet	Oxidized black liquor		fluidized bed reactor	DCE	Venturi scrubber	75	5420	1400	RF1	smelt	690000	process water {weak wash}	45										435	STRIPPER		hog fuel	0.95	12.6	MMBtu/ton	0.23	natural gas	0.05			startup, backup	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 2: PIII Permit limits

OMB Control No:	xxxx-xxxx
Expiration Date:	xx/xx/xxxx				Place an "X" in the box below if all permit limits were supplied under Part I
Review Draft
Note: If you already included all of your permit limits in Part I of the survey, then you do not need to complete this spreadsheet. Please mark the box to the right.
UK = Unknown. NA = Not Applicable. See instruction document for details on use of these terms.
Pulp and Paper sector permit data.
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 PIII 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 PIII 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	RF1	RF01	PM - filterable		0.02	gr/dscf @ 8% O2
	99999	RF1	RF01	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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1500

---

Sheet 3: PIII 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.

Complete this tab for air pollution control devices used on the Part III chemical recovery combustion sources listed in Part III Attachment 1.

Instruction:

Provide for all entries. This should match NEI Site ID used in Part II.

Enter APCD_ID matching the PIII Equip detail tab

Enter Emission Unit ID or Collection system ID matching the Equip detail tab.

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 III emission sources (such as semi-chemical liquor combustors) 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 the auxillary fuel type used in the thermal oxidizer (i.e., fuel other than the organic emissions controlled by the thermal oxidizer)

Enter the auxillary fuel heat input. An approximation based on the average from 2009 or a target value will suffice.

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) if used to control any Part III emission sources. 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 PIII 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 recirculated 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)

Auxillary fuel type

Approximate auxillary fuel use, MMBtu/hr

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

Coen

pre-1990

4

98

90

Methanol

Single-stage combustion chamber

NA

1300

1.8

natural gas

0.3

no

NA

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)

22,000

1999

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)

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Sheet 4: PCC

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.
Instruction:	Provide for all entries. This should match NEI Site ID used in Part II.	Enter Emission Unit ID routing exhaust to the PCC plant. This should match the Emission Unit ID in the PIII Equip detail tab.	Select yes/no	If answer to the previous question is no, please explain if exhaust does not pass through the full emission control system prior to being routed to the PCC plant.	Enter numeric value. Use the average from 2009 or a target value.	This will be 1 (for 100%), unless if the exhaust stream in split such that only a portion of the volume goes to the PCC plant. Enter decimal percent (e.g., enter "0.15" for 15%). Use the average from 2009 or a target value.	Specify	Select yes/no	Answer "yes" unless the PCC plant is included in your title V permit	Optional. Enter any comments you have on the data supplied.
Survey reference:
Field:	NEI Site ID	Emission Unit ID routing exhaust to a PCC plant	Does exhaust pass through the emission unit air pollution control device(s) prior to being routed to PCC plant?	If no, explain control configuration relevant to the exhaust stream routed to the PCC plant	hr/yr exhaust routed to PCC plant	Volume percent of exhaust stream routed to PCC plant	Owner of PCC plant	Is PCC plant located on P&P mill property	Does the PCC plant have a separate air permit from the P&P mill?	Comments
Example entry:	99999	LK1	yes		1500	0.15	Carbonate Minerals, Inc	no	yes
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Sheet 5: PIII 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
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 2 of the Part III survey instructions 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 PIII Equip detail tab.	Leave columns that do not apply for a given emission unit blank. Specify the collection system if applicable. Collection system IDs should match those used in other tabs such as the PIII Equip detail tab. (Note: Unlike in Part I, few (if any) collection systems are expected to be reported for Part III emission units.)	Provide the APCD used during the emissions test. APCD_IDs should match those used in other tabs such as the PIII Equip detail tab (unless equipment configuration has changed).	Enter combustion controls used during the emission test (e.g., combustion modifications/controls specified in the PIII 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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