# Completion of the tabs in this spreadsheet isOPTIONAL.

Any cost information that you provide would be very useful to EPA for purposes of evaluating the costs of control measures that may be considered as regulatory options. Cost information from within the last 10-12 years is requested (e.g., costs dating back to 1998). Cost information could come from vendor quotes for APCD or equipment changes that either have been implemented or were not implemented.

The EPA recognizes that cost information can be sensitive. You may claim any information provided in this spreadsheet as confidential business information (CBI) and EPA will handle the information accordingly. The EPA's procedures for handling CBI are described in the letter that accompanied the pulp and paper information collection request (ICR). If your spreadsheet response contains any CBI, please be sure to follow the instructions in section C2 of the survey instruction document for submitting CBI.

Two tables are included in this spreadsheet: APCD costs, and Equip change costs

The EPA is particularly interested in costs of the following air pollution control devices (APCD). Please supply this information using the**APCD costs**template

**.** - Controls that reduce HAP emissions from wastewater handling and treatment systems - Bleach plant CO control devices - Paper machine HAP emissions capture and control systems

The EPA is particularly interested in costs of the following process changes or equipment changes/upgrades. Please supply this information using the**Equip change costs**template

**.** - Process changes that reduce HAP emissions from wastewater handling and treatment systems - Process changes to improve lime mud washing or to control makeup water quality in the causticizing area - Process changes that reduce paper machine HAP emissions

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

**Expiration Date: 2/28/2014**  **Did you consider the entire contents of this spreadsheet tab to be CBI?** If yes, be sure to shade the CBI-containing cells red and submit this spreadsheet according to the section C of the survey overview document.

Complete the table below for air pollution control devices (APCD) installed/retrofitted in 1998 or later. **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 other portions of your survey response. Enter Emission Unit ID(s) controlled by the APCD Enter APCD_ID for which cost information is being provided Was the APCD retrofitted on an existing emission unit? Select yes/no Was the APCD installed at the same time the emission unit was newly installed? Select yes/no Identify the expected equipment life of the installed control device. This should be provided in years and estimated from the initial date of installation. **CAPITAL COSTS**

Year of the capital costs (e.g., 2006). EPA will use to scale costs to the current year used for regulatory analyses. Include in the Purchased Equipment Costs the cost of control device and any required ancillary equipment (e.g., fans, pumps, ductwork), instrumentation, sales tax, and freight. Calculated by summing items in B Calculated by summing items in C

**Survey overview reference: A.** Purchased Equipment Costs **B.**Direct Installation Costs **C**. Indirect Costs

**Field: NEI Site ID**  **Emission Unit ID APCD_ID**  **Retrofit to existing emission unit? Installation on new**  **emission unit? Expected control device**  **equipment life (in yrs) Base year for capital costs (XXXX)**  **Purchased Equipment Costs, Total ($)**  **Foundation and supports, $**  **Handling and**

**erection, $ Electrical, $**  **Piping, $ Insulation for**  **ductwork and piping, $**  **Painting, $ Other, $**  **Description of other Total Direct**  **Installation Costs, Total $**  **Engineering Construction**  **and field**

**expenses Contractor fees**  **Start-up Performance test**  **Contingencies Total Indirect Costs, Total $**  **Example entry:** 99999 RF1 SCRB1 yes no 15 2001 583,800 700,500 1,335,000 58,000 1,751,000 58,000 25,000 3,927,500 500,000 584,000 584,000 58,000 36,000 175,000 1,937,000 99999 RF1 SNCR1 yes no 20 2001 2,817,000 0 140,000 141,000 141,000 78,000 500,000 99999 LK1 ESP1 yes no 20 2001 1,498,000 59,900 748,700 119,800 15,000 29,900 30,000 1,003,300 300,000 295,000 150,000 15,000 15,000 75,000 850,000 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

APCD costs 0900006480f7efd2.xls 1 of 3**OMB Control No:**

**Expiration Date:**

Complete the table below for air pollution control devices (APCD) installed/retrofitted in 1998 or later. **UK = Unknown** 

.**NA = Not Applicable**

**Instruction:**

**Survey overview reference:**

**Field: Example entry:** 

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 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 TOTAL Capital Investment (TCI) = (A + B + C)

Calculated OPERATING COSTS

Year of the operating costs. Operating costs should be provided for the last 12 month period (calendar or fiscal year) for which the mill has Please identify any major maintenance materials or parts and specify the approximate annual expenditures per item used for the APCD. Specify total annual labor hours and $/hr Calculated Purchased electricity costs (specify kWh/yr and $/kWh) Calculated Purchased water usage Calculated Specify if natural gas

or propane used (select from menu). Specify

scf/yr and $/scf. Calculated Steam costs (specify lb

per year and $/lb) Calculated List any additives, chemicals, or sorbents needed to operate the APCD Enter the amount of additive, chemical, or sorbent used. Include units. If multiple types are used, enter the amount separated by commas (e.g., NaOH-4 tpy, KMnO4-0.5 tpy) Enter estimated annual costs for any additives, chemicals, or sorbents needed to operate the APCD **TOTAL Capital Investment (TCI)**  **D.**Maintenance materials and replacement parts **E.**Operation/maintenance labor costs **F.**Utility costs **G. Additive/chemical/sorbent costs**

**TOTAL Capital Investment, Total $**  **Base year for operating costs (XXXX)**  **Item 1 description Item 1 cost,**  **$/yr Item 2** 

**description Item 2 cost,** 

**$/yr Item 3** 

**description Item 3 cost,** 

**$/yr Item 4** 

**description Item 4 cost, $/yr**  **Annual maintenance**  **labor hours Maintenance labor** 

**rate, $/hr Annual**  **labor costs, $/yr**  **Electricity,**

**kWhr/yr Electricity** 

**rate, $/KW Annual** 

**electricity costs, $/yr**  **Water, gal/yr Water rate,**  **$/gal Annual water** 

**costs, $/yr Fuel used**  **Amount used,**  **scf/yr Fuel rate,** 

**$/scf Annual fuel** 

**costs, $/yr Steam** 

**use, lb/yr Steam rate,** 

**$/lb Annual steam** 

**costs, $/yr Waste treatment or disposal costs,** 

**$/yr Additive/chemical/sorbent type**  **Additive/chemical/sorbent amount Additive/chemical/sorbent costs, $/year**  6,448,300 2001 Various parts 53,000 1,050 25.4 26,670 10,963,120 0.05 548,156 74,592,000 0.00058 43,263.36 3189.6450% caustic soda 380,000 gal/yr 390,000 3,317,000 2001 Parts 178,980 1,050 25.4 26,670 92,740 0.05 4,637 1,512,000 0.00058 877 urea 256 tpy 57,600 3,351,300 2001 Materials 101,000 800 25.4 20,320 1,571,700 0.05 78,585

APCD costs 0900006480f7efd2.xls 2 of 3**OMB Control No:**

**Expiration Date:**

Complete the table below for air pollution control devices (APCD) installed/retrofitted in 1998 or later. **UK = Unknown** 

.**NA = Not Applicable**

**Instruction:**

**Survey overview reference:**

**Field: Example entry:** 

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 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 Enter estimated annual costs for disposal of any additives, chemicals, or sorbents needed to operate the APCD Other operating cost description TOTAL Operating Costs = sum of D through I $/yr

Calculated

**H. Additive/chemical/sorbent disposal I. Other**  **TOTAL Operating Costs**

**Additive/chemical/sorbent disposal, $/yr Describe other operating**  **cost Other, $/yr**  **TOTAL Operating Costs, $** 16,000 Liquid analysis 1,800 1,082,079 268,764 199,905

APCD costs 0900006480f7efd2.xls 3 of 3**OMB Control No: 2060-0656**  **Did any of the responses (individual cells) you entered in this tab contain CBI? Expiration Date:**  **2/28/2014 Did you consider the entire contents of this spreadsheet tab to be CBI?**  If yes, be sure to shade the CBI-containing cells red and submit this spreadsheet according to the section C of the survey overview document.

Complete this table for any modifications to processes or equipment in the chemical recovery area (other than installation of new APCD's) that were made in 1998 or more recently to reduce air emissions of HAP/organics, PM, NOx, SO2, CO, or TRS or to improve combustion efficiency. **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 other portions of your survey response. Enter a description of process or equipment change for which information is being provided Enter Emission Unit ID(s) affected by the process or equipment change Enter APCD_ID affected by the

process or equipment change Was the process or

equipment change implemented on existing emission units and/or APCD in the process line? Select yes/no Was the APCD installed at the same time the emission unit was newly installed? Select yes/no Enter the year (e.g., 2006). This will be used as the base year for scaling of costs to current levels. Enter number of days of lost pulp production required to implement the process or equipment change.

If the change occurred during scheduled downtime that would have occurred regardless of the process or equipment change, then do not include the scheduled downtime. Only the days of lost production that can be specifically attributed to the process or equipment change are of interest. Please distinguish between one-time capital and annual operating costs where appropriate. If a breakdown of the specific capital or annual cost items is available, please provide as a separate attachment.

Enter the total capital cost associated with the process or equipment change in this cell. Provide changes in annual operating costs (if estimated). Otherwise, leave blank.

Include annual operating costs that are an increase to prior operating costs (e.g., additional operating costs due to addition of ESP fields).

If the process or equipment change resulted in decreased annual operating costs, then indicate the cost decrease as a negative number. Describe the air pollutants affected and emissions reduction achieved. indicate the basis for emissions reduction reported (e.g., air emissions testing before and after modification). You may provide this information as a separate attachment to your response if it does not fit here. **Survey overview reference:**

**Field: NEI Site ID**  **Process or equipment change description Emission Unit ID**  **APCD_ID Retrofit to existing**  **equipment in an existing process line?**  **Change implemented in a new process**  **line? Year of process or equipment change**  **(XXXX) Number of days process shut down in order to make**  **the change (days of lost production) Total capital cost, $**  **Total annual operating cost, $/yr Emission reduction achieved (if quantified)**  Example entry: 99999 Changing from a DCE to NDCE recovery furnace RF2 yes no 2001 20 19664100 187350gaseous organic HAP - 80% 99999 Changing from a wet to a dry bottom ESP RF1 ESP1 yes no 2001 3 3266300 88000 Methanol - 48% 99999Adding fields to an existing ESP RF1 ESP1 yes no 2001 3 5372400 214000 PM -66%

99999 Installation of quarterary air ports in the recovery furnace to improve combustion efficiency RF1 yes no 2001 3 624140 39800 NOx - 20% 99999 Replacing a recovery furnace with a black liquor gasification system RF2 yes no 2001 90 150000000 -16340100 HAP-98%; PM-92% 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

Equip change costs 0900006480f7efd2.xls 1 of 1