Date: April 22, 2013

Subject: Emissions Test Data for the Kraft Pulp Mill NSPS Review

EPA Contract No. EP-D-11-084; Work Assignment No. 1-08

From: Katie Hanks

To: Kelley Spence and Bill Schrock

U.S. Environmental Protection Agency

Research Triangle Park, NC 27711

I. Introduction

Under section 111(b)(1)(B) of the Clean Air Act (CAA), the U.S. Environmental 

Protection Agency (EPA) is required to review and, if appropriate, revise existing new source 

performance standards (NSPS) at least every 8 years. The NSPS for kraft pulp mills (40 CFR 

part 60, subpart BB) were promulgated in 1978 and last reviewed in 1986, and are due for 

another review. On December 6, 2011, the Center for Biological Diversity, Greenpeace, and Port 

Townsend AirWatchers filed a complaint with the U.S. District Court for the Northern District of 

California to compel the EPA to review the kraft pulp mills NSPS as directed under CAA section 

111(b)(1)(B). The EPA has entered into a consent decree with petitioners, specifying proposal of 

the NSPS review by May 15, 2013 and promulgation by March 14, 2014. See docket ID number 

EOA-HQ-OGC-2012-0730 for a copy of the consent decree.

The kraft pulp mill NSPS regulate emissions of particulate matter (PM) from new, 

modified, and reconstructed recovery furnaces, smelt dissolving tanks (SDTs), and lime kilns at 

kraft pulp mills. The NSPS also regulate emissions of total reduced sulfur (TRS) compounds 

from new, modified, and reconstructed digesters, brown stock washers, multiple-effect 

evaporators, condensate strippers, recovery furnaces, SDTs, and lime kilns at kraft pulp mills. 

Total reduced sulfur compounds are defined under 40 CFR 60.281(c) of the kraft pulp mills 

NSPS to include the following four compounds: hydrogen sulfide (H2S), methyl mercaptan 

(CH4S), dimethyl sulfide ((CH3)2S), and dimethyl disulfide ((CH3)2S2).

In February 2011, the EPA initiated a three-part Information Collection Request (ICR) to 

gather information from U.S. pulp and paper manufacturers needed to conduct various CAArequired regulatory reviews, including the kraft pulp mill NSPS review. Emissions test data, 

including stack test reports and continuous emissions monitoring system (CEMS) data were 

submitted with Parts I and III of the ICR.1 Stack test data and/or CEMS data were requested for 

filterable PM, filterable PM2.5, condensable PM, and TRS. Continuous opacity monitoring 

system (COMS) data were also requested. Test data for additional pollutants and processes 

outside the scope of the kraft pulp mill NSPS (40 CFR part 60, subpart BB) were also requested, 

and will be reviewed at a later date. 

 1 Part II of the ICR involved updates to pulp and paper mills’ National Emissions Inventory data 

sets, but did not involve submission of stack test or CEMS data.
2

The purpose of this memorandum is to summarize the approach for reviewing the stack 

test reports submitted to EPA with the ICR responses that were used in reviewing the existing 

kraft pulp NSPS. To date, the stack test data tabulation and review has included only those 

pollutants and processes relevant for the NSPS review, specifically: 

• PM from recovery furnaces, SDTs, and lime kilns

• TRS from SDTs

No PM CEMS data were received. A separate memorandum discusses evaluation of the COMS 

data received for recovery furnaces and lime kilns, and the TRS CEMS data received for 

recovery furnaces, lime kilns and non-condensable gas (NCG) emission sources. (EPA 2013)

Section II of this memorandum discusses the general approach used to tabulate stack test 

data, and Section III lists references. The tabulated test data are provided in appendices A 

through D. Appendices A through C contain PM data for recovery furnaces, lime kilns, and 

SDTs respectively. Appendix D contains TRS data for SDTs.

II. General Approach to Tabulating Stack Test Data

This section describes how the emissions test reports collected with the ICR responses 

were prioritized for review, how data were extracted from the test reports, the quality assurance 

and quality control (QA/QC) measures employed, and how the PM and TRS test data were 

tabulated.

A. Prioritizing Stack Test Data Received with the ICR

The majority of emissions test reports relevant for the NSPS review were submitted with 

responses to Part III of the ICR in August 2011, though a few of the reports were submitted 

earlier with response to Part I of the ICR in April 2011. Part III of the ICR focused on chemical 

recovery combustion sources, such as recovery furnaces, SDTs, and lime kilns. The ICR 

requested PM data for recovery furnaces, SDTs, and lime kilns dating back to 2001 (the 

compliance date for 40 CFR part 63 subpart MM) and the most recent TRS stack test data. The 

ICR respondents were asked: (1) to submit copies of full emission test reports (i.e., with field and 

lab data sheets and example calculations); and (2) to complete a spreadsheet table listing the 

processes and pollutants included in each test report submitted, the test method used, test year, 

air pollution control device (APCD), and whether the configuration of the emission unit had 

changed since the emissions test was performed. 

The test report lists (item 2 above) from each ICR response were compiled in a data base 

(PIII_Emissions_test_data table) and used to prioritize which emissions test reports to tabulate

for the NSPS review. Obtaining an exact count of the pollutants and processes for which test 

reports were submitted through the ICR is complicated by the fact that many test reports include

a mixture of processes and pollutants tested, though some processes may only have been tested 

for a particular pollutant. Some mills included such multi-pollutant and multi-process test reports 

on a single row in the test report list (item 2 above) used to compile the PIII_Emissions_test_data 
3

table, making an exact count impossible without looking at each test report.

2 Nevertheless, the 

PIII_Emissions_test_data table provided sufficient information to prioritize stack test data for 

tabulation and obtain a good indication of the volume of stack test data submitted with the ICR 

responses. The following are approximate counts of PM and TRS stack test results available by 

process subject to the NSPS:

• 730 recovery furnace PM tests (including both direct-contact evaporator (DCE) and nondirect contact evaporator (NDCE) recovery furnaces)

• 650 lime kiln PM tests

• 620 SDT PM tests

• 220 SDT TRS tests

RTI anticipates performing a more robust count of the emissions test results by process and 

pollutant at a later date (as project timelines allow).

Given the large (and somewhat unanticipated) volume of stack test reports received with 

the ICR responses (particularly for PM), it was necessary to prioritize test reports for tabulation 

to meet the court-ordered NSPS review project timeline. The nationwide list of recovery 

furnaces, SDTs, and lime kilns and their controls provided in the Part III ICR data base was used 

to help prioritize stack tests for tabulation for the NSPS review. Each emission unit in the Part III 

ICR data base was reviewed to determine its generic process type, such as Lime Kiln, SDT 

(Kraft), DCE, or NDCE. Next, standardized control device codes were assigned based on the 

type of control device reported in the ICR responses. Table 1 below lists the control device codes

relevant for NSPS sources.

Table 1. Standardized Control Device Codes Applicable for NSPS Sources

Control device codes Description

SCBR scrubber

PBSCBR packed-bed scrubber

DBESP recovery furnace dry-bottom ESP

DBESP-WPR recovery furnace dry-bottom ESP with wet PM return system

WBESP recovery furnace wet-bottom ESP

ESP electrostatic precipitator

OTH other – refers to mist eliminators on SDTs

In addition to the controls listed in Table 1, there are combinations of controls (e.g., ESP/SCBR) and two 

unique recovery furnace controls include a furnace with three parallel ESPs (a DBESP-WPR and two 

DBESPs) DBESP-WPR/DBESP/DBESP and a two-sided dry-bottom and wet-bottom ESP (DB-WBESP 

[2-sided dry and wet]).

These standardized codes were included in the PIII_Emissions_test_data table in order to 

pair test reports with a standardized emission unit and control device type. Next, the test years 

for each type of emission unit and control device were considered. In general, the most recent

test for each emission unit was tabulated in order to ensure coverage and understand variability 

 2 For example, a 2010 report for one mill may have noted 2 recovery furnaces, 2 lime kilns, and 

2 SDTs tested for PM, NOx, SO2, and TRS, when in fact, the test may have included PM and 

NOx for recovery furnaces, SO2 for lime kilns, and TRS for SDTs (not all of the listed pollutants 

for every process).
4

within the U.S. population of emission units. Additional data were compiled for emission units 

with controls of interest (e.g., ESP-scrubber combinations on recovery furnaces and lime kilns, 

ESPs on lime kilns) in order to understand emissions variability for each unit and determine the 

performance of these systems.

B. Extraction of Stack Test Data into a Test Data Spreadsheet

The stack test data of interest for the NSPS review were extracted from the test reports 

into a test data spreadsheet by RTI staff and RTI’s subcontractor, VEETech. Appendix A at the 

end of this memorandum lists and describes the parameters extracted into the test data 

spreadsheet from each test report and provides the test data spreadsheet structure. The emissions 

test data spreadsheet includes:

• General information from the ICR, such as the test report file name, identification codes, 

emission unit type, APCD type, pulping process, and whether configuration changes have 

occurred since testing. The PIII_Emissions_test_data table was used as the basis for 

much of this information (which was separated into rows according to test date for each 

process stack and pollutant tested).

• Test report information, such as a description of the emission unit and stack tested, fuel 

burned during the test, test date, test method used, and whether other data are provided in 

the test report (for tabulation at a later date)

• Emission unit production rate. Preferred units of measure needed for consistency in 

emission factors were tons of black liquor solids per hour (tons BLS/hr) for recovery 

furnaces and SDTs and tons of lime (calcium oxide) product per hour (tons CaO/hr) for 

lime kilns.

• Inlet and outlet emissions test results, including sampling time; isokinetic sampling rate; 

air flow in actual cubic feet per minute (acfm) and dry standard cubic feet per minute 

(dscfm); stack gas moisture percent, temperature (°F), stack pressure (in. Hg), oxygen 

(O2) percent, carbon dioxide (CO2) percent, pollutant concentration (parts per million 

[ppm] or grains per dscf corrected to 8 percent O2 for recovery furnaces and 10 percent

O2 for lime kilns); pollutant mass emission rate (pounds per hour [lb/hr]); pollutant 

emission factor (pounds per unit of production); and number of test runs and number of 

non-detect test runs.

• Pollutant removal efficiency for any inlet-outlet tests.

• Test report comments and any notes pertaining to suspect data that may need to be 

excluded from analyses.

The data in the emission test spreadsheet are based on test averages (e.g., the average of 

three test runs for a three-run test). Test average parameters were calculated, as needed, from the 

run-by-run data in each test report if test averages were not provided in the test report. However, 

run-by-run data were not tabulated for purposes of NSPS review analyses.

Test data were extracted in batches, by emission unit type initially, beginning with tests 

on emissions units anticipated to have the best-performing controls and then expanding to all 

emission units (to observe mill-to-mill and unit-to-unit variability) and additional tests of 

emission units with selected controls (in order to observe test-to-test variability). Batches of test 
5

data were entered until the project timeline necessitated cessation of data entry and beginning of 

NSPS review data analyses.

The fuel type or mix burned in an emission unit such as a lime kiln can change over time. 

Only the fuel types noted in the test reports were provided in the emissions test data base so the 

test results would be representative of the fuel type combusted during the test. If a fuel type 

during the test was not specified, then “unspecified” was entered for the fuel type. It was 

common for auxiliary fuel type to be unspecified for recovery furnaces because recovery 

furnaces typically only combust fossil fuels during startup or shutdown or intermittently to 

sustain combustion conditions. Black liquor solids are combusted during normal operations.

Tests of emissions units with multiple stacks were entered on separate rows, one for each 

stack. Multiple stacks were more common for recovery furnaces than for lime kilns or SDTs. 

The concentration data from each stack was kept separate for comparison to the NSPS 

concentration emission limit (e.g., gr/dscf @ 8% O2 for recovery furnaces). However, the mass 

emission rates (lb/hr and lb/production) for emission units with multiple stacks were added in a 

separate column to provide the total mass emission rate from the emission unit for further 

analysis. These records were labeled as “separate stacks” in the test data spreadsheet.

Some emission units were tested under multiple conditions. These emissions were labeled 

as “separate conditions” in the test data spreadsheet so their results could be tabulated properly in 

NSPS analyses (e.g., the results were averaged together when arriving at a single performance 

level for each emission unit for purposes of the baseline and impacts analyses [RTI 2013a]; 

however, the results from separate conditions were graphed separately in technology review

analyses [RTI 2013b]).

C. Quality Assurance and Quality Control (QA/QC)

Emissions test data were extracted from the appendices of the emissions test reports as 

opposed to the summary pages whenever feasible. It is important to note that this initial review 

and extraction of emissions test data from test reports did not include an in-depth look at field 

and laboratory procedures to evaluate the degree to which prescribed methods have been 

followed. For purposes of this review, it was assumed that testing contractors and analytical 

laboratories have followed the procedures of the methods that have been indicated in the test 

reports.

Nevertheless, QA/QC was performed on the stack test data entered into the test data 

spreadsheet in preparation for data analyses to identify and correct any obvious calculation errors 

in the test reports, screen for data entry errors, properly label blanks, identify and recheck any 

outliers, check calculations, ensure consistency in reported test methods and units of measure for 

a given emission unit type and pollutant, identify emissions test reports that should be excluded 

from analyses, and note duplicate tests of the same emission unit for special treatment. Most of 

this QA was accomplished by grouping data for like units and looking at data ranges provided to 

spot inconsistencies in the reported data.
6

Emission units were labeled with concatenations of the RTI Code plus Emission Unit ID, 

and RTI Code plus Emission Unit ID plus Pollutant to search for duplicate emissions tests of the 

same emission unit. As noted previously, emission units that had multiple stacks or that were 

tested under separate conditions were common reasons for duplicate emissions tests, as were 

emissions tests for the same pollutant performed in multiple years.

For PM tests, the ioskinetic sampling rate was reviewed to ensure it fell between 90 and 

110 percent. When reviewing test reports, the filter temperature readings for PM stack tests

recorded on field data sheets were checked to ensure the filter temperature was within the 248° ± 

25°F window specified in EPA Method 5. The filter temperature was not tabulated in the test 

data spreadsheet because the majority of tests provided hand-written raw temperature readings 

but did not provide an average of the filter temperature readings.

The total number of test runs and number of non-detect runs below the method detection 

limit (MDL) was considered. None of the PM test runs for recovery furnaces, lime kilns, or 

SDTs were non-detect, so treatment of MDLs was not an issue. For TRS from SDTs, some 

specific TRS compounds (e.g., methyl mercaptan, dimethyl sulfide, or dimethyl disulfide) were 

below the detection limit in Method 16, but the total TRS value was above the detection limit in 

all TRS tests (including Method 16 and Method 16A/B/C tests). Concentration values for nondetect compounds were treated as zero in the Method 16 tests where only selected compounds 

were non-detect. 

D. Particulate Matter Test Data for Recovery Furnaces, SDTs, and Lime Kilns

The current NSPS are based on filterable PM measured with EPA Method 5 or Method 

17. Filterable PM stack test data for the NSPS review were compiled for DCE and NDCE 

recovery furnaces, SDTs, and lime kilns. The filterable PM data evaluated for the NSPS review 

were measured with EPA Method 5. Subpart BB also allows use of EPA Method 17, but no 

Method 17 PM data were provided by ICR respondents in the test reports reviewed. Some mills 

used Oregon Department of Environmental Quality Method 5 (ODEQ Method 5) in addition to 

or instead of EPA Method 5. In some cases, test data were labeled as both (e.g., EPA/ODEQ 

Method 5). Preference was given to using EPA Method 5 data over ODEQ data, but ODEQ data 

were used if no EPA Method 5 data were available. The ODEQ tests were included in the data 

set for the NSPS review but were labeled as possibly suspect.

Test data for forms of PM other than filterable PM were observed in some of the test 

reports and may be useful for future analyses outside the scope of the current NSPS review. 

Some test reports contained condensable PM data, based on measurements made using EPA 

Method 202 and its predecessor EPA OTM 28, or the back half to ODEQ Method 5. Total PM 

emissions data (filterable + condensable), based on measurements made using Method 5/Method 

202, Method 5/OTM 28, or EPA/ODEQ Method5 front and back half, were noted in some test 

reports. Also, two total PM10 tests (filterable PM10 + condensable), based on measurements 

made using Method 201A/Method 202 tests, were noted in the ICR responses. Additional data 

are likely available in the test reports submitted with the ICR responses, but as described above, 

a detailed accounting of the test data submitted would be helpful in determining whether enough 

data for PM fractions other than filterable PM are available for detailed regulatory analyses. 
7

In addition to the mass emissions data tabulated in lb/hr, the filterable PM data were also 

tabulated in the following units of measure:

Emission unit type: Concentration units: Emission factor units:

Recovery furnaces gr/dscf @ 8% O2 consistent 

with the NSPS limit

lb/ton BLS

SDTs gr/dscf (uncorrected for O2) lb/ton BLS consistent with the 

NSPS limit

Lime kilns gr/dscf @ 8% O2 consistent 

with the NSPS limit

lb/ton CaO

Production data for the recovery furnace discharging smelt into the SDT (tons BLS per 

hour) are required to obtain SDT PM emissions analogous to the lb/ton BLS NSPS limit. Test 

reports lacking production data or lacking production data in the desired units were tabulated but 

were not used in reevaluating the SDT PM limit (e.g., the lb/ton BLS emission factor was labeled 

as “unspecified”).

E. Total Reduced Sulfur Test Data

Subpart BB requires an initial TRS stack test for recovery furnaces, SDTs, and lime kilns. 

Ongoing compliance with the NSPS TRS limits for these emission units is based on continuous 

emissions monitoring for recovery furnaces and lime kilns, and scrubber parameter monitoring 

for SDTs. With the 2011 ICR, EPA collected 1 year of TRS CEMS data for nearly every 

recovery furnace and lime kiln in the U.S., including recovery furnaces and lime kilns that are 

not yet subject to NSPS but are required to continuously monitor TRS emissions by their State 

(as suggested in the TRS emission guidelines published by EPA in 1979). (EPA 1979) Few TRS 

stack test reports were submitted through the ICR in comparison to the volume of TRS CEMS 

data submitted for recovery furnaces or lime kilns. Thus, it appears that most mills are using TRS 

CEMS data as opposed to repeat stack testing to demonstrate ongoing compliance with the TRS 

emission limits for recovery furnaces and lime kilns; therefore, CEMS data were used to 

reevaluate the NSPS limits as part of the current NSPS review, and the relatively few recovery 

furnace and lime kiln TRS stack test reports were not tabulated. A separate memorandum 

presents the TRS CEMS data for recovery furnaces and lime kilns. This memorandum also 

presents TRS CEMS data received for non-condensable gas (NCG) sources. (EPA 2013) 

Continuous emissions monitoring systems (CEMS) are not required for SDTs. Numerous 

SDT TRS stack test reports were submitted with the ICR responses relative to the number 

submitted for recovery furnaces and lime kilns. Therefore, TRS stack test data were tabulated 

and used to reevaluate the NSPS TRS limit for SDTs.

The current NSPS limit is in terms of pounds of TRS as H2S per ton of black liquor solids 

(lb as H2S/ton BLS). Production data for the recovery furnace discharging smelt into the SDT

(tons BLS per hour) are required to obtain SDT TRS emissions in the format of the NSPS limit. 

Test reports lacking production data or lacking production data in the desired units were 

tabulated but were not used in reevaluating the NSPS emission limits (e.g., the lb as H2S/ton 

BLS emission factor was labeled as “unspecified” if the required production data were 

unavailable).
8

The NSPS defines TRS as the sum of four specific compounds (H2S, MeSH, DMS, and 

DMDS), as measured by EPA Method 16. Methods 16A and 16B are allowed as alternatives to 

Method 16. More recently, Method 16C has been promulgated as an alternative to Method 16. 

(77 FR 44488, July 30, 2012) Method 16 measures all four TRS compounds. Methods 16A 

through 16C measure TRS as SO2. The ppm concentration returned by each of the methods is 

equivalent to “as S,” though it was reported by test companies as ppm, ppm as S, ppm as SO2, 

ppm as H2S, etc., all of which have one sulfur molecule. Common TRS abbreviations from test 

reports are noted in Table 2 below, along with their respective molecular weights.

Table 2. TRS Nomenclature and Molecular Weight

TRS compound Abbrev. Formula Molecular Weight

Dimethyl sulfide DMS (CH3)2S 62.13

Dimethyl disulfide DMDS (CH3)2S2 94.2

Methyl mercaptan MM CH3SH 48.11

Hydrogen sulfide H2S H2S 34.08

Measured with EPA Method 16 - TRS dry ppm determined as S as follows:

ppm TRS = ppm H2S + ppm CH3SH + ppm (CH3)2S + [2 x ppm (CH3)2S2]

It was necessary to ensure that SDT TRS data were reported “as H2S” for comparison to

the NSPS limit. Equations in the test report were reviewed to determine if the H2S molecular 

weight was used in mass emission rate calculations. Separate calculations using the H2S 

molecular weight to convert to lb/hr from ppm were also used to test whether mass emissions 

were provided on an “as H2S” basis.
9

III. References

EPA 1979 U.S. Environmental Protection Agency. Kraft Pulping: Control of TRS 

Emissions from Existing Mills. Publication No. EPA-450/2-78-003b. 

March 1979.

EPA 2013 Spence, K., U.S. Environmental Protection Agency. Review of the 

Continuous Emission Monitoring and Continuous Opacity Monitoring 

Data from the Pulp and Paper Information Collection Request Responses 

Pertaining to Subpart BB Sources. Memorandum to Docket ID No. EPAHQ-OAR-2012-0640. April 5, 2013.

RTI 2013a T. Holloway and K. Hanks, RTI International. Emissions Inventory for 

Kraft Pulp Mills and Costs/Impacts of the Section 111(b) Review of the 

Kraft Pulp Mills NSPS. Memorandum to K. Spence and B. Schrock, U.S. 

EPA. February 4, 2013.

RTI 2013b K. Hanks and T. Holloway, RTI International. Technology Review and 

Regulatory Options for the Kraft Pulp Mill NSPS. Memorandum to K. 

Spence and B. Schrock, U.S. EPA. March 29, 2013.
Appendix A

Particulate Matter Emissions Data for Recovery Furnaces
Appendix A: Pulp and Paper Emissions Test Data Spreadsheet for NSPS Review ‐ Recovery Furnace Filterable Particulate Matter

General Information

Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process T

NEI40686_RTI100_DomtarJohnsonburgMill_MACT II Test Report_July2004.pdf 100 NEI40686 037A 100.037A 100‐‐C037A DBESP Kraft 

NEI9201_DOM No5RB PM Report 4.30.09.pdf 103 NEI9201 G‐158 103.G‐158 103‐‐RBESP DBESP Kraft 2010_PM_Lime_Kiln,_No_4_Rec_and_No_4_Smelt.pdf 105 NEI45182 EU445C 105.EU445C

105‐‐CD 456‐110, CD445‐480,

and CD 445‐447 DBESP‐WPR Tertiary air in #4RB only Kraft, Secondary 

SECTION 2.pdf/ SECTION 7.pdf 107 NEI47074 08‐P1 107.08‐P1 107‐‐08‐E1 DBESP Overfire Air Kraft 

2010 RB3 PM Compliance.pdf 108 NEI33025 RB3 108.RB3 108‐‐ESP DBESP None Kraft 

NEI32869 PR 2008016 OCT 2008.pdf 109 NEI32869A RB3 109.RB3

109‐‐RB3ESP, RB4ESP, ST3SBR,ST4SBR DBESP Kraft 

NEI32869 PR 2008016 OCT 2008.pdf 109 NEI32869A RB4 109.RB4 109‐‐RB4ESP DBESP Kraft 

NEI45206_P&P Survey_2‐2011 Recovery Furnace

& Smelt Dissolvi.pdf 111 NEI45206 G‐44 111.G‐44 111‐‐STWS and ES 455‐001 DBESP‐WPR NA Kraft 

NEI26506_PM_December_2008.pdf 114 NEI26506 U500 114.U500 114‐‐CDU1 DBESP Kraft 

NEI26506_PM_December_2008.pdf 114 NEI26506 U500 114.U500 114‐‐CDU1 DBESP Kraft 

NEI8619_IP Pine Hill Recovery Sept 2010 Stack

Test Report.pdf 116 NEI8619 003 116.003 116‐‐RFESP WBESP

Kraft, Secondary,

SemiChem 

No. 20 No. 21 Rec Funr Nov Dec 2010.pdf 119 NEI46814 EQT008 119.EQT008 119‐‐ESP008 DBESP Kraft, Secondary 

Emission Tests Report No. 21 Jan 2010.pdf 119 NEI46814 EQT010 119.EQT010 119‐‐ESP010 DBESP Kraft, Secondary 

No. 20 No. 21 Rec Funr Nov Dec 2010.pdf 119 NEI46814 EQT010 119.EQT010 119‐‐ESP010 DBESP Kraft, Secondary 

Recovery Furnace PM Emissions Test

Report_NEI26495.pdf 120 NEI26495 F7 120.F7 120‐‐ESP5 DBESP Kraft 

0910‐29 RB1.pdf 124 NEI8278 001 124.001 124‐‐ESP 001 DBESP Kraft 

0910‐29 RB1.pdf 124 NEI8278 001 124.001 124‐‐ESP 001 DBESP Kraft 

NEI 42317 Hopewell VA Dec 2009 RF TSP, TRS and

SO2.pdf 126 NEI42317 RECOV 126.RECOV 126‐‐RecESP WBESP Kraft 

NEI 42317 Hopewell VA Dec 2009 RF TSP, TRS and

SO2.pdf 126 NEI42317 RECOV 126.RECOV 126‐‐RecESP WBESP Kraft 

NEI 42317 Hopewell VA Dec 2009 RF TSP, TRS and

SO2.pdf 126 NEI42317 RECOV 126.RECOV 126‐‐RecESP WBESP Kraft 

NEI 42317 Hopewell VA Dec 2009 RF TSP, TRS and

SO2.pdf 126 NEI42317 RECOV 126.RECOV 126‐‐RecESP WBESP Kraft 

NEI7933_PIII ‐ Recovery Boiler (North and South

Stacks) ‐ PM ‐ April 6, 2011.pdf 127 NEI7933 REC1N 127.REC1N 127‐‐E101A WBESP Kraft, Secondary 

NEI7933_PIII ‐ Recovery Boiler (North and South

Stacks) ‐ PM ‐ April 6, 2011.pdf 127 NEI7933 REC1N 127.REC1N 127‐‐E101A WBESP Kraft, Secondary 

NEI 42254 RockTenn WP Stack Tests.pdf 131 NEI42254 6 131.6 131‐‐CR05CD DBESP Kraft, Secondary 

NEI 42254 RockTenn WP Stack Tests.pdf 131 NEI42254 5 131.5 131‐‐CR01CD DBESP Kraft, Secondary 

NEI 42254 RockTenn WP Stack Tests.pdf 131 NEI42254 5 131.5 131‐‐CR01CD DBESP Kraft, Secondary 

NEI 42254 RockTenn WP Stack Tests.pdf 131 NEI42254 5 131.5 131‐‐CR01CD DBESP Kraft, Secondary 

2010 RB5.pdf 132 NEI8261 5RB 132.5RB 132‐‐ESP2 DBESP‐WPR Kraft, Secondary 

2010 RB5.pdf 132 NEI8261 5RB 132.5RB 132‐‐ESP2 DBESP‐WPR Kraft, Secondary 2010 RB4.pdf 132 NEI8261 4RB 132.4RB 132‐‐ESP1 DBESP‐WPR Kraft, Secondary RB4MS inhouse PM Source Tests 2011.pdf 133 NEI13363 10 133.10 133‐‐RB4MS DBESP Kraft 

RB4MS inhouse PM Source Tests 2011.pdf 133 NEI13363 10 133.10 133‐‐RB4MS DBESP Kraft 

Test_data_memo_appendices.xlsx App A RF PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process T

2011 RB & ST PM #103.pdf 135 NEI33118 003‐1 135.003‐1 135‐‐003‐7, 003‐8, 003‐9 DBESP Kraft 

2011 RB & ST PM #103.pdf 135 NEI33118 003‐1 135.003‐1 135‐‐003‐7, 003‐8 DBESP Kraft 

2010 ‐ SDT(PM‐TRS) + RB10(PM‐Hg).pdf 136 NEI12368 EU 005 136.EU 005 136‐‐CE 007 DBESP Kraft 

2010‐09‐15 5RF PM‐NOx Test Report.pdf 137 NEI26581 721 137.721 137‐‐PC(721) DBESP‐WPR Kraft 

2010‐09‐16 4RF PM Test Report.pdf 137 NEI26581 189 137.189 137‐‐PC(189) DBESP‐WPR Kraft PM Recovery Furnace SN‐02 March 2009.pdf 138 NEI18652 002 138.002 138‐‐ESP RB1 DBESP‐WPR Kraft 

RTI1#WAL.pdf 142 NEI41552 CU7214 142.CU7214 142‐‐CD‐7214 DBESP Kraft, Secondary 

NEI26504_RTI143_PCA Valdosta Mill_1,2,3 RB

PM_November 2009.pdf 143 NEI26504 7010 143.7010 143‐‐C013 WBESP Kraft 

NEI26504_RTI143_PCA Valdosta Mill_1,2,3 RB

PM_November 2009.pdf 143 NEI26504 7020 143.7020 143‐‐C015 WBESP Kraft 

NEI759 EUID8 No1RF2011.pdf 146 NEI759 8 146.8 146‐‐RF101 WBESP Tertiary Air Kraft 

NEI759 EUID8 No1RF2011.pdf 146 NEI759 8 146.8 146‐‐RF101 WBESP Tertiary Air Kraft 

MEADWESTVACO SILSBEE, TX MAY 08 # 3 RB

COMPLIANCE REPORT.pdf 147 NEI6450 14 147.14 147‐‐C‐620 DBESP Tertiary Air, Low NOX Burners Kraft 

MEADWESTVACO SILSBEE, TX MAY 08 # 3 RB

COMPLIANCE REPORT.pdf 147 NEI6450 14 147.14 147‐‐C‐620 DBESP Tertiary Air, Low NOX Burners Kraft 

MEADWESTVACO SILSBEE FEB 09 #4 RB COMP

TEST REPORT.pdf 147 NEI6450 5 147.5 147‐‐C‐622 DBESP Tertiary Air, Low NOX Burners Kraft 

MEADWESTVACO SILSBEE FEB 09 #4 RB COMP

TEST REPORT.pdf 147 NEI6450 5 147.5 147‐‐C‐622 DBESP Tertiary Air, Low NOX Burners Kraft 

NEI46931_7 20‐21 10 No. 1 RF & SDT & No. 2 RF

& SDT Compliance Test Report.pdf 148 NEI46931 007 148.007 148‐‐RF2ESP DBESP

Three air streams‐‐primary, secondary & 2

tertiary Kraft, Secondary 

NEI46931_7 20‐21 10 No. 1 RF & SDT & No. 2 RF

& SDT Compliance Test Report.pdf 148 NEI46931 001 148.001 148‐‐RF1ESP DBESP

Three air streams‐‐primary, secondary &

tertiary Kraft, Secondary 

150 NewPage Rumford TRC 2007 Report_CRec

and Smelt Tank_PM.pdf 150 NEI6273 CREC‐1 150.CREC‐1 150‐‐SCRBSTa, SCRBSTb SCBR Kraft, Mechanica

NEI11338_WPC ‐ RF_SDT_LK ‐ Mar 2007.pdf 152 NEI11338 03 152.03 152‐‐03‐ESP, 03‐SCBR WBESP/SCBR Kraft 

NEI11338_WPC ‐ RF_SDT_LK ‐ Mar 2007.pdf 152 NEI11338 03 152.03 152‐‐03‐ESP, 03‐SCBR WBESP/SCBR Kraft 

150 NewPage Rumford TRC 2011 Report_CRec

NOx_SO2 _TRS_Lime K.pdf 155 NEI33883 RECOVERY FURNACE

155.RECOVERYFURNACE 155‐‐RF ESP DBESP quarternary air Kraft, Mechanica

M52010RF22.pdf 156 NEI42338 RF22 156.RF22 156‐‐RF22EP DBESP Electrostatic Precipitator

Unknown (Kraft & 

chem) 

M52010RF22.pdf 156 NEI42338 RF22 156.RF22 156‐‐RF22EP DBESP Electrostatic Precipitator

Unknown (Kraft & 

chem) 

Test_data_memo_appendices.xlsx App A RF PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process T

M52010RF22.pdf 156 NEI42338 RF22 156.RF22 156‐‐RF22EP DBESP Electrostatic Precipitator

Unknown (Kraft & 

chem) 

M52010RF22.pdf 156 NEI42338 RF22 156.RF22 156‐‐RF22EP DBESP Electrostatic Precipitator

Unknown (Kraft & 

chem) 

M52010RF18.pdf 156 NEI42338 RF18 156.RF18 156‐‐RF18EP WBESP Electrostatic Precipitator

Unknown (Kraft & 

chem) 

M52010RF18.pdf 156 NEI42338 RF18 156.RF18 156‐‐RF18EP WBESP Electrostatic Precipitator

Unknown (Kraft & 

chem) 

M52010RF19.pdf 156 NEI42338 RF19 156.RF19 156‐‐RF19EP WBESP Electrostatic Precipitator

Unknown (Kraft & 

chem) 

M52010RF19.pdf 156 NEI42338 RF19 156.RF19 156‐‐RF19EP WBESP Electrostatic Precipitator

Unknown (Kraft & 

chem) 

M52010RF19.pdf 156 NEI42338 RF19 156.RF19 156‐‐RF19EP WBESP Electrostatic Precipitator

Unknown (Kraft & 

chem) 

M52010RF19.pdf 156 NEI42338 RF19 156.RF19 156‐‐RF19EP WBESP Electrostatic Precipitator

Unknown (Kraft & 

chem) 

P_P ICR Part III_RTI162_InternationalPaper‐

EastoverMill_NEI46760_no 1 recovery furnace CO

NOx SO/P_P ICR Part

III_RTI162_InternationalPaper‐EastoverMill_NEI46760_no 1 recovery furnace

particul2/P_P ICR Part

III_RTI162_InternationalPaper‐EastoverMill_NEI46760_no 1 recovery furnace

particul3.pdf 162 NEI46760 381A 162.381A 162‐‐381AESP DBESP Kraft 

P_P ICR Part III_RTI162_InternationalPaper‐

EastoverMill_NEI46760_no 1 recovery furnace CO

NOx SO/P_P ICR Part

III_RTI162_InternationalPaper‐EastoverMill_NEI46760_no 1 recovery furnace

particul2/P_P ICR Part

III_RTI162_InternationalPaper‐EastoverMill_NEI46760_no 1 recovery furnace

particul3.pdf 162 NEI46760 381A 162.381A 162‐‐381AESP DBESP Kraft 

RTI163_International Paper ‐ Prattville

Mill_NEI8560_No 1 Recovery Furnace and Smelt

Dissolving Tanks testing.pdf 163 NEI8560 RF1901 163.RF1901 163‐‐RF1EP1, RF1EP2 WBESP Kraft, Secondary 

RTI163_International Paper ‐ Prattville

Mill_NEI8560_No 2 Recovery Furnace and Smelt

Dissolving Tank testing.pdf 163 NEI8560 RF2904 163.RF2904 163‐‐RF2EP1, RF2EP2 WBESP Kraft, Secondary 

RTI163_International Paper ‐ Prattville

Mill_NEI8560_No 2 Recovery Furnace and Smelt

Dissolving Tank testing.pdf 163 NEI8560 RF2904 163.RF2904 163‐‐RF2EP1, RF2EP2 WBESP Kraft, Secondary 

Boilers 8&10, June 10, 2008.pdf 164 NEI42710 B08,B10 combined 164.B08,B10 combined 164‐‐C08 for A ESP DBESP Kraft 

Boilers 8&10, June 10, 2008.pdf 164 NEI42710 B08,B10 combined 164.B08,B10 combined 164‐‐C08 for A ESP DBESP Kraft 

Boilers 8&10, Nov. 10, 2010.pdf 164 NEI42710 B08,B10 combined 164.B08,B10 combined 164‐‐C08 for A ESP DBESP Kraft 

Boilers 8&10, Nov. 10, 2010.pdf 164 NEI42710 B08,B10 combined 164.B08,B10 combined 164‐‐C08 for A ESP DBESP Kraft 

RTI165‐InternationalPaper‐

TexarkanaMill_NEI41628_PPTestReport‐2004SubpartMMIPT.pdf 165 NEI41628 000013 165.000013 165‐‐EP‐1N, EP‐1S DBESP Kraft 

RTI165‐InternationalPaper‐

TexarkanaMill_NEI41628_PPTestReport‐2004SubpartMMIPT.pdf 165 NEI41628 000013 165.000013 165‐‐EP‐1N, EP‐1S DBESP Kraft 

Test_data_memo_appendices.xlsx App A RF PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process T

RTI165‐InternationalPaper‐

TexarkanaMill_NEI41628_PPTestReport‐

2004SubpartMMIPT.pdf 165 NEI41628 000006 165.000006 165‐‐351013, 351014 DBESP Kraft 

RTI165‐InternationalPaper‐

TexarkanaMill_NEI41628_PPTestReport‐

2004SubpartMMIPT.pdf 165 NEI41628 000006 165.000006 165‐‐351013, 351014 DBESP Kraft 

P_P_ICR Part III_RTI166_InternationalPaper‐GeorgetownMill_NEI_41314_LK1and2_RB1and2_ST1and2_PM_July 2009.PDF 166 NEI41314 RB01 166.RB01 166‐‐RB1 ESP WBESP Kraft 

P_P_ICR Part III_RTI166_InternationalPaper‐GeorgetownMill_NEI_41314_LK1and2_RB1and2_ST1and2_PM_July 2009.PDF 166 NEI41314 RB01 166.RB01 166‐‐RB1 ESP WBESP Kraft 

P_P_ICR Part III_RTI166_InternationalPaper‐GeorgetownMill_NEI_41314_RB2_CO_July2009.PDF 166 NEI41314 RB02 166.RB02 166‐‐RB2 ESP, RB2 Scrubber WBESP/SCBR Kraft RTI169‐IP‐MansfieldMill‐

NEI33013_Test_Report_RB_Compliance_(.pdf 169 NEI33013 04 169.04 169‐‐ESP WBESP Kraft, SemiChem 

RTI169‐IP‐MansfieldMill‐

NEI33013_Test_Report_RB_Compliance_(.pdf 169 NEI33013 05 169.05 169‐‐ESP WBESP Kraft, SemiChem RTI172_International Paper ‐ RiverdaleMill_NEI18335_Oct2010 RB02 PM Testing.pdf 172 NEI18335 RB02 172.RB02 172‐‐RB02 Precipitator WBESP Kraft, Secondary 

RTI172_International Paper ‐ RiverdaleMill_NEI18335_Oct2010 RB01 PM Testing.pdf 172 NEI18335 RB01 172.RB01 172‐‐RB01 Precipitator WBESP Kraft, Secondary 

P_P ICR Part III_RTI174_International Paper‐

Riegelwood M (1).pdf 174 NEI40247 G‐92 174.G‐92 174‐‐G‐92 ESP WBESP Kraft 

P_P ICR Part III_RTI174_International Paper‐

Riegelwood M (1).pdf 174 NEI40247 G‐92 174.G‐92 174‐‐G‐92 ESP WBESP Kraft 

P_P ICR Part III_RTI174_International Paper‐

Riegelwood M (1).pdf 174 NEI40247 G‐32 174.G‐32

174‐‐G‐18 ESP/G‐18 SCRUB, G‐32

ESP, G‐92 ESP, G‐63B SCRUB, G‐

63C EWSCRUB DBESP Kraft 

P_P_ICR Part III_RTI175_InternationalPaper‐AugustaMill_N (10).pdf 175 NEI26514 RB3A 175.RB3A 175‐‐RB3B DBESP Kraft 

KapStone RR, NC RB7 2010 Report Proper.PDF 176 NEI47104 RB7 176.RB7 176‐‐08‐CD‐004‐001 DBESP Kraft 

RecBoiler_WasteBoiler_SmeltTank_LimeKiln_Compliancetest2011_Part1.pdf 177 NEI33887 EU0804 177.EU0804 177‐‐EU0804ESP DBESP Kraft 

RTI179_Rock‐TennDemopolis_NEI45474_PPSurvey_RFTest2010.pdf 179 NEI45474 RF3 179.RF3 179‐‐RF3ESP DBESP Kraft 

NEI6057 2009 #4RB EMISSION TEST REPORT.pdf 181 NEI6057 9 181.9 181‐‐4RBN_ESPWB WBESP

Kraft, Secondary,

SemiChem 

NEI6057 2009 #4RB EMISSION TEST REPORT.pdf 181 NEI6057 10 181.10 181‐‐4RBS_ESPWB WBESP

Kraft, Secondary,

SemiChem 

NEI6057 2009 #5 RB EMISSION TEST REPORT.pdf 181 NEI6057 49 181.49 181‐‐5RBN_ESPDB DBESP

Kraft, Secondary,

SemiChem 

NEI6057 2009 #5 RB EMISSION TEST REPORT.pdf 181 NEI6057 50 181.50 181‐‐5RBS_ESPDB DBESP

Kraft, Secondary,

SemiChem 

Sources 036, 037, 110, Group 101 Test Report Aug

2009.pdf 182 NEI7181 037 182.037 182‐‐C37 DBESP Kraft 

Recovery Boilers #1 & #2_Compliance

Test2010_Part1.pdf 184 NEI46817 73 184.73 184‐‐ESP‐2 DBESP‐WPR Utilize staged combustion. Kraft 

Recovery Boilers #1 & #2_Compliance

Test2010_Part1.pdf 184 NEI46817 72 184.72 184‐‐ESP‐1 DBESP‐WPR Utilize staged combustion. Kraft 

2009.01 4RF PM.pdf 185 NEI46599 02 185.02 185‐‐RF4ESP/RF4SCB DBESP/SCBR Kraft 2009.04 4RF PM.pdf 185 NEI46599 02 185.02 185‐‐RF4ESP/RF4SCB DBESP/SCBR Kraft 2009.07 4RF PM.pdf 185 NEI46599 02 185.02 185‐‐RF4ESP/RF4SCB DBESP/SCBR Kraft 2009.08 4RF PM.pdf 185 NEI46599 02 185.02 185‐‐RF4ESP/RF4SCB DBESP/SCBR Kraft 2009.10 4RF PM.pdf 185 NEI46599 02 185.02 185‐‐RF4ESP/RF4SCB DBESP/SCBR Kraft 2009.11 4RF PM.pdf 185 NEI46599 02 185.02 185‐‐RF4ESP/RF4SCB DBESP/SCBR Kraft 2009.12 4RF PM.pdf 185 NEI46599 02 185.02 185‐‐RF4ESP/RF4SCB DBESP/SCBR Kraft 

2009 Annual PM.pdf 186 NEI18334 RB15 186.RB15 186‐‐CRUESP DBESP Kraft 

GP Crossett 8R Recovery Furnace (SN‐26) 2011

Compliance Test Report 02‐23‐11.pdf 189 NEI54342 SN26 189.SN26 189‐‐SN26E WBESP Kraft 

Georgia‐Pacific Cedar Springs NEI26491 P3 RB3

PM 09‐23‐2010 Compliance Test.pdf 190 NEI26491 R402 190.R402 190‐‐C402 DBESP

Kraft, Secondary,

SemiChem 

Georgia‐Pacific Cedar Springs NEI26491 P3 RB3

PM 09‐23‐2010 Compliance Test.pdf 190 NEI26491 R402 190.R402 190‐‐C402 DBESP

Kraft, Secondary,

SemiChem 

Test_data_memo_appendices.xlsx App A RF PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process T

Georgia‐Pacific Cedar Springs NEI26491 P3 RB2

PM, CO 10‐01‐2010.pdf 190 NEI26491 R401 190.R401 190‐‐C401 DBESP

Kraft, Secondary,

SemiChem 

2004 Method 5 Testing ‐ part 3 of 3.pdf 196 NEI18660 SN‐14 196.SN‐14 196‐‐SN‐14 DBESP ESP (dry) Kraft 

2004 Method 5 Testing ‐ part 1 of 3.pdf 196 NEI18660 SN‐06 196.SN‐06 196‐‐SN‐06 DBESP ESP (dry) Kraft 2010 Domtar Compliance Testing Part 1 of 6.pdf 196 NEI18660 SN‐06 196.SN‐06 196‐‐SN‐06 DBESP ESP (dry) Kraft 

RecBoiler_LimeKiln_HogBoiler_SmeltTank_ComplianceTest2008.pdf 197 NEI18657 2 197.2 197‐‐RECSCR, ESP DBESP/SCBR Kraft 

NEI41565 MACT II Test Report July 2004.pdf 198 NEI41565 019 198.019 198‐‐019_CD DBESP

Kraft, Mechanica

Secondary 

NEI47077 BOWATER CATAWBA APR 10 COMP

REPORT.pdf 200 NEI47077 007RF2 200.007RF2 200‐‐2505C DBESP Kraft, Mechanica

NEI47077 BOWATER CATAWBA APR 10 COMP

REPORT.pdf 200 NEI47077 007RF3 200.007RF3 200‐‐5105C

DB‐WBESP [2‐sided dry

and wet] quarternary air Kraft, Mechanica

1106‐104_Boise White Paper_Lime Kiln.pdf 202 NEI12411 Recovery Furnace EU320

202.Recovery Furnace

EU320 202‐‐CE320 DBESP

Original TR sets in precipitator first fields

were replaced in 2010 with SIR's to

maintain first field reliability for 6 minute

opacity requirement ‐ more air

distribution Kraft 

2010 12 RB3 PM.pdf 203 NEI42410 RF#3 203.RF#3 203‐‐RF#3‐Scr DBESP Tertiary air Kraft, Sulfite‐Na 

2009 08 RB2 PM SO2.pdf 203 NEI42410 RF#2 203.RF#2 203‐‐RF#2‐Scr DBESP Tertiary air Kraft, Sulfite‐Na 

2009 08 RB3 PM SO2.pdf 203 NEI42410 RF#3 203.RF#3 203‐‐RF#3‐Scr DBESP Tertiary air Kraft, Sulfite‐Na 

NEI7104 ‐ 2008 No. 3 Recovery Boiler.pdf 207 NEI7104 038 207.038 207‐‐C28 DBESP

use of teritiary air to reduce TRS within the

furnace box of the recovery boiler Kraft 

NEI7104 ‐ 2008 No. 3 Recovery Boiler.pdf 207 NEI7104 038 207.038 207‐‐C28 DBESP

use of tertiary air to reduce TRS within the

furnace box of the recovery boiler Kraft 

NEI33023_RF2,RF3_2010_PM,PM10.pdf 226 NEI33023 RECB1 226.RECB1 226‐‐RB2ESP WBESP

Kraft, Secondary,

SemiChem 

NEI33023_RF2,RF3_2010_PM,PM10.pdf 226 NEI33023 RECB1 226.RECB1 226‐‐RB2ESP WBESP

Kraft, Secondary,

SemiChem 

Rayonier Jesup RF6 PM test 07_27_10.pdf 240 NEI26526 RF04 240.RF04 240‐‐RFC3 DBESP Kraft 

Rayonier Jesup RF5 PM test 05_25_10.pdf 240 NEI26526 RF01 240.RF01 240‐‐RFC1 DBESP Kraft 

NEI 34066 Emission Test RB‐LK‐ SDT 2010.pdf 242 NEI34066 AA‐011 242.AA‐011 242‐‐UT‐9 DBESP Kraft 

8196_2009 Source Compliance Test Report.pdf 243 NEI8196 R407 243.R407 243‐‐REP6 DBESP Kraft 

8196_2009 Source Compliance Test Report.pdf 243 NEI8196 R401 243.R401 243‐‐R401R4 DBESP Kraft 

8196_2009 Source Compliance Test Report.pdf 243 NEI8196 R401 243.R401 243‐‐R401R4 DBESP Kraft 

P_P_ICR Part III_RTI531_InternationalPaper‐ Savnnah Mill (1).pdf 531 NEI8186 RF15 531.RF15 531‐‐AP14 DBESP Kraft, Secondary 

RTI600_InternationalPaper‐CourtlandMill‐NEI18357 JUN 10 3RF .pdf 600 NEI18357 G0806 600.G0806 600‐‐08‐CD‐03‐001 DBESP Kraft 

RTI600_InternationalPaper‐CourtlandMill‐NEI18357 NOV 10 1‐3L.pdf 600 NEI18357 G0803 600.G0803 600‐‐08‐CD‐02‐001 WBESP Kraft 

ODEQ‐Final Report‐CRF‐PSEL‐Comp‐2‐23‐11.pdf 615 NEI40554 24 615.24 615‐‐RFESP1 DBESP quarternary air Kraft 

ODEQ‐Final Report‐CRF‐PSEL‐Comp‐2‐23‐11.pdf 615 NEI40554 24 615.24 615‐‐RFESP1 DBESP quarternary air Kraft 

ODEQ‐Final Report‐CRF‐PSEL‐Comp‐2‐23‐11.pdf 615 NEI40554 24 615.24 615‐‐RFESP1 DBESP quarternary air Kraft 

ODEQ‐Final Report‐CRF‐PSEL‐Comp‐2‐23‐11.pdf 615 NEI40554 24 615.24 615‐‐RFESP1 DBESP quarternary air Kraft 

2011_0315‐17.1.pdf 617 NEI42695 B14 617.B14 617‐‐C01 DBESP Kraft 

Smelt Dissovlving Tank and Recovery Boiler Part

1.pdf 115 NEI26476 RE01 115.RE01 115‐‐RE1W DBESP Good Combustion Practices Kraft 

Test_data_memo_appendices.xlsx App A RF PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process T

Smelt Dissovlving Tank and Recovery Boiler Part

1.pdf 115 NEI26476 RE01 115.RE01 115‐‐RE1E DBESP Good Combustion Practices Kraft 

2007_PE_Lime_Kiln_ESP,_No_4_Rec_Boiler_ESP_and_Smelt_Dis_Tank.pdf 105 NEI45182 EU445C 105.EU445C 105‐‐CD445‐480 DBESP‐WPR Tertiary air in #4RB only Kraft, Secondary 

2008_PM_No_3_Rec_Furnace_and_No_3_Smelt_Dis_Tank_Vents.pdf 105 NEI45182 EU445A 105.EU445A 105‐‐CD445‐183 WBESP Kraft, Secondary 

TempleInland‐OrangeMill_NEI12492_PPTestReport‐

2002TestReport.pdf 121 NEI12492 000013 121.000013 121‐‐C‐REVB1 DBESP Kraft, Secondary 

TempleInland‐OrangeMill_NEI12492_PPTestReport‐

2002TestReport.pdf 121 NEI12492 000014 121.000014 121‐‐C‐REVB2 DBESP Kraft, Secondary 

TempleInland‐OrangeMill_NEI12492_PPTestReport‐

2004MACTIIReport.pdf 121 NEI12492 000013 121.000013 121‐‐C‐REVB1 DBESP Kraft, Secondary 

TempleInland‐OrangeMill_NEI12492_PPTestReport‐

2004MACTIIReport.pdf 121 NEI12492 000014 121.000014 121‐‐C‐REVB2 DBESP Kraft, Secondary 

0910‐29 RB2.pdf 124 NEI8278 019 124.019 124‐‐ESP 019 WBESP Kraft 

0910‐29 RB2.pdf 124 NEI8278 019 124.019 124‐‐ESP 019 WBESP Kraft 

2011 Stack Report‐AIR.pdf 130 NEI18338 1 130.1 130‐‐1RESP WBESP Kraft 2011 Stack Report‐AIR.pdf 130 NEI18338 1 130.1 130‐‐1RESP WBESP Kraft 2011 Stack Report‐AIR.pdf 130 NEI18338 2 130.2 130‐‐2RESP WBESP Kraft 2011 Stack Report‐AIR.pdf 130 NEI18338 2 130.2 130‐‐2RESP WBESP Kraft RTI1#3PR.PDF 142 NEI41552 CU7216 142.CU7216 142‐‐CD‐7216 WBESP Kraft, Secondary NEI26504_RTI143_PCA Valdosta Mill_1,2,3 RB

PM_November 2009.pdf 143 NEI26504 7000 143.7000 143‐‐C011 WBESP Kraft 

No.2 & 3 RB ESP Part Testing.pdf 145 NEI33135 54 145.54 145‐‐PR010‐02C WBESP Kraft 

No.2 & 3 RB ESP Part Testing.pdf 145 NEI33135 55 145.55 145‐‐PR010‐02C WBESP Kraft 

NEI46739 RB1_RB3 Combined Stack PM Test Data

March 2010.pdf 154 NEI46739

P39 and P37 ‐ Recovery

Furnace 1 and Recovery

Furnace 3

154.P39 and P37 ‐ 

Recovery Furnace 1

and Recovery Furnace

3 154‐‐C13 and C11 WBESP Kraft 

NEI46739 RB2 PM, THC, NOx, CO September

2009.pdf 154 NEI46739 P36 ‐ Recovery Furnace 2

154.P36 ‐ Recovery

Furnace 2 154‐‐C10 WBESP Kraft 

NEI46739 RB1 PM June 2011.pdf 154 NEI46739 P39 ‐ Recovery Furnace 1

154.P39 ‐ Recovery

Furnace 1 154‐‐C13 WBESP Kraft 

RTI167 NEI340702011_IPVicksburg_StackTestReport_(PB,LK,RB,SDT,SS).pdf 167 NEI34070 005RB 167.005RB 167‐‐RBESPA, RBESPB WBESP Kraft, Secondary 

RTI167 NEI340702011_IPVicksburg_StackTestReport_(PB,LK,RB,SDT,SS).pdf 167 NEI34070 005RB 167.005RB 167‐‐RBESPA, RBESPB WBESP Kraft, Secondary 

9‐0224C Evergreen F.pdf 171 NEI18658 002 171.002 171‐‐ESPRB2 DBESP‐WPR Kraft 

9‐0224C Evergreen F.pdf 171 NEI18658 003 171.003 171‐‐ESPRB3 DBESP‐WPR Kraft 

P_P_ICR Part III_RTI175_InternationalPaper‐

AugustaMill_N (6).PDF 175 NEI26514 RB2A 175.RB2A 175‐‐RB2B DBESP Kraft 

2010.0913‐0916.3Q.tests.pdf 188 NEI40600 016RB2 188.016RB2 188‐‐62‐301 WBESP overfire air

Kraft, Secondary,

SemiChem 

Test_data_memo_appendices.xlsx App A RF PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process T

2010.0913‐0916.3Q.tests.pdf 188 NEI40600 016RB2 188.016RB2 188‐‐62‐301 WBESP overfire air

Kraft, Secondary,

SemiChem 

2011.0606‐0609.2Q.tests.pdf 188 NEI40600 014RB1 188.014RB1 188‐‐62‐101 WBESP overfire air

Kraft, Secondary,

SemiChem 

NEI8601_Unit 009_2010.pdf 205 NEI8601 009 205.009 205‐‐ESP‐N WBESP Kraft, Secondary 

NEI8601_Unit 009_2010.pdf 205 NEI8601 009 205.009 205‐‐ESP‐S WBESP Kraft, Secondary 

NEI8601_Unit 009_2010.pdf 205 NEI8601 009 205.009 205‐‐ESP‐N, ESP‐S WBESP Kraft, Secondary 

RTI206_BRPRECOVB#1011.14.2007.pdf 206 NEI40282 G‐31 206.G‐31 206‐‐RB10 ESP WBESP Kraft 

RTI206_BRPRECOVB#1111.15.2007.pdf 206 NEI40282 G‐32 206.G‐32 206‐‐RB11 ESP WBESP Kraft 

2009 #1 RB.pdf 613 NEI11172 001L 613.001L 613‐‐1LPRCP DBESP Kraft, Secondary 

2009 #1 RB.pdf 613 NEI11172 001R 613.001R 613‐‐1RPRCP DBESP Kraft, Secondary 

2009 #1 RB.pdf 613 NEI11172 001L&001R 613.001L&001R DBESP Kraft, Secondary 

2009 #2 RB.pdf 613 NEI11172 002R 613.002R 613‐‐2RPRCP DBESP Kraft, Secondary 

2009 #2 RB.pdf 613 NEI11172 002L 613.002L 613‐‐2LPRCP DBESP Kraft, Secondary 

2009 #2 RB.pdf 613 NEI11172 002L&002R 613.002L&002R DBESP Kraft, Secondary 

NEI42341A_PIII_D2a_2011‐Q1 LK‐RB10‐SDTV10‐

HFB11.pdf 102 NEI42341A RB10 102.RB10 102‐‐RB‐ESP DBESP‐WPR Kraft 

#14 RB & SDT 2007 (1 of 3).pdf 117 NEI42689 B21 117.B21 117‐‐C21 DBESP Kraft 

2011 Stack Report‐AIR.pdf 130 NEI18338 3 130.3 130‐‐3RESP DBESP Kraft 

EPA M5 012011.pdf 140 NEI13340 55 140.55 140‐‐461‐170 DBESP Kraft 

NEI759 TSP Testing 2008 part 1.pdf 146 NEI759 16 146.16 146‐‐RF201 DBESP‐WPR Tertiary Air Kraft 

NEI33104‐RB2 2007 PM Compliance.PDF 157 NEI33104 RB2 157.RB2 157‐‐WESP WBESP Kraft 

NEI33104‐RB2 2007 PM Compliance.PDF 157 NEI33104 RB2 157.RB2 157‐‐WESP WBESP Kraft 

NEI33104‐RB2 2007 PM Compliance.PDF 157 NEI33104 RB2 157.RB2 157‐‐WESP WBESP Kraft 

Recovery Boiler PM Emissions Test Report

(NEI18177).pdf 159 NEI8177 F3 159.F3 159‐‐CD01 SCBR Kraft 

P_P ICR Part III_RTI162_InternationalPaper‐

EastoverMill_NEI46760_no 2 rec furnace

particulate 052.pdf 162 NEI46760 382A 162.382A 162‐‐382AESP DBESP Kraft RTI173 NEI 35908 IPTiconderoga Subpart MM

Stack Test for RB‐SDT‐LK 10‐04.pdf 173 NEI35908 RECOVB 173.RECOVB 173‐‐ESPA, ESPB DBESP NA Kraft 

RTI173 NEI 35908 IPTiconderoga Subpart MM

Stack Test for RB‐SDT‐LK 10‐04.pdf 173 NEI35908 RECOVB 173.RECOVB 173‐‐ESPA, ESPB DBESP NA Kraft 

IP PENSACOLA 2011 RF‐SDTV COMP REPORT.pdf 178 NEI26309 08P012 178.08P012 178‐‐08C012 DBESP Kraft 

IP PENSACOLA 2011 RF‐SDTV COMP REPORT.pdf 178 NEI26309 08P013 178.08P013 178‐‐08C013 DBESP Kraft 

NEI26471_No3_Recovery_Boiler_PM_TRS_NOx_CO_RATA_2010‐0324[1].pdf 180 NEI26471 D001 180.D001 180‐‐D01E DBESP Tertiary Air Kraft, Secondary Georgia‐Pacific Cedar Springs NEI26491 P3 RB1

PM & SDTV1 PM, TRS 09‐24‐2009 Compliance

Test.pdf 190 NEI26491 R400 190.R400 190‐‐C400 DBESP

Kraft, Secondary,

SemiChem 

NEI18390_002_004_PM_2011.pdf 199 NEI18390 002 199.002 199‐‐Z003 DBESP Kraft 

NEI7559RecoveryBoiler‐69‐01CompIPT2010.pdf 201 NEI7559 SR0001 201.SR0001 201‐‐ESP DBESP

Kraft, Mechanica

Secondary 

RecoveryBoilerSmeltTank#2LimeKiln_EmmisionsT

estReport_2005.pdf 340 NEI46852 005 340.005 340‐‐ESP DBESP Kraft, Secondary #4RB Compliance 042611.pdf 525 NEI8265 EU18 525.EU18 525‐‐RFESP DBESP‐WPR quarternary air Kraft 

47091_011_2010_PM.pdf 606 NEI47091 RB4 606.RB4 606‐‐ESP4 DBESP Kraft 

Test_data_memo_appendices.xlsx App A RF PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process T

47091_007_2010_PM.pdf 606 NEI47091 RB3 606.RB3 606‐‐ESP3 DBESP Kraft 

47091_007_2010_PM.pdf 606 NEI47091 RB3 606.RB3 606‐‐ESP3 DBESP Kraft 

47091_006_2011_PM.pdf 606 NEI47091 RB2 606.RB2 606‐‐ESP2 DBESP Kraft 

47091_006_2011_PM.pdf 606 NEI47091 RB2 606.RB2 606‐‐ESP2 DBESP Kraft 

610 Verso 2008 RB 1&2 Report.PDF 610 NEI6261 4, 5 610.4, 5 610‐‐ESP DBESP

stacked air installed in recovery boiler No.

1 in 2007; RB1 upper furnace rebuild in

2008 Kraft, Mechanica

610 Verso 2008 RB 1&2 Report.PDF 610 NEI6261 4, 5 610.4, 5 610‐‐ESP DBESP

stacked air installed in recovery boiler No.

1 in 2007; RB1 upper furnace rebuild in

2008 Kraft, Mechanica

610 Verso 2008 RB 1&2 Report.PDF 610 NEI6261 4, 5 610.4, 5 610‐‐ESP DBESP

stacked air installed in recovery boiler No.

1 in 2007; RB1 upper furnace rebuild in

2008 Kraft, Mechanica

610 Verso 2008 RB 1&2 Report.PDF 610 NEI6261 4, 5 610.4, 5 610‐‐ESP DBESP

stacked air installed in recovery boiler No.

1 in 2007; RB1 upper furnace rebuild in

2008 Kraft, Mechanica

2008_PM_Lime_Kiln,_No_4_Rec_Boiler_and_No_

4_Smelt_Dis_Tank.pdf 105 NEI45182 EU445C 105.EU445C 105‐‐CD445‐480 DBESP‐WPR Tertiary air in #4RB only Kraft, Secondary 

2008_PM_Lime_Kiln_Exh,_No_4_Rec_Boiler_and_

No_4_Smelt_Dis_Tank.pdf 105 NEI45182 EU445C 105.EU445C 105‐‐CD445‐480 DBESP‐WPR Tertiary air in #4RB only Kraft, Secondary 

2009_PM_No_3_Lime_Kiln,_No_4_Rec_Boiler_and_No_4_Smelt.pdf 105 NEI45182 EU445C 105.EU445C 105‐‐CD445‐480 DBESP‐WPR Tertiary air in #4RB only Kraft, Secondary 

2009_PM_No_3_Lime_Kiln_and_No_4_Smelt_Dis_Tank.pdf 105 NEI45182 EU445C 105.EU445C 105‐‐CD445‐480 DBESP‐WPR Tertiary air in #4RB only Kraft, Secondary 

Project #1997033 ‐ July 2004.pdf 109 NEI32869A RB4 109.RB4 109‐‐RB4ESP DBESP Kraft IP PENSACOLA SEPT 04 PM COMP REPORT.pdf 178 NEI26309 08P013 178.08P013 178‐‐08C013 DBESP Kraft 

IP PENSACOLA SEPT 04 PM COMP REPORT.pdf 178 NEI26309 08P012 178.08P012 178‐‐08C012 DBESP Kraft 

Mill code 139 part 1.pdf 139 NEI42357 02 139.02 139‐‐ESP1/ESP2&3

DBESP‐WPR/DBESP/DBESP Kraft, Secondary 

Mill code 139 part 3.pdf 139 NEI42357 02 139.02 139‐‐ESP1/ESP2&3

DBESP‐WPR/DBESP/DBESP Kraft, Secondary 

NEI11338_WPC ‐ RF ‐ Mar 2001.pdf 152 NEI11338 03 152.03 152‐‐03‐ESP WBESP/SCBR Kraft 

NEI11338_WPC ‐ RF_SDT_LK ‐ Sep 2004.pdf 152 NEI11338 03 152.03 152‐‐03‐ESP, 03‐SCBR WBESP/SCBR Kraft NEI11338_WPC ‐ RF ‐ Sep 2002.pdf 152 NEI11338 03 152.03 152‐‐03‐ESP, 03‐SCBR WBESP/SCBR Kraft 

P_P_ICR Part III_RTI166_InternationalPaper‐GeorgetownMill_NEI_41314_LK2_RB1and2_PM_2004.PDF 166 NEI41314 RB02 166.RB02 166‐‐RB2 ESP, RB2 Scrubber WBESP/SCBR Kraft 

Green rows were not used in the NSPS review.

Test_data_memo_appendices.xlsx App A RF PM 
ble Particulate Matter

RTI+EUID100.037A103.G‐158105.EU445C107.08‐P1

108.RB3109.RB3109.RB4111.G‐44114.U500114.U500116.003119.EQT008119.EQT010119.EQT010120.F7124.001124.001126.RECOV126.RECOV126.RECOV126.RECOV127.REC1N127.REC1N131.6131.5131.5131.5132.5RB132.5RB132.4RB133.10133.10

Configuration General Test Report Information Production Rate 

Has the configuration of

the emission unit,

combustion controls,

collection system, or

APCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly ProductionRate(value)

No PM 2004 Chemical Recovery Furnace unspecified 6/15/2004 M5 58.7

no PM 2009 No. 5 Recovery Boiler No. 2 fuel oil (low sulfur) 4/30/2009 M5 91.7

no PM 2010 No. 4 Recovery Boiler BL, Natural Gas 10/13/2010 M5 59.0

No PM 2009 Recovery Furnace unspecified 7/21/2009 M5 91.8

No PM 2010 Recovery Boiler No. 3 unspecified 8/18/2010 M5 106.4

No PM 2008 Recovery Boiler # 3 unspecified 7/30/2008 M5 55.4

No PM 2008 Recovery Boiler No. 4 unspecified 8/12/2008 M5 93.4

No PM 2011 Recovery Furnace

No. 2 fuel oil, BLS, Residual fuel oil,

and natural gas 1/28/2011 M5 88

No PM 2008 Recovery Furnace (low load) oil (secondary) 12/17/2008 M5 79

No PM 2008 Recovery Furnace (high load) oil (secondary) 12/18/2008 M5 105

No PM 2010 No. 2 Recovery Boiler Natural Gas and No. 6 Fuel Oil 9/2/2010 M5 9

No PM 2010 No. 20 Recovery Boiler unspecified 12/1/2010 M5 59

No PM 2010 No. 21 Recovery Furnace Fuel oil 1/5/2010 M5 67

No PM 2010 No. 21 Recovery Boiler unspecified 11/30/2010 M5 62

No PM 2010 Recovery Furnace 5

WFB Fuel Oil (was not used during

test run) 7/15/2010 M5 104.0

No PM 2010 No. 1 Recovery Boiler (South 1A) Fuel Oil 11/3/2010 M5 5

No PM 2010 No. 1 Recovery Boiler (North 1B) Fuel Oil 11/3/2010 M5 5

No PM 2009 Recovery Furnace West Stack 1st Set BL and No. 6 fuel oil 12/10/2009 M5 51

No PM 2009 Recovery Furnace East Stack 1st Set BL and No. 6 fuel oil 12/10/2009 M5 51

No PM 2009 Recovery Furnace West Stack 2nd Set BL and No. 6 fuel oil 12/10/2009 M5 51

No PM 2009 Recovery Furnace East Stack 2nd Set BL and No. 6 fuel oil 12/10/2009 M5 51

No PM 2011 Recovery Boiler North unspecified 4/6/2011 M5 72

No PM 2011 Recovery Boiler South unspecified 4/6/2011 M5 72

No PM 2003 Recovery Furnace 5 No. 2 Distillate Oil 12/9/2003 M5 62.6

No PM 2003 Recovery Furnace 4 No. 6 Fuel Oil 12/5/2003 M5 63.5

No PM 2003

Recovery Furnace 4 (two chambers operating) (Condition

#1) No. 6 Fuel Oil 12/2/2003 M5 unspecified 

No PM 2003

Recovery Furnace 4 (one chamber operating) (Condition #2

and #3) No. 6 Fuel Oil 12/3/2003 M5 unspecified 

PM 2010 #5 Recovery Boiler North Stack unspecified 5/18/2010 M5 69.7

PM 2010 #5 Recovery Boiler South Stack unspecified 5/18/2010 M5 69.7

PM 2010 Recovery Boiler 4 unspecified 5/20/2010 M5 63.3

No PM 2011 Recovery Furnace unspecified 3/22/2011 unspecified unspecified 

No PM 2011 Recovery Furnace unspecified 6/8/2011 unspecified unspecified 

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

135.003‐1135.003‐1136.EU 005

137.721137.189138.002142.CU7214143.7010143.7020146.8146.8147.14147.14147.5147.5148.007148.001150.CREC‐1

152.03152.03155.RECOVERYFURNACE156.RF22156.RF22

Has the configuration of

the emission unit,

combustion controls,

collection system, or

APCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly ProductionRate(value)

No PM 2011 Recovery Boiler (three ESP chamber in Operation) #6 residual oil 2/16/2011 M5 110.3

No PM 2011 Recovery Boiler (two ESP chambers in Operation) #6 residual oil 2/17/2011 M5 110.3

no PM 2010 Recovery Boiler #10 soap 5/18/2010 M5 112

No PM 2010 Recovery Furnace 5 unspecified 9/15/2010 M5 94.72

No PM 2010 Recovery Furnace 4 unspecified 9/16/2010 M5 27.38

No PM 2009 Recovery Furnace (filterable) unspecified 3/6/2009 M5 57.0

Yes

Source to be converted

from DCE to NDCE low‐

odor furnace beginning

September 2011. PM 2003 No. 2 Recovery Boiler unspecified 6/26/2003 M5 37

no PM 2009 No. 2 Recovery Furnace unspecified 11/3/2009 M5 17.8

no PM 2009 No. 3 Recovery Furnace unspecified 11/4/2009 M5 26

no PM 2011 No. 1 Recovery Furnace Upriver Stack unspecified 4/13/2011 M5 77.0

no PM 2011 No. 1 Recovery Furnace Downriver Stack unspecified 4/13/2011 M5 77.0

NO NA PM 2008 No. 3 Recovery Furnace ‐ North unspecified 4/30/2008 M5 59.3

NO NA PM 2008 No. 3 Recovery Furnace ‐ South unspecified 4/30/2008 M5 59.3

NO NA PM 2009 No. 4 Recovery Furnace ‐ Front Half unspecified 1/28/2009 M5 10

NO NA PM 2008 No. 4 Recovery Furnace unspecified 7/17/2008 M5 97

no PM 2010 No. 2 Recovery Furnace unspecified 7/26/2010 M5 81.7

no PM 2010 No. 1 Recovery Furnace unspecified 7/21/2010 M5 58.5

No PM 2007 Recovery Furnace unspecified 8/29/2007 M5 unspecified 

Yes added intermediate air (3rPM 2007 Recovery Furnace ‐ Condition 1 (Operating 5 ESPs) unspecified 3/7/2007 M5 66

Yes added intermediate air (3rPM 2007 Recovery Furnace ‐ Condition 2 (Operating 6 ESPs) unspecified 3/9/2007 M5 67No PM 2004 No. 10 Recovery Furnace unspecified 9/2/2004 M5 71.8

No PM 2010 Recovery Furnace 22 unspecified 2/16/2010 M5 8

No PM 2010 Recovery Furnace 22 unspecified 4/28/2010 M5 7

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

156.RF22156.RF22156.RF18156.RF18156.RF19156.RF19156.RF19156.RF19162.381A162.381A163.RF1901163.RF2904163.RF2904164.B08,B10 combined

164.B08,B10 combined

164.B08,B10 combined

164.B08,B10 combined

165.000013165.000013

Has the configuration of

the emission unit,

combustion controls,

collection system, or

APCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly ProductionRate(value)

No PM 2010 Recovery Furnace 22 unspecified 9/14/2010 M5 51.3

No PM 2010 Recovery Furnace 22 unspecified 12/1/2010 M5 65.4

No PM 2010 Recovery Furnace 18 unspecified 3/4/2010 M5 36

No PM 2010 Recovery Furnace 18 unspecified 7/28/2010 M5 4

No PM 2010 Recovery Furnace 19 unspecified 5/12/2010 M5 54.9

No PM 2010 Recovery Furnace 19 unspecified 9/22/2010 M5 6

No PM 2010 Recovery Furnace 19 unspecified 11/4/2010 M5 56.6

No PM 2010 Recovery Furnace 19 unspecified 11/4/2010 M5 56

No PM 2008 No. 1 Recovery Furnace No. 6 fuel oil/ No. 2 fuel oil 12/3/2008 M5 52

No PM 2008 No. 1 Recovery Furnace No. 6 fuel oil/ No. 2 fuel oil 8/6/2008 M5 52

No PM 2011 No. 1 Recovery Furnace unspecified 6/1/2011 M5 82

No PM 2011 No. 2 Recovery Furnace ‐ North Duct unspecified 6/2/2011 M5 65.4

No PM 2011 No. 2 Recovery Furnace ‐ South Duct unspecified 6/2/2011 M5 65.4

PM 2008 Recovery Boiler 8 & 10 ESP side B unspecified 6/8/2008 M5 41.7

PM 2008 Recovery Boiler 8 & 10 ESP side A unspecified 6/8/2008 M5 41.7

PM 2010 Recovery Boiler 8 & 10 ESP side B unspecified 11/10/2010 M5 39.5

PM 2010 Recovery Boiler 8 & 10 ESP side A unspecified 11/10/2010 M5 38.7

No PM 2004 No. 1 Recovery Furnace ‐ North Stack unspecified 7/24/2004 M5 49

No PM 2004 No. 1 Recovery Furnace ‐ South Stack unspecified 7/24/2004 M5 49

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

165.000006165.000006166.RB01166.RB01166.RB02169.04169.05172.RB02172.RB01174.G‐92174.G‐92174.G‐32175.RB3A176.RB7177.EU0804179.RF3181.9181.10181.49181.50182.037184.73184.72185.02185.02185.02185.02185.02185.02185.02186.RB15189.SN26190.R402190.R402

Has the configuration of

the emission unit,

combustion controls,

collection system, or

APCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly ProductionRate(value)

No PM 2004 No. 2 Recovery Furnace ‐ East Stack unspecified 7/21/2004 M5 90

No PM 2004 No. 2 Recovery Furnace ‐ West Stack unspecified 7/21/2004 M5 90

No PM 2009 No. 1 Recovery Furnace Stack A unspecified 7/14/2009 M5 68

No PM 2009 No. 1 Recovery Furnace Stack B unspecified 7/14/2009 M5 68

No PM 2009 No. 2 Recovery Furnace unspecified 7/16/2009 M5 82

No PM 2010 No. 1 Recovery Boiler unspecified 9/21/2010 M5 76

No PM 2010 No. 2 Recovery Boiler unspecified 9/22/2010 M5 79

no PM 2010 No. 2 Recovery Boiler unspecified 10/25/2010 M5 unspecified 

no PM 2010 No. 1 Recovery Boiler unspecified 10/26/2010 M5 unspecified 

PM 2004 No. 4 Recovery Furnace North Stack unspecified 10/25/2004 M5 50

PM 2004 No. 4 Recovery Furnace ‐ South Stack unspecified 10/25/2004 M5 50

PM 2004 No. 5 Recovery Furnace unspecified 10/20/2004 M5 139

no PM 2010 No. 3 Recovery Boiler unspecified 3/22/2010 M5 120

No PM 2010 No. 7 Recovery Boiler unspecified 7/27/2010 M5 65.2

No PM 2011 Recovery Boiler unspecified 3/24/2011 M5 83.5

No PM 2010 No. 3 Recovery Furnace unspecified 6/2/2010 M5 93.2

No PM 2009 No. 4 Recovery Boiler ‐ North Stack unspecified 2/25/2009 M5 53.9

No PM 2009 No. 4 Recovery Boiler ‐ South Stack unspecified 2/25/2009 M5 53.9

No PM 2009 No. 5 Recovery Boiler ‐ North Stack unspecified 2/17/2009 M5 33.7

No PM 2009 No. 5 Recovery Boiler ‐ South Stack unspecified 2/17/2009 M5 33.7

no PM 2009 Recovery Boiler No. 3

Fuel Oil (start‐up and load

maintenance procedures) 8/24/2009 M5 64.2

No PM 2010 No. 2 Recovery Furnace unspecified 9/29/2010 M5 89.5

No PM 2010 No. 1 Recovery Furnace unspecified 9/28/2010 M5 56.2

No PM 2009 No. 4 Recovery Furnace unspecified 1/14/2009 M5 22

No PM 2009 No. 4 Recovery Furnace unspecified 4/9/2009 M5 21

No PM 2009 No. 4 Recovery Furnace unspecified 7/8/2009 M5 20

No PM 2009 No. 4 Recovery Furnace unspecified 8/5/2009 M5 20

No PM 2009 No. 4 Recovery Furnace unspecified 10/9/2009 M5 22

No PM 2009 No. 4 Recovery Furnace unspecified 11/11/2009 M5 22

No PM 2009 No. 4 Recovery Furnace unspecified 12/10/2009 M5 22

No PM 2009 No. 4 Recovery Furnace unspecified 7/13/2009 M5 124

No PM 2011 8R Recovery Furnace unspecified 2/23/2011 M5 113.12

No PM 2010 No. 3 Recovery Furnace ‐ North unspecified 9/21/2010 M5 72.8

No PM 2010 No. 3 Recovery Furnace ‐ South unspecified 9/21/2010 M5 72.8

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

190.R401196.SN‐14196.SN‐06196.SN‐06197.2198.019200.007RF2200.007RF3202.Recovery Furnace

EU320203.RF#3203.RF#2203.RF#3207.038207.038226.RECB1226.RECB1240.RF04240.RF01242.AA‐011

243.R407243.R401243.R401531.RF15600.G0806600.G0803615.24615.24615.24615.24617.B14115.RE01

Has the configuration of

the emission unit,

combustion controls,

collection system, or

APCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly ProductionRate(value)

No PM 2010 No. 2 Recovery Furnace unspecified 10/1/2010 M5 44

no PM 2004 No. 3 Recovery Furnace unspecified 9/2/2004 M5 112.7

no PM 2004 No. 2 Recovery Furnace unspecified 9/7/2004 M5 71.4

no PM 2010 No. 2 Recovery Furnace unspecified 4/20/2010 M5 79.1

No PM 2008 Recovery Boiler unspecified 9/19/2008 M5 15

No PM 2004 Recovery Furnace 3 unspecified 7/27/2004 M5 112.7

No PM 2010 Recovery Furnace No. 2 unspecified 3/31/2010 M5 40.8580

No PM 2010 Recovery Furnace No. 3 unspecified 4/7/2010 M5 78.4

no

Particulate matter test

includes condensable aswell as method 5

filterable PM 2011 Recovery Furnace EU320 unspecified 7/20/2011 M5 57.6

No PM 2010 #3 Recovery Furnace unspecified 12/17/2010 M5 100.7

No PM 2009 #2 Recovery Furnace unspecified 8/25/2009 M5 17.5

No PM 2009 Recovery Furnace #3 unspecified 8/5/2009 M5 104.6

No NA PM 2008 #3 Recovery Boiler ‐ West Exhaust Stack No. 6 fuel oil and/or Natural Gas 4/22/2008 M5 18.7

No NA PM 2008 #3 Recovery Boiler ‐ East Exhaust Stack No. 6 fuel oil and/or Natural Gas 4/22/2008 M5 18.7

no PM 2010 #2 Recovery Furnace ‐ South Stack unspecified 11/30/2010 M5 78

no PM 2010 #2 Recovery Furnace ‐ North Stack unspecified 11/30/2010 M5 78

No PM 2010 No. 6 Recovery Furnace unspecified 7/27/2010 M5 119

No PM 2010 No. 5 Recovery Furnace unspecified 5/25/2010 M5 67

No PM 2010 Recovery Furnace unspecified 9/15/2010 M5 126.4

No PM 2009 #6 Recovery Boiler (R407) unspecified 10/27/2009 M5 122.5

No PM 2009 #5 Recovery Boiler (R401) ‐ North unspecified 11/3/2009 M5 81

No PM 2009 #5 Recovery Boiler (R401) ‐ South unspecified 11/3/2009 M5 81

No PM 2011 No. 15 Recovery Boiler unspecified 5/4/2011 M5 15

no PM 2010 No. 3 Recovery Furnace unspecified 6/8/2010 M5 10

no PM 2010 No. 2 Recovery Furnace unspecified 11/2/2010 M5 85.2

yes LVHC combusted in chemicPM 2011 Chemical Recovery Furnace ‐ West Stack Front Half Natural Gas 2/23/2011 M5 66.1

yes LVHC combusted in chemicPM 2011 Chemical Recovery Furnace ‐ East Stack Front Half Natural Gas 2/23/2011 M5 66.1

yes LVHC combusted in chemicPM 2011 Chemical Recovery Furnace ‐ West Stack ODEQ 5 Natural Gas 2/23/2011 ODEQ M5 66.1

yes LVHC combusted in chemicPM 2011 Chemical Recovery Furnace ‐ East Stack ODEQ 5 Natural Gas 2/23/2011 ODEQ M5 66.1no PM 2011 Recovery Boiler (S20) unspecified 3/15/2011 M5 38

no PM 2010 No. 3 Recovery Boiler (West stack) unspecified 9/9/2010 M5 87

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

115.RE01105.EU445C105.EU445A121.000013121.000014121.000013121.000014124.019124.019130.1130.1130.2130.2142.CU7216143.7000145.54145.55154.P39 and P37 ‐ 

Recovery Furnace 1

and Recovery Furnace

3154.P36 ‐ Recovery

Furnace 2

154.P39 ‐ Recovery

Furnace 1

167.005RB167.005RB171.002171.003175.RB2A188.016RB2

Has the configuration of

the emission unit,

combustion controls,

collection system, or

APCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly ProductionRate(value)

no PM 2010 No. 3 Recovery Boiler (East stack) unspecified 9/9/2010 M5 87

No PM 2007 No. 4 Recovery Boiler Natural Gas 05/16/2007

EPA\ODEQM5 64.4

no PM 2008 # 3 Recovery Boiler Natural Gas 2/21/2008 M5 5

No PM 2002 No. 1 Recovery Furnace Unspecified 10/29/2002 M5 34

No PM 2002 No. 2 Recovery Furnace Unspecified 10/30/2002 M5 34

No PM 2004 No. 1 Recovery Furnace Unspecified 8/23/2004 M5 3No PM 2004 No. 2 Recovery Furnace Unspecified 8/19/2004 M5 3

No PM 2010 RB2 ‐ 2A South stack Unspecified 11/4/2010 M5 5

No PM 2010 RB2 ‐ 2B North stack Unspecified 11/4/2010 M5 5

No PM 2011 No. 1 RF North stack Unspecified 6/23/2011 M5 19

No PM 2011 No. 1 RF South stack Unspecified 6/23/2011 M5 19

No PM 2011 No. 2 RF North stack Unspecified 6/22/2011 M5 18

No PM 2011 No. 2 RF South stack Unspecified 6/22/2011 M5 18

Yes

Conversion from DCE to

NDCE low‐odor furnace

during 2011. PM 2001 No. 1 Recovery Boiler Unspecified 6/11/2001 M5 Unspecified 

no PM 2009 No. 1 RB Unspecified 11/3/2009 M5 17.7

No PM 2009 No. 2 Recovery Boiler Unspecified 4/22/2009 M5 Unspecified 

No PM 2009 No. 3 Recovery Boiler Unspecified 4/22/2009 M5 Unspecified 

No PM 2010 RB 1 and RB 3 Common Stack Unspecified 3/16/2010 M5 62.1366666

No PM 2009 Recovery Boiler 2 Unspecified 9/16/2009 M5 34.17

No PM 2011 Recovery Boiler 1 Unspecified 6/21/2011 M5 32.72

no NA PM 2011 Recovery Furnace North ESP (Wet bottom) Unspecified 1/18/2011 M5 69.44133

no NA PM 2011 Recovery Furnace South ESP (Wet bottom) Unspecified 1/18/2011 M5 62.17

no PM 2009 Recovery Boiler 2 Unspecified 7/8/2009 M5 27.1

no PM 2009 Recovery Boiler 3 Unspecified 7/9/2009 M5 27.6

no PM 2009 No 2 Recovery Boiler Unspecified 6/9/2009 M5 31

No PM 2010 Recovery Boiler 2 Unspecified 9/14/2010 M5 28.030562

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

188.016RB2188.014RB1205.009205.009205.009206.G‐31206.G‐32613.001L613.001R613.001L&001R613.002R613.002L613.002L&002R102.RB10117.B21130.3140.55146.16157.RB2157.RB2157.RB2159.F3162.382A173.RECOVB173.RECOVB178.08P012178.08P013180.D001190.R400199.002201.SR0001340.005525.EU18606.RB4

Has the configuration of

the emission unit,

combustion controls,

collection system, or

APCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly ProductionRate(value)

No PM 2010 Recovery Boiler 2 Unspecified 9/14/2010 ODEQ M5 28.030562

No PM 2011 Recovery Boiler 1 Unspecified 6/9/2011 M5 28.1472083

No PM 2010 RB North Unspecified 7/21/2010 M5 30

No PM 2010 RB South Unspecified 7/21/2010 M5 30

No PM 2010 RB Total Unspecified 7/21/2010 M5 30

no PM 2007 Recovery Boiler 10 Unspecified 11/14/2007 M5 Unspecified no PM 2007 Recovery Boiler 11 Unspecified 11/15/2007 M5 Unspecified 

No PM 2009 No. 1 RB ESP ‐ Left Side ESP Unspecified 10/28/2009 M5 Unspecified 

No PM 2009 No. 1 RB ESP ‐ Right Side ESP Unspecified 10/28/2009 M5 Unspecified 

No PM 2009 No. 1 RB ESP ‐ Combined Unspecified 10/28/2009 M5 Unspecified 

No PM 2009 No. 2 RB ESP ‐ Right Side Unspecified 10/27/2009 M5 Unspecified 

No PM 2009 No. 2 RB ESP ‐ Left Side Unspecified 10/27/2009 M5 Unspecified 

No PM 2009 No. 2 RB ESP‐ Combined Unspecified 10/27/2009 M5 Unspecified 

No PM 2011 #10 Recovery Boiler unspecified 1/6/2011 M5 11

No PM 2007 #14 Recovery Boiler unspecified 7/17/2007 M5 18.7

No PM 2011 No. 3 Recovery Furnace unspecified 6/21/2011 M5 47.59126

No PM 2011 RFEU unspecified 1/27/2011 M5 50.4166666

No PM 2008 Recovery Boiler 2 unspecified 10/16/2008 M5 114.187

No PM 2007 Recovery Boiler West Stack unspecified 10/9/2007 M5 33.5416666

No PM 2007 Recovery Boiler East Stack unspecified 10/9/2007 M5 33.5416666

No PM 2007 Recovery Boiler Combined unspecified 10/9/2007 M5 Unspecified 

No PM 2011 Recovery Boiler unspecified 6/7/2011 M5 32.08

No PM 2007 No. 2 Recovery Furnace unspecified 5/23/2007 M5 unspecified

No PM 2004 Recovery Boiler ‐ Old Stack unspecified 9/30/2004 M5 43

No PM 2004 Recovery Boiler ‐ New Stack unspecified 9/30/2004 M5 43

No PM 2011 Recovery Furnace No. 1 unspecified 6/21/2011 M5 51.7

No PM 2011 Recovery Furnace No. 2 unspecified 6/22/2011 M5 51.7

No PM 2010 No. 3 Recovery Furnace unspecified 3/24/2010 M5 8

No PM 2009 RB NO. 1 unspecified 9/24/2009 M5 47.273

No PM 2011 No. 3 Recovery Furnace unspecified 6/15/2011 M5 76.2

No PM 2010 Recovery Boiler unspecified 10/26/2010 M5 Unspecified 

No PM 2005 Recovery Boiler, SN‐05A unspecified 6/22/2005 M5 47.6666666

No PM 2011 No. 4 Recovery Boiler unspecified 4/26/2011 M5 unspecified 

no PM 2010 Recovery Boiler 4 unspecified 10/25/2010 M5 62.4

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

606.RB3606.RB3606.RB2606.RB2610.4, 5610.4, 5610.4, 5610.4, 5105.EU445C105.EU445C105.EU445C105.EU445C109.RB4178.08P013178.08P012139.02139.02152.03152.03152.03166.RB02

Has the configuration of

the emission unit,

combustion controls,

collection system, or

APCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly ProductionRate(value)

no PM 2010 Recovery Boiler 3 unspecified 10/25/2010 M5 3

no PM 2010 Recovery Boiler 3 unspecified 10/26/2010 M5 3

no PM 2011 Recovery Boiler 2 ‐Scenario 1 unspecified 4/5/2011 M5 65.7

no PM 2011 Recovery Boiler 2 ‐Scenario 2 unspecified 4/5/2011 M5 67.7

no PM 2008

Combined Recovery Boiler Stack ‐ Condition 1: Max Liquor

Rec. Boilers 1 & 2 unspecified 11/11/2008 M5 Unspecified

no PM 2008

Combined Recovery Boiler Stack ‐ Condition 2: 1 ESP Bank

down, Maximum Liquor Rec. Boilers 1 & 2 One ESP Side

Down Max Liquor Rec. Boiler 2, Oil Fire Rec. Boiler 1 unspecified 11/12/2008 M5 Unspecified

no PM 2008

Combined Recovery Boiler Stack ‐ Condition 3: 2 ESP Banks

Down, Controlled Liquor Firing Rec. Boilers 1 & 2 unspecified 11/15/2008 M5 Unspecified

no PM 2008

Combined Recovery Boiler Stack ‐ Condition 4: One ESP Side

Down Maximum Liquor Rec. Boiler 2, Oil Fire Rec. Boiler 1 unspecified 11/10/2008 M5 Unspecified

no PM 2008 No. 4 Recovery Boiler Natural Gas 05/20/2008

EPA\ODEQ

M5 6

no PM 2008 No. 4 Recovery Boiler Natural Gas 10/22/2008

EPA\ODEQM5 59

no PM 2009 No. 4 Recovery Boiler Natural Gas 06/03/2009

EPA\ODEQM5 57.7

no PM 2009 No. 4 Recovery Boiler Natural Gas 9/24/2009

EPA\ODEQM5 53.0

No PM 2004 No. 4 Recovery Boiler unspecified 06/02/2004 M5 82.0

No PM 2004 No. 2 Recovery Furnace unspecified 9/8/2004 M5 60.2No PM 2004 No. 1 Recovery Furnace unspecified 09/07/2004 M5 60.2

No PM 2004 Recovery furnace unspecifIed 8/18/2004 M5 53.0

No PM 2004 Recovery furnace unspecified 9/9/2004 M5 61.821

Yes

added intermediate air

(3rd level) in Fall 2007 PM 2001 Recovery furnace scrubber inlet and outlet unspecified 3/29/2001 M5 70.2777777

Yes

added intermediate air

(3rd level) in Fall 2007 PM 2004 Recovery furnace unspecified 9/1/2004 M5 67

Yes

added intermediate air

(3rd level) in Fall 2007 PM 2002 Recovery furnace unspecified 9/24/2002 M5 unspecified 

No PM 2004 No. 2 Recovery Furnace unspecified 6/15/2004 M5 unspecified 

Test_data_memo_appendices.xlsx App A RF PM 
ble Particulate Matter

RTI+EUID100.037A103.G‐158105.EU445C107.08‐P1

108.RB3109.RB3109.RB4111.G‐44114.U500114.U500116.003119.EQT008119.EQT010119.EQT010120.F7124.001124.001126.RECOV126.RECOV126.RECOV126.RECOV127.REC1N127.REC1N131.6131.5131.5131.5132.5RB132.5RB132.4RB133.10133.10

Inlet ‐ Testing Methodology Data Inlet ‐ Average Stack Gas Parameters Inlet ‐ Average Emissions DataAverage Sampling Run

Length_Inlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflowRate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number ofInlet Test Runs

Count InletNon‐DetectRuns

82 101.3 321000 148000 32.7 319 30.26 15.9 15.9 4 gr/dscf @ 8% O2 3 

76.33 102.2 287000 136000 32.3 310 30.51 13.2 6.5 3.1 gr/dscf @ 8% O2 3 

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

135.003‐1135.003‐1136.EU 005

137.721137.189138.002142.CU7214143.7010143.7020146.8146.8147.14147.14147.5147.5148.007148.001150.CREC‐1

152.03152.03155.RECOVERYFURNACE156.RF22156.RF22

Average Sampling Run

Length_Inlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflowRate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number ofInlet Test Runs

Count InletNon‐DetectRuns

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

156.RF22156.RF22156.RF18156.RF18156.RF19156.RF19156.RF19156.RF19162.381A162.381A163.RF1901163.RF2904163.RF2904164.B08,B10 combined

164.B08,B10 combined

164.B08,B10 combined

164.B08,B10 combined

165.000013165.000013

Average Sampling Run

Length_Inlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflowRate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number ofInlet Test Runs

Count InletNon‐DetectRuns

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

165.000006165.000006166.RB01166.RB01166.RB02169.04169.05172.RB02172.RB01174.G‐92174.G‐92174.G‐32175.RB3A176.RB7177.EU0804179.RF3181.9181.10181.49181.50182.037184.73184.72185.02185.02185.02185.02185.02185.02185.02186.RB15189.SN26190.R402190.R402

Average Sampling Run

Length_Inlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflowRate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number ofInlet Test Runs

Count InletNon‐DetectRuns

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

190.R401196.SN‐14196.SN‐06196.SN‐06197.2198.019200.007RF2200.007RF3202.Recovery Furnace

EU320203.RF#3203.RF#2203.RF#3207.038207.038226.RECB1226.RECB1240.RF04240.RF01242.AA‐011

243.R407243.R401243.R401531.RF15600.G0806600.G0803615.24615.24615.24615.24617.B14115.RE01

Average Sampling Run

Length_Inlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflowRate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number ofInlet Test Runs

Count InletNon‐DetectRuns

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

115.RE01105.EU445C105.EU445A121.000013121.000014121.000013121.000014124.019124.019130.1130.1130.2130.2142.CU7216143.7000145.54145.55154.P39 and P37 ‐ 

Recovery Furnace 1

and Recovery Furnace

3154.P36 ‐ Recovery

Furnace 2

154.P39 ‐ Recovery

Furnace 1

167.005RB167.005RB171.002171.003175.RB2A188.016RB2

Average Sampling Run

Length_Inlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflowRate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number ofInlet Test Runs

Count InletNon‐DetectRuns

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

188.016RB2188.014RB1205.009205.009205.009206.G‐31206.G‐32613.001L613.001R613.001L&001R613.002R613.002L613.002L&002R102.RB10117.B21130.3140.55146.16157.RB2157.RB2157.RB2159.F3162.382A173.RECOVB173.RECOVB178.08P012178.08P013180.D001190.R400199.002201.SR0001340.005525.EU18606.RB4

Average Sampling Run

Length_Inlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflowRate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number ofInlet Test Runs

Count InletNon‐DetectRuns

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

606.RB3606.RB3606.RB2606.RB2610.4, 5610.4, 5610.4, 5610.4, 5105.EU445C105.EU445C105.EU445C105.EU445C109.RB4178.08P013178.08P012139.02139.02152.03152.03152.03166.RB02

Average Sampling Run

Length_Inlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflowRate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number ofInlet Test Runs

Count InletNon‐DetectRuns

60 95.9 360912 174336 30.9 302.9 30.23 11.7 8.3 0.086 gr/dscf @ 8%O2 3 

Test_data_memo_appendices.xlsx App A RF PM 
ble Particulate Matter

RTI+EUID100.037A103.G‐158105.EU445C107.08‐P1

108.RB3109.RB3109.RB4111.G‐44114.U500114.U500116.003119.EQT008119.EQT010119.EQT010120.F7124.001124.001126.RECOV126.RECOV126.RECOV126.RECOV127.REC1N127.REC1N131.6131.5131.5131.5132.5RB132.5RB132.4RB133.10133.10

Outlet ‐ Testing Methodology Data Outlet ‐ Average Stack Gas Parameters Outlet ‐ Average Emissions Data

Average Sampling Run

Length_Outlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outlet

concentration units

NumbeOutlet 

Runs

69.33 97.4 258000 116000 24.2 382 28.41 14.3 5.2 0.014 gr/dscf @ 8% O2 

71.67 104.6 507000 260000 20.4 358.4 29.81 13.8 5.5 0.0099 gr/dscf @ 8% O2 

80 94.3 243590 112870 26.14 358.85 29.12 14.34 5.6 0.0112 gr/dscf @ 8% O2 

60 98.2 456770 222392 24.8 349.9 29.701 15.02 4.75 0.0045 gr/dscf @ 8% O2 

60 101.73 490732.7 224253.5 28.9 362.6 29.95 14 7.8 0.0025 gr/dscf @ 8% O2 

60 99.97 239860 122473.3 24.03 317.47 29.6 12.93 5.93 0.024 gr/dscf @ 8% O2 

64 102.27 301152.3 97763.3 25.1 377.57 29.5 15.27 3.8 0.018 gr/dscf @ 8% O2 

69.7 99.25 459566 216459 21.9 408.02 29.67 12.9 6.63 0.00333 gr/dscf @ 8% O2 

60 100.7 389727 186632 25.6 357.67 39.83 14 5.87 0.0138 gr/dscf @ 8% O2 

60 103.8 521241 238195 26 393.3 29.88 14 5.6 0.0143 gr/dscf @ 8% O2 

65.67 91.34 423933 196609 25.5 390.89 29.88 14.27 5.19 0.01 gr/dscf @ 8% O2 

60 107.33 330253.7 176574 22.97 306.76 30.14 9 10.8 0.0107 gr/dscf @ 8% O2 

60 102.03 399960 225102 19.378 302.94 30.269 9.6 9.9 0.02844 gr/dscf @ 8% O2 

60 104 374913 205562 22.2 286.46 29.81 10.5 9.27 0.017 gr/dscf @ 8% O2 

64.67 100.8 458305 222779 25.43 338 29.49 15.5 3.7 0.01 gr/dscf @ 8% O2 

62 97.9 160000 78419 31.1 275.1 29.56 11 8 0.0014 gr/dscf @ 8% O2 

61.7 100.8 161000 77743 31.6 285.8 29.88 11 8.1 0.0019 gr/dscf @ 8% O2 

64 104.08 150435 71712 23.88 368.4 29.4 13.57 6.49 0.0245 gr/dscf @ 8% O2 

64 95.05 141404 65745 25.26 374 29.4 13.76 6.16 0.0132 gr/dscf @ 8% O2 

64 106.26 146024 71741 21.74 366.3 29.4 13.94 6.13 0.0177 gr/dscf @ 8% O2 

64 98.31 137567 64668 24.77 370.2 29.4 14.19 5.83 0.0114 gr/dscf @ 8% O2 

61 101 152000 72073 24.6 382.4 30.02 14 5 0.0065 gr/dscf @ 8% O2 

61.667 100.6 158000 75849 23.5 382.5 30.02 14 5.1 0.0121 gr/dscf @ 8% O2 

73 100.6 316000 140000 29.1 387 29.92 13.9 5.5 0.011 gr/dscf @ 8% O2 

75 99.3 343000 154000 33.9 315 29.89 14 5.8 0.019 gr/dscf @ 8% O2 

82 100.6 323000 147000 34 310 30.08 14.3 5.3 0.004 gr/dscf @ 8% O2 

76.33 97.6 287000 138000 32.3 437.8 30.34 12.4 7.3 0.008 gr/dscf @ 8% O2 

60 99.72 192377 83074 26.9 432.72 29.88 15.1 5.05 0.0079 gr/dscf @ 8% O2 

60 100.37 184022 81523 25.23 430.04 29.87 14.7 5.5 0.0031 gr/dscf @ 8% O2 

60 98.263 373806 164912 25.12 433.21 29.81 13.96 6.11 0.0061 gr/dscf @ 8% O2 

72 101.62 413958 192424 27.57 412 29.92 14.5 5.8 0.0015 gr/dscf @ 8% O2 

72 103.44 407949 182740 26.99 407 29.92 13.1 6.4 0.0117 gr/dscf @ 8% O2 

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

135.003‐1135.003‐1136.EU 005

137.721137.189138.002142.CU7214143.7010143.7020146.8146.8147.14147.14147.5147.5148.007148.001150.CREC‐1

152.03152.03155.RECOVERYFURNACE156.RF22156.RF22

Average Sampling Run

Length_Outlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outlet

concentration units

NumbeOutlet 

Runs

60 104.3 580521 263245 24.5 425 30.13 14.1 5.6 0.013 gr/dscf @ 8% O2 

60 103.1 445047 209598 24.8 387 30.07 11.9 5.5 0.009 gr/dscf @ 8% O2 

60 100.2 488000 226000 23.6 369 28.6 15 4.6 0.008 gr/dscf @ 8% O2 

60 101.8 414035 189397 25.32 379.25 29.14 15.89 3.36 0.0037 gr/dscf @ 8% O2 

60 102.8 168000 81900 23.15 351 29.11 14.17 5.22 0.0117 gr/dscf @ 8% O2 

65 96.18 322899 156539.37 23.78 370.13 29.96 8.53 5.93 0.01251 gr/dscf @ 8% O2 

66 93.28 165371 66043 35.6 379 29.56 14.25 5.72 0.004 gr/dscf @ 8% O2 

60 106.33 98945 46223 34.17 287.79 30.07 11.4 7.2 0.003 gr/dscf @ 8% O2 

64.67 105.3 148513 67391 31 342 30 11.57 6.5 0.007 gr/dscf @ 8% O2 

65 98.9 198000 84874 32.9 307.3 27.84 11.2 7.6 0.0218 gr/dscf @ 8% O2 

65 101 238000 104000 32.6 297.8 27.81 10.7 8.3 0.0091 gr/dscf @ 8% O2 

62.67 96 142366 70100 22 371 29.86 12.9 6.7 0.0127 gr/dscf @ 8% O2 

62.67 96 141734 71600 21 366 29.87 13.1 6.6 0.0117 gr/dscf @ 8% O2 

60 98.5 532080 259940 21.7 383.3 29.82 11.4 8.1 0.00967 gr/dscf @ 8% O2 

60 97.8 524183 249844 22.2 400 29.85 11.8 7.8 0.0108 gr/dscf @ 8% O2 

78.3 104.7 379365 176204 25.8 388 30.09 15.4 6.4 0.0128 gr/dscf @ 8% O2 

75 102.4 299477 130819 26.9 429 30.1 13.2 6.8 0.0147 gr/dscf @ 8% O2 

60 99.7 460220 204885 25.2 431 30.02 14.5 3.9 0.014 gr/dscf @ 8% O2 

60 97.8 331941 191448 33.8 159.7 29.8 11.3 8.6 0.0373 gr/dscf @ 8% O2 

60 97.5 340398 196976 33.9 159.8 29.89 11.1 8.9 0.03 gr/dscf @ 8% O2 

67 98.6 425330 182395 25.2 461 29.9 17 3.5 0.0229 gr/dscf @ 8% O2 

60 103 332243 183052 20.5 284 30.19 13.1 5.8 0.0014 gr/dscf @ 8% O2 

60 102.8 281672 154887 22.1 261 29.72 12.4 6.5 0.0013 gr/dscf @ 8% O2 

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

156.RF22156.RF22156.RF18156.RF18156.RF19156.RF19156.RF19156.RF19162.381A162.381A163.RF1901163.RF2904163.RF2904164.B08,B10 combined

164.B08,B10 combined

164.B08,B10 combined

164.B08,B10 combined

165.000013165.000013

Average Sampling Run

Length_Outlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outlet

concentration units

NumbeOutlet 

Runs

60 105.2 228757 124294 23.3 268 30.02 12.7 6.2 0.0025 gr/dscf @ 8% O2 

60 106.2 257871 136158 24.4 277 29.98 13.3 5.6 0.0003 gr/dscf @ 8% O2 

60 106 276170 159329 22.4 235 30.05 8.8 10.7 0.0011 gr/dscf @ 8% O2 

60 104.5 333017 196875 26.3 177 30.01 10.2 9.3 0.0036 gr/dscf @ 8% O2 

60 99.8 328145 180179 26.4 249 30.33 10.3 9.2 0.0017 gr/dscf @ 8% O2 

60 97.8 427002 231635 23.3 271 29.84 10.1 9.4 0.0056 gr/dscf @ 8% O2 

60 99.3 359458 195853 26.6 247 30.1 10.1 9.4 0.0022 gr/dscf @ 8% O2 

60 95.5 351891 196955 23.4 256 30.1 10.5 9 0.0029 gr/dscf @ 8% O2 

67.7 101 289000 131000 26 401 29.97 13.6 6.4 0.009 gr/dscf @ 8% O2 

67.3 103 277000 121000 27 408 29.41 14.2 5.4 0.007 gr/dscf @ 8% O2 

63.3 99.7 245035 116011 34.2 281 29.94 14.8 4.1 0.00551 gr/dscf @ 8% O2 

60 99.4 181987 82237 24.8 410 30.02 14 4.7 0.017 gr/dscf @ 8% O2 

60 99.5 182796 87036 21.7 400 30.02 10.17 8.5 0.016 gr/dscf @ 8% O2 

60 102.5 119336 51621 26 431.1 29.11 9.9 10 0.0262 gr/dscf @ 8% O2 

60 99.8 150948 66317 25 416.4 29.09 10.9 9 0.0167 gr/dscf @ 8% O2 

60 98.9 138751 64122 21.7 416.5 29.31 8.8 11.2 0.0373 gr/dscf @ 8% O2 

60 100.5 172020 77522 22.2 433 29.31 9.3 10.7 0.0216 gr/dscf @ 8% O2 

64.3 97 141430 65800 23 404 29.6 12.4 7.4 0.023 gr/dscf @ 8% O2 

64.3 95 160321 78100 21 385 29.59 11 9 0.029 gr/dscf @ 8% O2 

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

165.000006165.000006166.RB01166.RB01166.RB02169.04169.05172.RB02172.RB01174.G‐92174.G‐92174.G‐32175.RB3A176.RB7177.EU0804179.RF3181.9181.10181.49181.50182.037184.73184.72185.02185.02185.02185.02185.02185.02185.02186.RB15189.SN26190.R402190.R402

Average Sampling Run

Length_Outlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outlet

concentration units

NumbeOutlet 

Runs

64.3 100 265261 121000 23.8 414 29.55 14.3 5.5 0.02 gr/dscf @ 8% O2 

64.3 99 239077 109000 23.8 414 29.55 13.7 6.1 0.015 gr/dscf @ 8% O2 

60 103.5 174027 72552 35.7 342.9 29.53 13.3 5.3 0.0175 gr/dscf @ 8% O2 

60 97.7 185571 85801 30.2 325.6 29.52 13.4 5.4 0.0094 gr/dscf @ 8% O2 

60 98 364537 185388 38.7 169.9 29.63 15.2 4.9 0.0294 gr/dscf @ 8% O2 

60 94.6 334532 148630 27.6 386.7 29.46 15.3 4.4 0.0072 gr/dscf @ 8% O2 

60 94.8 353179 160425 26.2 388 29.58 14 5.7 0.0095 gr/dscf @ 8% O2 

60 103 254247 120496 23.3 393.67 29.92 12.5 5.06 0.016 gr/dscf @ 8% O2 

60 105.2 181917 87327 24.8 367 29.92 13.67 5.03 0.0192 gr/dscf @ 8% O2 

60 102.5 147312 70361 28.3 327.4 29.75 11.5 8.4 0.0238 gr/dscf @ 8% O2 

60 100.9 146651 65787 30.8 348.8 29.72 12.8 7.2 0.0206 gr/dscf @ 8% O2 

60 100.8 619514 295924 22.3 392.6 29.71 14.7 5.1 0.0052 gr/dscf @ 8% O2 

60 101.4 531445 230685 28.3 408.6 29.79 16.63 3.18 0.0166 gr/dscf @ 8% O2 

60 102.2 338207 157603 23.6 404 29.89 14.7 4.8 0.0038 gr/dscf @ 8% O2 

60 102.3 429145 187441 26.7 393 28.8 14.7 4.5 0.0093 gr/dscf @ 8% O2 

60 95.3 437017 205989 22.4 395.3 29.47 14.8 3.8 0.009 gr/dscf @ 8% O2 

60 98.8 117636.3 53706 25.7 396.7 29.82 13.3 5.7 0.0227 gr/dscf @ 8% O2 

60 99.8 163100.3 73735.3 27.23 403.5 29.81 14.0 5.0 0.0294 gr/dscf @ 8% O2 

60 97.8 121816 59674 23.9 360.7 29.96 13.1 6.2 0.0186 gr/dscf @ 8% O2 

60 97.3 127058 62264 23.1 370.2 29.99 12.3 7.2 0.0108 gr/dscf @ 8% O2 

96 100.2 240265.3 113084.3 24 380.5 29.52 15.2 3.9 0.0027 gr/dscf @ 8% O2 

60 100.5 408197.9 190996.1 22.38 412 29.84 14 4.70 0.0036 gr/dscf @ 8% O2 

60 100.0 264041.2 128828.9 21.62 384.4 29.79 13.5 5.81 0.0039 gr/dscf @ 8% O2 

60 98.8 214116.45 132150 28.19 154.33 29.92 9.83 7.47 0.0237 gr/dscf @ 8% O2 

60 95.4 225236.17 140852 27.24 154.33 29.92 12 7.13 0.019 gr/dscf @ 8% O2 

60 96.5 214548.70 142444 23.51 148.33 29.92 8.67 7.37 0.0305 gr/dscf @ 8% O2 

60 96.8 215615.44 141331 24.40 149 29.92 8 7.6 0.03007 gr/dscf @ 8% O2 

60 95.1 209095.78 140158 22.81 148 29.92 11 6.93 0.02217 gr/dscf @ 8% O2 

60 97.7 205788.90 139843 22.01 146 29.92 11.83 7.23 0.017 gr/dscf @ 8% O2 

60 97.2 215277.94 146335 21.98 146 29.92 10.67 7.16 0.018 gr/dscf @ 8% O2 

60 95.07 577045 253748 27.23 414.3 29.95 15.5 5.2 0.0042 gr/dscf @ 8% O2 

60 97.47 585204.6 258279.2 30.69 372 30.02 17.42 2.8 0.0067 gr/dscf @ 8% O2 

60 102.1 149082 64630 30.2 395.33 30.1 14.32 5.45 0.006 gr/dscf @ 8% O2 

60 103 175568 77053 31.1 375 30.14 14.25 5.44 0.005 gr/dscf @ 8% O2 

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

190.R401196.SN‐14196.SN‐06196.SN‐06197.2198.019200.007RF2200.007RF3202.Recovery Furnace

EU320203.RF#3203.RF#2203.RF#3207.038207.038226.RECB1226.RECB1240.RF04240.RF01242.AA‐011

243.R407243.R401243.R401531.RF15600.G0806600.G0803615.24615.24615.24615.24617.B14115.RE01

Average Sampling Run

Length_Outlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outlet

concentration units

NumbeOutlet 

Runs

60 103.1 250816 119201 26.9 348.67 29.8 13.299 6.96 0.007 gr/dscf @ 8% O2 

60 100.3 499177 221767 26.4 413.1 29.864 17.23 1.73 0.0051 gr/dscf @ 8% O2 

60 99.7 406112 188857 23.8 400.1 29.754 14.77 5.76 0.0073 gr/dscf @ 8% O2 

60 99.7 421002 201168 21.9 397.7 29.76 15.2 3.8 0.0082 gr/dscf @ 8% O2 

60 105.5 73051 42947 32 152.5 30.01 9.97 8.1 0.0126 gr/dscf @ 8% O2 

60 96.9 457140 214314 23.9 370.6 28.978 15.19 3.98 0.01 gr/dscf @ 8% O2 

64 99.4 236959 114493 24.6 349.2 29.39 12.5 7.1 0.001 gr/dscf @ 8% O2 

60 99.5 433996 209845 23 364.9 29.46 13.3 6.5 0.021 gr/dscf @ 8% O2 

60 102 319000 142000 22.74 405 28.3 14.3 4.5 0.0058 gr/dscf @ 8% O2 

60 102 298210.06 163169 22.9 284 30.04 unspecified 6.8 0.0022 gr/dscf @ 8% O2 

78.67 99.47 83828.67 41937 23.67 335 29.522 9.32 9.915 0.0074 gr/dscf @ 8% O2 

78 99.53 350042.33 158072 24.71 409.3 29.549 13.1 5.592 0.0017 gr/dscf @ 8% O2 

60 100.77 56337.33 24510.33 28.5 373.67 28.76 11.25 8.58 0.013 gr/dscf @ 8% O2 

60 105.37 59683.33 26019.67 28.68 369.67 28.75 11.17 15.72 0.013666667 gr/dscf @ 8% O2 

60 100.9 235861 124134 22.2 313.9 29.69 9.7 9.2 0.0111 gr/dscf @ 8% O2 

60 99.1 173822 92786 21.6 308.6 29.68 9.7 9.1 0.003 gr/dscf @ 8% O2 

60 105.1 722308 331224 25.2 395.9 29.76 15.6 3.9 0.0064 gr/dscf @ 8% O2 

60 98.1 397532 185688 26.9 357.2 29.62 14.2 5.4 0.004 gr/dscf @ 8% O2 

60 102.4 637978 283698 26.5 408 29.76 14.7 4.2 0.0101 gr/dscf @ 8% O2 

60 97.9 480683 227756 25.1 369.3 29.73 14.1 5.4 0.016 gr/dscf @ 8% O2 

60 101.9 232134 110250 22.4 399.4 29.83 13 6.8 0.004 gr/dscf @ 8% O2 

60 101.6 234775 113459 21.1 399.6 29.83 12.9 6.9 0.003 gr/dscf @ 8% O2 

60 103.7 668962 333464 22.1 360.8 29.78 15.5 4.7 0.0098 gr/dscf @ 8% O2 

60 99 436346 191923 25 419.1 29.23 14.2 3.9 0.008 gr/dscf @ 8% O2 

60 101.1 490958 221784 29.6 344.6 29.28 12.3 7.5 0.013 gr/dscf @ 8% O2 

60 100.9 172823 77721 26 404.8 29.77 13.87 4.85 0.0163 gr/dscf @ 8% O2 

60 99.7 178766 78177 25.9 399.8 28.77 14.03 5.01 0.0246 gr/dscf @ 8% O2 

60 100.9 172823 77721 26 404.8 29.77 13.87 4.85 0.0198 gr/dscf @ 8% O2 

60 99.7 178766 78177 25.9 399.8 28.77 14.03 5.01 0.0282 gr/dscf @ 8% O2 

77 91.3 189986 96726 17.2 380.9 29.29 14.3 4.7 0.0054 gr/dscf @ 8% O2 

65.66666667 96.4 283000 127000 26.1 406 29.9 14.4 4.3 0.002023952 gr/dscf @ 8% O2 

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

115.RE01105.EU445C105.EU445A121.000013121.000014121.000013121.000014124.019124.019130.1130.1130.2130.2142.CU7216143.7000145.54145.55154.P39 and P37 ‐ 

Recovery Furnace 1

and Recovery Furnace

3154.P36 ‐ Recovery

Furnace 2

154.P39 ‐ Recovery

Furnace 1

167.005RB167.005RB171.002171.003175.RB2A188.016RB2

Average Sampling Run

Length_Outlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outlet

concentration units

NumbeOutlet 

Runs

65.66666667 105.1 307000 145000 22.4 407.3 29.9 14.7 4.1 0.005538462 gr/dscf @ 8% O2 

81.33333333 96.9 258148 123293 27.35 337.76 29.73 14.17 5.00 0.0175 gr/dscf @ 8% O2 

60 96 306462 138706 28.57 343.76 28.87 14.01 5.52 0.0099 gr/dscf @ 8% O2 

60 101 224108 102000 31 331 29.68 11.1 8.9 0.015 gr/dscf @ 8% O2 

60 102 215092 98000 31 327 28.95 11 8.9 0.012 gr/dscf @ 8% O2 

60 103 220083 106000 30 322 30.44 12.6 8 0.008 gr/dscf @ 8% O2 

60 103 206796 95300 33 320 30.58 14.3 6.3 0.006 gr/dscf @ 8% O2 

60 105.1 160000 77340 30.9 288.8 29.63 11.3 7.5 0.0195 gr/dscf @ 8% O2 

60 94.6 170000 74441 32.4 344.5 29.62 11.5 7.3 0.0304 gr/dscf @ 8% O2 

60 97.6 99057 50530 26.4 291.66 29.52 11.02 9.15 0.0154 gr/dscf @ 8% O2 

60 99 101976 47286 30.2 324.33 29.51 11.02 9.15 0.0172 gr/dscf @ 8% O2 

60 99.8 113664 56267 28.5 288.33 29.36 10.97 9.32 0.0115 gr/dscf @ 8% O2 

60 103.2 108340 52914 27.7 307.33 29.39 10.97 9.32 0.0115 gr/dscf @ 8% O2 

62.33333333 88 150327 64588 34.8 339 29.89 12.13333333 5.97 0.006 gr/dscf @ 8% O2 

68.66666667 102 106748 50130 31 322 30.09 10 7.8 0.007 gr/dscf @ 8% O2 

62.5 105.1 250436 108454 31.5 337.33 28.76 14.8 6.1 0.002919932 gr/dscf @ 8% O2 

60 102.4 208555 95455 27.7 342.33 28.8 13.8 6.7 0.007199595 gr/dscf @ 8% O2 

60 97.67 322223 160757 27.3 265.3 28.21 13.2 6.7 0.0159 gr/dscf @ 8% O2 

60 101.13 145521 70646 30.9 275.9 29.25 14.5 5.4 0.0147 gr/dscf @ 8% O2 

60 101.6 194684 99093 27 260.2 28.45 10.8 9.5 0.0076 gr/dscf @ 8% O2 

60 97 164475 70774 37.1 315 30.15 13.7 6.54 0.013 gr/dscf @ 8% O2 

60 96 161717 73287 32.8 325 30.15 13.11 7.72 0.033 gr/dscf @ 8% O2 

60 100.8 117276 60677 28 269 29.82 14.8 5.6 0.025 gr/dscf @ 8% O2 

60 104.8 117395 57231 31 281.9 29.69 13.3 6.4 0.02 gr/dscf @ 8% O2 

60 97.5 222986 116304 25.4 293.6666667 29.92 8.2 10.9 0.01 gr/dscf @ 8% O2 

72 98.36 200741 103060 28.48 282.5 30.2 10.6 9.6 0.012 gr/dscf @ 8% O2 

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

188.016RB2188.014RB1205.009205.009205.009206.G‐31206.G‐32613.001L613.001R613.001L&001R613.002R613.002L613.002L&002R102.RB10117.B21130.3140.55146.16157.RB2157.RB2157.RB2159.F3162.382A173.RECOVB173.RECOVB178.08P012178.08P013180.D001190.R400199.002201.SR0001340.005525.EU18606.RB4

Average Sampling Run

Length_Outlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outlet

concentration units

NumbeOutlet 

Runs

72 98.36 200741 103060 28.48 282.5 30.2 10.6 9.6 0.013 gr/dscf @ 8% O2 

60 99.08 170932 86912 28.91 280 30 11.6 8.9 0.006 gr/dscf @ 8% O2 

61 99.1 128,730 55,790 Unspecified 329 29.95 12.83333333 5.6 0.012 gr/dscf @ 8% O2 

61 101.6 134,269 58,759 Unspecified 325 29.95 12.83333333 5.366666667 0.012 gr/dscf @ 8% O2 

Unspecified Unspecified Unspecified Unspecified Unspecified Unspecified Unspecified Unspecified Unspecified 0.012 gr/dscf @ 8% O2 

60 94.3 399000 188000 27.3 279.7 27.26 11 9.1 0.011361345 gr/dscf @ 8% O2 

60 98.2 408000 189000 28.3 284.3 27.15 12.7 7.3 0.012525547 gr/dscf @ 8% O2 

60 94 183237 89461 26.4 331 29.7296 13.68 6.09 0.019 gr/dscf @ 8% O2 

60 94 153509 75810 29 300 29.94 12.73 7.02 0.022 gr/dscf @ 8% O2 

Unspecified Unspecified Unspecified 165271 Unspecified Unspecified Unspecified Unspecified Unspecified Unspecified Unspecified 

60 95 151379 70577 29.8 325 29.56 14.09 5.68 0.0058 gr/dscf @ 8% O2 

60 95 154706 73366 28.5 326 29.56 13.93 5.89 0.0109 gr/dscf @ 8% O2 

Unspecified Unspecified Unspecified 143942 Unspecified Unspecified Unspecified Unspecified Unspecified Unspecified Unspecified 

60 98.67 531996 249578 26.25 377.3 30.18 13.9 5.7 0.0047 gr/dscf @ 8% O2 

60 96.9 123189 58982 unspecified 369 unspecified 12.9 6.9 0.0131 gr/dscf @ 8% O2 

60 99 241271 109424 25 412.33 29.94 13.95 5.86 0.00295 gr/dscf @ 8% O2 

60 100.8 230507 106006 23.07 421.3 29.98 12.7 6.07 0.012 gr/dscf @ 8% O2 

60 95.1 527000 247000 22.6 380.4 28.78 15.8 2.9 0.004022099 gr/dscf @ 8% O2 

60 96.1 82804 35775 28.4 417 30.02 15 4.17 0.038 gr/dscf @ 8% O2 

60 99.5 77359 33805 28.2 410 30.03 15.3 3.7 0.048 gr/dscf @ 8% O2 

unspecified unspecified unspecified unspecified unspecified unspecified unspecified unspecified unspecified 0.043 gr/dscf @ 8% O2 

60 101 159040 unspecified 31 137 29.87 unspecified 7.6 0.032 gr/dscf @ 8% O2 

60 100 541000 243000 26 406 29.8 15.1 4.1 0.0083 gr/dscf @ 8% O2 

60 103.1 unspecified 67700 22 412 unspecified 11.3 9.4 0.0134 gr/dscf @ 8% O2 

60 105.2 unspecified 45300 25.2 406 unspecified 12 8.2 0.00296 gr/dscf @ 8% O2 

60 105 324757 141409 26 420 29.45 14.4 5 0.017 gr/dscf @ 8% O2 

60 104 314904 135618 27 417 29.45 14.4 5.3 0.014 gr/dscf @ 8% O2 

60 95 373105 184000 23 362 29.69 13.4 5.8 0.005 gr/dscf @ 8% O2 

60 95.1 277000 137000 24.4 343.4 29.72 12.2 7.4 0.0099 gr/dscf @ 8% O2 

60 100 unspecified 225000 21 384 29.23 12.4 6.4 0.0109 gr/dscf @ 8% O2 

60 100.65 457352.9 214191.8 25.79 369.4 29.61 13.51 6.31 0.0164 gr/dscf @ 8% O2 

60 98 237348 122869 21.06666667 347 30.006 14.1 6.2 0.0239 gr/dscf @ 8% O2 

60 100 387371 unspecified 21 392 unspecified unspecified 4.6 0.004 gr/dscf @ 8% O2 

60 100.63 337630 146198 26.44 437.72 30.03 12.73 6.39 0.0258 gr/dscf @ 8% O2 

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

606.RB3606.RB3606.RB2606.RB2610.4, 5610.4, 5610.4, 5610.4, 5105.EU445C105.EU445C105.EU445C105.EU445C109.RB4178.08P013178.08P012139.02139.02152.03152.03152.03166.RB02

Average Sampling Run

Length_Outlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outlet

concentration units

NumbeOutlet 

Runs

60 103.82 197006 108567 21.31 297 30.03 12.25 8.01 0.0285 gr/dscf @ 8% O2 

60 103.09 202041 105093 25.28 300.57 29.99 12.15 8.16 0.0037 gr/dscf @ 8% O2 

60 99.62 241107 114000 24.26 385 29.86 12.34 7.62 0.0162 gr/dscf @ 8% O2 

60 98.84 257081 118143 26.06 390 29.93 12.71 7.37 0.0235 gr/dscf @ 8% O2 

60 104.3 559591 262821.5667 24.8 391.7 unspecified 13.42 5.87 0.011 gr/dscf @ 8% O2 

60 105 576491 268060 25 395.1 unspecified 13.54 5.86 0.013 gr/dscf @ 8% O2 

60 104.6 540472 245517 25.4 390.6 unspecified 13.55 5.73 0.017 gr/dscf @ 8% O2 

60 99.2 362223 198932 16.9 342.8 unspecified 9.19 10.22 0.033 gr/dscf @ 8% O2 

88.3 95.4 270724 130045 24.96 351.06 29.43 12.8 6.87 0.0208 gr/dscf @ 8% O2 

91 97.7 254749 123511 25.91 342.79 29.78 14.52 4.69 0.0165 gr/dscf @ 8% O2 

67 99.4 270638 128101 26.08 342.28 29.12 14.27 4.47 0.0177 gr/dscf @ 8% O2 

73.3 99.6 229078 110212 26.52 325 29.13 13.1 5.9 0.0222 gr/dscf @ 8% O2 

64 99.6 288260 132840 26.39 371.4 29.5 14.37 5 0.0287 gr/dscf @ 8% O2 

60 98.8 322880 141390 25.3 425.5 29.42 10.9 5.8 0.023 gr/dscf @ 8% O2 

60 99.4 315084 136180 25.7 432.8 29.42 11.9 4 0.013 gr/dscf @ 8% O2 

60 97 343794 193722 16.99 325.8 30.23 6.4 14.1 0.076 gr/dscf @ 8% O2 

60 96.2 179558 16.8 341 unspecified unspecified 13.3 0.015194805 gr/dscf @ 8% O2 

60 98.9 330799 184725 34.4 164.1 30.1 12.1 7.6 0.019 gr/dscf @ 8% O2 

60 96.4 339964 189037 34.1 162 29.78 12.6 7.5 0.0308 gr/dscf @ 8% O2 

60 102.4 321774 185066 32.9 161.6 30.2 12.3 7.7 0.031278195 gr/dscf @ 8% O2 

60 102.12 376044 196126 38.55 168 30.07 15.71 4.44 0.011 gr/dscf @ 8% O2 

Test_data_memo_appendices.xlsx App A RF PM 
ble Particulate Matter

RTI+EUID100.037A103.G‐158105.EU445C107.08‐P1

108.RB3109.RB3109.RB4111.G‐44114.U500114.U500116.003119.EQT008119.EQT010119.EQT010120.F7124.001124.001126.RECOV126.RECOV126.RECOV126.RECOV127.REC1N127.REC1N131.6131.5131.5131.5132.5RB132.5RB132.4RB133.10133.10

Removal Efficiency Suspect Data Exclude Comment

AverageLb/Production units

Average Pollutant Removal

Efficiency(%) Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

99.9%99.8%

lb/ton BLS

lb/ton BLS

lb/ton BLS

Yes

Only 1 run from in‐

house emission test

lb/day emission rate provided (instead of lb/hr;

divided by 24)

Yes

Only 1 run; summary

of in‐house test only

lb/day emission rate provided (instead of lb/hr;

divided by 24)

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

135.003‐1135.003‐1136.EU 005

137.721137.189138.002142.CU7214143.7010143.7020146.8146.8147.14147.14147.5147.5148.007148.001150.CREC‐1

152.03152.03155.RECOVERYFURNACE156.RF22156.RF22

AverageLb/Production units

Average Pollutant Removal

Efficiency(%) Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

Source to be converted from DCE to NDCE low‐

odor furnace beginning September 2011.

Source to be converted from DCE to NDCE low‐

odor furnace beginning September 2011.

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

Yes

Upon the completion

of the first test, New

Page contacted the

Maine DEP in regards

to processoperational concerns

in regards to an

unscheduled

shutdown and

subsequent start‐up

of the hardwood pulp

mill that supplies the

black liquor fuel for

this boiler. It was

conclude that the

field parameter

values were

abnormal and testing

was thereby delayed

one day for more

representative,higher boiler load

conditions.

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

156.RF22156.RF22156.RF18156.RF18156.RF19156.RF19156.RF19156.RF19162.381A162.381A163.RF1901163.RF2904163.RF2904164.B08,B10 combined

164.B08,B10 combined

164.B08,B10 combined

164.B08,B10 combined

165.000013165.000013

AverageLb/Production units

Average Pollutant Removal

Efficiency(%) Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS Summary sheets only; no test report M

lb/ton BLS Summary sheets only; no test report M

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

165.000006165.000006166.RB01166.RB01166.RB02169.04169.05172.RB02172.RB01174.G‐92174.G‐92174.G‐32175.RB3A176.RB7177.EU0804179.RF3181.9181.10181.49181.50182.037184.73184.72185.02185.02185.02185.02185.02185.02185.02186.RB15189.SN26190.R402190.R402

AverageLb/Production units

Average Pollutant Removal

Efficiency(%) Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

190.R401196.SN‐14196.SN‐06196.SN‐06197.2198.019200.007RF2200.007RF3202.Recovery Furnace

EU320203.RF#3203.RF#2203.RF#3207.038207.038226.RECB1226.RECB1240.RF04240.RF01242.AA‐011

243.R407243.R401243.R401531.RF15600.G0806600.G0803615.24615.24615.24615.24617.B14115.RE01

AverageLb/Production units

Average Pollutant Removal

Efficiency(%) Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

lb/ton BLS

lb/ton BLS Yes

lb/ton BLS Yes

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS Yes Only 1 run

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS M ODEQ M5 test

lb/ton BLS M ODEQ M5 test

lb/ton BLS

lb/ton BLS

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

115.RE01105.EU445C105.EU445A121.000013121.000014121.000013121.000014124.019124.019130.1130.1130.2130.2142.CU7216143.7000145.54145.55154.P39 and P37 ‐ 

Recovery Furnace 1

and Recovery Furnace

3154.P36 ‐ Recovery

Furnace 2

154.P39 ‐ Recovery

Furnace 1

167.005RB167.005RB171.002171.003175.RB2A188.016RB2

AverageLb/Production units

Average Pollutant Removal

Efficiency(%) Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

lb/ton BLS

lb/ton BLS M ODEQ M5 test

lb/ton BLS No. 3 Recovery ESP Exhaust.

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS Separate stacks: RB2 south stack

lb/ton BLS Separate stacks: RB2 north stack

Separate stacks: No. 1 RF North

Separate stacks: No. 1 RF South

Separate stacks: No. 2 RF North

Separate stacks: No. 2 RF South

Yes Failed isokinetics No production data was included. No filter temp

lb/ton BLS No production data was included.

No production data was included. The PDF only

included what appear as field data sheets,

commonly provided as an appendix. No filter

temp. Converted concentraion to 8% O2

No production data was included. The PDF only

included what appear as field data sheets,

commonly provided as an appendix. No filter

temp. Converted concentraion to 8% O2

lb/ton BLS

Represnts 2 RFs. RB 1 & 3 Common Stack.

Combined production values and averaged.

lb/ton BLS 4 test runs

lb/ton BLS

lb/ton BLS RF ESP has separate stacks.

lb/ton BLS RF ESP has separate stacks.

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

188.016RB2188.014RB1205.009205.009205.009206.G‐31206.G‐32613.001L613.001R613.001L&001R613.002R613.002L613.002L&002R102.RB10117.B21130.3140.55146.16157.RB2157.RB2157.RB2159.F3162.382A173.RECOVB173.RECOVB178.08P012178.08P013180.D001190.R400199.002201.SR0001340.005525.EU18606.RB4

AverageLb/Production units

Average Pollutant Removal

Efficiency(%) Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

lb/ton BLS M ODEQ M5 test

lb/ton BLS

Separate stacks.

Separate stacks.

Total from separate stacks

Corrected to 8% O2

Corrected to 8% O2

No. 1 RB ESP ‐ Combined

No. 2 RB ESP‐ Combined

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS

Test report summary table had 0.0172 gr/dscf in

initial summary but this did not match the 0.0056

gr/dscf in the detail tables (or the lb/hr rate).

Used 0.0056 and corrected to 8% O2.

lb/ton BLS Separate stacks: Recovery Boiler West Stack

lb/ton BLS Separate stacks: Recovery Boiler East Stack

Yes

duplicate combiningtests above Recovery Boiler Combined

lb/ton BLS

Production rate suspect so did not calculate

emission factor.

lb/ton BLS Separate stacks: Old Stack

lb/ton BLS Separate stacks: New Stack

lb/ton BLS

lb/ton BLS

Run 2 did not meet isokinetic criteria. The value

was not included in the averages

lb/ton BLS

lb/ton BLS Yes 31‐minute test run

lb/ton BLS

lb/ton BLS

lb/ton BLS

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

606.RB3606.RB3606.RB2606.RB2610.4, 5610.4, 5610.4, 5610.4, 5105.EU445C105.EU445C105.EU445C105.EU445C109.RB4178.08P013178.08P012139.02139.02152.03152.03152.03166.RB02

AverageLb/Production units

Average Pollutant Removal

Efficiency(%) Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

lb/ton BLS

Condition 1: All 3 fields in service. DCE has 2‐

chamber ESP with 3 fields each.

lb/ton BLS

Condition 2: Two fields in service. DCE has 2‐

chamber ESP with 3 fields each. Concentration

matches report, though would think having 1 ESP

field out of service would result in greater

emissions than for Condition 1.

lb/ton BLS

Recovery Boiler 2 ‐Scenario 1 (all ESP fields in

service).

lb/ton BLS

Recovery Boiler 2 ‐Scenario 2 (one ESP field out

of service).Combined Stacks ‐ Condition 1Max Liquor Rec. Boilers 1 & 2

Combined Stacks ‐ Condition 2:

1 ESP Bank down, Maximum Liquor Rec. Boilers 1

& 2 One ESP Side Down Max Liquor Rec. Boiler 2,

Oil Fire Rec. Boiler 1

Combined Stacks ‐ Condition 3: 2 ESP Banks

Down, Controlled Liquor Firing Rec. Boilers 1 & 2

Combined Stacks ‐ Condition 4: One ESP Side

Down Maximum Liquor Rec. Boiler 2, Oil Fire Rec.

Boiler 1

lb/ton BLS M ODEQ M5 test

lb/ton BLS M ODEQ M5 test

lb/ton BLS M ODEQ M5 test

lb/ton BLS M ODEQ M5 test

lb/ton BLS

lb/ton BLS

lb/ton BLS

lb/ton BLS Exceeds emission lmit

Exceeds emission limit of 0.044 gr/dscf. The limit

is stated incorrectly in the report as 0.44.

Retested next month.

lb/ton BLS Retest

lb/ton BLS 75.7

Scrubber uses caustic. Scrubber inlet/outlet

provided.

lb/ton BLS Scrubber uses caustic

unspecifiedunspecified

Run 3 was discontinued due to problems with the

BLOX system. Data was not used for compliance

determination. A fourth run was conducted in its

place.

Test_data_memo_appendices.xlsx App A RF PM 
ble Particulate Matter

RTI+EUID100.037A103.G‐158105.EU445C107.08‐P1

108.RB3109.RB3109.RB4111.G‐44114.U500114.U500116.003119.EQT008119.EQT010119.EQT010120.F7124.001124.001126.RECOV126.RECOV126.RECOV126.RECOV127.REC1N127.REC1N131.6131.5131.5131.5132.5RB132.5RB132.4RB133.10133.10

Data analysis notes Multi‐stack sums

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production Sort order

Unit totallb/hr (values)

Unit total EF

(values)

100.037A.PM 17.1 0.2911 1 17.1 0.2911103.G‐158.PM 26.28 0.2864 2 26.28 0.2864

105.EU445C.PM 12.69 0.2149 3 12.69 0.2149107.08‐P1.PM 10.73 0.1168 4 10.73 0.1168

108.RB3.PM 4.859 0.0456 5 4.859 0.0456109.RB3.PM 28.7 0.5180 6 28.7 0.5180109.RB4.PM different years 28.5 0.3050 7 28.5 0.3050

111.G‐44.PM 6.83 0.0772 8 6.83 0.0772114.U500.PM

Separate conditions: RF (low load; 2

chambers) 25.84 0.3238 9 25.84 0.3238

114.U500.PM

Separate conditions: RF (high load; 3

chambers) 34.63 0.3273 10 34.63 0.3273

116.003.PM 20.61 0.2170 11 20.61 0.2170

119.EQT008.PM 12.66 0.2142 12 12.66 0.2142119.EQT010.PM different dates w/in same year 46.764 0.6928 13 46.764 0.6928

119.EQT010.PM different dates w/in same year 26.92 0.4307 14 26.92 0.4307

120.F7.PM 25.33 0.2434 15 25.33 0.2434124.001.PM separate stacks 16

124.001.PM separate stacks 2.252 0.038827586 17 2.252 0.038827586

126.RECOV.PM

Separate conditions: Recovery Furnace

West Stack 1st Set 18

126.RECOV.PM

Separate conditions: Recovery Furnace

East Stack 1st Set 25.241 0.489166667 19 25.241 0.489166667

126.RECOV.PM

Separate stacks/conditions: RecoveryFurnace West Stack 2nd Set. A second set

of particulate tests (3 one‐hour runs) was

run on the recovery furnace with the

west side inlet slide gates closed slightly

to balance flue gas flow between the east

and west sides. 20

126.RECOV.PM

Separate stacks/conditions: RecoveryFurnace East Stack 2nd Set. A second set

of particulate tests (3 one‐hour runs) was

run on the recovery furnace with the

west side inlet slide gates closed slightly

to balance flue gas flow between the east

and west sides. 19.972 0.387054264 21 19.972 0.387054264

127.REC1N.PM separate stacks 22

127.REC1N.PM separate stacks 12.423 0.171351724 23 12.423 0.171351724

131.6.PM 15.2 0.2425 24 15.2 0.2425131.5.PM Separate conditions: Recovery Furnace 4 29.8 0.4691 25 29.8 0.4691

131.5.PM

Separate conditions: Recovery Furnace 4

(both ESP chambers and all fields

operating) (Condition #1) 5.6 unspecified 26 5.6 unspecified

131.5.PM

Separate conditions: Recovery Furnace 4

(1‐2 fields out of service) (Condition #2

and #3) 9.8 unspecified 27 9.8 unspecified

132.5RB.PM separate stacks 28

132.5RB.PM separate stacks 8.976 0.128706625 29 8.976 0.128706625

132.4RB.PM 9.905 0.1563 30 9.905 0.1563133.10.PM different dates w/in same year 2.46125 unspecified 31 2.46125 unspecified

133.10.PM different dates w/in same year 18.35416667 unspecified 32 18.35416667 unspecified

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

135.003‐1135.003‐1136.EU 005

137.721137.189138.002142.CU7214143.7010143.7020146.8146.8147.14147.14147.5147.5148.007148.001150.CREC‐1

152.03152.03155.RECOVERYFURNACE156.RF22156.RF22

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production Sort order

Unit totallb/hr (values)

Unit total EF

(values)

135.003‐1.PM

Separate conditions: Recovery Boiler

(three ESP chambers in Operation) 34.8 0.3153 33 34.8 0.3153

135.003‐1.PM

Separate conditions: Recovery Boiler (two

ESP chambers in Operation) 20.2 0.1830 34 20.2 0.1830

136.EU 005.PM 19.4 0.1724 35 19.4 0.1724

137.721.PM 8.1 0.0855 36 8.1 0.0855137.189.PM 9.99 0.3648 37 9.99 0.3648138.002.PM 16.816 0.2946 38 16.816 0.2946142.CU7214.PM 2.96 0.0790 39 2.96 0.0790143.7010.PM 1.1 0.0615 40 1.1 0.0615143.7020.PM 4.41 0.1639 41 4.41 0.1639146.8.PM separate stacks 42

146.8.PM separate stacks 24.319 0.3155 43 24.319 0.3155

147.14.PM separate stacks 44

147.14.PM separate stacks 16.5 0.278011794 45 16.5 0.278011794

147.5.PM different years 21.4 0.2140 46 21.4 0.2140

147.5.PM different years 24.4 0.2503 47 24.4 0.2503

148.007.PM 21.7 0.2654 48 21.7 0.2654148.001.PM 17.9 0.3057 49 17.9 0.3057150.CREC‐1.PM 33.6 unspecified 50 33.6 unspecified152.03.PM

Separate conditions: Recovery Furnace ‐ 

Condition 1 (Operating 5 ESPs) 58.37 0.9000 51 58.37 0.9000

152.03.PM

Separate conditions: Recovery Furnace ‐ 

Condition 2 (Operating 6 ESPs) 47.18 0.7000 52 47.18 0.7000

155.RECOVERY FURNACE.PM 48.6 0.6761 53 48.6 0.6761156.RF22.PM different dates w/in same year 2.43 0.0279 54 2.43 0.0279

156.RF22.PM different dates w/in same year 2.06 0.0286 55 2.06 0.0286

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

156.RF22156.RF22156.RF18156.RF18156.RF19156.RF19156.RF19156.RF19162.381A162.381A163.RF1901163.RF2904163.RF2904164.B08,B10 combined

164.B08,B10 combined

164.B08,B10 combined

164.B08,B10 combined

165.000013165.000013

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production Sort order

Unit totallb/hr (values)

Unit total EF

(values)

156.RF22.PM different dates w/in same year 2.95 0.0574 56 2.95 0.0574

156.RF22.PM different dates w/in same year 0.57 0.0087 57 0.57 0.0087

156.RF18.PM different dates w/in same year 1.27 0.0344 58 1.27 0.0344

156.RF18.PM different dates w/in same year 5.45 0.1267 59 5.45 0.1267

156.RF19.PM different dates w/in same year 2.33 0.0424 60 2.33 0.0424

156.RF19.PM different dates w/in same year 9.74 0.1498 61 9.74 0.1498

156.RF19.PM

Two 3‐run tests on same day ‐reason

unspecified 3.24 0.0572 62 3.24 0.0572

156.RF19.PM

Two 3‐run tests on same day ‐reason

unspecified 4.57 0.0806 63 4.57 0.0806

162.381A.PM different dates w/in same year 11 0.2095 64 11 0.2095

162.381A.PM different dates w/in same year 9.1 0.1733 65 9.1 0.1733

163.RF1901.PM 7.2 0.0874 66 7.2 0.0874163.RF2904.PM separate stacks 67

163.RF2904.PM separate stacks 25.6 0.39131764 68 25.6 0.39131764

164.B08,B10 combined.PM

separate stacks and different years. Flue

gasses from B08 and B10 recovery

furnaces combine and then split off to the

two 3 field ESPs, C03 and C04. 69

164.B08,B10 combined.PM

separate stacks and different years. Flue

gasses from B08 and B10 recovery

furnaces combine and then split off to the

two 3 field ESPs, C03 and C04. 32.32 0.773575874 70 32.32 0.773575874

164.B08,B10 combined.PM

separate stacks and different years. Flue

gasses from B08 and B10 recovery

furnaces combine and then split off to the

two 3 field ESPs, C03 and C04. 71

164.B08,B10 combined.PM

separate stacks and different years. Flue

gasses from B08 and B10 recovery

furnaces combine and then split off to the

two 3 field ESPs, C03 and C04. 37.517 0.957358345 72 37.517 0.957358345

165.000013.PM separate stacks 73

165.000013.PM separate stacks 31.83 0.6435 74 31.83 0.6435

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

165.000006165.000006166.RB01166.RB01166.RB02169.04169.05172.RB02172.RB01174.G‐92174.G‐92174.G‐32175.RB3A176.RB7177.EU0804179.RF3181.9181.10181.49181.50182.037184.73184.72185.02185.02185.02185.02185.02185.02185.02186.RB15189.SN26190.R402190.R402

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production Sort order

Unit totallb/hr (values)

Unit total EF

(values)

165.000006.PM separate stacks 75

165.000006.PM separate stacks 40.68 0.4457 76 40.68 0.4457

166.RB01.PM separate stacks 77

166.RB01.PM separate stacks 21.5 0.3129 78 21.5 0.3129

166.RB02.PM different dates 57.9 0.7013 79 57.9 0.7013

169.04.PM 11.79 0.1535 80 11.79 0.1535169.05.PM 15.38 0.1900 81 15.38 0.1900172.RB02.PM 19.75 unspecified 82 19.75 unspecified172.RB01.PM 17.63 unspecified 83 17.63 unspecified174.G‐92.PM separate stacks 84

174.G‐92.PM separate stacks 26.2 0.517786561 85 26.2 0.517786561

174.G‐32.PM 16.1 0.1157 86 16.1 0.1157175.RB3A.PM 45.168 0.3758 87 45.168 0.3758176.RB7.PM 6.43 0.0986 88 6.43 0.0986177.EU0804.PM 19.061 0.2283 89 19.061 0.2283179.RF3.PM 21.09 0.2262 90 21.09 0.2262181.9.PM

Same emission unit as 181.10 (separate

stacks) 12.26666667 0.2275 91 12.26666667 0.2275

181.10.PM

Same emission unit as 181.9 (separate

stacks) 22.86666667 0.4241 92 22.86666667 0.4241

181.49.PM

Same emission unit as 181.50 (separate

stacks) 10.8 0.3210 93 10.8 0.3210

181.50.PM

Same emission unit as 181.49 (separate

stacks) 6.1 0.1810 94 6.1 0.1810

182.037.PM 3.4767 0.0541 95 3.4767 0.0541184.73.PM 7.792 0.0870 96 7.792 0.0870184.72.PM 4.987 0.0887 97 4.987 0.0887185.02.PM different dates w/in same year 26.84532857 unspecified 98 26.84532857 unspecified

185.02.PM different dates w/in same year 22.93875429 unspecified 99 22.93875429 unspecified

185.02.PM different dates w/in same year 37.23893143 unspecified 100 37.23893143 unspecified

185.02.PM different dates w/in same year 36.42705574 unspecified 101 36.42705574 unspecified

185.02.PM different dates w/in same year 26.63402451 unspecified 102 26.63402451 unspecified

185.02.PM different dates w/in same year 20.37712286 unspecified 103 20.37712286 unspecified

185.02.PM different dates w/in same year 22.5774 unspecified 104 22.5774 unspecified

186.RB15.PM 11.06 0.0890 105 11.06 0.0890189.SN26.PM 20.67 0.1827 106 20.67 0.1827190.R402.PM separate stacks 107190.R402.PM separate stacks 7.6 0.104347826 108 7.6 0.104347826

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

190.R401196.SN‐14196.SN‐06196.SN‐06197.2198.019200.007RF2200.007RF3202.Recovery Furnace

EU320203.RF#3203.RF#2203.RF#3207.038207.038226.RECB1226.RECB1240.RF04240.RF01242.AA‐011

243.R407243.R401243.R401531.RF15600.G0806600.G0803615.24615.24615.24615.24617.B14115.RE01

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production Sort order

Unit totallb/hr (values)

Unit total EF

(values)

190.R401.PM 8 0.1782 109 8 0.1782196.SN‐14.PM 14.46 0.1283 110 14.46 0.1283

196.SN‐06.PM different years 13.76 0.1926 111 13.76 0.1926

196.SN‐06.PM different years 18.66 0.2357 112 18.66 0.2357197.2.PM 4.61 0.3033 113 4.61 0.3033198.019.PM 26.24 0.2330 114 26.24 0.2330200.007RF2.PM 1.45 0.0355 115 1.45 0.0355200.007RF3.PM 41.18 0.5252 116 41.18 0.5252202.Recovery Furnace EU320.PM 7.08 0.1229 117 7.08 0.1229

203.RF#3.PM 6.8 0.0675 118 6.8 0.0675

203.RF#2.PM 2.271 0.1296 119 2.271 0.1296203.RF#3.PM 2.759 0.0264 120 2.759 0.0264207.038.PM separate stacks 121207.038.PM separate stacks 4.86 0.259476775 122 4.86 0.259476775

226.RECB1.PM separate stacks 123226.RECB1.PM separate stacks 12.9 0.16433121 124 12.9 0.16433121

240.RF04.PM 23.87 0.1995 125 23.87 0.1995240.RF01.PM 8.4 0.1242 126 8.4 0.1242242.AA‐011.PM 31.86 0.2518 127 31.86 0.2518243.R407.PM 37.63 0.3071 128 37.63 0.3071243.R401.PM separate stacks 129243.R401.PM separate stacks 6.35 0.0778 130 6.35 0.0778

531.RF15.PM 35.2 0.2347 131 35.2 0.2347600.G0806.PM 17.2 0.1650 132 17.2 0.1650600.G0803.PM 26.39 0.3096 133 26.39 0.3096615.24.PM

Separate stacks/separate methods:

Chemical Recovery Furnace ‐ West Stack

Front Half 134

615.24.PM

Separate stacks/separate methods:

Chemical Recovery Furnace ‐ East Stack

Front Half 33.84 0.511769953 135 33.84 0.511769953

615.24.PM

Separate stacks/separate methods:

Chemical Recovery Furnace ‐ West Stack

ODEQ 5 136

615.24.PM

Separate stacks/separate methods:

Chemical Recovery Furnace ‐ East Stack

ODEQ 5 39.66 0.599787125 137 39.66 0.599787125

617.B14.PM 5.59 0.1456 138 5.59 0.1456115.RE01.PM separate stacks 139

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

115.RE01105.EU445C105.EU445A121.000013121.000014121.000013121.000014124.019124.019130.1130.1130.2130.2142.CU7216143.7000145.54145.55154.P39 and P37 ‐ 

Recovery Furnace 1

and Recovery Furnace

3154.P36 ‐ Recovery

Furnace 2

154.P39 ‐ Recovery

Furnace 1

167.005RB167.005RB171.002171.003175.RB2A188.016RB2

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production Sort order

Unit totallb/hr (values)

Unit total EF

(values)

115.RE01.PM separate stacks 11.924 0.135808656 140 11.924 0.135808656

105.EU445C.PM 22.56 0.3500 141 22.56 0.3500105.EU445A.PM 13.98 0.2369 142 13.98 0.2369121.000013.PM 12 0.3519 143 12 0.3519121.000014.PM 9.2 0.2690 144 9.2 0.2690121.000013.PM different years 7.3 0.1872 145 7.3 0.1872

121.000014.PM different years 5.3 0.1359 146 5.3 0.1359124.019.PM Separate stacks 147124.019.PM Separate stacks 32.853 0.566431034 148 32.853 0.566431034

130.1.PM Separate stacks 149130.1.PM Separate stacks 12.4 150 12.4130.2.PM Separate stacks 151130.2.PM Separate stacks 9.61 152 9.61142.CU7216.PM 4.05 153 4.05143.7000.PM 3.08 0.1738 154 3.08 0.1738145.54.PM 3.15 155 3.15145.55.PM 6.74 156 6.74154.P39 and P37 ‐ Recovery Furnace 1 aCommon stack (represents 2 RFs) 24.151 0.3887 157 24.151 0.3887

154.P36 ‐ Recovery Furnace 2.PM 10.624 0.3109 158 10.624 0.3109154.P39 ‐ Recovery Furnace 1.PM 5.74 0.1754 159 5.74 0.1754167.005RB.PM Separate stacks 160167.005RB.PM Separate stacks 33.6 0.602 161 33.6 0.602171.002.PM 22.8 0.8385 162 22.8 0.8385171.003.PM 17.5 0.6331 163 17.5 0.6331175.RB2A.PM 7.67 0.2458 164 7.67 0.2458188.016RB2.PM Separate methods (M5) 8.97 0.3200 165 8.97 0.3200

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

188.016RB2188.014RB1205.009205.009205.009206.G‐31206.G‐32613.001L613.001R613.001L&001R613.002R613.002L613.002L&002R102.RB10117.B21130.3140.55146.16157.RB2157.RB2157.RB2159.F3162.382A173.RECOVB173.RECOVB178.08P012178.08P013180.D001190.R400199.002201.SR0001340.005525.EU18606.RB4

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production Sort order

Unit totallb/hr (values)

Unit total EF

(values)

188.016RB2.PM Separate methods (ORDEQ5) 10.36 0.3696 166 10.36 0.3696

188.014RB1.PM 3.93 0.1396 167 3.93 0.1396205.009.PM Separate stacks 168205.009.PM Separate stacks 14.2 169 14.2205.009.PM 14.2 170 14.2206.G‐31.PM 16.808 171 16.808206.G‐32.PM 21.279 172 21.279613.001L.PM Separate stacks 173613.001R.PM Separate stacks 32.24 174 32.24613.001L&001R.PM 32.24 175 32.24613.002R.PM Separate stacks 176613.002L.PM Separate stacks 12.08 177 12.08613.002L&002R.PM 12.08 178 12.08102.RB10.PM 11.9 0.1017 179 11.9 0.1017117.B21.PM 7.19 0.3829 180 7.19 0.3829130.3.PM 3.19 0.0670 181 3.19 0.0670140.55.PM 12.45833333 0.2300 182 12.45833333 0.2300146.16.PM 11.848 0.1038 183 11.848 0.1038157.RB2.PM Separate stacks 184157.RB2.PM Separate stacks 33.7 1.004720497 185 33.7 1.004720497157.RB2.PM 33.6 186 33.6159.F3.PM 26.847 0.8369 187 26.847 0.8369162.382A.PM 22 188 22173.RECOVB.PM Separate stacks 189173.RECOVB.PM Separate stacks 8.07 0.184246575 190 8.07 0.184246575178.08P012.PM different years 25 0.4800 191 25 0.4800178.08P013.PM different years 20 0.3800 192 20 0.3800180.D001.PM 8.4 0.1024 193 8.4 0.1024190.R400.PM 11.666 0.2468 194 11.666 0.2468199.002.PM 23.5 0.3082 195 23.5 0.3082

201.SR0001.PM 34.167 196 34.167340.005.PM 28.32 0.5941 197 28.32 0.5941525.EU18.PM 8.3 198 8.3606.RB4.PM 36.448 0.5836 199 36.448 0.5836

Test_data_memo_appendices.xlsx App A RF PM 
RTI+EUID

606.RB3606.RB3606.RB2606.RB2610.4, 5610.4, 5610.4, 5610.4, 5105.EU445C105.EU445C105.EU445C105.EU445C109.RB4178.08P013178.08P012139.02139.02152.03152.03152.03166.RB02

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production Sort order

Unit totallb/hr (values)

Unit total EF

(values)

606.RB3.PM Separate conditions 26.666 0.6837 200 26.666 0.6837

606.RB3.PM Separate conditions 3.301 0.0846 201 3.301 0.0846606.RB2.PM Separate conditions 16.46 0.2504 202 16.46 0.2504606.RB2.PM Separate conditions 25.061 0.3700 203 25.061 0.3700

610.4, 5 .PM Combined stacks and separate conditions 32.36 204 32.36

610.4, 5 .PM Combined stacks and separate conditions 39.87 205 39.87

610.4, 5 .PM Combined stacks and separate conditions 44.61 206 44.61

610.4, 5 .PM Combined stacks and separate conditions 46.34 207 46.34

105.EU445C.PM different dates within same year 25.06 0.4042 208 25.06 0.4042

105.EU445C.PM different dates within same year 21.9 0.3699 209 21.9 0.3699

105.EU445C.PM different dates within same year 24.58 0.4256 210 24.58 0.4256

105.EU445C.PM different dates within same year 24.35 0.4590 211 24.35 0.4590

109.RB4.PM different years 40.48933333 0.4930 212 40.48933333 0.4930

178.08P013.PM different years 32.17 0.5340 213 32.17 0.5340

178.08P012.PM different years 20.12 0.3337 214 20.12 0.3337139.02.PM 66.9 1.2606 215 66.9 1.2606139.02.PM 23.38584712 0.3783 216 23.38584712 0.3783152.03.PM different dates 30.45 0.4333 217 30.45 0.4333152.03.PM different dates 51.8 0.7650 218 51.8 0.7650

152.03.PM different dates 49.94 unspecified 219 49.94 unspecified166.RB02.PM different dates 24.44 unspecified 220 24.44 unspecified

Test_data_memo_appendices.xlsx App A RF PM 
Appendix B

Particulate Matter Emissions Data for Lime Kilns 
Appendix B: Pulp and Paper Emissions Test Data Spreadsheet for NSPS Review ‐ Lime Kiln Filterable Particulate Matter

General InformationTest report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

GenericProcess Type

NEI40686_RTI100_DomtarJohnsonburgMill_ MACT

II Test Report_July2004.pdf 100 NEI40686 115 100.115 100‐‐C24 ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2011‐Q1 LK‐RB10‐SDTV10‐

HFB11.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2011‐Q1 LK‐RB10‐SDTV10‐

HFB11.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI9201_Lime Kiln Particulate Test Results August

28, 2008/ NEI9201_20080801 PM&TRS LK5‐d.pdf 103 NEI9201 G‐165 103.G‐165 103‐‐LK5VS/LK5BAG SCBR Kraft Lime Kiln

2010_PM_Lime_Kiln,_No_4_Rec_and_No_4_Smelt.pdf 105 NEI45182 EU455 105.EU455

105‐‐CD 456‐110, CD445‐480, and

CD 445‐447 ESP Kraft, Secondary Lime Kiln

SECTION 2.pdf/ SECTION 7.pdf 107 NEI47074 11‐P14 107.11‐P14 107‐‐11‐P13 ESP Kraft Lime Kiln

2004 LK RB1‐2 Stack Test.pdf 108 NEI33025 LK1 108.LK1 108‐‐LKSCRB SCBR None Kraft Lime Kiln

2004 LK RB1‐2 Stack Test.pdf 108 NEI33025 LK1 108.LK1 108‐‐LKSCRB SCBR None Kraft Lime Kiln

2004 LK RB1‐2 Stack Test.pdf 108 NEI33025 LK1 108.LK1 108‐‐LKSCRB SCBR None Kraft Lime Kiln

NEI45206_P&P Survey_2009 LK NOx and PM Test

Report WITH APPE.pdf 111 NEI45206 G‐35 111.G‐35 111‐‐LK ESP ESP NA Kraft Lime Kiln

NEI45206_P&P Survey_2009 LK NOx and PM Test

Report WITH APPE.pdf 111 NEI45206 G‐35 111.G‐35 111‐‐LK ESP ESP NA Kraft Lime Kiln

NEI26506_PM_December_2008.pdf 114 NEI26506 U800 114.U800 114‐‐CDU7 ESP Kraft Lime KilnNEI26506_PM_December_2008.pdf 114 NEI26506 U800 114.U800 114‐‐CDU7 ESP Kraft Lime KilnLime Kilns, Smelt Tank and Recovery Furnace

Emissions Test Report_NEI26495.pdf 120 NEI26495 M19 120.M19 120‐‐LK2S SCBR Kraft Lime Kiln

Lime Kilns, Smelt Tank and Recovery Furnace

Emissions Test Report_NEI26495.pdf 120 NEI26495 M18 120.M18 120‐‐LK1S SCBR Kraft Lime Kiln

0910‐29 LIME KILN COMPLIANCE.pdf 124 NEI8278 004‐1 124.004‐1 124‐‐mc004, lksbr004 SCBR low nox burner Kraft Lime Kiln

NEI 42317 Hopewell VA Dec 2009 LK TSP.pdf 126 NEI42317 LK 126.LK 126‐‐LKPPT, LKScr ESP/SCBR Kraft Lime Kiln

NEI7933_PIII ‐ Lime Kilns 1 and 2 ‐ PM ‐ April 4 and

5, 2011.pdf 127 NEI7933 LK2 127.LK2 127‐‐ESP2 ESP Kraft, Secondary Lime Kiln

NEI7933_PIII ‐ Lime Kilns 1 and 2 ‐ PM ‐ April 4 and

5, 2011.pdf 127 NEI7933 LK1 127.LK1 127‐‐ESP1 ESP Kraft, Secondary Lime Kiln

NEI 42254 RockTenn WP Stack Tests.pdf 131 NEI42254 18 131.18 131‐‐CZ11‐1 SCBR Kraft, Secondary Lime Kiln

NEI 42254 RockTenn WP Stack Tests.pdf 131 NEI42254 18 131.18 131‐‐CZ11‐1 SCBR Kraft, Secondary Lime KilnNEI 42254 RockTenn WP Stack Tests.pdf 131 NEI42254 18 131.18 131‐‐CZ11‐1 SCBR Kraft, Secondary Lime KilnNEI 42254 RockTenn WP Stack Tests.pdf 131 NEI42254 18 131.18 131‐‐CZ11‐1 SCBR Kraft, Secondary Lime Kiln2010 LK4.pdf 132 NEI8261 21LK4 132.21LK4 132‐‐4LKESP ESP Kraft, Secondary Lime Kiln2010 ‐ LK(NOx‐PM).pdf 136 NEI12368 EU 033 136.EU 033 136‐‐CE 019 ESP Kraft Lime Kiln

2008‐05‐13 #4 LK Particulate Matter Horizon.pdf 137 NEI26581 512 137.512 137‐‐PC(512), PC(512)S ESP/PBSCBR Kraft Lime Kiln

Mill code 139 part 2.pdf 139 NEI42357 04 139.04 139‐‐LKSCBR SCBR Kraft, Secondary Lime Kiln

NEI26504_RTI143_PCA Valdosta Mill_1,2,3 RB

PM_November 2009.pdf 143 NEI26504 6063 143.6063 143‐‐C009 ESP Kraft Lime Kiln

Lime Kiln Part Testing.pdf 145 NEI33135 001 145.001 145‐‐ SCBR Kraft Lime Kiln

NEI759 TSP Testing 2008 part 1.pdf 146 NEI759 30 146.30 146‐‐LK201/LK202 ESP/SCBR Kraft Lime KilnNEI759 EUID6 No1LK2009.pdf 146 NEI759 6 146.6 146‐‐LK101 SCBR Kraft Lime KilnNo1LimeKilnStackTest2010.pdf 147 NEI6450 3 147.3 147‐‐C‐827 SCBR None Kraft Lime KilnNo7LimeKilnStackTest2010.pdf 147 NEI6450 55 147.55 147‐‐C‐829 ESP None Kraft Lime KilnNo7LimeKilnStackTest2010.pdf 147 NEI6450 55 147.55 147‐‐C‐829 ESP None Kraft Lime KilnNEI46931_5 25‐27 2010 No. 1 LK & No. 2 LK

Compliance Test Report.pdf 148 NEI46931 003 148.003 148‐‐LK1SCB SCBR primary air Kraft, Secondary Lime KilnNEI46931_5 25‐27 2010 No. 1 LK & No. 2 LK

Compliance Test Report.pdf 148 NEI46931 009 148.009 148‐‐LK2ESP ESP primary air Kraft, Secondary Lime Kiln150 NewPage Rumford TRC 2009 Report_Lime

Kiln_PM and NOx.pdf 150 NEI6273 CAU‐12 150.CAU‐12 150‐‐SCRBLK SCBR Kraft, Mechanical Lime Kiln

NEI46739 Kiln PM December 2010 ‐ On Oil.pdf 154 NEI46739 P30 ‐ Lime Kiln 154.P30 ‐ Lime Kiln 154‐‐C05 and C06 ESP/SCBR Kraft Lime Kiln

M52010LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52010LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52010LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52010LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52010LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52010LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52010LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐chem) Lime Kiln

M52010LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐chem) Lime Kiln

Test_data_memo_appendices.xlsx App B LK PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

GenericProcess Type

M52010LK4.pdf 156 NEI42338 145000 156.145000 156‐‐LK04WS SCBR Wet scrubber

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52010LK4.pdf 156 NEI42338 145000 156.145000 156‐‐LK04WS SCBR Wet scrubber

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52010LK4.pdf 156 NEI42338 145000 156.145000 156‐‐LK04WS SCBR Wet scrubber

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52010LK4.pdf 156 NEI42338 145000 156.145000 156‐‐LK04WS SCBR Wet scrubber

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52010LK3.pdf 156 NEI42338 143100 156.143100 156‐‐LK03WS SCBR Wet scrubber

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52010LK3.pdf 156 NEI42338 143100 156.143100 156‐‐LK03WS SCBR Wet scrubber

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52010LK3.pdf 156 NEI42338 143100 156.143100 156‐‐LK03WS SCBR Wet scrubber

Unknown (Kraft & Semi‐chem) Lime Kiln

Lime Kiln PM Emissions Test Report (NEI18177).pdf 159 NEI8177 F4 159.F4 159‐‐CD03 SCBR Kraft Lime Kiln

P_P ICR Part III_RTI162_InternationalPaper‐

EastoverMill_NEI46760_no 1 recovery furnace CO

NOx SO/P_P ICR Part III_RTI162_InternationalPaper‐

EastoverMill_NEI46760_no 1 recovery furnace

particul2/P_P ICR Part

III_RTI162_InternationalPaper‐EastoverMill_NEI46760_no 1 recovery furnace

particul3.pdf 162 NEI46760 372A 162.372A 162‐‐372AESP ESP Kraft Lime Kiln

P_P ICR Part III_RTI162_InternationalPaper‐

EastoverMill_NEI46760_no 1 recovery furnace CO

NOx SO/P_P ICR Part III_RTI162_InternationalPaper‐

EastoverMill_NEI46760_no 1 recovery furnace

particul2/P_P ICR Part

III_RTI162_InternationalPaper‐EastoverMill_NEI46760_no 1 recovery furnace

particul3.pdf 162 NEI46760 371A 162.371A 162‐‐371ASCRUB SCBR Kraft Lime KilnRTI163_International Paper ‐ PrattvilleMill_NEI8560_No 1 Lime Kiln testing.pdf 163 NEI8560 LK1501 163.LK1501 163‐‐LK1SCR SCBR Kraft, Secondary Lime Kiln

RTI163_International Paper ‐ PrattvilleMill_NEI8560_No 2 Lime Kiln testing.pdf 163 NEI8560 LK2502 163.LK2502 163‐‐LK2SCR SCBR Kraft, Secondary Lime Kiln

Lime Kiln, August 17, 2010.pdf 164 NEI42710 P12 164.P12 164‐‐C17 SCBR Kraft Lime Kiln

P_P_ICR Part III_RTI166_InternationalPaper‐GeorgetownMill_NEI_41314_LK1and2_RB1and2_ST1and2_PM_July 2009.PDF 166 NEI41314 LK01 166.LK01 166‐‐LK01 Scrubber SCBR Kraft Lime KilnP_P_ICR Part III_RTI166_InternationalPaper‐GeorgetownMill_NEI_41314_LK2_TRS_April2009.PDF 166 NEI41314 LK02 166.LK02 166‐‐LK02 Scrubber SCBR Kraft Lime KilnRTI172_International Paper ‐ RiverdaleMill_NEI18335_Oct2009 LK03 (Fuel Oil)

PM,NOx,SO2,CO Testing.pdf 172 NEI18335 LK03 172.LK03 172‐‐LK03 Scrubber SCBR Kraft, Secondary Lime Kiln

RTI172_International Paper ‐ RiverdaleMill_NEI18335_Oct2009 LK03 (Natural Gas)PM,NOx,SO2,CO Testing.pdf 172 NEI18335 LK03 172.LK03 172‐‐LK03 Scrubber SCBR Kraft, Secondary Lime Kiln

P_P ICR Part III_RTI174_International Paper‐

Riegelwood M (1).pdf 174 NEI40247 G‐18 174.G‐18

174‐‐G‐18 ESP/G‐18 SCRUB, G‐32

ESP, G‐92 ESP, G‐63B SCRUB, G‐

63C EWSCRUB ESP/SCBR Kraft Lime Kiln

P_P_ICR Part III_RTI175_InternationalPaper‐AugustaMill_N (7).pdf 175 NEI26514 LK2A 175.LK2A 175‐‐LK2B SCBR Kraft Lime Kiln

P_P_ICR Part III_RTI175_InternationalPaper‐AugustaMill_N (7).pdf 175 NEI26514 LK2A 175.LK2A 175‐‐LK2B SCBR Kraft Lime Kiln

P_P_ICR Part III_RTI175_InternationalPaper‐AugustaMill_N (8).pdf 175 NEI26514 LK1A 175.LK1A 175‐‐LK1B SCBR Kraft Lime Kiln

P_P_ICR Part III_RTI175_InternationalPaper‐AugustaMill_N (8).pdf 175 NEI26514 LK1A 175.LK1A 175‐‐LK1B SCBR Kraft Lime Kiln

P_P_ICR Part III_RTI175_InternationalPaper‐AugustaMill_N (9).pdf 175 NEI26514 LK1A 175.LK1A 175‐‐LK1B SCBR Kraft Lime Kiln

IP PENSACOLA JUNE 10 LK COMP REPORT.pdf 178 NEI26309 09P037 178.09P037 178‐‐09P37A ESP/SCBR Kraft Lime Kiln

IP PENSACOLA JUNE 10 LK COMP REPORT.pdf 178 NEI26309 09P037 178.09P037 178‐‐09P37A ESP/SCBR Kraft Lime KilnRTI179_Rock‐TennDemopolis_NEI45474_PPSurvey_LKTest2010.pdf 179 NEI45474 LK3 179.LK3 179‐‐LK3ESP ESP Kraft Lime KilnNEI26471_No1_Lime_Kiln_PM_NOx_Compliance,_TRS_RATA_2010‐0324[1].pdf 180 NEI26471 L001 180.L001 180‐‐L01S SCBR Kraft, Secondary Lime Kiln

NEI26471_No2_Lime_Kiln_PM_NOx_Compliance,_TRS_RATA_2010‐0325[1].pdf 180 NEI26471 L002 180.L002 180‐‐L02S SCBR Kraft, Secondary Lime Kiln

LimeKiln#2_EmissionsTest2004_Part1.pdf 184 NEI46817 LK2 184.LK2 184‐‐11 SCBR Kraft Lime KilnLimeKiln#2_EmissionsTest2004_Part1.pdf 184 NEI46817 LK2 184.LK2 184‐‐11 SCBR Kraft Lime KilnLimeKiln#1 Compliance Test2010.pdf 184 NEI46817 LK1 184.LK1 184‐‐10 SCBR Kraft Lime KilnLimeKiln#1 Compliance Test2010.pdf 184 NEI46817 LK1 184.LK1 184‐‐10 SCBR Kraft Lime Kiln2009.01 4LK PM.pdf 185 NEI46599 07 185.07 185‐‐LK4SCB SCBR Kraft Lime Kiln

Test_data_memo_appendices.xlsx App B LK PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

GenericProcess Type

2009.04 4LK PM.pdf 185 NEI46599 07 185.07 185‐‐LK4SCB SCBR Kraft Lime Kiln

2009.07 4LK PM.pdf 185 NEI46599 07 185.07 185‐‐LK4SCB SCBR Kraft Lime Kiln

2009.10 4LK PM.pdf 185 NEI46599 07 185.07 185‐‐LK4SCB SCBR Kraft Lime Kiln

2009 Annual PM.pdf 186 NEI18334 LK 186.LK 186‐‐LKESP/LK27 ESP/SCBR Kraft Lime Kiln

GP Crossett No. 4 Lime Kiln (SN‐25) Compliance

Testing 2011.pdf 189 NEI54342 SN25 189.SN25 189‐‐SN25S SCBR Kraft Lime Kiln

GP Crossett No. 4 Lime Kiln (SN‐25) Compliance

Testing 2011.pdf 189 NEI54342 SN25 189.SN25 189‐‐SN25S SCBR Kraft Lime Kiln

2010 Domtar Compliance Testing Part 1 of 6.pdf 196 NEI18660 SN‐02 196.SN‐02 196‐‐SN‐02 ESP ESP (dry) Kraft Lime Kiln

RecBoiler_LimeKiln_HogBoiler_SmeltTank_ComplianceTest2008.pdf 197 NEI18657 1 197.1

197‐‐VENTSCR, PEABODYSCR,

DUSTSCR SCBR Kraft Lime Kiln

NEI41565 Lime Kiln Particulate Testing 9‐9‐05.pdf 198 NEI41565 004 198.004 198‐‐004_CD SCBR

Kraft, Mechanical,

Secondary Lime Kiln

NEI18390_011_PM_2011.pdf 199 NEI18390 011 199.011 199‐‐Z032 SCBR Kraft Lime Kiln

NEI47077 BOWATER CATAWBA APR 10 COMP

REPORT.pdf 200 NEI47077 007_10 200.007_10 200‐‐2723C ESP low NOx burners Kraft, Mechanical Lime Kiln

NEI7559Lime Kiln‐69‐04Comp2007Petcoke.pdf 201 NEI7559 SR0003 201.SR0003 201‐‐LKS SCBR

Kraft, Mechanical,

Secondary Lime Kiln

1106‐104_Boise White Paper_Lime Kiln.pdf 202 NEI12411 Lime Kiln EU340 202.Lime Kiln EU340 202‐‐CE341 and CE340 SCBR Kraft Lime Kiln

2011 02 LK PM.pdf 203 NEI42410 LKScr 203.LKScr 203‐‐LKScr‐Scr SCBR Secondary air Kraft, Sulfite‐Na Lime Kiln

2011 03 LK PM.pdf 203 NEI42410 LKScr 203.LKScr 203‐‐LKScr‐Scr SCBR Secondary air Kraft, Sulfite‐Na Lime Kiln2011 04 LK PM SO2.pdf 203 NEI42410 LKScr 203.LKScr 203‐‐LKScr‐Scr SCBR Secondary air Kraft, Sulfite‐Na Lime Kiln2011 03 LK PM.pdf 203 NEI42410 LKScr 203.LKScr 203‐‐LKScr‐Scr SCBR Secondary air Kraft, Sulfite‐Na Lime KilnRTI206_BRPLK#511.13.2007.pdf 206 NEI40282 G‐38 206.G‐38 206‐‐LK5 DEM/LK5 SCRUB SCBR Kraft Lime Kiln

NEI7104 ‐ 2011 Recovery Boiler and Lime Kiln.pdf 207 NEI7104 103A 207.103A 207‐‐C23 SCBR

use hot, fresh water for lime mud washing

to reduce soda in mud (sulfur) Kraft Lime Kiln

NEI7104 ‐ 2011 Recovery Boiler and Lime Kiln.pdf 207 NEI7104 103A 207.103A 207‐‐C23 SCBR

use hot, fresh water for lime mud washing

to reduce soda in mud (sulfur) Kraft Lime Kiln

NEI7104 ‐ 2011 Recovery Boiler and Lime Kiln.pdf 207 NEI7104 103A 207.103A 207‐‐C23 SCBR

use hot, fresh water for lime mud washing

to reduce soda in mud (sulfur) Kraft Lime Kiln

NEI7104 ‐ 2011 Recovery Boiler and Lime Kiln.pdf 207 NEI7104 103A 207.103A 207‐‐C23 SCBR

use hot, fresh water for lime mud washing

to reduce soda in mud (sulfur) Kraft Lime Kiln

NEI33023_LK1_2004_PM.pdf 226 NEI33023 LK1 226.LK1 226‐‐LKS1 SCBR

Kraft, Secondary,

SemiChem Lime Kiln

NEI33023_LK2_2004_PM.pdf 226 NEI33023 LK2 226.LK2 226‐‐LKS2 SCBR

Kraft, Secondary,

SemiChem Lime Kiln

Rayonier Jesup DLK PM test 03_16_10.pdf 240 NEI26526 CA81 240.CA81 240‐‐CAC4 ESP Kraft Lime Kiln

NEI 34066 Emission Test RB‐LK‐ SDT 2010.pdf 242 NEI34066 AA‐013 242.AA‐013 242‐‐RC‐6a, RC‐6b ESP/SCBR Kraft Lime Kiln

8196_2009 Source Compliance Test Report.pdf 243 NEI8196 LG07 243.LG07 243‐‐LEP1, LKS1 ESP/SCBR Kraft Lime Kiln

8196_2009 Source Compliance Test Report.pdf 243 NEI8196 LG07 243.LG07 243‐‐LEP1, LKS1 ESP/SCBR Kraft Lime Kiln

P_P_ICR Part III_RTI531_InternationalPaper‐ Savnnah Mill_NEI.pdf 531 NEI8186 LK7 531.LK7 531‐‐AP01 ESP Kraft, Secondary Lime Kiln

RTI600_InternationalPaper‐CourtlandMill‐NEI18357NOV 10 1‐3L.pdf 600 NEI18357 G0908 600.G0908 600‐‐09‐CD‐03‐001 SCBR Kraft Lime Kiln

RTI600_InternationalPaper‐CourtlandMill‐NEI18357JUN 11 2LK .pdf 600 NEI18357 G0905 600.G0905 600‐‐09‐CD‐02‐001 SCBR Kraft Lime Kiln

RTI600_InternationalPaper‐CourtlandMill‐NEI18357

NOV 10 1‐3L.pdf 600 NEI18357 G0903 600.G0903 600‐‐09‐CD‐01‐001 SCBR Kraft Lime Kiln

RTI600_InternationalPaper‐CourtlandMill‐NEI18357

JUN 10 3RF .pdf 600 NEI18357 G0905 600.G0905 600‐‐09‐CD‐02‐001 SCBR Kraft Lime Kiln

47091_024_2011_PM.pdf 606 NEI47091 LK4 606.LK4 606‐‐ESP1 ESP Kraft Lime Kiln

ODEQ‐Final‐Report‐LK‐TSP‐10‐22‐09. Report.pdf 615 NEI40554 21 615.21 615‐‐LKSCB1 SCBR Kraft Lime KilnODEQ‐Final‐Report‐LK‐TSP‐10‐22‐09. Report.pdf 615 NEI40554 21 615.21 615‐‐LKSCB1 SCBR Kraft Lime KilnRTI169‐IP‐MansfieldMill‐

NEI33013_2010_Emission_Test_Report‐R.pdf 169 NEI33013 03 169.03 169‐‐LKSCRB SCBR Kraft, SemiChem Lime Kiln2011_0315‐17.1.pdf 617 NEI42695 P22 617.P22 617‐‐C10 ESP Kraft Lime Kiln

NEI 42317 Hopewell VA Feb 2004 LK MM

Compliance.pdf 126 NEI42317 LK 126.LK 126‐‐LKPPT, LKScr ESP/SCBR Kraft Lime Kiln

2007 LK.pdf 132 NEI8261 21LK4 132.21LK4 132‐‐4LKESP ESP Kraft, Secondary Lime Kiln

2008 LK.pdf 132 NEI8261 21LK4 132.21LK4 132‐‐4LKESP ESP Kraft, Secondary Lime Kiln2006 LK.pdf 132 NEI8261 21LK4 132.21LK4 132‐‐4LKESP ESP Kraft, Secondary Lime Kiln2005 LK.pdf 132 NEI8261 21LK4 132.21LK4 132‐‐4LKESP ESP Kraft, Secondary Lime Kiln2004 All sources.pdf 132 NEI8261 21LK4 132.21LK4 132‐‐4LKESP ESP Kraft, Secondary Lime Kiln2003 All sources.pdf 132 NEI8261 21LK4 132.21LK4 132‐‐4LKESP ESP Kraft, Secondary Lime Kiln2002 All sources.pdf 132 NEI8261 21LK4 132.21LK4 132‐‐4LKESP ESP Kraft, Secondary Lime Kiln

Test_data_memo_appendices.xlsx App B LK PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

GenericProcess Type

2001 All sources.pdf 132 NEI8261 21LK4 132.21LK4 132‐‐4LKESP ESP Kraft, Secondary Lime Kiln2009 LK.pdf 132 NEI8261 21LK4 132.21LK4 132‐‐4LKESP ESP Kraft, Secondary Lime Kiln

2001 ‐ LK(PM‐VOC‐SO2‐NOx‐CO‐TRS‐Hg).pdf 136 NEI12368 EU 033 136.EU 033 136‐‐CE 019 ESP Kraft Lime Kiln

2008 ‐ LK(PM) + RB10(PM).pdf 136 NEI12368 EU 033 136.EU 033 136‐‐CE 019 ESP Kraft Lime Kiln2006 ‐ LK(PM).pdf 136 NEI12368 EU 033 136.EU 033 136‐‐CE 019 ESP Kraft Lime Kiln2004 ‐ LK(PM).pdf 136 NEI12368 EU 033 136.EU 033 136‐‐CE 019 ESP Kraft Lime Kiln2002 ‐ LK(PM).pdf 136 NEI12368 EU 033 136.EU 033 136‐‐CE 019 ESP Kraft Lime Kiln2005‐06‐15 3 LK results PM.pdf 137 NEI26581 511 137.511 137‐‐PC(511) ESP Kraft Lime Kiln

2004‐08‐12 3LK sub mm results.pdf 137 NEI26581 511 137.511 137‐‐PC(511) ESP Kraft Lime Kiln2005‐04‐12 #4 LK Particulate Testing AMTEST.pdf 137 NEI26581 512 137.512 137‐‐PC(512), PC(512)S ESP Kraft Lime Kiln

2005‐07‐15 4LK Particulate Matter Horizon.pdf 137 NEI26581 512 137.512 137‐‐PC(512), PC(512)S ESP Kraft Lime Kiln

2004‐08‐12 #4 LK Particulate AMTEST.pdf 137 NEI26581 512 137.512 137‐‐PC(512), PC(512)S ESP Kraft Lime Kiln2008‐05‐14 #3 LK Particulate Matter Horizon.pdf 137 NEI26581 511 137.511 137‐‐PC(511) ESP Kraft Lime Kiln

2002‐07‐18 #4 LK Particulate Testing Interpoll.pdf 137 NEI26581 512 137.512 137‐‐PC(512), PC(512)S ESP/PBSCBR Kraft Lime Kiln

2002‐07‐16 No. 3 and 4 LK Particulate Testing 118

pg.pdf 137 NEI26581 512 137.512 137‐‐PC(512), PC(512)S ESP Kraft Lime Kiln

NEI759 MACTII Compliance Test.pdf 146 NEI759 30 146.30 146‐‐LK201/LK202 ESP/SCBR Kraft Lime Kiln

NEI46739 Kiln PM October 2003.pdf 154 NEI46739 P30 ‐ Lime Kiln 154.P30 ‐ Lime Kiln 154‐‐C05 and C06 ESP Kraft Lime Kiln

NEI46739 Kiln PM August 2007.pdf 154 NEI46739 P30 ‐ Lime Kiln 154.P30 ‐ Lime Kiln 154‐‐C05 and C06 ESP/SCBR Kraft Lime Kiln

NEI46739 Kiln PM December 2008 ‐ On Oil.pdf 154 NEI46739 P30 ‐ Lime Kiln 154.P30 ‐ Lime Kiln 154‐‐C05 and C06 ESP/SCBR Kraft Lime Kiln

NEI46739 Kiln PM August 2009.pdf 154 NEI46739 P30 ‐ Lime Kiln 154.P30 ‐ Lime Kiln 154‐‐C05 and C06 ESP/SCBR Kraft Lime Kiln

Lime Kiln 2007.pdf 186 NEI18334 LK 186.LK 186‐‐LKESP/LK27 ESP/SCBR Kraft Lime Kiln

Lime Kiln 2006.pdf 186 NEI18334 LK 186.LK 186‐‐LKESP/LK27 ESP/SCBR Kraft Lime Kiln

Lime Kiln.pdf 186 NEI18334 LK 186.LK 186‐‐LKESP/LK27 ESP/SCBR Kraft Lime Kiln

Lime Kiln 2005.pdf 186 NEI18334 LK 186.LK 186‐‐LKESP/LK27 ESP/SCBR Kraft Lime Kiln

8196_2005 Source Compliance Test Report.pdf 243 NEI8196 LG07 243.LG07 243‐‐LEP1, LKS1 ESP/SCBR Kraft Lime Kiln

8196_2007 Source Compliance Test Report.pdf 243 NEI8196 LG07 243.LG07 243‐‐LEP1, LKS1 ESP/SCBR Kraft Lime Kiln

2007_PE_Lime_Kiln_ESP,_No_4_Rec_Boiler_ESP_and_Smelt_Dis_Tank.pdf 105 NEI45182 EU455 105.EU455 105‐‐CD 456‐110 ESP Kraft, Secondary Lime KilnTempleInland‐OrangeMill_NEI12492_PPTestReport‐

2002TestReport.pdf 121 NEI12492 000011 121.000011 121‐‐C‐REVB1, C‐REVB2 SCBR Kraft, Secondary Lime Kiln

TempleInland‐OrangeMill_NEI12492_PPTestReport‐

2004MACTIIReport.pdf 121 NEI12492 000011 121.000011 121‐‐C‐REVB1, C‐REVB2 SCBR Kraft, Secondary Lime Kiln

NEI42341A_PIII_D2a_2008‐Q1_LK‐S1.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2008‐Q1_LK‐S2.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

Test_data_memo_appendices.xlsx App B LK PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

GenericProcess Type

NEI42341A_PIII_D2a_2008‐Q2_LK‐S1.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2008‐Q2_LK‐S2.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2008‐Q3_LK‐S1.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2008‐Q3_LK‐S2.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2008‐Q4_LK‐S1.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2008‐Q4_LK‐S2.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2010‐Q1 LK.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2010‐Q1 LK.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2010‐Q2_LK‐SDTV10‐RB10‐

HFB11.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2010‐Q2_LK‐SDTV10‐RB10‐

HFB11.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2010‐Q3_LK‐SDTV10‐RB10‐

HFB11.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

Test_data_memo_appendices.xlsx App B LK PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

GenericProcess Type

NEI42341A_PIII_D2a_2010‐Q3_LK‐SDTV10‐RB10‐

HFB11.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2010‐Q4_LK‐SDTV10‐RB10‐

HFB11.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2010‐Q4_LK‐SDTV10‐RB10‐

HFB11.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2009‐Q1 LK‐S1.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2009‐Q1 LK‐S2.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2009‐Q2 LK‐S1.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2009‐Q2 LK‐S2 final.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2009‐Q3 LK.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2009‐Q3 LK.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2009‐Q4 LK.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

NEI42341A_PIII_D2a_2009‐Q4 LK.pdf 102 NEI42341A LK 102.LK 102‐‐LK‐ESP ESP Kraft Lime Kiln

Test_data_memo_appendices.xlsx App B LK PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

GenericProcess Type

2008_PM_Lime_Kiln,_No_4_Rec_Boiler_and_No_4_Smelt_Dis_Tank.pdf 105 NEI45182 EU455 105.EU455 105‐‐CD 456‐110 ESP Kraft, Secondary Lime Kiln2008_PM_Lime_Kiln_Exh,_No_4_Rec_Boiler_and_No_4_Smelt_Dis_Tank.pdf 105 NEI45182 EU455 105.EU455 105‐‐CD 456‐110 ESP Kraft, Secondary Lime Kiln2009_PM_No_3_Lime_Kiln,_No_4_Rec_Boiler_and_No_4_Smelt.pdf 105 NEI45182 EU455 105.EU455 105‐‐CD 456‐110 ESP Kraft, Secondary Lime Kiln2009_PM_No_3_Lime_Kiln_and_No_4_Smelt_Dis_Tank.pdf 105 NEI45182 EU455 105.EU455 105‐‐CD 456‐110 ESP Kraft, Secondary Lime KilnSECTION 2.pdf 107 NEI47074 11‐P14 107.11‐P14 107‐‐11‐P13 ESP Kraft Lime Kiln

SECTION 2.pdf 107 NEI47074 11‐P14 107.11‐P14 107‐‐11‐P13 ESP Kraft Lime KilnProject #1997033 ‐ July 2004.pdf 109 NEI32869A LK1 109.LK1 109‐‐LKESP ESP Kraft Lime KilnNEI32869 PROJECT 2008016 NOV 2008.pdf 109 NEI32869A LK1 109.LK1 109‐‐LKESP ESP Kraft Lime KilnNEI26506_Lime_Kiln_December_2005.pdf 114 NEI26506 U800 114.U800 114‐‐CDU7 ESP Kraft Lime KilnNEI26506_Lime_Kiln_December_2005.pdf 114 NEI26506 U800 114.U800 114‐‐CDU7 ESP Kraft Lime KilnNEI7933_PII ‐ Lime Kilns 1 and 2 ‐ PM ‐ February 16,

2005.pdf 127 NEI7933 LK1 127.LK1 127‐‐ESP1 ESP Kraft, Secondary Lime Kiln

NEI7933_PIII ‐ Lime Kilns 1 and 2 ‐ PM ‐ April 24‐25,

2007.pdf 127 NEI7933 LK1 127.LK1 127‐‐ESP1 ESP Kraft, Secondary Lime Kiln

NEI7933_PIII ‐ Lime Kilns 1 and 2 ‐ PM ‐ April 28 and

29, 2009.pdf 127 NEI7933 LK1 127.LK1 127‐‐ESP1 ESP Kraft, Secondary Lime Kiln

NEI7933_PII ‐ Lime Kilns 1 and 2 ‐ PM ‐ February 16,

2005.pdf 127 NEI7933 LK2 127.LK2 127‐‐ESP2 ESP Kraft, Secondary Lime Kiln

NEI7933_PIII ‐ Lime Kilns 1 and 2 ‐ PM ‐ April 24‐25,

2007.pdf 127 NEI7933 LK2 127.LK2 127‐‐ESP2 ESP Kraft, Secondary Lime Kiln

NEI7933_PIII ‐ Lime Kilns 1 and 2 ‐ PM ‐ April 28 and

29, 2009.pdf 127 NEI7933 LK2 127.LK2 127‐‐ESP2 ESP Kraft, Secondary Lime Kiln

NEI46931_11 2 2007 No. 2 BB, No. 3 BB, No. 2 LK,

No. 1 RF, No. 1 SDT Compliance Test Report.pdf 148 NEI46931 009 148.009 148‐‐LK2ESP ESP primary air Kraft, Secondary Lime Kiln

NEI46931_5 12‐14 2008 No. 1 & 2 LK, No. 1 & 2 RF,

No. 1 & 2 SDT Compliance Test Report.pdf 148 NEI46931 009 148.009 148‐‐LK2ESP ESP primary air Kraft, Secondary Lime Kiln

NEI46931_6 15‐17 2009 No. 1 & 2 LK, No. 1 RF, No.

1 SDT Compliance Test Report.pdf 148 NEI46931 009 148.009 148‐‐LK2ESP ESP primary air Kraft, Secondary Lime Kiln

M52009LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52009LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52009LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52009LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52009LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐

chem) Lime Kiln

M52009LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐chem) Lime Kiln

M52009LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐chem) Lime Kiln

M52009LK5.pdf 156 NEI42338 LK5 156.LK5 156‐‐LK5ESP ESP Electrostatic Precipitator

Unknown (Kraft & Semi‐chem) Lime Kiln

P_P ICR Part III_RTI162_InternationalPaper‐

EastoverMill_NEI46760_no 2 lime kiln particulate

matte.pdf 162 NEI46760 372A 162.372A 162‐‐372AESP ESP Kraft Lime Kiln

IP PENSACOLA SEPT 04 PM COMP REPORT.pdf 178 NEI26309 09P037 178.09P037 178‐‐09P37A ESP/SCBR Kraft Lime Kiln

IP PENSACOLA SEPT 04 PM COMP REPORT.pdf 178 NEI26309 09P037 178.09P037 178‐‐09P37A ESP/SCBR Kraft Lime Kiln

IP PENSACOLA SEPT 04 PM COMP REPORT.pdf 178 NEI26309 09P037 178.09P037 178‐‐09P37A ESP/SCBR Kraft Lime Kiln

Test_data_memo_appendices.xlsx App B LK PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

GenericProcess Type

RTI179_Rock‐TennDemopolis_NEI45474_PP

Survey_LKTest2001.pdf 179 NEI45474 LK3 179.LK3 179‐‐LK3ESP ESP Kraft Lime Kiln

2004 Method 5 Testing ‐ part 1 of 3.pdf 196 NEI18660 SN‐02 196.SN‐02 196‐‐SN‐02 ESP ESP (dry) Kraft Lime Kiln

NEI47077 BOWATER CATAWBA AUG 04 #2&3RF &

#2LK COMP RPT.pdf 200 NEI47077 007_10 200.007_10 200‐‐2723C ESP low NOx burners Kraft, Mechanical Lime Kiln

NEI47077 BOWATER CATAWBA SEP 06 #2 LK

EMISSION REPORT.pdf 200 NEI47077 007_10 200.007_10 200‐‐2723C ESP low NOx burners Kraft, Mechanical Lime Kiln

NEI47077 BOWATER CATAWBA SEP 08 #2 LK PM

NOX CO SO2 EMISSION REPORT.pdf 200 NEI47077 007_10 200.007_10 200‐‐2723C ESP low NOx burners Kraft, Mechanical Lime Kiln

Rayonier Jesup DLK PM test 09_23_03.pdf 240 NEI26526 CA81 240.CA81 240‐‐CAC4 ESP Kraft Lime Kiln

47091_024_2008_PM.pdf 606 NEI47091 LK4 606.LK4 606‐‐ESP1 ESP Kraft Lime Kiln47091_024_2009_PM.pdf 606 NEI47091 LK4 606.LK4 606‐‐ESP1 ESP Kraft Lime Kiln47091_024_2010_PM.pdf 606 NEI47091 LK4 606.LK4 606‐‐ESP1 ESP Kraft Lime Kiln47091_024_2010_PM.pdf 606 NEI47091 LK4 606.LK4 606‐‐ESP1 ESP Kraft Lime Kiln47091_024_2010_PM.pdf 606 NEI47091 LK4 606.LK4 606‐‐ESP1 ESP Kraft Lime Kiln2006_0808‐10.1.pdf 617 NEI42695 P22 617.P22 617‐‐C10 ESP Kraft Lime Kiln2007_0821.pdf 617 NEI42695 P22 617.P22 617‐‐C10 ESP Kraft Lime Kiln2010_0317.1.pdf 617 NEI42695 P22 617.P22 617‐‐C10 ESP Kraft Lime KilnNEI18373_009_Particulate_2009.pdf 208228535 NEI18373 009 208228535.009 208228535‐‐X014 ESP Unknown (Kraft) Lime Kiln

NEI18373_009_Particulate_2008.pdf 208228535 NEI18373 009 208228535.009 208228535‐‐X014 ESP Unknown (Kraft) Lime Kiln

NEI8619_IP Pine Hill LK 083010.pdf 116 NEI8619 001 116.001 116‐‐LKSCR SCBR

Kraft, Secondary,

SemiChem Lime Kiln

Lime Kiln 2001.pdf 117 NEI42689 P36 117.P36 117‐‐C53 SCBR Kraft Lime Kiln

Lime Kiln April 2008.pdf 119 NEI46814 EQT006 119.EQT006 119‐‐SCBR05 SCBR Kraft, Secondary Lime Kiln

LK#1 inhouse PM Source Tests 2011.pdf 133 NEI13363 14 133.14 133‐‐LK#1 SCBR Kraft Lime Kiln

LK#1 inhouse PM Source Tests 2011.pdf 133 NEI13363 14 133.14 133‐‐LK#1 SCBR Kraft Lime Kiln2004 RB & LK & SDT PM #69.pdf 135 NEI33118 004‐1 135.004‐1 135‐‐007‐5 SCBR Kraft Lime Kiln2004 RB & LK & SDT PM #69.pdf 135 NEI33118 004‐1 135.004‐1 135‐‐007‐5 SCBR Kraft Lime KilnPM_SO2_NOX_CO Lime Kiln SN‐01 May 2007.pdf 138 NEI18652 001 138.001 138‐‐SCRB LK1 SCBR Kraft Lime Kiln

LK OM5 052011.pdf 140 NEI13340 32 140.32 140‐‐481‐141 SCBR Kraft Lime Kiln

LK EPA M5 102009.pdf 140 NEI13340 32 140.32 140‐‐481‐141 SCBR Kraft Lime KilnRTI1#B09.PDF 142 NEI41552 P6009 142.P6009 142‐‐CD‐6009 SCBR Kraft, Secondary Lime KilnRTI1#802.PDF 142 NEI41552 P6025 142.P6025 142‐‐CD‐6025 SCBR Kraft, Secondary Lime KilnNEI40488 B011, P001, P005 ‐ 2009 Title VCompliance Test Rep.pdf 149 NEI40488 P001 149.P001 149‐‐MC‐102, SC‐102 SCBR Kraft Lime KilnNEI11338_WPC ‐ RF_SDT_LK ‐ Mar 2007.pdf 152 NEI11338 08 152.08 152‐‐07‐SCBR SCBR Kraft Lime KilnNEI33883 ‐ Lime Kiln ‐ February 18, 2004 ‐ 

Particulate Emission Sampling.pdf 155 NEI33883 LIME KILN 155.LIME KILN 155‐‐LK SCRUBBER SCBR Kraft, Mechanical Lime Kiln

RTI165‐InternationalPaper‐TexarkanaMill_NEI41628_PPTestReport‐

2004SubpartMMIPT.pdf 165 NEI41628 000019 165.000019 165‐‐VS‐2 SCBR Kraft Lime Kiln

RTI165‐InternationalPaper‐TexarkanaMill_NEI41628_PPTestReport‐2004SubpartMMIPT.pdf 165 NEI41628 000002 165.000002 165‐‐263009 SCBR Kraft Lime KilnRTI167 NEI340702011_IPVicksburg_StackTestReport_(PB,LK,RB,SDT,SS).pdf 167 NEI34070 004LK 167.004LK 167‐‐LKSCBR SCBR Kraft, Secondary Lime Kiln

Test_data_memo_appendices.xlsx App B LK PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

GenericProcess Type

RTI173 NEI 35908 IPTiconderoga Subpart MM Stack

Test for RB‐SDT‐LK 10‐04.pdf 173 NEI35908 LK1 173.LK1 173‐‐LKSCBR SCBR NA Kraft Lime Kiln

P_P ICR Part III_RTI174_International Paper‐Riegelwood Mill_.pdf 174 NEI40247 G‐95 174.G‐95 174‐‐G‐95 SCRUB/G‐95 CYC SCBR Kraft Lime Kiln

KapStone RR, NC Kiln October 2010 Report

Proper.PDF 176 NEI47104 G‐5 176.G‐5 176‐‐09‐CD‐004‐001 SCBR Kraft Lime Kiln

RecBoiler_WasteBoiler_SmeltTank_LimeKiln_Compliancetest2011_Part1.pdf 177 NEI33887 EU0905 177.EU0905 177‐‐EU0905SCR SCBR Kraft Lime Kiln

NEI6057 2009 #2 LK EMISSION TEST REPORT.pdf 181 NEI6057 14 181.14 181‐‐LK2_SCBR SCBR low NOx burners

Kraft, Secondary,

SemiChem Lime Kiln

NEI6057 2009 #2 LK EMISSION TEST REPORT.pdf 181 NEI6057 14 181.14 181‐‐LK2_SCBR SCBR low NOx burners

Kraft, Secondary,

SemiChem Lime Kiln

NEI6057 2009 #1LK EMISSION TEST REPORT.pdf 181 NEI6057 1 181.1 181‐‐LK1_SCBR SCBR low NOx burners

Kraft, Secondary,

SemiChem Lime Kiln

Georgia‐Pacific Cedar Springs NEI26491 P3 LK2 PM

09‐24‐2010 Compliance Test.pdf 190 NEI26491 L601 190.L601 190‐‐C601 SCBR

Kraft, Secondary,

SemiChem Lime Kiln

Georgia‐Pacific Cedar Springs NEI26491 P3 LK1 PM

2‐23‐2011 Compliance Test.pdf 190 NEI26491 L600 190.L600 190‐‐C600 SCBR

Kraft, Secondary,

SemiChem Lime Kiln

195_TR_ME DEP Summary Worksheet ‐ Lime

Kiln.PDF 195 NEI46835 002 195.002 195‐‐LKSCR SCBR Kraft Lime Kiln2004 Method 5 Testing ‐ part 1 of 3.pdf 196 NEI18660 SN‐09 196.SN‐09 196‐‐SN‐09 SCBR Scrubber Kraft Lime Kiln

NEI8601_Unit 008_2011.pdf 205 NEI8601 008 205.008 205‐‐LKS SCBR Kraft, Secondary Lime KilnRecoveryBoilerSmeltTank#2LimeKiln_EmmisionsTestReport_2005.pdf 340 NEI46852 008 340.008 340‐‐LKVS SCBR Kraft, Secondary Lime Kiln#4LK Compliance 042711.pdf 525 NEI8265 EU17 525.EU17 525‐‐LKSCB SCBR Kraft Lime Kiln610 Verso 2009 LK A&B Report with Apn.pdf 610 NEI6261 7 610.7 610‐‐LKB‐VS SCBR Kraft, Mechanical Lime Kiln

610 Verso 2009 LK A&B Report with Apn.pdf 610 NEI6261 7 610.7 610‐‐LKB‐VS SCBR Kraft, Mechanical Lime Kiln

610 Verso 2009 LK A&B Report with Apn.pdf 610 NEI6261 7 610.7 610‐‐LKB‐VS SCBR Kraft, Mechanical Lime Kiln

610 Verso 2010 LKA Report.pdf 610 NEI6261 7 610.7 610‐‐ALK‐WS SCBR Kraft, Mechanical Lime Kiln610 Verso 2010 LKA Report.pdf 610 NEI6261 7 610.7 610‐‐ALK‐WS SCBR Kraft, Mechanical Lime Kiln

610 Verso 2009 LK A&B Report with Apn.pdf 610 NEI6261 8 610.8 610‐‐LKB‐VS SCBR Kraft, Mechanical Lime Kiln

610 Verso 2009 LK A&B Report with Apn.pdf 610 NEI6261 8 610.8 610‐‐LKB‐VS SCBR Kraft, Mechanical Lime Kiln

610 Verso 2009 LK A&B Report with Apn.pdf 610 NEI6261 8 610.8 610‐‐LKB‐VS SCBR Kraft, Mechanical Lime Kiln

2009 LK.pdf 613 NEI11172 009 613.009 613‐‐LKSCR SCBR Kraft, Secondary Lime Kiln

2009 LK.pdf 613 NEI11172 009 613.009 613‐‐LKSCR SCBR Kraft, Secondary Lime Kiln

2011 Stack Report‐AIR.pdf 130 NEI18338 4 130.4 130‐‐4LKSCR SCBR Kraft Lime Kiln

2011 Stack Report‐AIR.pdf 130 NEI18338 5 130.5 130‐‐5LKSCR SCBR Kraft Lime KilnNEI 42254 RockTenn WP Stack Tests.pdf 131 NEI42254 16 131.16 131‐‐CZ12‐2 SCBR Kraft, Secondary Lime Kiln

NEI 42254 RockTenn WP Stack Tests.pdf 131 NEI42254 16 131.16 131‐‐CZ12‐2 SCBR Kraft, Secondary Lime Kiln

NEI33104‐KILN 2007 PM Compliance.pdf 157 NEI33104 KILN 157.KILN 157‐‐VENSCR SCBR Kraft Lime Kiln

2011.0606‐0609.2Q.tests.pdf 188 NEI40600 001LK1, 002LK2, 003LK3

188.001LK1, 002LK2,003LK3

188‐‐LK1SCB, 188‐‐LK2SCB, 188‐‐

LK3SCB SCBR

Kraft, Secondary,

SemiChem Lime Kiln

RTI206_BRPLK#411.13.2007.pdf 206 NEI40282 G‐37 206.G‐37 206‐‐LK4 DEM/LK4 SCRUB SCBR Kraft Lime Kiln

9‐0224C Evergreen F.pdf 171 NEI18658 009 171.009 171‐‐VSLK1 SCBR Kraft Lime Kiln

9‐0224C Evergreen F.pdf 171 NEI18658 010 171.010 171‐‐VSLK2 SCBR Kraft Lime KilnIPPB OCT 05 MACT II REPORT ‐ 1.pdf (3 parts) 171 NEI18658 009 171.009 171‐‐VSLK1 SCBR Kraft Lime Kiln

Green rows were not used in the NSPS review.

Test_data_memo_appendices.xlsx App B LK PM 
ate Matter

RTI+EUID100.115102.LK102.LK103.G‐165

105.EU455107.11‐P14

108.LK1108.LK1108.LK1111.G‐35

111.G‐35

114.U800114.U800120.M19120.M18124.004‐1126.LK127.LK2127.LK1131.18131.18131.18131.18132.21LK4136.EU 033137.512139.04143.6063145.001146.30146.6147.3147.55147.55148.003148.009150.CAU‐12

154.P30 ‐ Lime Kiln156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5

Configuration General Test Report Information Production Rate Inlet/OutletHas the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet data

provided?

No PM 2004 Lime Kiln Natural Gas 6/17/2004 M5 7.52 ton CaO/hr Outlet

No PM 2011 #1 Lime Kiln‐ South Stack Natural Gas 1/4/2011 M5 13.8 ton CaO/hr Outlet

No PM 2011 #1 Lime Kiln‐ North Stack Natural Gas 1/4/2011 M5 13.8 ton CaO/hr Outlet

no PM 2008 No. 5 Lime Kiln No. 6 fuel oil 8/28/2008 M5 17.08 ton CaO/hr Outlet

no PM 2010 Lime Kiln No.3 unspecified 10/12/2010 M5 8.695 ton CaO/hr Outlet

PM 2010 Lime Kiln Natural Gas, Pet Coke 7/21/2010 M5 15.7 ton CaO/hr Outlet

No PM 2004

Lime Kiln ‐ Performance Engineering Testcond. I unspecified 3/9/2004 M5 10.23 ton CaO/hr Outlet

No PM 2004

Lime Kiln ‐ Performance Engineering Testcond. II unspecified 3/10/2004 M5 10.22 ton CaO/hr Outlet

No PM 2004 Lime Kiln ‐ MACT II Compliance Test unspecified 6/19/2004 M5 10.1 ton CaO/hr Outlet

No PM 2009 Lime Kiln ‐ Cond. I No. 6 fuel oil 8/4/2009 M5 12.63 ton CaO/hr Outlet

No PM 2009 Lime Kiln ‐ Cond II Natural Gas 8/6/2009 M5 12.47 ton CaO/hr Outlet

No PM 2008 Lime Kiln Natural Gas 12/16/2008 M5 16.66666667 ton CaO/hr

Converted from ton CaO/day (p.

111 of report) Outlet

No PM 2008 Lime Kiln Oil 12/16/2008 M5 16.49166667 ton CaO/hr

Converted from ton CaO/day (p.

111 of report) Outlet

No PM 2009 Lime Kiln 2A Natural gas 7/20/2009 M5 7.542 ton CaO/hr Outlet

No PM 2009 Lime Kiln 1A Natural gas 7/21/2009 M5 8.17 ton CaO/hr Outlet

No PM 2010 Lime Kiln Natural gas and pet coke 11/2/2010 M5 38.6 ton CaO/hr Outlet

No PM 2009 Lime Kiln unspecified 12/11/2009 M5 15.373 ton CaO/hr Outlet

No PM 2011 Lime Kiln No. 2 Oil 4/5/2011 M5 7.167 ton CaO/hr Outlet

No PM 2011 Lime Kiln No. 1 Oil 4/4/2011 M5 6.99 ton CaO/hr Outlet

No PM 2004 Lime Kiln 1 Residual Fuel Oil 1/19/2004 M5 9.2 ton CaO/hr Outlet

No PM 2004 Lime Kiln 1 Residual Fuel Oil 1/20/2004 M5 7.94 ton CaO/hr Outlet

No PM 2004 Lime Kiln 1 Residual Fuel Oil 3/9/2004 M5 10.6 ton CaO/hr Outlet

No PM 2004 Lime Kiln 1 Residual Fuel Oil 3/10/2004 M5 6.8 ton CaO/hr Outlet

PM 2010 Lime Kiln 4 Fuel oil 7/27/2010 M5 24 ton CaO/hr Outlet

no PM 2010 Rotary Lime Kiln Natural gas 2/10/2010 M5 16.95 ton CaO/hr Outlet

No PM 2008 Lime Kiln 4 Natural gas 5/13/2008 M5 8.7 ton CaO/hr Outlet

No PM 2004 Lime Kiln unspecified 9/9/2004 M5 6600 g/h mud flow rate Only units given Outlet

no PM 2004 No. 4 Lime Kiln unspecified 6/4/2004 M5 19.79 ton CaO/hr Outlet

No PM 2002 Lime Kiln ‐ filterable unspecified 10/23/2002 M5 unspecified Outlet

No PM 2008 No. 2 Lime Kiln unspecified 10/15/2008 M5 26.60 ton CaO/hr Outlet

No PM 2009 No. 1 Lime Kiln unspecified 4/20/2009 M5 375.04 mud feed rate only units given Outlet

NO NA PM 2010 No. 1 Lime Kiln unspecified 6/15/2010 M5 unspecified Outlet

NO NA PM 2010 No. 7 Lime Kiln unspecified 9/23/2010 M5 18.42 ton CaO/hr Outlet

NO NA PM 2010 No. 7 Lime Kiln unspecified 10/22/2010 M5 18.33 ton CaO/hr Outlet

no PM 2010 No.1 Lime Kiln unspecified 5/25/2010 M5 13.723 ton CaO/hr Outlet

no PM 2010 No. 2 Lime Kiln unspecified 5/26/2010 M5 unspecified Outlet

No PM 2009 Lime Kiln Natural Gas 10/13/2009 M5 unspecified OutletNo PM 2010 Lime Kiln Fuel Oil 12/8/2010 M5 12.94 ton CaO/hr Outlet

No PM 2010 Lime Kiln 5 ‐ North Stack Natural Gas 3/30/2010 M5 11.8 ton CaO/hr Outlet

No PM 2010 Lime Kiln 5 ‐ South Stack Natural Gas 3/30/2010 M5 11.8 ton CaO/hr Outlet

No PM 2010 Lime Kiln 5 ‐ North Stack Natural Gas 6/8/2010 M5 11.04 ton CaO/hr Outlet

No PM 2010 Lime Kiln 5 ‐ South Stack Natural Gas 6/8/2010 M5 11.04 ton CaO/hr Outlet

No PM 2010 Lime Kiln 5 ‐ North Stack Natural Gas 8/12/2010 M5 9.2 ton CaO/hr Outlet

No PM 2010 Lime Kiln 5 ‐ South Stack Natural Gas 8/12/2010 M5 9.2 ton CaO/hr Outlet

No PM 2010 Lime Kiln 5 ‐ North Stack Natural Gas 10/5/2010 M5 7.9 ton CaO/hr Outlet

No PM 2010 Lime Kiln 5 ‐ South Stack Natural Gas 10/5/2010 M5 7.9 ton CaO/hr Outlet

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

156.145000156.145000156.145000156.145000156.143100156.143100156.143100159.F4162.372A162.371A163.LK1501163.LK2502164.P12166.LK01166.LK02172.LK03172.LK03174.G‐18

175.LK2A175.LK2A175.LK1A175.LK1A175.LK1A178.09P037178.09P037179.LK3180.L001180.L002184.LK2184.LK2184.LK1184.LK1185.07

Has the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet data

provided?

No PM 2010 Lime Kiln 4 Natural Gas 2/18/2010 M5 7.5 ton CaO/hr Outlet

No PM 2010 Lime Kiln 4 Natural Gas 4/22/2010 M5 7.5 ton CaO/hr Outlet

No PM 2010 Lime Kiln 4 Natural Gas 9/3/2010 M5 7.92 ton CaO/hr Outlet

No PM 2010 Lime Kiln 4 Natural Gas 12/15/2010 M5 8.33 ton CaO/hr Outlet

No PM 2010 Lime Kiln 3 Natural Gas 1/28/2010 M5 5.21 ton CaO/hr Outlet

No PM 2010 Lime Kiln 3 Natural Gas 2/9/2010 M5 7.3 ton CaO/hr Outlet

No PM 2010 Lime Kiln 3 Natural Gas 11/24/2010 M5 5.92 ton CaO/hr Outlet

No PM 2010 Lime Kiln unspecified 12/3/2010 M5 14.56 ton mud/hour only units given Outlet

No PM 2008 No. 2 Lime Kiln No.6 fuel oil 8/5/2008 M5 14.54 ton CaO/hr Outlet

No PM 2009 No. 1 Lime Kiln No. 6 fuel oil 5/20/2009 M5 9.63 ton CaO/hr Outlet

No PM 2011 No. 1 Lime Kiln Natural Gas 6/9/2011 M5 14.163 ton CaO/hr Outlet

No PM 2011 No. 2 Lime Kiln Natural Gas/ Coke 6/8/2011 M5 14.55 ton CaO/hr Outlet

PM 2010 Lime Kiln ‐ Front Half only No.6 fuel oil 8/17/2010 M5 4.83 ton CaO/hr Outlet

No PM 2009 No. 1 Lime Kiln Fuel Oil 7/24/2009 M5 10.96 ton CaO/hr Outlet

No PM 2009 No. 2 Lime Kiln Fuel Oil 7/23/2009 M5 12.33 ton CaO/hr Outlet

no PM 2009 No. 3 Lime Kiln Fuel Oil 10/21/2009 M5 11.78 ton CaO/hr Outlet

no PM 2009 No. 3 Lime Kiln Natural Gas 10/20/2009 M5 11.53 ton CaO/hr Outlet

PM 2004 No. 4 Lime Kiln Fuel Oil 10/27/2004 M5 31.1 ton CaO/hr Outlet

no PM 2010 No. 2 Lime Kiln ‐ Shutdown Natural Gas 1/12/2010 M5 16.4 ton CaO/hr Outlet

no PM 2010 No. 2 Lime Kiln ‐ Startup Natural Gas 1/14/2010 M5 14.3 ton CaO/hr Outlet

no PM 2010 No. 1 Lime Kiln ‐ Shutdown Natural Gas 2/4/2010 M5 2.917 ton CaO/hr Outlet

no PM 2010 No. 1 Lime Kiln ‐ Startup Natural Gas 2/4/2010 M5 4.104 ton CaO/hr Outlet

no PM 2010 No. 1 Lime Kiln Natural Gas 8/9/2010 M5 9.205 ton CaO/hr Outlet

No PM 2010 Lime Kiln (Scrubber Outlet) ‐ Firing Gas Natural Gas 5/27/2010 M5 14.1 ton CaO/hr Outlet

No PM 2010 Lime Kiln (Scrubber Outlet) ‐ Firing Oil Oil 5/26/2010 M5 14.1 ton CaO/hr Outlet

No PM 2010 No. 3 Lime Kiln Natural Gas 10/12/2010 M5 21.21 ton CaO/hr Outlet

No PM 2010 No. 1 Lime Kiln Oil 3/24/2010 M5 5.00 ton CaO/hr Outlet

No PM 2010 No. 2 Lime Kiln Oil 3/25/2010 M5 5 ton CaO/hr Outlet

No PM 2004 No. 2 Lime Kiln ‐ Condition I Natural Gas 10/22/2004 M5 10.84 ton CaO/hr Outlet

No PM 2004 No. 2 Lime Kiln ‐ Condition II Pet coke and natural gas 10/26/2004 M5 10.94 ton CaO/hr Outlet

No PM 2010 No. 1 Lime Kiln ‐ High CaO Production Natural Gas and Pet Coke 3/4/2010 M5 12.71 ton CaO/hr Outlet

No PM 2010 No. 1 Lime Kiln ‐ Low CaO Production Natural Gas and Pet Coke 3/4/2010 M5 8.08 ton CaO/hr Outlet

No PM 2009 No. 4 Lime Kiln Natural Gas 1/23/2009 M5 186 gpm (firing rate) only units given Outlet

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

185.07185.07185.07186.LK189.SN25189.SN25196.SN‐02

197.1198.004199.011200.007_10201.SR0003202.Lime Kiln EU340

203.LKScr203.LKScr203.LKScr203.LKScr206.G‐38

207.103A207.103A207.103A207.103A226.LK1226.LK2240.CA81242.AA‐013243.LG07243.LG07531.LK7600.G0908600.G0905600.G0903600.G0905606.LK4615.21615.21169.03617.P22126.LK132.21LK4132.21LK4132.21LK4132.21LK4132.21LK4132.21LK4132.21LK4

Has the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet data

provided?

No PM 2009 No. 4 Lime Kiln Natural Gas 4/15/2009 M5 175 gpm (firing rate) only units given Outlet

No PM 2009 No. 4 Lime Kiln Natural Gas 7/23/2009 M5 185 gpm (firing rate) only units given Outlet

No PM 2009 No. 4 Lime Kiln Natural Gas 10/7/2009 M5 180 gpm (firing rate) only units given Outlet

No PM 2009 No. 3 Lime Kiln

Natural Gas and No. 6 Fuel

Oil 7/14/2009 M5 21.00 ton/hour

only units given/converted to

hours and assumed CaO Outlet

no PM 2011 No. 4 Lime Kiln Oil and Natural Gas 3/22/2011 M5 480.05 gpm mud flow Only units given Outlet

no PM 2011 No. 4 Lime Kiln Oil and Natural Gas 4/1/2011 M5 412.1 gpm mud flow Only units given Outletno PM 2010 No. 3 Lime Kiln unspecified 4/23/2010 M5 15.5 ton CaO/hr Outlet

No PM 2008 Lime Kiln Natural Gas 9/16/2008 M5 67.11 ton CaO/hr Outlet

Yes

burner, duct, and

conveyor modifications PM 2005 Lime Kiln unspecified 9/9/2005 M5 13.83 ton CaO/hr Outlet

No PM 2011 No. 3 Lime Kiln unspecified 7/7/2011 M5 13.31 ton CaO/hr Outlet

No PM 2010 No. 2 Lime Kiln Natural Gas 3/30/2010 M5 16.3 ton mud/hour

only units given/converted to

hours Outlet

No PM 2007 Lime Kiln

Natural Gas and Pet. Coke

fuel 5/8/2007 M5 14.18 ton CaO/hr Outlet

no

Particulate matter testincludes condensable as

well as method 5

filterable PM PM 2011 Lime Kiln Natural Gas 7/21/2011 M5 7.54 ton CaO/hr Outlet

No PM 2011 Lime Kiln Natural Gas 2/8/2011 M5 220 gpm mud flow only units given Outlet

No PM 2011 Lime Kiln Natural Gas 3/22/2011 M5 240 gpm mud flow only units given Outlet

No PM 2011 Lime Kiln Natural Gas 4/5/2011 M5 240 gpm mud flow only units given OutletNo PM 2011 Lime Kiln Natural Gas 4/22/2011 M5 240 gpm mud flow only units given Outlet

no PM 2007 Lime Kiln #5 unspecified 11/13/2007 M5 unspecified Outlet

no NA PM 2011 Lime Kiln ‐ Normal Condition Natural Gas 6/7/2011 M5 2.88 ton CaO/hr Outlet

no NA PM 2011 Lime Kiln ‐Condition I Natural Gas 6/7/2011 M5 2.88 ton CaO/hr Outlet

no NA PM 2011 Lime Kiln ‐ Condition II Natural Gas 6/8/2011 M5 2.88 ton CaO/hr Outletno NA PM 2011 Lime Kiln ‐ Condition III Natural Gas 6/8/2011 M5 2.88 ton CaO/hr Outletno PM 2004 Lime Kiln #1 unspecified 8/10/2004 M5 323 gpm mud flow only units given Outlet

no PM 2004 Lime Kiln #2 unspecified 1/16/2004 M5 300 gpm mud flow only units given Outlet

No PM 2010 D Lime Kiln unspecified 3/16/2010 M5 27.56 ton CaO/hr Outlet

No PM 2010 Lime Kiln unspecified 9/1/2010 M5 18 ton CaO/hr Outlet

No PM 2009 No. 5 Lime Kiln ‐ Condition I Natural Gas 10/29/2009 M5 58 ton mud/hour only units given Outlet

No PM 2009 No. 5 Lime Kiln ‐ Condition II Natural Gas 10/29/2009 M5 33.5 ton mud/hour only units given Outlet

No PM 2011 No. 7 Lime Kiln Natural Gas 5/4/2011 M5 26.04 ton CaO/hr Outlet

no PM 2010 No. 3 Lime Kiln Natural Gas 11/14/2010 M5 12.07 ton CaO/hr Outlet

no PM 2011 No. 2 Lime Kiln Natural Gas 6/16/2011 M5 12.09 ton CaO/hr Outlet

no PM 2010 No. 1 Lime Kiln Natural Gas 11/3/2010 M5 7.9625 ton CaO/hr Outlet

no PM 2010 No. 2 Lime Kiln Natural Gas 6/9/2010 M5 12.08 ton CaO/hr Outlet

no PM 2011 Lime Kiln 4 unspecified 4/6/2011 M5 27.1 ton CaO/hr Outlet

no PM 2009 Lime Kiln ‐ Front Half Natural Gas 10/22/2009 M5 9.983 ton CaO/hr Outlet

no PM 2009 Lime Kiln ‐  ODEQ 5 Natural Gas 10/22/2009 M5 9.983 ton CaO/hr Outlet

No PM 2010 Lime Kiln unspecified 9/24/2010 M5 425.2333333 gpm mud flow

ton CaO/hr not provided. 74.5

TBLS/hr provided. Outlet

no PM 2011 S22 Lime Kiln unspecified 3/17/2011 M5 6.333333333 ton CaO/hr OutletNo PM 2004 Lime Kiln Unspecified 2/5/2004 M5 8.441 ton CaO/hr Outlet

No PM 2007 No. 4 Lime Kiln Fuel Oil 5/22/2007 M5 25.24 ton CaO/hr Outlet

No PM 2008 No. 4 Lime Kiln Fuel Oil 6/19/2008 M5 22.22 ton CaO/hr Outlet

No PM 2006 No. 4 Lime Kiln Fuel Oil 6/15/2006 M5 23.27666667 ton CaO/hr Outlet

No PM 2005 No. 4 Lime Kiln Unspecified 6/2/2005 M5 23.7 ton CaO/hr Outlet

No PM 2004 No. 4 Lime Kiln Unspecified 05/24/2004 M5 Unspecified Unspecified Outlet

No PM 2003 No. 4 Lime Kiln Unspecified 05/19/2003 M5 Unspecified Unspecified Outlet

No PM 2002 No. 4 Lime Kiln Unspecified 05/21/2002 M5 Unspecified Unspecified Outlet

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

132.21LK4132.21LK4136.EU 033136.EU 033136.EU 033136.EU 033136.EU 033137.511137.511137.512137.512137.512137.511137.512137.512146.30154.P30 ‐ Lime Kiln154.P30 ‐ Lime Kiln154.P30 ‐ Lime Kiln154.P30 ‐ Lime Kiln186.LK186.LK186.LK186.LK243.LG07243.LG07105.EU455121.000011121.000011102.LK102.LK

Has the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet data

provided?

No PM 2001 No. 4 Lime Kiln Unspecified 05/22/2001 M5 22.467 ton CaO/hr

Assumed Suspect Production

Rate was hourly rate. Suspect

production rate listed as

"averaged 22.467 TPD" may be

hourly rate as on order of

magnitude of other tests for

hourly rate. Could not check by

Part III data base because

claimed CBI. Permit has 630

tons CaO/day ‐> 26 tons CaO/hr. Outlet

No PM 2009 No. 4 Lime Kiln Fuel Oil 06/17/2009 M5 24.5 ton CaO/hr OutletNo PM 2001 Lime Kiln Natural Gas 01/23/2001 M5 15.24166667 ton CaO/hr OutletNo PM 2008 Lime Kiln Unspecified 07/07/2008 M5 18.13333333 ton CaO/hr Outlet

No PM 2006 Lime Kiln Natural Gas 07/12/2006 M5 18.13333333 ton CaO/hr Outlet

No PM 2004 Lime Kiln Natural Gas 10/28/2004 M5 17.40694444 ton CaO/hr OutletNo PM 2002 Lime Kiln Unspecified 11/14/2002 M5 17.21388889 ton CaO/hr Outlet

No PM 2005 No. 3 Lime Kiln Natural Gas 6/15/2005 M5 8.541666667 ton CaO/hr Outlet

No PM 2004 No. 3 Lime Kiln Natural Gas 8/12/2004 M5 7.9 ton CaO/hr OutletYes No PBSCBR PM 2005 No. 4 Lime Kiln Natural Gas 04/12/2005 M5 8.7 ton CaO/hr OutletYes No PBSCBR PM 2005 No. 4 Lime Kiln Natural Gas 07/15/2005 M5 8.7 ton CaO/hr Outlet

Yes No PBSCBR PM 2004 No. 4 Lime Kiln Natural Gas 08/12/2004 M5 7.9 ton CaO/hr Outlet

No PM 2008 No. 3 Lime Kiln Natural Gas 05/14/2008 M5 9 ton CaO/hr Outlet

No PM 2002 No. 4 Lime Kiln Natural Gas 07/18/2002 M5 9.34 ton CaO/hr Outlet

Yes

No indication scrubber in

use. PM 2002 No. 4 Lime Kiln Unspecified 07/18/2002 M5 9.3 ton CaO/hr

"Hourly production rate"

assumed to be ton CaO/hr

because it is very close to the

production rate in a separate

test for this kiln. Inlet/Outlet

No PM 2004 No. 2 Lime Kiln unspecified 02/18/2004 M5 unspecified Outlet

Yes Scrubber shut down. PM 2003 Lime Kiln Natural Gas 10/30/2003 M5 365 gpm mud flow CaO production unspecified Outlet

No PM 2007 Lime Kiln Natural Gas 08/01/2007 M5 12.97222222 ton CaO/hr

310 TPD Lime Mud = 369.7 gpmLime Mud Outlet

No PM 2008 Lime Kiln No. 2 Fuel Oil 12/04/2008 M5 11.69444444 ton CaO/hr

294 TPD Lime Mud = 320.2 gpmLime Mud Outlet

No PM 2009 Lime Kiln Natural Gas 08/25/2009 M5 12.84722222 ton CaO/hr

338 TPD Lime Mud = 391 gpm

Lime Mud Outlet

No PM 2007 No. 3 Lime Kiln

Natural Gas and/or No. 6 Fuel

Oil 09/05/2007 M5 21.78391319 ton CaO/hr

Assume this is ton CaO/hr

(seems reasonable). Listed asCaus.Kiln TPD (converted) Outlet

No PM 2006 No. 3 Lime Kiln

Natural Gas and/or No. 6 Fuel

Oil 07/26/2006 M5 17.41666667 ton CaO/hr

Calculated from ton CaO/day onprocess screen prints Outlet

No PM 2008 Lime Kiln Unspecified 10/15/2008 M5 19.79583333 ton CaO/hr Outlet

No PM 2005 No. 3 Lime Kiln

Natural Gas and/or No. 6 Fuel

Oil 11/22/2005 M5 420 gpm mud flow Outlet

No PM 2005 No. 5 Lime Kiln Fuel Oil 11/01/2005 M5 59.7 ton mud/hour OutletNo PM 2007 No. 5 Lime Kiln Natural Gas 10/30/2007 M5 55.5 ton mud/hour OutletNo PM 2007 No. 3 Lime Kiln Natural Gas 05/15/2007 EPA\ODEQ M5 20.32083333 ton CaO/hr OutletNo PM 2002 Lime Kiln Unspecified 10/31/2002 M5 10.25 ton CaO/hr

Converted from ton CaO/day (p.

275 of report) Outlet

No PM 2004 Lime Kiln Unspecified 8/24/2004 M5 330 gpm Not in ton CaO Outlet

No PM 2008 Lime Kiln (No. 1 South Stack) Natural Gas 1/29/2008 M5 11.9 ton CaO/hr Outlet

No PM 2008 Lime Kiln (No. 2 North Stack) Natural Gas 01/29/2008 M5 11.9 ton CaO/hr Outlet

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK

Has the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet data

provided?

No PM 2008 Lime Kiln (No. 1 South Stack) Natural Gas 04/11/2008 M5 13.1 ton CaO/hr Outlet

No PM 2008 Lime Kiln (No. 2 North Stack) Natural Gas 04/11/2008 M5 13.1 ton CaO/hr OutletNo PM 2008 Lime Kiln (No. 1 South Stack) Natural Gas 07/07/2008 M5 14.51 ton CaO/hr Outlet

No PM 2008 Lime Kiln (No. 2 North Stack) Natural Gas 07/08/2008 M5 14.51 ton CaO/hr OutletNo PM 2008 Lime Kiln (No. 1 South Stack) Natural Gas 10/10/2008 M5 13.09 ton CaO/hr Outlet

No PM 2008 Lime Kiln (No. 2 North Stack) Natural Gas 10/10/2008 M5 13.09 ton CaO/hr OutletNo PM 2010 Lime Kiln (No. 1 South Stack) Natural Gas 01/12/2010 M5 10.59 ton CaO/hr Outlet

No PM 2010 Lime Kiln (No. 2 North Stack) Natural Gas 01/12/2010 M5 10.59 ton CaO/hr OutletNo PM 2010 Lime Kiln (No. 1 South Stack) Natural Gas 05/04/2010 M5 14.1 ton CaO/hr Outlet

No PM 2010 Lime Kiln (No. 2 North Stack) Natural Gas 05/04/2010 M5 14.1 ton CaO/hr OutletNo PM 2010 Lime Kiln (No. 1 South Stack) Natural Gas 08/25/2010 M5 14.9 ton CaO/hr Outlet

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK

Has the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet data

provided?

No PM 2010 Lime Kiln (No. 2 North Stack) Natural Gas 08/25/2010 M5 14.9 ton CaO/hr OutletNo PM 2010 Lime Kiln (No. 1 South Stack) Natural Gas 10/14/2010 M5 14.33 ton CaO/hr Outlet

No PM 2010 Lime Kiln (No. 1 South Stack) Natural Gas 10/14/2010 M5 14.33 ton CaO/hr Outlet

No PM 2009 Lime Kiln (No. 1 South Stack) Natural Gas 01/23/2009 M5 13.14 ton CaO/hr Outlet

No PM 2009 Lime Kiln (No. 2 North Stack) Natural Gas 01/23/2009 M5 13.14 ton CaO/hr OutletNo PM 2009 Lime Kiln (No. 1 South Stack) Natural Gas 04/10/2009 M5 14.1 ton CaO/hr Outlet

No PM 2009 Lime Kiln (No. 2 North Stack) Natural Gas 04/10/2009 M5 14.1 ton CaO/hr Outlet

No PM 2009 Lime Kiln (No. 1 South Stack) Natural Gas 07/06/2009 M5 13.85 ton CaO/hr Outlet

No PM 2009 Lime Kiln (No. 2 North Stack) Natural Gas 07/06/2009 M5 13.85 ton CaO/hr OutletNo PM 2009 Lime Kiln (No. 1 South Stack) Natural Gas 10/16/2009 M5 14.08 ton CaO/hr Outlet

No PM 2009 Lime Kiln (No. 2 North Stack) Natural Gas 10/16/2009 M5 14.08 ton CaO/hr Outlet

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

105.EU455105.EU455105.EU455105.EU455107.11‐P14

107.11‐P14

109.LK1109.LK1114.U800114.U800127.LK1127.LK1127.LK1127.LK2127.LK2127.LK2148.009148.009148.009156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5162.372A178.09P037178.09P037178.09P037

Has the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet data

provided?

no PM 2008 No. 3 Lime Kiln Natural Gas, Pet Coke 05/22/2008 EPA\ODEQ M5 11.65

ton CaO/hr(calculated)

1016.9 ADMT/day pulp

production provided in

appendix; 480.4 ton/day CaCO3(kiln input); and 185 gpm

CaCO3. Used convention of 550

lb CaO/ADTP for kraft mills. Outlet

no PM 2008 No. 3 Lime Kiln Natural Gas 10/21/2008 EPA\ODEQ M5 11.48

ton CaO/hr(calculated)

Used convention of 550 lb

CaO/ADTP for kraft mills. Outlet

no PM 2009 No. 3 Lime Kiln Natural Gas, Pet Coke 06/02/2009 EPA\ODEQ M5 10.87

ton CaO/hr(calculated)

Used convention of 550 lb

CaO/ADTP for kraft mills. Outlet

no PM 2009 No. 3 Lime Kiln Natural Gas, Methanol 09/22/2009 EPA\ODEQ M5 11.43

ton CaO/hr(calculated)

Used convention of 550 lb

CaO/ADTP for kraft mills. Outlet

PM 2007 Lime Kiln Natural Gas, Pet Coke 10/11/2007 M5 15.8 ton CaO/hr Based on daily average Outlet

PM 2008 Lime Kiln Natural Gas 06/17/2008 M5 15.13 ton CaO/hr Based on daily average Outlet

No PM 2004 No. 3 Lime Kiln Natural Gas, Coke 06/03/2004 M5 13.54 ton CaO/hr Outlet

No PM 2008 No. 3 Lime Kiln Natural Gas 09/03/2008 M5 13.13 ton CaO/hr Based on daily average Outlet

No PM 2005 Lime Kiln No. 6 fuel oil 12/13/2005 M5 16.22 ton CaO/hr

Production reported as "Kiln

production = 389.3 ODT/day."

PIII has 408 ton CaO/day, so

interpreted ODT/day to be ton

CaO/day. Outlet

No PM 2005 Lime Kiln Natural Gas 12/14/2005 M5 16.22 ton CaO/hr

Production reported as "Kiln

production = 389.3 ODT/day."

PIII has 408 ton CaO/day, so

interpreted ODT/day to be ton

CaO/day. Outlet

No PM 2005 Lime Kiln No. 1 Oil 02/16/2005 M5 6.75 ton CaO/hr Outlet

No PM 2007 Lime Kiln No. 1 Oil 04/25/2007 M5 5.85 ton CaO/hr Outlet

No PM 2009 Lime Kiln No. 1 Oil 04/28/2009 M5 7.2 ton CaO/hr

assumed this was the daily rate

consistent with other testedproduction rates for this kiln Outlet

No PM 2005 Lime Kiln No. 2 Oil 02/16/2005 M5 6.78 ton CaO/hr Outlet

No PM 2007 Lime Kiln No. 2 Oil 04/24/2007 M5 5.98 ton CaO/hr Outlet

No PM 2009 Lime Kiln No. 2 Oil 04/29/2009 M5 6.7 ton CaO/hr

assumed this was the daily rate

consistent with other testedproduction rates for this kiln Outlet

no PM 2007 No. 2 Lime Kiln unspecified 10/29/2007 M5 unspecified No production data given Outletno PM 2008 No. 2 Lime Kiln unspecified 05/14/2008 M5 unspecified No production data given Outletno PM 2009 No. 2 Lime Kiln unspecified 06/16/2009 M5 unspecified No production data given OutletNo PM 2009 Lime Kiln No. 5 ‐ North Natural Gas 03/27/2009 M5 7.29 ton CaO/hr Based on daily average Outlet

No PM 2009 Lime Kiln No. 5 ‐ South Natural Gas 03/27/2009 M5 7.29 ton CaO/hr Based on daily average Outlet

No PM 2009 Lime Kiln No. 5 ‐ North Natural Gas 06/03/2009 M5 5.17 ton CaO/hr Based on daily average Outlet

No PM 2009 Lime Kiln No. 5 ‐ South Natural Gas 06/03/2009 M5 5.17 ton CaO/hr Based on daily average Outlet

No PM 2009 Lime Kiln No. 5 ‐ North Natural Gas 08/27/2009 M5 10.83 ton CaO/hr Based on daily average Outlet

No PM 2009 Lime Kiln No. 5 ‐ South Natural Gas 08/27/2009 M5 10.83 ton CaO/hr Based on daily average Outlet

No PM 2009 Lime Kiln No. 5 ‐ North Natural Gas 10/22/2009 M5 10 ton CaO/hr Based on daily average Outlet

No PM 2009 Lime Kiln No. 5 ‐ South Natural Gas 10/22/2009 M5 10 ton CaO/hr Based on daily average Outlet

No PM 2006 No. 2 Lime Kiln No. 6 fuel oil 08/03/2006 M5 14.17 ton CaO/hr Based on daily average Outlet

No PM 2004 Lime Kiln fuel oil 09/08/2004 M5 18.6 ton CaO/hr OutletNo PM 2004 Lime Kiln ‐ low load fuel oil 09/09/2004 M5 2.9 ton CaO/hr Outlet

No PM 2004 Lime Kiln ‐ Retest Natural Gas, fuel oil 11/18/2004 M5 18 ton CaO/hr Outlet

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

179.LK3196.SN‐02

200.007_10200.007_10200.007_10240.CA81606.LK4606.LK4606.LK4606.LK4606.LK4617.P22617.P22617.P22208228535.009208228535.009116.001117.P36119.EQT006133.14133.14135.004‐1135.004‐1138.001140.32140.32142.P6009142.P6025149.P001152.08155.LIME KILN

165.000019165.000002167.004LK

Has the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet data

provided?

No PM 2001 No. 3 Lime Kiln fuel oil 09/26/2001 M5 15.23 ton CaO/hr Outlet

no PM 2004 No. 3 Lime Kiln unspecified 09/01/2004 M5 12.53 ton CaO/hr Outlet

No PM 2004 No. 2 Lime Kiln Natural Gas, fuel oil 08/06/2004 M5 16.27 ton CaO/hr

Reported as CaCO but reported

as production not feed rate.

Therefore assumed CaO. Close

to production rate in PIII (465

ton CaO/day). Outlet

No PM 2006 No. 2 Lime Kiln Natural Gas 08/22/2006 M5 17.01 ton CaO/hr

Reported as CaCO but reported

as production not feed rate.

Therefore assumed CaO. Closeto production rate in PIII (465ton CaO/day). Outlet

No PM 2008 No. 2 Lime Kiln Natural Gas 08/28/2008 M5 15.40 ton CaO/hr

Reported as CaCO but reported

as production not feed rate.

Therefore assumed CaO. Close

to production rate in PIII (465ton CaO/day). Outlet

No PM 2003 "D" Lime Kiln unspecified 09/23/2003 M5 unspecified Outletno PM 2008 No. 4 Lime Kiln Natural Gas 05/30/2008 M5 27 ton CaO/hr Outlet

no PM 2009 No. 4 Lime Kiln Fuel Oil 04/21/2009 M5 27.27 ton CaO/hr Outletno PM 2010 No. 4 Lime Kiln No. 6 fuel oil 04/23/2010 M5 27.08 ton CaO/hr Outletno PM 2010 No. 4 Lime Kiln No. 6 fuel oil 04/24/2010 M5 27.08 ton CaO/hr Outletno PM 2010 No. 4 Lime Kiln No. 6 fuel oil 04/25/2010 M5 unspecified Outlet

no PM 2006 Lime Kiln unspecified 08/08/2006 M5 6.04 ton CaO/hr Based on daily average Outlet

no PM 2007 Lime Kiln Natural Gas 08/21/2007 M5 5.65 ton CaO/hr

Stated as Lime mud. Only

production value given. PIII has

119 ton CaO/day = 5 ton CaO/hr

so assume value provided is ton

CaO/hr. Outlet

no PM 2010 Lime Kiln Natural Gas 03/17/2010 M5 6.26 ton CaO/hr

Production data was difficult toread Outlet

No PM 2009 No. 2 Lime Kiln CTO 04/30/2009 M5 530 gpm CaCO Only production data given. Outlet

No PM 2008 No. 2 Lime Kiln unspecified 05/01/2008 M5 540 gpm CaCO Only production data given. Outlet

No PM 2010 Lime Kiln Natural Gas & Petcoke 8/30/2010 M5 10.4 ton CaO/hr Outlet

No PM 2001 Lime Kiln Natural Gas 3/13/2001 M5 3.1375 ton CaO/hr Outlet

No PM 2008 Lime Kiln unspecified 4/3/2008 M5 unspecified unspecified Outlet

No PM 2011 Lime Kiln #1 unspecified 3/21/2011

M5 modifiedper AOP unspecified unspecified Outlet

No PM 2011 Lime Kiln #1 unspecified 6/9/2011

M5 modifiedper AOP unspecified unspecified Outlet

No PM 2004 Lime Kiln No. 6 Oil 7/13/2004 M5 12.70833333 ton CaO/hr OutletNo PM 2004 Lime Kiln No. 6 Oil 7/14/2004 M5 13.45833333 ton CaO/hr OutletNo PM 2007 Lime Kiln (SN‐01) PetCoke & Natural Gas 5/23/2007 M5 7.283333333 ton CaO/hr

Converted from ton CaO/day (p.

73 of report) Outlet

No PM 2011 Lime Kiln unspecified 5/16/2011 ODEQ M5 7.3 ton CaO/hr Outlet

PM 2009 Lime Kiln natural gas 10/22/2009 M5 8.4 ton CaO/hr Outlet

No PM 2003 LIME KILN #2 unspecified 7/14/2003 M5 7.370833333 ton CaO/hr Outlet

No PM 2003 LIME KILN #1 unspecified 7/30/2003 M5 6.145833333 ton CaO/hr Outletno PM 2009 Rotary Lime Kiln unspecified 4/2/2009 M5 unspecified unspecified Outlet

No PM 2007 lime kiln unspecified 3/8/2007

M5 modifiedperTexas ACB

Procedure ‐ cyclonic flow 15.2 ton CaO/hr Outlet

No PM 2004 Lime Kiln unspecified 2/18/2004 M5 10.5 ton CaO/hr Outlet

No PM 2004 No. 1 Lime Kiln (LK01) unspecified 7/23/2004 M5 7.7 ton CaO/hr Outlet

No PM 2004 No. 2 Lime Kiln (LK02) unspecified 7/26/2004 M5 15.2 ton CaO/hr Outlet

No NA PM 2011 Lime Kiln Natural Gas 1/20/2011 M5 11.4 ton CaO/hr Outlet

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

173.LK1174.G‐95

176.G‐5

177.EU0905181.14181.14181.1190.L601190.L600195.002196.SN‐09

205.008340.008525.EU17610.7610.7610.7610.7610.7610.8610.8610.8613.009613.009130.4130.5131.16131.16157.KILN188.001LK1, 002LK2,

003LK3206.G‐37

171.009171.010171.009

Has the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date(mm/dd/yyyy)

Emission TestMethod

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet data

provided?

No NA PM 2004 lime kiln #6 residual oil 9/29/2004 M5 8.5 ton CaO/hr Outlet

PM 2003 No. 3 Lime Kiln unspecified 6/3/2003 M5 14.328 ton CaO/hr Outlet

No PM 2010 Lime Kiln

No 4/ No. 6 & Natural Gas

(w/ NCGs) 9/15/2010 M5 9.14 ton CaO/hr Outlet

No PM 2011 Lime Kiln unspecified 3/31/2011 M5 28.08333333 ton CaO/hr Outlet

No PM 2009 No. 2 Lime Kiln ‐ W/O NCGs unspecified 2/10/2009 M5 11.6 ton CaO/hr Outlet

No PM 2009 No. 2 Lime Kiln ‐ W/ NCGs unspecified 2/11/2009 M5 11.1 ton CaO/hr OutletNo PM 2009 No. 1 Lime Kiln unspecified 3/12/2009 M5 12.2 ton CaO/hr Outlet

No PM 2010 Lime Kiln No. 2 unspecified 9/24/2010 M5 11.7 ton CaO/hr Outlet

No PM 2011 Lime Kiln No. 1 unspecified 2/23/2011 M5 27.9 ton CaO/hr Outlet

No PM 2010 Lime Kiln unspecified 11/15/2010 M5 19.03333333 ton CaO/hr Outlet

no PM 2004 #2 Lime Kiln unspecified 9/12/2004 M5 12.5 ton CaO/hr Outlet

No PM 2011 Lime Kiln unspecified 1/26/2011 M5 unspecified unspecified Outlet

No PM 2005 Number 2 Lime Kiln, SN‐08 unspecified 6/23/2005 M5 50.5 ton CaO/hr

Appendix had 10.8 (but units of

measure were unclear), andsummary had 50.5 tons CaO/hr Outlet

No PM 2011 No. 4 Lime Kiln Fuel Oil 4/27/2011 M5 40.5 ton CaO/hr Outlet

no PM 2009 A Lime Kiln

No. 6 Oil run 1, No. 6 Oil run

2, Waste Oil run 3 6/18/2009 M5 14 ton CaO/hr Outlet

no PM 2009 A Lime Kiln Waste Oil 6/18/2009 M5 16 ton CaO/hr Outlet

no PM 2009 A Lime Kiln Waste Oil 6/22/2009 M5 17 ton CaO/hr Outlet

no PM 2010 A Lime Kiln Waste Oil 6/15/2010 M5 16 ton CaO/hr Outlet

no PM 2010 A Lime Kiln Waste Oil 6/16/2010 M5 14 ton CaO/hr Outlet

no PM 2009 B Lime Kiln Waste Oil 6/17/2009 M5 14 ton CaO/hr Outlet

no PM 2009 B Lime Kiln

Waste Oil run 1, No. 6 Fuel

Oil Runs 2 & 3 6/17/2009 M5 16 ton CaO/hr Outlet

no PM 2009 B Lime Kiln Waste Oil 6/19/2009 M5 17 ton CaO/hr Outlet

No PM 2009 Lime Kiln Natural Gas, Without Petcoke 12/3/2009 M5 unspecified unspecified Outlet

No PM 2009 Lime Kiln Natural Gas, With Petcoke 12/4/2009 M5 unspecified unspecified Outlet

No PM 2011 No. 1 Lime Kiln unspecified 06/24/2011 M5 6.03 ton CaO/hr based on daily average Outlet

No PM 2011 No. 2 Lime Kiln unspecified 06/24/2011 M5 5.75 ton CaO/hr based on daily average Outlet

No PM 2003 No. 2 Lime Kiln Fuel Oil 12/11/2003 M5 unspecified OutletNo PM 2003 No. 2 Lime Kiln Fuel Oil 12/12/2003 M5 unspecified OutletNo PM 2007 Lime Kiln No. 6 Fuel Oil 07/18/2007 M5 3.71 ton CaO/hr OutletNo PM 2011 Combined Lime Kilns Natural Gas 06/07/2011 M5 12.10 ton CaO/hr Outletno PM 2007 No. 4 Lime Kiln Natural Gas 11/13/2007 M5 unspecified production data was reserved. Outletno PM 2009 No. 1 Lime Kiln unspecified 7/7/2009 M5 7.68 ton CaO/hr

Assumed tons per day provided

based on magnitude ofproduction in PIII data, and from

other tests Outlet

no PM 2009 No. 2 Lime Kiln unspecified 7/6/2009 M5 7.270833333 ton CaO/hr

Assumed tons per day providedbased on magnitude ofproduction in PIII data, and from

other tests Outlet

no PM 2005 No. 1 Lime Kiln natural gas 7/20/2005 M5 7.81 ton CaO/hr Outlet

Test_data_memo_appendices.xlsx App B LK PM 
ate Matter

RTI+EUID100.115102.LK102.LK103.G‐165

105.EU455107.11‐P14

108.LK1108.LK1108.LK1111.G‐35

111.G‐35

114.U800114.U800120.M19120.M18124.004‐1126.LK127.LK2127.LK1131.18131.18131.18131.18132.21LK4136.EU 033137.512139.04143.6063145.001146.30146.6147.3147.55147.55148.003148.009150.CAU‐12

154.P30 ‐ Lime Kiln156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5

Inlet ‐ Testing Methodology Data Inlet ‐ Average Stack Gas Parameters Inlet ‐ Average Emissions Data

Average Sampling RunLength_Inlet(mins)

Average Fraction of

Isokinetic Sampling

Rate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

156.145000156.145000156.145000156.145000156.143100156.143100156.143100159.F4162.372A162.371A163.LK1501163.LK2502164.P12166.LK01166.LK02172.LK03172.LK03174.G‐18

175.LK2A175.LK2A175.LK1A175.LK1A175.LK1A178.09P037178.09P037179.LK3180.L001180.L002184.LK2184.LK2184.LK1184.LK1185.07

Average Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

185.07185.07185.07186.LK189.SN25189.SN25196.SN‐02

197.1198.004199.011200.007_10201.SR0003202.Lime Kiln EU340

203.LKScr203.LKScr203.LKScr203.LKScr206.G‐38

207.103A207.103A207.103A207.103A226.LK1226.LK2240.CA81242.AA‐013243.LG07243.LG07531.LK7600.G0908600.G0905600.G0903600.G0905606.LK4615.21615.21169.03617.P22126.LK132.21LK4132.21LK4132.21LK4132.21LK4132.21LK4132.21LK4132.21LK4

Average Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

132.21LK4132.21LK4136.EU 033136.EU 033136.EU 033136.EU 033136.EU 033137.511137.511137.512137.512137.512137.511137.512137.512146.30154.P30 ‐ Lime Kiln154.P30 ‐ Lime Kiln154.P30 ‐ Lime Kiln154.P30 ‐ Lime Kiln186.LK186.LK186.LK186.LK243.LG07243.LG07105.EU455121.000011121.000011102.LK102.LK

Average Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

61.66666667 102.3 43011 14707 37.88 462 28.85 20.28 2.87 28.21290678 gr/dscf @ 10% O2 3 0 5856.22 629.7010753 lb/ton CaO

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK

Average Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK

Average Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

105.EU455105.EU455105.EU455105.EU455107.11‐P14

107.11‐P14

109.LK1109.LK1114.U800114.U800127.LK1127.LK1127.LK1127.LK2127.LK2127.LK2148.009148.009148.009156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5162.372A178.09P037178.09P037178.09P037

Average Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

179.LK3196.SN‐02

200.007_10200.007_10200.007_10240.CA81606.LK4606.LK4606.LK4606.LK4606.LK4617.P22617.P22617.P22208228535.009208228535.009116.001117.P36119.EQT006133.14133.14135.004‐1135.004‐1138.001140.32140.32142.P6009142.P6025149.P001152.08155.LIME KILN

165.000019165.000002167.004LK

Average Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

173.LK1174.G‐95

176.G‐5

177.EU0905181.14181.14181.1190.L601190.L600195.002196.SN‐09

205.008340.008525.EU17610.7610.7610.7610.7610.7610.8610.8610.8613.009613.009130.4130.5131.16131.16157.KILN188.001LK1, 002LK2,

003LK3206.G‐37

171.009171.010171.009

Average Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App B LK PM 
ate Matter

RTI+EUID100.115102.LK102.LK103.G‐165

105.EU455107.11‐P14

108.LK1108.LK1108.LK1111.G‐35

111.G‐35

114.U800114.U800120.M19120.M18124.004‐1126.LK127.LK2127.LK1131.18131.18131.18131.18132.21LK4136.EU 033137.512139.04143.6063145.001146.30146.6147.3147.55147.55148.003148.009150.CAU‐12

154.P30 ‐ Lime Kiln156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5

Outlet ‐ Testing Methodology Data Outlet ‐ Average Stack Gas Parameters Outlet ‐ Average Emissions Data Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐Detect

Runs

Average_Outlet(lb/hr)

Average_(lb/produ

113.33 98.9 16700 7050 31.7 353 28.54 20.1 5.6 0.009 gr/dscf @ 10% O2 3 0 0.7 

66.7 97.3 25686 11496 25.1 427.5 30.07 16.52 8.36 0.0006 gr/dscf @ 10% O2 3 0 0.063 

66 101.3 25393 11041 29.3 403.5 30.07 16.89 7.89 0.0008 gr/dscf @ 10% O2 3 0 0.084 

75.67 100.3 39017 20221 37.9 166 29.63 25.3 3.1 0.0561 gr/dscf @ 10% O2 3 0 16 

64 105.6 46243 26557 18.47 285.28 29.75 11.22 11.9 0.0106 gr/dscf @ 10% O2 3 0 1.96 

60 95 22796 10437 28.3 365.1 29.878 23.02 4.89 0.0025 gr/dscf @ 10% O2 3 0 0.32 

67 106.67 34913.33 19333 34.78 166.54 30.15 21.77 7.5 0.072 gr/dscf @ 10% O2 3 0 14.1 

65 106.27 36386 20236 35.05 166.92 30.42 20.43 6.83 0.045 gr/dscf @ 10% O2 3 0 10.1 

60 98.83 31484.33 18128.83 32.67 161.78 30.115 18.68 6.37 0.028 gr/dscf @ 10% O2 6 0 5.78 

66.67 103.19 58881.38 23485.33 31.31 447.63 29.87 22.57 4.61 0.0119 gr/dscf @ 10% O2 3 0 3.579 

66.67 107.81 58508.9 23631.44 32.57 419.74 29.87 19.63 4.96 0.0055 gr/dscf @ 10% O2 3 0 1.622 

62.67 95.3 55569 22518 35.51 379.3 29.88 20 5.367 0.0011 gr/dscf @ 10% O2 3 0 0.3 

60 92.8 54584 23621 31.5 376 29.92 20 6.2 0.0018 gr/dscf @ 10% O2 3 0 0.5 

60 104.1 35485 16520 43.4 172.3 29.45 15.3 3.3 0.041 gr/dscf @ 10% O2 3 0 5.8056 

60 103.8 19960 10934 41.3 162.2 29.46 15.6 3.6 0.013 gr/dscf @ 10% O2 3 0 1.21836 

69.3 99.2 71706 39621 35.2 161.4 30.01 17.5 7.3 0.0247 gr/dscf @ 10% O2 3 0 10.451 

60 96.69 21380 14990 20.65 138.1 29.36 21.88 3 0.0014 gr/dscf @ 10% O2 3 0 0.292 

61.67 101.8 42963 21648 19.6 372.9 29.59 13.4 9.8 0.0033 gr/dscf @ 10% O2 3 0 0.638 

61.67 102.6 39621 18989 21.8 397.4 29.79 14.9 7.6 0.0016 gr/dscf @ 10% O2 3 0 0.314 

99.33 97.2 24500 15500 26.8 152 29.76 23.3 3.3 0.03 gr/dscf @ 10% O2 3 0 6.5 

85.33 93.3 18200 12400 22.3 145 30.04 22.1 4.2 0.032 gr/dscf @ 10% O2 3 0 5.1 

88.33 94.7 21800 13000 30.2 159 30.03 24 2.9 0.074 gr/dscf @ 10% O2 3 0 13.6 

71.33 98.9 18700 11600 29.5 156 30.17 17 7.4 0.087 gr/dscf @ 10% O2 3 0 10.8 

60 102.5 67116 32716 24.87 353.92 29.9 17.58 7.4 0.0583 gr/dscf @ 10% O2 3 0 22.066 

60 100.9 69900 24200 28.8 582 28.74 23.1 34.3 0.03 gr/dscf @ 10% O2 3 0 10 

60 98.88 53700 19900 28.67 531.86 29.23 16.26 6.65 0.002 gr/dscf @ 10% O2 3 0 0.44 

60 100.67 27045 16762 28.76 154.9 30.14 22.6 4.2 0.06 gr/dscf @ 10% O2 3 0 13.3 unspecifi

63.67 101 35312 17622 24.6 341.4 30.05 18.83 5.4 0.0044 gr/dscf @ 10% O2 3 0 0.94 

60 98.33 44630.67 22130 39.67 170 29.36 17.867 5 0.038 gr/dscf @ 10% O2 3 0 10.3 unspecifi60 96.8 81084 45561 35.3 166.2 28.8 23.8 4.1 0.0053 gr/dscf @ 10% O2 3 0 2.969 

60 94.9 37469 22294 25.7 146.2 27.51 13.2 9.4 0.03 gr/dscf @ 10% O2 3 0 6.072 unspecifi60 97.2 30474 14727 41.9 171.4 29.75 16.2 5.2 0.0413 gr/dscf @ 10% O2 3 0 7.45 unspecifi60 99.5 88893 31360 28.7 597 29.65 18.5 6.1 0.022 gr/dscf @ 10% O2 3 0 7.94 

60 98.9 83951 29490 28.8 596.3 29.56 19.1 5.9 0.012 gr/dscf @ 10% O2 3 0 4.15 

66.25 96.8 44954 28116 25.6 149.33 29.04 23.5 4.1 0.03 gr/dscf @ 10% O2 4 0 11.2 

67 59.7 37110 14330 35.9 389 28.97 23.2 3.4 0.015 gr/dscf @ 10% O2 3 0 3.01 unspecifi65 99.6 33813 28452 37.8 169 30 20 5.1 0.024 gr/dscf @ 10% O2 3 0 5.4 unspecifi

69.3 101.53 23474 13012 32.5 164.4 29.06 19.6 7.2 0.0004 gr/dscf @ 10% O2 3 0 0.05 

64 110.8 21107 9604 32.4 308 29.48 20.8 4 0.0019 gr/dscf @ 10% O2 2 0 0.24 

64 110.8 23560 10277 34.3 318 29.48 20.8 4 0.0026 gr/dscf @ 10% O2 2 0 0.36 

60 106.3 21030 8563 33.8 396 30.05 19.3 5.5 0.0014 gr/dscf @ 10% O2 2 0 0.15 

60 106.3 21768 10191 25.3 381 30.05 19.3 5.5 0.0008 gr/dscf @ 10% O2 2 0 0.1 

60 101.7 12888 6230 29 316 30.03 18.6 6.2 0.0019 gr/dscf @ 10% O2 2 0 0.14 

60 101.7 12972 6545 25.2 317 30.03 18.6 6.2 0.0126 gr/dscf @ 10% O2 2 0 0.85 

60 91.9 16252 8305 23.7 335 30.37 19.1 5.7 0.0032 gr/dscf @ 10% O2 2 0 0.32 

60 91.9 15455 7519 24.5 367 30.37 19.1 5.7 0.0016 gr/dscf @ 10% O2 2 0 0.14 

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

156.145000156.145000156.145000156.145000156.143100156.143100156.143100159.F4162.372A162.371A163.LK1501163.LK2502164.P12166.LK01166.LK02172.LK03172.LK03174.G‐18

175.LK2A175.LK2A175.LK1A175.LK1A175.LK1A178.09P037178.09P037179.LK3180.L001180.L002184.LK2184.LK2184.LK1184.LK1185.07

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐DetectRuns

Average_Outlet(lb/hr)

Average_(lb/produ

69.3 104.7 20726 18329 24.3 140 30.11 17.6 6.2 0.0183 gr/dscf @ 10% O2 3 0 2.94 

65.3 102.1 19206 17455 12.9 123 30.08 18.6 4.7 0.0098 gr/dscf @ 10% O2 3 0 1.9 

68 98.7 20857 18110 20.3 146 29.89 18.5 5 0.0093 gr/dscf @ 10% O2 3 0 1.7 

68 103.2 20724 17851 26 149 29.81 17.2 6.7 0.0134 gr/dscf @ 10% O2 3 0 1.98 

60 101.9 21535 19301 16.2 130 30.06 12.9 10.4 0.0137 gr/dscf @ 10% O2 3 0 1.85 

60 100.7 23620 20876 15.9 138 30.06 13.7 9.6 0.0149 gr/dscf @ 10% O2 3 0 2.29 

60 102.7 21266 18993 17.3 137 30.31 12.2 11.1 0.0212 gr/dscf @ 10% O2 3 0 2.56 

62 102.9 14703 9527 25.6 150.3 30.13 15.5 7.2 0.0385 gr/dscf @ 10% O2 3 0 3.952 unspecifi

65.3 105 59400 22800 31 477 29.43 23.5 5.5 0.011 gr/dscf @ 10% O2 3 0 3 

62.7 100 23000 17600 15 130 29.98 24.2 4.4 0.06 gr/dscf @ 10% O2 3 0 14 

66.7 101.5 28688 14309 40.5 171 29.92 17.3 4.6 0.059 gr/dscf @ 10% O2 3 0 10.7 

66.7 97.2 42380 21949 38.3 168 29.92 18.7 5.7 0.053 gr/dscf @ 10% O2 3 0 13.9 

60 100 13799 8936 23.9 148.5 29.34 20 7.2 0.0902 gr/dscf @ 10% O2 3 0 9.02 

60 101.6 38301 20817 35.9 166 30.07 20.4 6.3 0.1338 gr/dscf @ 10% O2 3 0 32 

60 97.2 42225 22279 37.4 168.7 30.04 20.9 5.5 0.0323 gr/dscf @ 10% O2 3 0 8.7 

60 99.5 40104 26920 23.4 147.67 29.92 17.5 7.94 0.028 gr/dscf @ 10% O2 3 0 7.6 

60 100.5 43434 27367 27.6 154.67 29.92 18.5 7.3 0.034 gr/dscf @ 10% O2 3 0 9.9 

60 103.7 109493 46586 30.4 405.3 29.98 22.8 5.7 0.0045 gr/dscf @ 10% O2 3 0 2.5 

60 100.3 49315 29768 26 146.97 29.28 10.49666667 13.57333333 0.0383 gr/dscf @ 10% O2 3 0 8.3 

60 102.1 33846 26084 11.5 117 29.3 5.86 14.2 0.0154 gr/dscf @ 10% O2 3 0 2.6 

60 94.2 20912 13896 22.5 142.3 29.25 10.235 15.94666667 0.0172 gr/dscf @ 10% O2 3 0 0.99 

60 94.6 22626 16641 16 130.33 29.3 9.84 10.7 0.0145 gr/dscf @ 10% O2 3 0 1.9 

60 101.2 23382 13552 31.7 165 30.05 18.6 4.93 0.0109 gr/dscf @ 10% O2 3 0 1.6 

60 105.8 68416 33178 41.5 172.4 29.73 17.7 6 0.005 gr/dscf @ 10% O2 3 0 1.9 

64 99.8 67534 34855 38.1 169.5 29.73 19.2 6.2 0.005 gr/dscf @ 10% O2 3 0 2 

60 103.9 81076 33507 32.2 398 29.67 16.3 7.2 0.0113 gr/dscf @ 10% O2 3 0 4.1 

60 94.4 20417 13061 24.8 155.8 29.7 15.4 8.1 0.0673 gr/dscf @ 10% O2 3 0 8.9 

60 99.9 20820 13743 23.2 148.3 29.58 15.2 8.8 0.0585 gr/dscf @ 10% O2 3 0 7.7 

60 105.6 41232.7 20784.7 40.3 166.7 29.9 15.5 6.67 0.0045 gr/dscf @ 10% O2 3 0 1.0333 

60 101.0 39876.3 22403.7 34.3 160 29.9 18.4 6.33 0.0021 gr/dscf @ 10% O2 3 0 0.52 

60 97.5 30655 21779 31.08 153.4 29.9 14 2.59 0.0175 gr/dscf @ 10% O2 3 0 5.81 

60 99.8 26029 19407 26.96 150.2 29.92 14 4.9 0.0186 gr/dscf @ 10% O2 3 0 4.55 

60 unspecified 23137.44 14945 24.52 157 29.92 14 3.73 0.0172 gr/dscf @ 10% O2 3 0 2.20332 unspecifi

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

185.07185.07185.07186.LK189.SN25189.SN25196.SN‐02

197.1198.004199.011200.007_10201.SR0003202.Lime Kiln EU340

203.LKScr203.LKScr203.LKScr203.LKScr206.G‐38

207.103A207.103A207.103A207.103A226.LK1226.LK2240.CA81242.AA‐013243.LG07243.LG07531.LK7600.G0908600.G0905600.G0903600.G0905606.LK4615.21615.21169.03617.P22126.LK132.21LK4132.21LK4132.21LK4132.21LK4132.21LK4132.21LK4132.21LK4

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐DetectRuns

Average_Outlet(lb/hr)

Average_(lb/produ

60 unspecified 17109.44 12042 18.24 153.33 29.92 14.83 7.83 0.0217 gr/dscf @ 10% O2 3 0 2.239812 unspecifi

60 unspecified 22438.25 14169 26.25 156.66 29.92 11 4.26 0.0105 gr/dscf @ 10% O2 3 0 1.27521 unspecifi

60 unspecified 32756.54 22785 19.2 153.33 29.92 19.33 5.36 0.01055 gr/dscf @ 10% O2 3 0 2.060415 unspecifi

60 100.69 68427 35387 32.14 233 30 21.1 5.9 0.0133 gr/dscf @ 10% O2 3 0 5.56 

60 99.71 58888.8 31552.4 36.49 163 29.77 18.22 7.08 0.0679 gr/dscf @ 10% O2 3 0 23.7 unspecifi

66 94.85 57157.1 29559.6 36.39 165 30.02 17.65 6.58 0.0164 gr/dscf @ 10% O2 3 0 5.67 unspecifi

60 105 56575 23206 36.9 352.8 29.92 16 4.5 0.0052 gr/dscf @ 10% O2 3 0 1.56 

60 105.9 15487 8872 32.9 163.1 30.18 11.87 8.63 0.0428 gr/dscf @ 10% O2 3 0 3.68 

60 99.2 34013 24155 19.7 140.4 30.1 17.7 6 0.0525 gr/dscf @ 10% O2 3 0 14.82 

60 99.5 26302 11747 45.1 175.2 29.3 19.5 3.6 0.0179 gr/dscf @ 10% O2 3 0 2.9 

60 100.8 57649 24909 29.9 380.4 29.39 18.7 6.5 0.002 gr/dscf @ 10% O2 3 0 0.67 unspecifi

60 98 39357.8 23135 31.01 159.2 29.9 16.22 8.92 0.0664 gr/dscf @ 10% O2 3 0 14.47 

60 100.23 24600 12800 39.76 166.9 28.56 21.3 4.6 0.034 gr/dscf @ 10% O2 3 0 5.56 

60 97.6 27895 16037 32.56 163.72 30.13 19.24 4.78 0.034 gr/dscf @ 10% O2 3 0 6.94 unspecifi65 104.5 26141 14776 33.4 159.75 29.88 20.37 4.13 0.029 gr/dscf @ 10% O2 3 0 5.97 unspecifi60 94.1 28231 16329 31.09 159.78 29.49 20.07 4.32 0.033 gr/dscf @ 10% O2 3 0 6.947 unspecifi65 104 26100 14800 33.4 160 29.88 20.4 4.1 0.029 gr/dscf @ 10% O2 3 0 6 unspecifi

67.33 108.8 34083 21654 20.5 145 27.38 19.6 5.8 0.0334 gr/dscf @ 10% O2 3 0 8.571 unspecifi

65 99.2 7743 4360 32.04 158.8 29.08 18.56 4.42 0.058 gr/dscf @ 10% O2 3 0 3.27 

61.33 99.2 7948 4547 31.14 157.8 29.08 19.24 4.48 0.058 gr/dscf @ 10% O2 3 0 3.43 

61 102 8316 4707 31.51 158.8 29.98 19.35 4.08 0.067 gr/dscf @ 10% O2 3 0 4.15 

61.33 101.9 8273 4573 33.04 159.6 29.98 19.67 4.04 0.082 gr/dscf @ 10% O2 3 0 4.96 

63.33 100 68255 39907 31 165 29.9 12.67 9.3 0.0378 gr/dscf @ 10% O2 3 0 13.69 unspecifi

64 96 54174 34241 26.2 159.9 30.07 14.7 6.93 0.0065 gr/dscf @ 10% O2 3 0 2.42 unspecifi60 97.9 68787 38462 33.8 161.7 29.67 25.8 2.1 0.0014 gr/dscf @ 10% O2 3 0 0.8 

60 103.2 59707 35205 30.3 159.2 29.72 17.8 9.2 0.0072 gr/dscf @ 10% O2 3 0 2.312 

60 101.1 92698 49098 36.6 168.9 29.79 20.2 5.9 0.003 gr/dscf @ 10% O2 3 0 1.75 unspecifi60 101.4 74452 42716 32.4 162.7 29.93 19.8 6 0.026 gr/dscf @ 10% O2 3 0 12.88 unspecifi60 94.9 80882 31717 26.5 526.8 29.84 22.7 3.9 0.0023 gr/dscf @ 10% O2 3 0 0.96 

60 96.5 30504 18236 29.7 158.4 29.64 22.1 4.9 0.014 gr/dscf @ 10% O2 3 0 3.1 

60 98.6 43643 22079 39.6 167.1 29.29 18.2 5.5 0.0344 gr/dscf @ 10% O2 3 0 9.2 

60 105 21956 11062 42.1 167.6 29.31 20.8 3.5 0.091 gr/dscf @ 10% O2 3 0 13.68 

60 97.8 45706.2 23206.7 40 166.4 29.3 17.1 5.5 0.0476 gr/dscf @ 10% O2 3 0 13.3 

60 96.07 89952 36817 27.84 472.69 29.97 22.16 3.89 0.0074 gr/dscf @ 10% O2 3 0 20 

60 100.7 22503 15465 21.7 145.3 30.12 16.04 6.72 0.0223 gr/dscf @ 10% O2 3 0 3.88 

60 100.7 22503 15465 21.7 145.3 30.12 16.04 6.72 0.0248 gr/dscf @ 10% O2 3 0 4.31 

70 101.7 51672 29575 32.8 160.6 29.79 17.8 7.67 0.075093773 gr/dscf @ 10% O2 3 0 23.34 unspecifi65 106.5 29522 11347 34.6 403.5 28.77 16.6 7.2 0.0044 gr/dscf @ 10% O2 3 0 0.5484 0.0

66 100.5666667 37899 19253 27.3 296.9333333 29.89 15.6 4.8 0.003779835 gr/dscf @ 10% O2 3 0 0.923333333 0.1

60 94.97 64987 31604 24.01 371.75 30.15 18.31 7.23 0.0013 gr/dscf @ 10% O2 3 0 0.477 0.0

60 98.30666667 59983 27629 26.77 377.67 29.88 16.50 8.83 0.0026 gr/dscf @ 10% O2 3 0 0.727 0.0

64 98.1 63621.33333 28946.66667 28.9 365.3 29.93 16.4 7.0 0.004557143 gr/dscf @ 10% O2 3 0 1.447 0.0

64 95.3 62998 28443 27.2 392.1 29.96 13.3 7.9 0.004954198 gr/dscf @ 10% O2 3 0 1.448 

unspecified unspecified unspecified unspecified unspecified unspecified unspecified unspecified unspecified 0.0165 gr/dscf @ 10% O2 3 0 4.786 

unspecified unspecified unspecified unspecified unspecified unspecified unspecified unspecified unspecified 0.0033 gr/dscf @ 10% O2 3 0 0.898 unspecifi

66 102.7 63578 31369 22.9 365.2 29.92 15.6 9.2 0.013516949 gr/dscf @ 10% O2 3 0 3.889 

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

132.21LK4132.21LK4136.EU 033136.EU 033136.EU 033136.EU 033136.EU 033137.511137.511137.512137.512137.512137.511137.512137.512146.30154.P30 ‐ Lime Kiln154.P30 ‐ Lime Kiln154.P30 ‐ Lime Kiln154.P30 ‐ Lime Kiln186.LK186.LK186.LK186.LK243.LG07243.LG07105.EU455121.000011121.000011102.LK102.LK

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐DetectRuns

Average_Outlet(lb/hr)

Average_(lb/produ

unspecified unspecified unspecified unspecified unspecified unspecified unspecified unspecified unspecified 0.0368 gr/dscf @ 10% O2 unspecified unspecified 10.13 0.4

60 104.3266667 60235 28173 30.64 326.58 30.05 17.51 7.71 0.0143 gr/dscf @ 10% O2 3 0 4.62 0.1

74.66666667 101.6666667 71086.33333 26098.66667 25.47333333 571.6666667 17.36666667 6.066666667 0.016794643 gr/dscf @ 10% O2 3 0 5.01 0.

64.66666667 71633.33333 25100 29.48333333 562.1 28.8 24.55 2.65 0.029613079 gr/dscf @ 10% O2 3 0 10.62333333 0.5

65.66666667 97.1 65250.66667 24128 27.53333333 553.3333333 29.31 20.7 5.6 0.023866667 gr/dscf @ 10% O2 3 0 6.93 0.3

63.66666667 97.8 68467.66667 23438 28.21666667 603.3333333 28.75 21.33666667 3.266666667 0.01937406 gr/dscf @ 10% O2 3 0 6.3 0.3

63.33333333 103.1 76919 25660 30.23 598 28.75 21.35 4.29 0.0258 gr/dscf @ 10% O2 3 0 8.625 0.5

73.66666667 104 41500 16100 31.6 454 29.48 20.38 3.3 0.0009 gr/dscf @ 10% O2 3 0 0.21 0.0

62.33333333 99 38894 15287 29.97 460 29.26 23.9 2.6 0.0004 gr/dscf @ 10% O2 3 0 0.093 0.0

63 100 49663 17524 34.06 501.05 29.14 20.15 3.9 0.00105 gr/dscf @ 10% O2 6 0 0.25 0.0

69.33333333 101 52200 17900 31.2 566 29.08 23 4.3 0.0011 gr/dscf @ 10% O2 3 0 0.28 0.0

63 101.6666667 42895 15312 32.72 514.2 29.29 21.3 2.1 0.0004 gr/dscf @ 10% O2 3 0 0.099 0.0

74 101 46700 17700 29.9 494 29.33 20.9 3.4 0.0017 gr/dscf @ 10% O2 3 0 0.42 0.0

68 100.1 38947 14773 34.77 411 28.77 19.13 4.23 0.00068873 gr/dscf @ 10% O2 3 0 0.133 0.0

60.66666667 100.8 37586 14725 33.31 402 28.77 19.33 4.08 0.000981678 gr/dscf @ 10% O2 3 0 0.191 0.0

64.66666667 101.2 76736 34499 44.9 164.3 28.86 23.6 5.3 0.0034 gr/dscf @ 10% O2 3 0 1.458 unspecifi

67.66666667 97.5 39800 17300 31.5 326 28.32 21.3 5.0 0.0040 gr/dscf @ 10% O2 3 0 0.863333333 unspecifi

70.66666667 107 32406 16805 37.9 166.4 29.62 19.0 4.3 0.0015 gr/dscf @ 10% O2 3 0 0.321 0.070.66666667 96.33333333 29953 17301 31.1 161 29.52 21.1 6.28 0.0009 gr/dscf @ 10% O2 3 0 0.180 0.075.33333333 96.73333333 27947 15259 34 169.7 29.53666667 17.4 6.99 0.0004 gr/dscf @ 10% O2 3 0 0.059 0.065.66666667 94.7 78560 42734 32.2 202 30.11 13.9 6.7 0.00986 gr/dscf @ 10% O2 3 0 4.67 0.2

64 95.7 73438 39373 33.4 195 29.87 14.33666667 6.05 0.0235 gr/dscf @ 10% O2 3 0 10.8 0.6

66 105.1 67951 34503 33 235 30.03 23.2 4.9 0.050 gr/dscf @ 10% O2 3 0 21 1.0

64 96.6 63222 34965 33.3 172 29.71 20.32 6.2 0.0132 gr/dscf @ 10% O2 3 0 5.32 unspecifi

64.33333333 98 75393 41135 36 165 30.17 20.8 5.8 0.007 gr/dscf @ 10% O2 3 0 3.2 unspecifi64.66666667 99 84991 52129 28.6 159 30.09 17.4 7.3 0.002 gr/dscf @ 10% O2 3 0 1.23 unspecifi

63 102.4 57016 29327 21.99 327.67 29.44 11.00 11.73 0.0047 gr/dscf @ 10% O2 3 0 0.98 0.0

60 100 33350 21900 25 150 30.12 7.9 12.6 0.015 gr/dscf @ 10% O2 3 0 2.2 0.2

60 100 39175 22800 33 163 30.57 19 5.7 0.017 gr/dscf @ 10% O2 3 0 4.5 unspecifi60 101 14927 7222.1 28.75 307.2 29.55 17.7 7.4 0.0009 gr/dscf @ 10% O2 3 1 0.069 0.0

60 94.3 16374 7664.5 30.85 308.4 29.54 18 7.3 0.0005 gr/dscf @ 10% O2 3 2 0.046 0.0

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐DetectRuns

Average_Outlet(lb/hr)

Average_(lb/produ

60 98.7 23916 11300 29.45 342.9 30.44 17.2 7.2 0.0006 gr/dscf @ 10% O2 3 0 0.071 0.0

60 98 26069 12038 31.99 331.1 30.44 17.4 6.9 0.001 gr/dscf @ 10% O2 3 0 0.132 0.0

60 100 40810 18160 31.98 351.9 30.1 17 7.5 0.0008 gr/dscf @ 10% O2 3 0 0.161 0.0

60 102.3 40802 17824 35.25 326.9 30.1 16.8 7.8 0.001 gr/dscf @ 10% O2 3 0 0.178 0.0

60 96.3 28119 13194 27.27 367.7 30.29 19.4 6.7 0.0001 gr/dscf @ 10% O2 3 2 0.014 0.0

60 103 30312 14407 26.63 366.3 30.3 19.5 6.7 0.0007 gr/dscf @ 10% O2 3 0 0.105 0.

72 96.3 15256 7121.3 27.75 351.7 29.72 15.3 8.82 0.0035 gr/dscf @ 10% O2 3 0 0.237 0.0

72 99.3 19290 9039.5 28.68 338.1 29.72 14.95 9.06 0.0053 gr/dscf @ 10% O2 3 0 0.454 0.0

60 92 33000 15000 28.1 392 30.49 15.3 8.7 0.00056 gr/dscf @ 10% O2 3 0 0.08 0.0

60 100 32500 14700 30.3 371 30.49 14.3 9.4 0.0014 gr/dscf @ 10% O2 3 0 0.21 0.0

68 99 20700 9090 27.1 414 29.89 18 11.7 0.00055 gr/dscf @ 10% O2 3 0 0.036 0.0

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐DetectRuns

Average_Outlet(lb/hr)

Average_(lb/produ

67 107 21500 9020 31.1 408 29.89 16 8 0.0011 gr/dscf @ 10% O2 3 0 0.1 0.0

60 102 28800 12000 31.7 411 30.16 17.3 7.4 0.00091 gr/dscf @ 10% O2 3 0 0.11 0.0

60 105 31400 12700 34.8 396 30.16 17.4 7.4 0.0014 gr/dscf @ 10% O2 3 0 0.18 0.0

60 92 30266 13942 27.86 374.9 30.19 17.7 7.5 0.0001 gr/dscf @ 10% O2 3 1 0.013 0.0

60 94 29825 13622 30.2 356.5 30.2 17.9 7.5 0.0005 gr/dscf @ 10% O2 3 0 0.07 0.0

60 101.7 31389 13941 29.52 375.7 29.85 18.1 7.2 0.0001 gr/dscf @ 10% O2 3 2 0.011 0.0

60.3 106 29599 12185 36.85 347.7 29.84 18 7.2 0.001 gr/dscf @ 10% O2 3 0 0.122 0.0

60 96 24524 11067 27.69 388.6 30.03 17.79 7.4 0.0007 gr/dscf @ 10% O2 3 0 0.088 0.0

60 94.7 25981 11463 30.8 370.5 30.03 17.55 7.64 0.0014 gr/dscf @ 10% O2 3 0 0.177 0.0

60 103.7 16862 7589 28.17 386.2 30.05 18.29 7.32 0.0002 gr/dscf @ 10% O2 3 2 0.018 0.0

60 104 22585 10014 30.76 368.2 30.06 18.23 7.29 0.0011 gr/dscf @ 10% O2 3 0 0.119 0.0

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

105.EU455105.EU455105.EU455105.EU455107.11‐P14

107.11‐P14

109.LK1109.LK1114.U800114.U800127.LK1127.LK1127.LK1127.LK2127.LK2127.LK2148.009148.009148.009156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5162.372A178.09P037178.09P037178.09P037

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐DetectRuns

Average_Outlet(lb/hr)

Average_(lb/produ

68.3 95.3 60570 34494 17.08 297.33 29.50 8.79 13.81 0.021 gr/dscf @ 10% O2 3 0 4.23 unspecifi

64 99.7 52505 29133 21.7 288.51 30.06 9.25 12.95 0.0014 gr/dscf @ 10% O2 3 0 0.26 unspecifi

63.7 99.7 48572 25778 22.65 298.14 29.50 10.53 11.93 0.0023 gr/dscf @ 10% O2 3 0 0.37 unspecifi

69.3 95.3 46766 26088 20.75 281.48 29.54 11.07 12 0.0024 gr/dscf @ 10% O2 3 0 0.45 unspecifi

60 98.8 21000 9305 28.6 379.6 29.54 23.7 3.8 0.0029 gr/dscf @ 10% O2 3 0 0.367 

60 100.2 21689 9735 30.9 346.4 29.71 25.37 3.33 0.0046 gr/dscf @ 10% O2 3 0 0.619 

72 103.4 29639 12974 31.60 367.8 30.04 21.83 4.47 0.0066 gr/dscf @ 10% O2 3 0 1.1 

60 98.1 55729 24492 26.53 419.1 29.8 24.8 4.2 0.0049 gr/dscf @ 10% O2 3 0 1.54 

63.3 105.5 48640 21578 30.13 365 29.69 19.33 6 0.0039 gr/dscf @ 10% O2 3 0 0.97 

62.3 105.5 60370 23753 32 448 29.77 14.5 4.6 0.0033 gr/dscf @ 10% O2 3 0 1.02 

63 102.6 35725 17376 21.6 392.3 29.98 12 9.2 0.011 gr/dscf @ 10% O2 3 0 1.743 

65.7 98 35047 16904 23.3 380.5 29.94 14.9 7.7 0.0109 gr/dscf @ 10% O2 3 0 1.919 

69.7 94 38361 21817 20 288.6 30.15 14.8 7.7 0.0079 gr/dscf @ 10% O2 3 0 1.795 

63.3 92.6 38319 18563 20.4 409.7 29.98 12.4 11.5 0.0061 gr/dscf @ 10% O2 3 0 0.834 

60 100.5 35436 17065 22.6 392.3 30.05 13 10.2 0.0138 gr/dscf @ 10% O2 3 0 1.982 

67 99.9 40980 22369 21.8 303.2 30.16 13.3 9.8 0.013 gr/dscf @ 10% O2 3 0 2.542 

69.7 96.2 33980 15078 30.8 368.7 30.09 23.09 2.75 0.00647 gr/dscf @ 10% O2 3 0 1.28 unspecifi

67 109.3 42303 18191 36.2 323.7 29.92 3.66 3.66 0.0061 gr/dscf @ 10% O2 3 0 1.5 unspecifi64 104.6 41292 16293 38.2 340.7 28.95 20.07 4.42 0.00588 gr/dscf @ 10% O2 3 0 1.25 unspecifi60 100.3 15463 7325 30.6 317 18.7 6.1 0.0003 gr/dscf @ 10% O2 2 0 0.02 

60 107.7 15565 7243 31.4 324 18.7 6.1 0.0001 gr/dscf @ 10% O2 2 0 0.01 

60 99.1 7345 3803 26 300 18 6.8 0.0014 gr/dscf @ 10% O2 2 0 0.06 

60 101.1 9704 4723 29.2 305 18 6.8 0.0011 gr/dscf @ 10% O2 2 0 0.06 

60 106.3 18876 8141 32.9 361 19.1 5.7 0.0317 gr/dscf @ 10% O2 2 0 3.09 

60 108.8 21175 9649 32.4 322 19.2 5.6 0.0039 gr/dscf @ 10% O2 2 0 0.45 

60 101.3 14239 6588 31.4 326 19.6 5.2 0.001 gr/dscf @ 10% O2 2 0 0.08 

60 110 20220 9163 32.8 326 19.6 5.2 0.0009 gr/dscf @ 10% O2 2 0 0.1 

60 101.3 50710 20483 29.2 456.33 29.6 22.5 4.9 0.0023 gr/dscf @ 10% O2 3 0 0.59 

64 96 54965 27220 39.8 170.5 29.43 16.9 5 0.057 gr/dscf @ 10% O2 3 0 18.88 

64 99 31548 18623 29.6 160.7 29.48 17.5 5.4 0.006 gr/dscf @ 10% O2 3 0 1.45 

64 96.8 41309 21583 37.7 169.8 29.96 17.8 6.2 0.024 gr/dscf @ 10% O2 3 0 5.8 

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

179.LK3196.SN‐02

200.007_10200.007_10200.007_10240.CA81606.LK4606.LK4606.LK4606.LK4606.LK4617.P22617.P22617.P22208228535.009208228535.009116.001117.P36119.EQT006133.14133.14135.004‐1135.004‐1138.001140.32140.32142.P6009142.P6025149.P001152.08155.LIME KILN

165.000019165.000002167.004LK

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐DetectRuns

Average_Outlet(lb/hr)

Average_(lb/produ

60 103.4 41554 22433 26.9 256.2 30.11 16 8.8 0.012 gr/dscf @ 10% O2 3 0 2.64 

62.7 98.6 57981 23874 35.7 369.4 30.11 19.97 4.67 0.0026 gr/dscf @ 10% O2 3 0 0.8 

60 103.2 66265 27964 32.5 376.7 29.69 23.8 3.6 0.0056 gr/dscf @ 10% O2 3 0 2.1 

60 99.9 68541 26013 32 469.8 29.43 20.5 4.4 0.0049 gr/dscf @ 10% O2 3 0 1.7 

60 100 65149 25104 28.5 495.6 29.2 20.6 5.4 0.006 gr/dscf @ 10% O2 3 0 1.82 

60 107 90131 54400 29.1 160 29.91 22.4 4.5 0.011 gr/dscf @ 10% O2 2 0 7.912 unspecifi

66.7 99.33 104362 40766 27.4 526 30.08 22.9 4.17 0.0173 gr/dscf @ 10% O2 3 0 9.31 

60 99.1 93594 36138 26 549.2 29.84 24 3.2 0.0103 gr/dscf @ 10% O2 3 0 5.2 

60 102.0 116388 41644 32.48 543 19.64 4.09 0.0093 gr/dscf @ 10% O2 3 0 5.42 

71.7 100.9 107786 39009 31.28 538 20.82 3.79 0.009 gr/dscf @ 10% O2 3 0 5.14 

60 99.4 109573 39503 30.74 559 20.38 3.79 0.0082 gr/dscf @ 10% O2 3 0 4.37 unspecifi

66 92.1 28405 11922 24.97 462.1 29.26 15 8.6 0.0046 gr/dscf @ 10% O2 3 0 0.533 

72.3 102.8 30169 12422 27.8 436.1 28.96 15 8.6 0.0061 gr/dscf @ 10% O2 3 0 0.513 unspecifi70.3 103 29099 12010 28.4 426.1 28.96 16 8.2 0.0032 gr/dscf @ 10% O2 3 0 0.375 61.7 102.3 68373 28627 26.6 467.7 21.33 5.27 0.004 gr/dscf @ 10% O2 3 0 1.4 unspecifi62.3 96.5 62186 25904 26.7 462.7 25.17 3.77 0.011 gr/dscf @ 10% O2 3 0 4 unspecifi

60 96 39393 25620 25.4 153 unspecified 20 6.5 0.046 gr/dscf @ 10% O2 3 0 13.36 1.2

60 100.8 13510 7585 30.3 155 unspecified 18.1 5.3 0.029426752 gr/dscf @ 10% O2 3 0 2.75 0.8

60 97.1 55400 27320 41.2 170 29.97 21 3.25 0.293126761 gr/dscf @ 10% O2 3 0 110.8 unspecifi72 100.33 33071 19594 31 159 unspecified 16.9 6.9 0.0335 gr/dscf @ 10% O2 1 0 5.634166667 unspecifi60 99.03 36640 22573 29 156 unspecified 16.8 6.1 0.0222 gr/dscf @ 10% O2 1 0 4.289166667 unspecifi60 98.2 48400 27200 35.5 161 29.8 22.6 4.9 0.034 gr/dscf @ 10% O2 3 0 11.6 0.9

60 101.8 47600 26600 36.5 161 29.62 20.6 5.1 0.037 gr/dscf @ 10% O2 3 0 12.2 0.9

60 95.8 31189.34454 27844.86667 15.77 133 30 5.27 11.67 0.0264 gr/dscf @ 10% O2 3 0 2.65 0.3

60 98.2 26679 12785 41.93333333 171 29.50333333 17 4.233333333 0.024 gr/dscf @ 10% O2 3 0 4 0.5

60 102.4 24863 12943 38.6 168.7 30.2 18.56666667 3.733333333 0.020666667 gr/dscf @ 10% O2 3 0 3.6 0.4

60 101 29191 16762 31.9 159 29.56 23.7 3.7 0.051 gr/dscf @ 10% O2 3 0 11.64 1.5

60 101 29826 17699 29.9 156 29.56 15.79 8.6 0.035 gr/dscf @ 10% O2 3 0 6.03 0.9

60 103.5 22300 12100 35 161 28.97 21.5 2.9 0.02929851 gr/dscf @ 10% O2 3 0 5 unspecifi60 100 27915 16095 33.5 159.8 29.83 16.1 7.9 0.062 gr/dscf @ 10% O2 3 0 10.2 0.

60 104.13 33623 27960 33.43 161 unspecified 10 8.93 0.0615 gr/dscf @ 10% O2 3 0 10.78 1.0

60 97 22959 16400 19 138 29.7 14.7 10.7 0.052 gr/dscf @ 10% O2 3 0 6.8 0.8

60 101 53640 32300 30 157 29.85 13.7 10.4 0.028 gr/dscf @ 10% O2 3 0 7.7 0.5

60 94 47144 24703 38.2 167 30.14076667 19.62 4.62 0.102478632 gr/dscf @ 10% O2 3 0 32.21 2.8

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

173.LK1174.G‐95

176.G‐5

177.EU0905181.14181.14181.1190.L601190.L600195.002196.SN‐09

205.008340.008525.EU17610.7610.7610.7610.7610.7610.8610.8610.8613.009613.009130.4130.5131.16131.16157.KILN188.001LK1, 002LK2,

003LK3206.G‐37

171.009171.010171.009

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐DetectRuns

Average_Outlet(lb/hr)

Average_(lb/produ

60 100 25342 14685 32.2 161 30.1 14.7 10.8 0.0533 gr/dscf @ 10% O2 3 0 6.21 0.7

60 97.5 35893 26306 17.4 136 29.98 16 9.1 0.055 gr/dscf @ 10% O2 3 0 13.3 0.9

60 98.39 27264 15417 34.02 162.78 30 23.87 3.57 0.064 gr/dscf @ 10% O2 3 0 13.4108 1.

60 94.5 43296 21942 36.7 169.4 28.55 22.4 3.6 0.0281 gr/dscf @ 10% O2 3 0 8.339 0.2

60 104 22432 12800 33 161 29.87 19.1 3.9 0.018 gr/dscf @ 10% O2 3 0 3 0.

60 104.6 23702 12500 37 166 29.73 15.3 4.8 0.051 gr/dscf @ 10% O2 3 0 8 0.7

60 94.3 28798 18300 16.2 154 30.06 16.2 7 0.022 gr/dscf @ 10% O2 3 0 4.4 0.3

60 102.3 46474 24426 37.8 170.33 30.15 14.12 6.87 0.016 gr/dscf @ 10% O2 3 0 4.38 unspecifi

60 96.7 45983 27917 28.7 159.33 29.92 15.1 6.99 0.037 gr/dscf @ 10% O2 3 0 11.2 0.4

60 92.6 37592 27809 16.5 136 29.89 17.4 8.9 0.017 gr/dscf @ 10% O2 3 0 4.4 0.

60 97 46388 25151 35.5 171.5 30.03 20.9 5.73 0.0538 gr/dscf @ 10% O2 4 0 16.6 1.3

60 100 26078 13400 38.7 170.6666667 unspecified 16.3 5.26 0.03 gr/dscf @ 10% O2 3 0 5 unspecifi

60 93 40324 24712 28.6 159 30.01 14.33333333 5.9 0.0856 gr/dscf @ 10% O2 3 0 24.62 0.4

60 98 49058 29506 30 158 29.91 23.03 4.5 0.024059756 gr/dscf @ 10% O2 3 0 9.2 0.2

60 102 24583 13878.1 33.5 163 unspecified 21.22 5.3 0.075 gr/dscf @ 10% O2 3 0 12.82 0.9

60 104.1 26508 14291.75 36.2 166.6 unspecified 21.31 4.91 0.089 gr/dscf @ 10% O2 3 0 16.03 

60 101 30143 15791.08333 37.3 166 unspecified 21.56 4.93 0.077 gr/dscf @ 10% O2 3 0 15.29 0.8

60 101 26550 15153.5 33.7 161.6 unspecified 22.02 5.15 0.073 gr/dscf @ 10% O2 3 0 13.78 

60 101 25303 14677.4 32.3 161.8 unspecified 21.26 5.32 0.073 gr/dscf @ 10% O2 3 0 13.16 

60 103.8 19551 10513.95 36.6 166 unspecified 20.3 5.4 0.066 gr/dscf @ 10% O2 3 0 8.44 0.6

60 107 21155 11196.88333 37.3 166.5 unspecified 21.5 4.86 0.062 gr/dscf @ 10% O2 3 0 8.73 

60 106.5 21992 11409.96667 38 168.3 unspecified 23.7 3.3 0.062 gr/dscf @ 10% O2 3 0 9.73 0.5

60 92 48185 28834 29.9 160 30.0026 19.57 4.51 0.0288 gr/dscf @ 10% O2 3 0 10.7 unspecifi60 97 53105 34481 25.4 152 30.1612 19.55 6.39 0.0317 gr/dscf @ 10% O2 3 0 12.48 unspecifi

64.00 102.30 21546 11084 38.90 168.7 29.98 13.08 7.54 0.033 gr/dscf @ 10% O2 3 0 3.77 

63.33 98.50 22709 13268 31.50 159.3 29.94 10.10 10.75 0.0318 gr/dscf @ 10% O2 3 0 3.37 

65.67 97.40 27800 14100 37.70 173.0 29.28 23.40 4.00 0.09 gr/dscf @ 10% O2 3 0 16.8 unspecifi65.00 95.60 20100 11800 29.00 178.0 29.93 20.10 5.80 0.093 gr/dscf @ 10% O2 3 0 13.1 unspecifi60.00 unspecified 18217 10428 unspecified 161.0 29.90 15.90 9.40 0.046 gr/dscf @ 10% O2 3 0 4.4 

60.00 101.09 34700 20806 30.24 157.3 29.91 16.30 6.50 0.069 gr/dscf @ 10% O2 3 0 16.06 

62.00 96.90 24303 14026 27.40 148.3 27.40 18.00 6.70 0.0417 gr/dscf @ 10% O2 3 0 6.52 unspecifi60.00 99.30 58102 30805 36.80 166.7 29.81 12.40 7.50 0.0322 gr/dscf @ 10% O2 3 0 10.44 1.3

60.00 101.00 37294 19086 38.70 169.1 29.77 12.70 7.20 0.0828 gr/dscf @ 10% O2 3 0 15.42 2.1

60.00 92.40 34779 18476 36.80 134.5 29.89 18.60 5.60 0.0194 gr/dscf @ 10% O2 3 0 4.3 

Test_data_memo_appendices.xlsx App B LK PM 
ate Matter

RTI+EUID100.115102.LK102.LK103.G‐165

105.EU455107.11‐P14

108.LK1108.LK1108.LK1111.G‐35

111.G‐35

114.U800114.U800120.M19120.M18124.004‐1126.LK127.LK2127.LK1131.18131.18131.18131.18132.21LK4136.EU 033137.512139.04143.6063145.001146.30146.6147.3147.55147.55148.003148.009150.CAU‐12

154.P30 ‐ Lime Kiln156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5

Suspect Data Exclude Comment Data analysis notes Multi‐stack sums

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

Yes Run 1 stopped due to storm M 100.115.PM 0.7 0.0931 

102.LK .PM separate stacks 

102.LK .PM separate stacks 0.147 0.010652174 

103.G‐165.PM 16 0.9368 

Two lime kilns vent through the same ESP. Only

lime kiln 3 was operating during the test. 105.EU455.PM 1.96 0.2254 

107.11‐P14.PM 0.32 0.0204 

108.LK1.PM

Separate conditions: Performance

Engineering Test cond. I (Scrubber P‐drop =

8 in. H2O) 14.1 1.3783 

108.LK1.PM

Separate conditions: Performance

Engineering Test cond. II (Scrubber P‐drop= 9.2 in. H2O) 10.1 0.9883 

108.LK1.PM

different dates w/in same year (MACT

compliance test) 5.78 0.5740 

111.G‐35.PM Separate conditions: Cond 1 = fuel oil 3.579 0.2834 

111.G‐35.PM Separate conditions: Cond 2 = gas 1.622 0.1301 114.U800.PM Separate conditions: gas 0.3 0.0180 114.U800.PM Separate conditions: oil 0.5 0.0303 120.M19.PM 5.8056 0.7698 120.M18.PM 1.21836 0.1491 124.004‐1.PM 10.451 0.2708 126.LK.PM 0.292 0.0190 127.LK2.PM different years 0.638 0.0890 

127.LK1.PM different years 0.314 0.0449 

131.18.PM different dates w/in same year 6.5 0.7100 

131.18.PM different dates w/in same year 5.1 0.7100 

131.18.PM different dates w/in same year 13.6 1.2800 

131.18.PM different dates w/in same year 10.8 1.5800 132.21LK4.PM 22.066 0.9194 136.EU 033.PM 10 0.5900 

Yes

Second Run PM Conc value is 2.5 times then First

and Third Run M 137.512.PM 0.44 0.0506 

139.04.PM 13.3 143.6063.PM 0.94 0.0475 145.001.PM 10.3 unspecified 146.30.PM 2.969 0.1116 146.6.PM 6.072 unspecified 147.3.PM 7.45 unspecified 147.55.PM different dates w/in same year 7.94 0.4311 

147.55.PM different dates w/in same year 4.15 0.2264 148.003.PM 11.2 0.8161 

Yes

Failed isokinetics<90% 148.009.PM different years 3.01 unspecified 

150.CAU‐12.PM 5.4 unspecified 154.P30 ‐ Lime Kiln.PM 0.05 0.0039 

M

Isokinetics exceed110% slightly; only 2

runs 156.LK5.PM

separate stacks and different dates w/in

same year 

M

Isokinetics exceed110% slightly; only 2

runs 156.LK5.PM

separate stacks and different dates w/in

same year 0.6 0.050847458 

M only 2 runs 156.LK5.PM

separate stacks and different dates w/in

same year 

M only 2 runs 156.LK5.PM

separate stacks and different dates w/in

same year 0.25 0.022644928 

M only 2 runs 156.LK5.PM

separate stacks and different dates w/in

same year 

M only 2 runs 156.LK5.PM

separate stacks and different dates w/in

same year 0.99 0.107608696 

M only 2 runs 156.LK5.PM

separate stacks and different dates w/in

same year 

M only 2 runs 156.LK5.PM

separate stacks and different dates w/in

same year 0.46 0.058227848 

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

156.145000156.145000156.145000156.145000156.143100156.143100156.143100159.F4162.372A162.371A163.LK1501163.LK2502164.P12166.LK01166.LK02172.LK03172.LK03174.G‐18

175.LK2A175.LK2A175.LK1A175.LK1A175.LK1A178.09P037178.09P037179.LK3180.L001180.L002184.LK2184.LK2184.LK1184.LK1185.07

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

156.145000.PM different dates w/in same year 2.94 0.3920 

156.145000.PM different dates w/in same year 1.9 0.2533 

156.145000.PM different dates w/in same year 1.7 0.2146 

156.145000.PM different dates w/in same year 1.98 0.2377 156.143100.PM different dates w/in same year 1.85 0.3551 

156.143100.PM different dates w/in same year 2.29 0.3137 156.143100.PM different dates w/in same year 2.56 0.4324 

159.F4.PM 3.952 unspecified 162.372A.PM different years 3 0.2063 

162.371A.PM 14 1.4538 163.LK1501.PM 10.7 0.7555 163.LK2502.PM 13.9 0.9553 164.P12.PM 9.02 1.8675 

emission factor seems too high 166.LK01.PM 32 2.9058 

166.LK02.PM 8.7 0.7043 172.LK03.PM Separate conditions: oil 7.6 0.6450 172.LK03.PM Separate conditions: gas 9.9 0.8584 174.G‐18.PM 2.5 0.0804 175.LK2A.PM

Separate conditions: No. 2 Lime Kiln ‐ 

Shutdown 8.3 0.5061 

175.LK2A.PM

Separate conditions: No. 2 Lime Kiln ‐ 

Startup 2.6 0.1818 

Yes Tested during shutdown

Tested during shutdown. %CO2 stadily decliningduring shutdown; based on 2 runs (3rd was

negative); %O2 steadily increased across 3 runs. 175.LK1A.PM

Separate conditions: No. 1 Lime Kiln ‐ 

Shutdown 0.99 0.3394 

175.LK1A.PM

Separate conditions: No. 1 Lime Kiln ‐ 

Startup 1.9 0.4629 

175.LK1A.PM

different dates w/in same year (No. 1 Lime

Kiln) 1.6 0.1738 

178.09P037.PM Separate conditions: gas 1.9 0.1348 178.09P037.PM Separate conditions: oil 2 0.1418 

179.LK3.PM different years 4.1 0.1933 180.L001.PM 8.9 1.7713 180.L002.PM 7.7 1.5321 

Run Number 2 was invalid due to plan operational

problems M 184.LK2.PM

Separate conditions: No. 2 Lime Kiln ‐ 

Condition I (gas) 1.033333333 0.0953 

Yes

Each RunConcentration variedby two to three times 184.LK2.PM

Separate conditions: No. 2 Lime Kiln ‐ 

Condition II (pet coke and gas) 0.52 0.0475 

184.LK1.PM CaO Production 5.81 0.4572 

184.LK1.PM

Separate conditions: No. 1 Lime Kiln ‐ Low

CaO Production 4.55 0.5629 

M Isokinetics unspecified 185.07.PM different dates w/in same year 2.20332 unspecified 

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

185.07185.07185.07186.LK189.SN25189.SN25196.SN‐02

197.1198.004199.011200.007_10201.SR0003202.Lime Kiln EU340

203.LKScr203.LKScr203.LKScr203.LKScr206.G‐38

207.103A207.103A207.103A207.103A226.LK1226.LK2240.CA81242.AA‐013243.LG07243.LG07531.LK7600.G0908600.G0905600.G0903600.G0905606.LK4615.21615.21169.03617.P22126.LK132.21LK4132.21LK4132.21LK4132.21LK4132.21LK4132.21LK4132.21LK4

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

M Isokinetics unspecified 185.07.PM different dates w/in same year 2.239812 unspecified 

M Isokinetics unspecified 185.07.PM different dates w/in same year 1.27521 unspecified 

M Isokinetics unspecified 185.07.PM different dates w/in same year 2.060415 unspecified 

186.LK.PM 5.56 0.2648 189.SN25.PM different dates w/in same year 23.7 unspecified 

189.SN25.PM different dates w/in same year 5.67 unspecified 196.SN‐02.PM different years 1.56 0.1006 

197.1.PM 3.68 0.0548 198.004.PM 14.82 1.0713 199.011.PM 2.9 0.2179 200.007_10.PM 0.67 unspecified 201.SR0003.PM 14.47 1.0202 202.Lime Kiln EU340.PM 5.56 0.7372 203.LKScr.PM different dates w/in same year 6.94 unspecified 

203.LKScr.PM different dates w/in same year 5.97 unspecified 

203.LKScr.PM different dates w/in same year 6.947 unspecified 203.LKScr.PM different dates w/in same year 6 unspecified 206.G‐38.PM 8.571 unspecified 207.103A.PM

Separate conditions: Lime Kiln ‐ Normal

Condition 3.27 1.1354 

207.103A.PM

Separate conditions: Lime Kiln ‐Condition I

(scrubber p‐drop =18 in H2O, recirc = 400gpm) 3.43 1.1910 

207.103A.PM

Separate conditions: Lime Kiln ‐ Condition

II (scrubber p‐drop =20 in H2O, recirc = 300

gpm) 4.15 1.4410 

207.103A.PM

Separate conditions: Lime Kiln ‐ Condition

III (scrubber p‐drop =18 in H2O, recirc =

295 gpm) 4.96 1.7222 

226.LK1.PM 13.69 unspecified 226.LK2.PM 2.42 unspecified 240.CA81.PM different years 0.8 0.0290 242.AA‐013.PM 2.312 0.1284 

243.LG07.PM

Separate conditions: No. 5 Lime Kiln ‐ 

Condition I (SCBR/ESP) 1.75 unspecified 

243.LG07.PM

Separate conditions: No. 5 Lime Kiln ‐ 

Condition II (SCBR only) 12.88 unspecified 

531.LK7.PM 0.96 0.0369 600.G0908.PM 3.1 0.2600 600.G0905.PM different years 9.2 0.7610 600.G0903.PM 13.68 1.7181 600.G0905.PM different years 13.3 1.1010 

606.LK4.PM 20 0.7380 615.21.PM Separate methods: Lime Kiln ‐ Front Half 3.88 0.3887 

615.21.PM Separate methods: Lime Kiln ‐  ODEQ 5 4.31 0.4317 

yes

PM for run 3 approximately 4x runs 1 and 2‐‐

testers believe due to contamination of probe. If

omit run 3, then avg concentration from runs 1‐2

is 0.045 gr/dscf at 8% O2.

Desired production units unavailable for emission

factor development. 169.03.PM 23.34 

617.P22.PM 0.5484 0.0866 126.LK.PM 0.923333333 0.1094 

132.21LK4.PM different years 0.477 0.0189 

132.21LK4.PM different years 0.727 0.0327 

132.21LK4.PM different years 1.447 0.0622 

132.21LK4.PM different years 1.448 0.0603 

Report only has list of all sources' averages. 132.21LK4.PM different years 4.786 0.1919 

Report only has list of all sources' averages. 132.21LK4.PM different years 0.898 

132.21LK4.PM different years 3.889 0.0562 

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

132.21LK4132.21LK4136.EU 033136.EU 033136.EU 033136.EU 033136.EU 033137.511137.511137.512137.512137.512137.511137.512137.512146.30154.P30 ‐ Lime Kiln154.P30 ‐ Lime Kiln154.P30 ‐ Lime Kiln154.P30 ‐ Lime Kiln186.LK186.LK186.LK186.LK243.LG07243.LG07105.EU455121.000011121.000011102.LK102.LK

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

Production.Report included

only summarysheets, Order Magnitude Summary sheets only (not full report) 132.21LK4.PM different years 10.13 0.4509 

132.21LK4.PM different years 4.62 0.1886 

136.EU 033.PM different years 5.01 0.3287 

136.EU 033.PM different years 10.62333333 0.5858 

136.EU 033.PM different years 6.93 0.3822 

136.EU 033.PM different years 6.3 0.3619 

136.EU 033.PM different years 8.625 0.5010 

137.511.PM different years 0.21 0.0246 

137.511.PM different years 0.093 0.0118 

Combination of 2 run type: 16 point traverse and

24 point traverse. Values are their mathematical

average. 137.512.PM

Separate conditions (tested ESP only);different dates w/in same year 0.25 0.0287 

Control Equipment: Environmental Elements ESPand Amarex SO2 scrubber. The scrubber was not

used during testing because NCGs were not routed

to the kiln. 137.512.PM

Separate conditions (tested ESP only);different dates w/in same year 0.28 0.0322 

137.512.PM

Separate conditions (tested ESP only);different years 0.099 0.0125 

137.511.PM different years 0.42 0.0467 

Control Equipment: Environmental Elements ESPand Amarex SO2 scrubber. 137.512.PM Separate conditions: Tested with ESP/SCBR 0.133 0.0142 

Control Equipment: Environmental Elements ESP;no indication SO2 scrubber in use. Inlet and outletwere not tested at the exact same time. 137.512.PM

Separate conditions: Tested ESP only (inlet

and outlet) 0.191 0.0205 

Operational data was reserved/unspecified 146.30.PM 1.458 

Measurements at > 90% capacity with scrubber

shut down. Desired production units unavailablefor emission factor development. 154.P30 ‐ Lime Kiln.PM

Separate condition: only ESP tested.

different years 0.863333333 

Some indication of "scrubber data" but report

does not mention ESP. 154.P30 ‐ Lime Kiln.PM different years 0.321 0.0247 

154.P30 ‐ Lime Kiln.PM different years 0.18 0.0154 154.P30 ‐ Lime Kiln.PM different years 0.059 0.0046 

Not sure of production units for what is listed as

Caus.Kiln TPD ‐ may be TPD CaO or may be lime

mud or other? Given magnitude, assumed tons

CaO/hr 186.LK.PM different years 4.67 0.2144 

186.LK.PM different years 10.8 0.6201 

186.LK.PM different years 21 1.0608 

Production data were not in correct units for

emission factor development. 186.LK.PM different years 5.32 

Production data were not in correct units for

emission factor development. 243.LG07.PM different years 3.2 Production data were not in correct units for

emission factor development. 243.LG07.PM different years 1.23 

M ODEQ M5 test

No. 3 Lime Kiln operating and No. 2 Lime Kiln

down during tests. Both kilns vent through same

ESP. 105.EU455.PM 0.98 0.0482 

121.000011.PM different years 2.2 0.2146 

Production units not ton CaO 121.000011.PM different years 4.5 

Yes

Run 3 was reported as 0 emissions. Final weight of

filter was less than tare weight so emissionsreported as 0 for these runs. Yes

See CauseSuspect.

Zero‐runs loweredoverall emissions.

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn from

each stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). Run 3 was reported as 0 emissions. 102.LK .PM 0.069 0.0058 

Yes

Runs 2 and 3 were reported a 0 emissions. Finalweight of filter was less than tare weight so

emissions reported as 0 for these runs. Yes

See CauseSuspect.

Zero‐runs loweredoverall emissions.

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). Runs 2 and 3 were reported a 0 emissions. 102.LK .PM 0.046 0.0039 

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn from

each stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) 0.203 0.015496183 Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) 

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn from

each stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) 0.339 0.023363198 

Yes

Runs 1 and 2 were reported as 0 emissions. Final

weight of filter was less than tare weight so

emissions reported as 0 for these runs. Yes

See CauseSuspect.

Zero‐runs lowered

overall emissions.

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). Runs 1 and 2 were reported as 0 emissions. 102.LK .PM 0.014 0.0011 

Yes

Excluded other stack

because of 0

emissions

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM 0.105 0.0080 

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) 

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) 0.691 0.065250236 

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) 

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) 0.29 0.020567376 Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) 

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK102.LK

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn from

each stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) 0.136 0.009127517 Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) 0.29 0.020237264 

Yes

Run 1 was reported as 0 emissions. Final weight

of filter was less than tare weight so emissions

reported as 0 for these runs. Yes

See CauseSuspect.

Zero‐runs lowered

overall emissions.

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). Run 1 was reported as 0 emissions. 102.LK .PM 0.013 0.0010 

Yes

Excluded other stack

because of 0

emissions

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM 0.07 0.0053 

Yes

Runs 2 and 3 were reported as 0 emissions. Final

weight of filter was less than tare weight so

emissions reported as 0 for these runs. Yes

See CauseSuspect.

Zero‐runs loweredoverall emissions.

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn from

each stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). Runs 2 and 3 were reported as 0 emissions. 102.LK .PM 0.011 0.0008 

Yes

Excluded other stack

because of 0

emissions

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn from

each stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM 0.122 0.0087 

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM Separate stacks (see note) 0.265 0.019133574 

Yes

Runs 1 and 3 were reported as 0 emissions. Final

weight of filter was less than tare weight so

emissions reported as 0 for these runs. Yes

See CauseSuspect.

Zero‐runs loweredoverall emissions.

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn from

each stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). Runs 1 and 3 were reported as 0 emissions. 102.LK .PM 0.018 0.0013 

Yes

Excluded other stack

because of 0

emissions

Separate stacks. This lime kiln has a 2‐chamber ESP

with each chamber exhausting to its own stack. A

portion of the ESP exhaust gas is withdrawn fromeach stack for use by SMI (a PCC plant). This

lowers the stack gas flow and reduces pollutant

mass emissions (though concentration remains the

same). 102.LK .PM 0.119 0.0085 

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

105.EU455105.EU455105.EU455105.EU455107.11‐P14

107.11‐P14

109.LK1109.LK1114.U800114.U800127.LK1127.LK1127.LK1127.LK2127.LK2127.LK2148.009148.009148.009156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5156.LK5162.372A178.09P037178.09P037178.09P037

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

M ODEQ M5 test

The lime kiln ESP is used for 2 lime kilns (no. 2 and

3). The no. 2 lime kiln was down during this test.

EF not provided; chose not to use calculated

production rate for EF development. 105.EU455.PM different dates within same year 4.23 unspecified 

M ODEQ M5 test

The lime kiln ESP is used for 2 lime kilns (no. 2 and

3). The no. 2 lime kiln was down during this test.

EF not provided; chose not to use calculated

production rate for EF development. 105.EU455.PM different dates within same year 0.26 unspecified 

M ODEQ M5 test

The lime kiln ESP is used for 2 lime kilns (no. 2 and

3). The no. 2 lime kiln was down during this test.EF not provided; chose not to use calculated

production rate for EF development. 105.EU455.PM different dates within same year 0.37 unspecified 

M ODEQ M5 test

The lime kiln ESP is used for 2 lime kilns (no. 2 and

3). The no. 2 lime kiln was down during this test.

EF not provided; chose not to use calculated

production rate for EF development. 105.EU455.PM different dates within same year 0.45 unspecified 

107.11‐P14.PM different years 0.367 0.0232 

107.11‐P14.PM different years 0.619 0.0409 

109.LK1.PM different years 1.1 0.0820 

109.LK1.PM different years 1.54 0.1173 

114.U800.PM Separate conditions: No. 6 fuel oil 0.97 0.0598 114.U800.PM Separate conditions: Natural Gas 1.02 0.0629 

127.LK1.PM different years 1.743 0.2583 

127.LK1.PM different years 1.919 0.3278 

Consistent with other tested production rates forthis kiln, production values were taken to be daily

rates not hourly rates as noted in the report.

Recalculated emission factor. 127.LK1.PM different years 1.795 0.2502 

127.LK2.PM different years 0.834 0.1230 

127.LK2.PM different years 1.982 0.3318 

Consistent with other tested production rates forthis kiln, production values were taken to be daily

rates not hourly rates as noted in the report.

Recalculated emission factor. 127.LK2.PM different years 2.542 0.3783 

148.009.PM different years 1.28 unspecified 

148.009.PM different years 1.5 unspecified 

The No. 2 Lime Kiln test had one sampling run (Run1) were the sampling rate was found to be 13%above the ideal isokinetic sampling rate. 148.009.PM different years 1.25 unspecified 

Test reports are 2 runs for the north stack and 2

runs for the south stack Separate stacks (North and South) 156.LK5.PM Separate stacks 

Test reports are 2 runs for the north stack and 2

runs for the south stack Separate stacks (North and South) 156.LK5.PM Separate stacks 0.03 0.004114286 

Test reports are 2 runs for the north stack and 2

runs for the south stack Separate stacks (North and South) 156.LK5.PM Separate stacks 

Test reports are 2 runs for the north stack and 2

runs for the south stack Separate stacks (North and South) 156.LK5.PM Separate stacks 0.12 0.023225806 

Test reports are 2 runs for the north stack and 2

runs for the south stack Separate stacks (North and South) 156.LK5.PM Separate stacks 

Test reports are 2 runs for the north stack and 2

runs for the south stack. Separate stacks (North and South) 156.LK5.PM Separate stacks 3.54 0.326769231 

Test reports are 2 runs for the north stack and 2

runs for the south stack Separate stacks (North and South) 156.LK5.PM Separate stacks 

Test reports are 2 runs for the north stack and 2

runs for the south stack Separate stacks (North and South) 156.LK5.PM Separate stacks 0.18 0.018 

Lime production was 101% of the maximum

sustained rating of 337 tons CaO per Day. 162.372A.PM different years 0.59 0.0416 

Separate conditions (normal load). The Lime Kiln

normal condition results were below the MACT II

limit but exceeded the source lb/hr limit. Re‐test

data were used for MACT II compliance purposes 178.09P037.PM Separate conditions: 18.6 ton CaO/hr 18.88 1.0136 

Separate conditions (low load) 178.09P037.PM Separate conditions: 2.9 ton CaO/hr 1.45 0.4870 

Retest (normal load) 178.09P037.PM 5.8 0.3222 

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

179.LK3196.SN‐02

200.007_10200.007_10200.007_10240.CA81606.LK4606.LK4606.LK4606.LK4606.LK4617.P22617.P22617.P22208228535.009208228535.009116.001117.P36119.EQT006133.14133.14135.004‐1135.004‐1138.001140.32140.32142.P6009142.P6025149.P001152.08155.LIME KILN

165.000019165.000002167.004LK

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

179.LK3.PM different years 2.64 0.1734 

196.SN‐02.PM different years 0.8 0.0639 200.007_10.PM different years 2.1 0.1291 200.007_10.PM different years 1.7 0.1000 200.007_10.PM different years 1.82 0.1182 

Only 2 run reported Only 2 run reported 240.CA81.PM different years 7.912 unspecified 

606.LK4.PM different years 9.31 0.3448 

606.LK4.PM different years 5.2 0.1907 

Condition 1 ‐ Three fields, normal power levels 606.LK4.PM Separate conditions; different years 5.42 0.2001 

Condition 2 ‐ Three fields, reduced power levels 606.LK4.PM Separate conditions; different years 5.14 0.1898 

Condition 3 ‐ Two fields on ‐ One field off ‐ normal

power levels 606.LK4.PM Separate conditions; different years 4.37 unspecified 

617.P22.PM different years 0.533 0.0882 

617.P22.PM different years 0.513 unspecified 

617.P22.PM different years 0.375 0.0599 

Fuel used was handwritten as CTO. Mud flow was

also handwritten in report. 208228535.009.PM different years 1.4 unspecified Mud flow was handwritten in operational data

section. 208228535.009.PM different years 4 unspecified 

116.001.PM 13.36 1.2846 117.P36.PM 2.75 0.8765 

No production data to calculate EF 119.EQT006.PM 110.8 unspecified 

Only 2‐pgsummaryprovided fromthis in‐housetest; data base

indicated M5was "modifiedper AOP" Yes

ICR response indicates

this was a single 1‐hr

test.

No production data to calculate EF. ICR responseindicates this was a single 1‐hr test. 133.14.PM 5.634166667 unspecified 

Only 2‐pg

summaryprovided fromthis in‐housetest; data baseindicated M5

was "modifiedper AOP" Yes

ICR response indicatesthis was a single 1‐hr

test.

No production data to calculate EF. ICR response

indicates this was a single 1‐hr test. 133.14.PM 4.289166667 unspecified 

Condition 1: Scrubber P‐drop = 25.1 in H2O 135.004‐1.PM Separate conditions 11.6 0.9128 

Condition 2: Scrubber P‐drop = 22.0 in H2O 135.004‐1.PM Separate conditions 12.2 0.9065 

Yes 138.001.PM 2.65 0.3638 

M ODEQ M5 test 140.32.PM different years 4 0.5479 

140.32.PM different years 3.6 0.4286 142.P6009.PM 11.64 1.5792 142.P6025.PM 6.03 0.9812 

No production data to calculate EF. 149.P001.PM 5 unspecified 

mod. M5 (Texas ACB Procedure ‐ cyclonic flow) 152.08.PM 10.2 0.6695 

155.LIME KILN.PM 10.78 1.0267 165.000019.PM 6.8 0.8831 165.000002.PM 7.7 0.5066 

PM bubble mill 167.004LK.PM 32.21 2.8254 

Test_data_memo_appendices.xlsx App B LK PM 
RTI+EUID

173.LK1174.G‐95

176.G‐5

177.EU0905181.14181.14181.1190.L601190.L600195.002196.SN‐09

205.008340.008525.EU17610.7610.7610.7610.7610.7610.8610.8610.8613.009613.009130.4130.5131.16131.16157.KILN188.001LK1, 002LK2,

003LK3206.G‐37

171.009171.010171.009

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

Found actual flow rate, pressure, and more precisedry standard flow rate in data summary table

further down in report. 173.LK1.PM 6.21 0.7306 

174.G‐95.PM 13.3 0.9283 

176.G‐5.PM 13.4108 1.4673 177.EU0905.PM 8.339 0.2969 

Without NCGs 181.14.PM Separate conditions: Without NCGs 3 0.2586 

With NCGs 181.14.PM Separate conditions: With NCGs 8 0.7207 

181.1.PM 4.4 0.3607 

Found lime production rate in test results table in

appendix. 190.L601.PM 4.38 unspecified 

190.L600.PM 11.2 0.4014 

yes

1‐page summary only (appendices were not

available for PM)

ME DEP summary shows that PM and NOx test

were conducted on same date and had same flow

rate, which indicates that both tests were

conducted at same time, with same parameters.

We may want to ask mill for appendices to PM test

(mill appears to have attached link to PM testappendices, but not actual appendices

themselves). 195.002.PM 4.4 0.2312 

196.SN‐09.PM 16.6 1.3251 

No lime production data to calculate EF, but havelime mud input and pulp production data. 205.008.PM 5 unspecified PM bubble mill 340.008.PM 24.62 0.4875 

525.EU17.PM 9.2 0.2272 

Separate conditions: production = 14 TPH; No. 6

Oil runs 1 & 2, Waste Oil run 3. 610.7.PM Separate conditons 12.82 0.9157 

Separate conditions: production = 16 TPH; WasteOil all 3 runs. 610.7.PM Separate conditons 16.03 1.0019 Separate conditions: production = 17 TPH; WasteOil all 3 runs. 610.7.PM Separate conditons 15.29 0.8994 Separate conditions: production = 16 TPH. WasteOil all 3 runs. According to ICR response, waste oil

is primary fuel, so 0.13 gr/dscf LK standard would

apply under current NSPS. PM bubble mill. 610.7.PM Separate conditons 13.78 0.8613 

Separate conditions: production = 14 TPH. WasteOil all 3 runs. 610.7.PM Separate conditons 13.16 0.9400 Separate conditions: production = 14 TPH; WasteOil all 3 runs. 610.8.PM Separate conditons 8.44 0.6029 Separate conditions: production = 16 TPH; Waste

Oil run 1, No. 6 Oil runs 2 & 3. 610.8.PM Separate conditons 8.73 0.5456 

Separate conditions: production = 17 TPH; WasteOil all 3 runs. 610.8.PM Separate conditons 9.73 0.5724 

Separate conditions: natural gas only, without

petcoke. No production data to calculate EF. 613.009.PM Separate conditons 10.7 unspecified 

Separate conditions: natural gas co‐fired withpetcoke. No production data to calculate EF. 613.009.PM Separate conditons 12.48 unspecified 

130.4.PM 3.77 0.6253 130.5.PM 3.37 0.5859 131.16.PM

Tested on 2 different days; report did not

specify why (unclear of separate

conditions) 16.8 unspecified 

131.16.PM

Tested on 2 different days; report did not

specify why (unclear of separate

conditions) 13.1 unspecified 

157.KILN.PM 4.4 1.1852 

All three lime kilns' data were combined into onereport. Separate values for each kiln were not

provided. 188.001LK1, 002LK2, 003LK3.PM 3 kilns combined 16.06 1.3280 

206.G‐37.PM 6.52 unspecified 171.009.PM different dates 10.44 1.3588 

171.010.PM 15.42 2.1208 171.009.PM different dates 4.3 0.5488 

Test_data_memo_appendices.xlsx App B LK PM 
Appendix C

Particulate Matter Emissions Data for Smelt Dissolving Tanks 
Appendix C: Pulp and Paper Emissions Test Data Spreadsheet for NSPS Review ‐ SDT Filterable Particulate Matter

General InformationTest report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

Generic ProcessType

2010_PM_Lime_Kiln,_No_4_Rec_and_No_4_Smelt.pdf 105 NEI45182 EU445D 105.EU445D

105‐‐CD 456‐110, CD445‐480, and

CD 445‐447 SCBR Kraft, Secondary SDT (Kraft)

SECTION 2.pdf 107 NEI47074 09‐P2 107.09‐P2 107‐‐09‐P2 SCBR Kraft SDT (Kraft)

NEI32869 PR 2008016 OCT 2008.pdf 109 NEI32869A SDT3 109.SDT3 109‐‐ST3SBR SCBR Kraft SDT (Kraft)

NEI32869 PR 2008016 OCT 2008.pdf 109 NEI32869A SDT4 109.SDT4 109‐‐ST4SBR SCBR Kraft SDT (Kraft)Project #2006009 ‐ June, 2006.pdf 109 NEI32869A SDT3 109.SDT3 109‐‐RB3ESP, ST3SBR SCBR Kraft SDT (Kraft)

NEI45206_P&P Survey_2‐2011 Recovery Furnace &

Smelt Dissolvi.pdf 111 NEI45206 G‐127 111.G‐127 111‐‐STWS and ES 455‐001 SCBR NA Kraft SDT (Kraft)

P_P_ICR Part III_RTI166_InternationalPaper‐GeorgetownMill_NEI_41314_LK1and2_RB1and2_ST1and2_PM_July 2009.PDF 166 NEI41314 ST01 166.ST01 166‐‐ST1 Scrubber SCBR Kraft SDT (Kraft)P_P_ICR Part III_RTI166_InternationalPaper‐GeorgetownMill_NEI_41314_LK1and2_RB1and2_ST1and2_PM_July 2009.PDF 166 NEI41314 ST02 166.ST02 166‐‐ST2 Scrubber SCBR Kraft SDT (Kraft)P_P ICR Part III_RTI174_International Paper‐

Riegelwood Mill_.pdf 174 NEI40247 G‐63B 174.G‐63B

174‐‐G‐18 ESP/G‐18 SCRUB, G‐

63B SCRUB, G‐63C EWSCRUB SCBR Kraft SDT (Kraft) P

_

P ICR Part III

_

RTI174

_

International Paper

Riegelwood Mill_.pdf 174 NEI40247 G‐63C 174.G‐63C 174‐‐G‐63C EWSCRUB SCBR Kraft SDT (Kraft)

P_P ICR Part III_RTI174_International Paper‐Riegelwood Mill_.pdf 174 NEI40247 G‐63C 174.G‐63C 174‐‐G‐63C EWSCRUB SCBR Kraft SDT (Kraft)

P_P ICR Part III_RTI174_International Paper‐Riegelwood M (1).pdf 174 NEI40247 G‐63B 174.G‐63B

174‐‐G‐18 ESP/G‐18 SCRUB, G‐32ESP, G‐92 ESP, G‐63B SCRUB, G‐

63C EWSCRUB SCBR Kraft SDT (Kraft)

P_P ICR Part III_RTI174_International Paper‐

Riegelwood M (1).pdf 174 NEI40247 G‐63C 174.G‐63C 174‐‐G‐63C EWSCRUB SCBR Kraft SDT (Kraft)

P_P ICR Part III_RTI174_International Paper‐

Riegelwood M (1).pdf 174 NEI40247 G‐63C 174.G‐63C 174‐‐G‐63C EWSCRUB SCBR Kraft SDT (Kraft)

SDTV No. 1 2010 Update 124 NEI8278 020 124.020 124‐‐sdtsbr020 SCBR Kraft SDT (Kraft)

0910‐29 SDTV No. 2 124 NEI8278 021 124.021 124‐‐sdtsbr021 SCBR Kraft SDT (Kraft)RecoveryBoilerSmeltTank#2LimeKiln_EmmisionsTestReport_2005.pdf 340 NEI46852 007 340.007 340‐‐SDTVS SCBR Kraft, Secondary SDT (Kraft)RecoveryBoilerSmeltTank#2LimeKiln_EmmisionsTestReport_2004 340 NEI46852 007 340.007 340‐‐SDTVS SCBR Kraft, Secondary SDT (Kraft)NEI40686_RTI100_DomtarJohnsonburgMill_Smelt

DissolvingTank Test_August2001.pdf 100 NEI40686 109 100.109 100‐‐C109 SCBR Kraft SDT (Kraft)

112_TR2009_Weyerhaeuser Final Report.pdf 112 NEI34064 AA‐101 112.AA‐101 112‐‐Scrubber SCBR Kraft SDT (Kraft)

NEI26506_PM_December_2008.pdf 114 NEI26506 U508 114.U508 114‐‐CDU5 SCBR Kraft SDT (Kraft)

Smelt Dissovlving Tank and Recovery Boiler Part1.pdf 115 NEI26476 SM01 115.SM01 115‐‐SMO1 SCBR SCBR Good Combustion Practices Kraft SDT (Kraft)

Smelt Dissovlving Tank and Recovery Boiler Part1.pdf 115 NEI26476 SM01 115.SM01 115‐‐SMO1 SCBR SCBR Good Combustion Practices Kraft SDT (Kraft)

NEI8619_July 2004 Stack Test Report.pdf 116 NEI8619 004 116.004 116‐‐SDTSCR SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

NEI8619_IP Pine Hill Recovery Sept 2010 Stack Test

Report.pdf 116 NEI8619 004 116.004 116‐‐SDTSCR SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

No 20 SDT Dec 2007.pdf 119 NEI46814 EQT005 119.EQT005 119‐‐SCBR04 SCBR Kraft, Secondary SDT (Kraft)

No 21 SDT March 2007.pdf 119 NEI46814 EQT011 119.EQT011 119‐‐SCBR11 SCBR Kraft, Secondary SDT (Kraft)

Lime Kilns, Smelt Tank and Recovery Furnace

Emissions Test Report_NEI26495.pdf 120 NEI26495 M3 120.M3 120‐‐STS5 SCBR Kraft SDT (Kraft)

NEI 42317 Hopewell VA Dec 2009 SDT PM and

TRS.pdf 126 NEI42317 SDT 126.SDT 126‐‐SDTScr SCBR Kraft SDT (Kraft)

NEI7933_PIII ‐ Smelt Dissolving Tank Vent ‐ PM ‐ 

February 15, 2005.pdf 127 NEI7933 SDT1 127.SDT1 127‐‐E111A SCBR Kraft, Secondary SDT (Kraft)NEI 42254 RockTenn WP Stack Tests.pdf 131 NEI42254 SDT4N 131.SDT4N 131‐‐CR02CD SCBR Kraft, Secondary SDT (Kraft)

NEI 42254 RockTenn WP Stack Tests.pdf 131 NEI42254 SDT4S 131.SDT4S 131‐‐CR03CD SCBR Kraft, Secondary SDT (Kraft)NEI 42254 RockTenn WP Stack Tests.pdf 131 NEI42254 SDT5 131.SDT5 131‐‐CRO6CD SCBR Kraft, Secondary SDT (Kraft)

2010 4 SDT.pdf 132 NEI8261 4SDT 132.4SDT 132‐‐SCBR1 SCBR Kraft, Secondary SDT (Kraft)

2010 5 SDT.pdf 132 NEI8261 5SDT 132.5SDT 132‐‐SCBR2 SCBR Kraft, Secondary SDT (Kraft)2010 ‐ SDT(PM‐TRS) + RB10(PM‐Hg).pdf 136 NEI12368 EU 031 136.EU 031 136‐‐CE 017 SCBR Kraft SDT (Kraft)

2010‐09‐15 5SDT PM‐TRS Test Report.pdf 137 NEI26581 204 137.204 137‐‐PC(204) SCBR Kraft SDT (Kraft)

TRS and PM Smelt Dissolving Tank SN‐03

September 2010.pdf 138 NEI18652 003 138.003 138‐‐SCRB SDT1, SCRB SDT2 PBSCBR Kraft SDT (Kraft)

Test_data_memo_appendices.xlsx App C SDT PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

Generic ProcessType

RTI1#QKT.PDF 142 NEI41552 P7413 142.P7413 142‐‐CD7217 SCBR Kraft, Secondary SDT (Kraft) (2)

NEI759 TSP Testing 2008 part 1.pdf 146 NEI759 10 146.10 146‐‐SDT101 SCBR Kraft SDT (Kraft)

NEI759 TSP Testing 2008 part 1.pdf 146 NEI759 10 146.10 146‐‐SDT101 SCBR Kraft SDT (Kraft)

NEI759 TSP Testing 2008 part 1.pdf 146 NEI759 17 146.17 146‐‐SDT201 SCBR Kraft SDT (Kraft)

MACTreports2004.pdf 147 NEI6450 161 147.161 147‐‐C‐635 SCBR None Kraft SDT (Kraft)MACTreports2004.pdf 147 NEI6450 244 147.244 147‐‐C‐623 SCBR None Kraft SDT (Kraft)NEI46931_7 20‐21 10 No. 1 RF & SDT & No. 2 RF &

SDT Compliance Test Report.pdf 148 NEI46931 002 148.002 148‐‐SDT1SCB SCBR Kraft, Secondary SDT (Kraft)

NEI46931_7 20‐21 10 No. 1 RF & SDT & No. 2 RF &

SDT Compliance Test Report.pdf 148 NEI46931 008 148.008 148‐‐SDT2SCB SCBR Kraft, Secondary SDT (Kraft)

NEI40488 B011, P001, P005 ‐ 2009 Title VCompliance Test Rep.pdf 149 NEI40488 P005 149.P005 149‐‐SC‐502 SCBR Kraft SDT (Kraft)150 NewPage Rumford TRC 2007 Report_CRec and

Smelt Tank_PM.pdf 150 NEI6273 CREC‐2b 150.CREC‐2b 150‐‐SCRBSTa SCBR Kraft, Mechanical SDT (Kraft)

150 NewPage Rumford TRC 2007 Report_CRec and

Smelt Tank_PM.pdf 150 NEI6273 CREC‐2a 150.CREC‐2a 150‐‐SCRBSTb SCBR Kraft, Mechanical SDT (Kraft)

NEI46739 SDT3 PM August 2006 Section 1.pdf 154 NEI46739 P38 ‐ Smelt Dissolving Tank 3

154.P38 ‐ Smelt

Dissolving Tank 3 154‐‐C12 PBSCBR Kraft SDT (Kraft)

NEI33883 ‐ Smelt Dissolving Tank ‐ March 3, 2011 ‐ 

Compliance Test Report.pdf 155 NEI33883 SDT 155.SDT 155‐‐SDT SCRUBBER PBSCBR Kraft, Mechanical SDT (Kraft)

M52010SD18.pdf 156 NEI42338 SMEL18 156.SMEL18 156‐‐ST18VS PBSCBR

Packed‐Gas Absorption Column, WetScrubber

Unknown (Kraft & Semi‐chem) SDT (Kraft)

M52010SD18.pdf 156 NEI42338 SMEL18 156.SMEL18 156‐‐ST18VS PBSCBR

Packed‐Gas Absorption Column, WetScrubber

Unknown (Kraft & Semi‐chem) SDT (Kraft)

M52010SD19.pdf 156 NEI42338 SMEL19 156.SMEL19 156‐‐ST19VS PBSCBR

Packed‐Gas Absorption Column, Wet

Scrubber

Unknown (Kraft & Semi‐chem) SDT (Kraft)

M52010SD19.pdf 156 NEI42338 SMEL19 156.SMEL19 156‐‐ST19VS PBSCBR

Packed‐Gas Absorption Column, WetScrubber

Unknown (Kraft & Semi‐chem) SDT (Kraft)

M52010SD19.pdf 156 NEI42338 SMEL19 156.SMEL19 156‐‐ST19VS PBSCBR

Packed‐Gas Absorption Column, WetScrubber

Unknown (Kraft & Semi‐chem) SDT (Kraft)

M52010SD19.pdf 156 NEI42338 SMEL19 156.SMEL19 156‐‐ST19VS PBSCBR

Packed‐Gas Absorption Column, WetScrubber

Unknown (Kraft & Semi‐chem) SDT (Kraft)

M52010SD19.pdf 156 NEI42338 SMEL19 156.SMEL19 156‐‐ST19VS PBSCBR

Packed‐Gas Absorption Column, Wet

Scrubber

Unknown (Kraft & Semi‐chem) SDT (Kraft)

M52010SD22.pdf 156 NEI42338 SMEL22 156.SMEL22 156‐‐ST22VS PBSCBR

Packed‐Gas Absorption Column, WetScrubber

Unknown (Kraft & Semi‐chem) SDT (Kraft)

M52010SD22.pdf 156 NEI42338 SMEL22 156.SMEL22 156‐‐ST22VS PBSCBR

Packed‐Gas Absorption Column, WetScrubber

Unknown (Kraft & Semi‐chem) SDT (Kraft)

M52010SD22.pdf 156 NEI42338 SMEL22 156.SMEL22 156‐‐ST22VS PBSCBR

Packed‐Gas Absorption Column, WetScrubber

Unknown (Kraft & Semi‐chem) SDT (Kraft)

M52010SD22.pdf 156 NEI42338 SMEL22 156.SMEL22 156‐‐ST22VS PBSCBR

Packed‐Gas Absorption Column, Wet

Scrubber

Unknown (Kraft & Semi‐chem) SDT (Kraft)

M52010SD22.pdf 156 NEI42338 SMEL22 156.SMEL22 156‐‐ST22VS PBSCBR

Packed‐Gas Absorption Column, WetScrubber

Unknown (Kraft & Semi‐chem) SDT (Kraft)

P_P ICR Part III_RTI162_InternationalPaper‐

EastoverMill_NEI46760_no 1 smelt dis tank

particulate2.pdf 162 NEI46760 381C 162.381C 162‐‐381CSCRUB SCBR Kraft SDT (Kraft)P_P ICR Part III_RTI162_InternationalPaper‐

EastoverMill_NEI46760_no 2 smelt dis tank

particulate2.pdf 162 NEI46760 382B 162.382B 162‐‐382BSCRUB SCBR Kraft SDT (Kraft)RTI163_International Paper ‐ PrattvilleMill_NEI8560_No 1 Recovery Furnace and Smelt

Dissolving Tanks testing.pdf 163 NEI8560 SD1902 163.SD1902 163‐‐SD1SC1 SCBR Kraft, Secondary SDT (Kraft)

RTI163_International Paper ‐ PrattvilleMill_NEI8560_No 1 Recovery Furnace and SmeltDissolving Tanks testing.pdf 163 NEI8560 SD1903 163.SD1903 163‐‐SD1SC2 SCBR Kraft, Secondary SDT (Kraft)

Test_data_memo_appendices.xlsx App C SDT PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

Generic ProcessType

RTI163_International Paper ‐ Prattville

Mill_NEI8560_No 2 Recovery Furnace and Smelt

Dissolving Tank testing.pdf 163 NEI8560 SD2906 163.SD2906 163‐‐SD2SCR SCBR Kraft, Secondary SDT (Kraft)

MACT II, June 14‐17, 2004.pdf 164 NEI42710 P08 164.P08 164‐‐C08 for A ESP SCBR Kraft SDT (Kraft)

MACT II, June 14‐17, 2004.pdf 164 NEI42710 P10 164.P10 164‐‐C08 for A ESP SCBR Kraft SDT (Kraft)RTI165‐InternationalPaper‐TexarkanaMill_NEI41628_PPTestReport‐2004SubpartMMIPT.pdf 165 NEI41628 000008 165.000008 165‐‐401015 SCBR Kraft SDT (Kraft)RTI165‐InternationalPaper‐TexarkanaMill_NEI41628_PPTestReport‐2004SubpartMMIPT.pdf 165 NEI41628 000014 165.000014 165‐‐SM01 SCBR Kraft SDT (Kraft)RTI169‐IP‐MansfieldMill‐

NEI33013_2010_Emission_Test_Report‐R.pdf 169 NEI33013 06 169.06 169‐‐Wet Scrubber PBSCBR Kraft, SemiChem SDT (Kraft)

RTI169‐IP‐MansfieldMill‐

NEI33013_2010_Emission_Test_Report‐R.pdf 169 NEI33013 07 169.07 169‐‐Wet Scrubber PBSCBR Kraft, SemiChem SDT (Kraft)

RTI172_International Paper ‐ RiverdaleMill_NEI18335_Oct2010 ST01 PM Testing.pdf 172 NEI18335 ST01 172.ST01 172‐‐ST01 Scrubber SCBR Kraft, Secondary SDT (Kraft)

P_P_ICR Part III_RTI175_InternationalPaper‐AugustaMill_N (5).PDF 175 NEI26514 ST2A 175.ST2A 175‐‐ST2B SCBR Kraft SDT (Kraft)

RecBoiler_WasteBoiler_SmeltTank_LimeKiln_Compliancetest2011_Part1.pdf 177 NEI33887 EU0805 177.EU0805 177‐‐CD0801 SCBR Kraft SDT (Kraft)

RTI179_Rock‐TennDemopolis_NEI45474_PPSurvey_SDTTest2010.pdf 179 NEI45474 SDT 179.SDT 179‐‐SDTSCR SCBR Kraft SDT (Kraft)RTI179_Rock‐TennDemopolis_NEI45474_PP

Survey_RFSDTTest2009.pdf 179 NEI45474 SDT 179.SDT 179‐‐SDTSCR SCBR Kraft SDT (Kraft)NEI26471_No3_Smelt_Tank_PM_TRS_2009‐0317[2].pdf 180 NEI26471 D002, D907 180.D002, D907 180‐‐D02S SCBR Kraft, Secondary SDT (Kraft)

NEI6057 2006 #4 & #5 RB & SDT EMISSION TEST

REPORT Pt 1 of 2.pdf 181 NEI6057 11 181.11 181‐‐4SDT_SCBR SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

NEI6057 2006 #4 & #5 RB & SDT EMISSION TEST

REPORT Pt 1 of 2.pdf 181 NEI6057 11 181.11 181‐‐4SDT_SCBR SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

NEI6057 2005 #4 SDT EMISSION TEST REPORT.pdf 181 NEI6057 11 181.11 181‐‐4SDT_SCBR SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

NEI6057 2006 #4 & #5 RB & SDT EMISSION TEST

REPORT Pt 1 of 2.pdf 181 NEI6057 51 181.51 181‐‐5SDT_SCBR SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

NEI6057 2006 #4 & #5 RB & SDT EMISSION TEST

REPORT Pt 1 of 2.pdf 181 NEI6057 51 181.51 181‐‐5SDT_SCBR SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

NEI6057 2006 #4 & #5 RB & SDT EMISSION TEST

REPORT Pt 1 of 2.pdf 181 NEI6057 51 181.51 181‐‐5SDT_SCBR SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

NEI6057 2005 #5 SDT EMISSION TEST REPORT.pdf 181 NEI6057 51 181.51 181‐‐5SDT_SCBR SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

Sources 037, 110 Test Report April 2005.pdf 182 NEI7181 110 182.110 182‐‐C10/SCR1 SCBR Kraft SDT (Kraft)

2009.02 4SD PM.pdf 185 NEI46599 05 185.05 185‐‐SD4SCB PBSCBR Kraft SDT (Kraft)2009.03 4SD PM.pdf 185 NEI46599 05 185.05 185‐‐SD4SCB PBSCBR Kraft SDT (Kraft)

2009.08 4SD PM.pdf 185 NEI46599 05 185.05 185‐‐SD4SCB PBSCBR Kraft SDT (Kraft)2009.11 4SD PM.pdf 185 NEI46599 05 185.05 185‐‐SD4SCB PBSCBR Kraft SDT (Kraft)2009.01 4SD PM.pdf 185 NEI46599 05 185.05 185‐‐SD4SCB PBSCBR Kraft SDT (Kraft)2009.06 4SD PM.pdf 185 NEI46599 05 185.05 185‐‐SD4SCB PBSCBR Kraft SDT (Kraft)2009 Annual PM.pdf 186 NEI18334 RB17 186.RB17 186‐‐SMSCR SCBR Kraft SDT (Kraft)

Smelt.pdf 186 NEI18334 RB17 186.RB17 186‐‐SMSCR SCBR Kraft SDT (Kraft)GP Crossett Paper Smelt Dissolving Tank

Compliance 2010.pdf 189 NEI54342 SN27 189.SN27 189‐‐SN27S SCBR Kraft SDT (Kraft)

GP Crossett Paper Smelt Dissolving Tank

Compliance 2010.pdf 189 NEI54342 SN28 189.SN28 189‐‐SN28S SCBR Kraft SDT (Kraft)

Georgia‐Pacific Cedar Springs NEI26491 P3 SDTV1

PM 04‐21‐2010 Compliance Test.pdf 190 NEI26491 R404 190.R404 190‐‐C404 SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

Georgia‐Pacific Cedar Springs NEI26491 P3 SDTV2 &

SDTV3 TRS 03‐23‐2010.pdf 190 NEI26491 R406 190.R406 190‐‐C406 SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

2010 Domtar Compliance Testing Part 1 of 6.pdf

and 2010 Domtar Compliance Testing Part 2 of

6.pdf 196 NEI18660 SN‐08North 196.SN‐08North 196‐‐SN‐08 SCBR Scrubber Kraft SDT (Kraft)

2010 Domtar Compliance Testing Part 1 of 6.pdf

and 2010 Domtar Compliance Testing Part 2 of

6.pdf 196 NEI18660 SN‐08South 196.SN‐08South 196‐‐SN‐08 SCBR Scrubber Kraft SDT (Kraft)

NEI41565 MACT II Test Report July 2004.pdf 198 NEI41565 020 198.020 198‐‐020_CD SCBR

Kraft, Mechanical,

Secondary SDT (Kraft)

Test_data_memo_appendices.xlsx App C SDT PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

Generic ProcessType

NEI47077 BOWATER CATAWBA AUG 09 COMP

RPT.pdf 200 NEI47077 007_8, 007_9 200.007_8, 007_9 200‐‐2511C SCBR Kraft, Mechanical SDT (Kraft)

1106‐104_Boise White Paper_SDT Report.pdf 202 NEI12411 Smelt Dissolving Tank EU322

202.Smelt DissolvingTank EU322 202‐‐CE322 SCBR

5 gph 50% caustic to reduce TRS; started

recycling scrubber overflow in 2010 to SDT

to reduce caustic and energy losses to

sewer. Kraft SDT (Kraft)

2010 10 2SDTV PM.pdf 203 NEI42410 2DTScr 203.2DTScr 203‐‐2DTScr‐Scr SCBR none Kraft, Sulfite‐Na SDT (Kraft)

2010 10 3SDTV PM.pdf 203 NEI42410 3DTScr 203.3DTScr 203‐‐3DTScr‐Scr SCBR none Kraft, Sulfite‐Na SDT (Kraft)

NEI7104 ‐ 2003 Smelt Tank.pdf 207 NEI7104 108 207.108 207‐‐C08 PBSCBR Kraft SDT (Kraft)NEI33023_SDT2_2004_PM.pdf 226 NEI33023 SDT1N 226.SDT1N 226‐‐SDT2NS SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

NEI33023_SDT2_2004_PM.pdf 226 NEI33023 SDT1S 226.SDT1S 226‐‐SDT2SS SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

NEI33023_SDT3_2004_PM.pdf 226 NEI33023 SDT2 226.SDT2 226‐‐SDT3S SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

Rayonier Jesup SDT5 PM &TRS test 05_25_10.pdf 240 NEI26526 RF02 240.RF02 240‐‐RFC2 SCBR Kraft SDT (Kraft)

Rayonier Jesup SDT6 PM &TRS test 03_17_10.pdf 240 NEI26526 RF05 240.RF05 240‐‐RFC4 SCBR Kraft SDT (Kraft)Rayonier Jesup SDT6 PM &TRS test 03_17_10.pdf 240 NEI26526 RF06 240.RF06 240‐‐RFC5 SCBR Kraft SDT (Kraft)NEI 34066 Emission Test RB‐LK‐ SDT 2010.pdf 242 NEI34066 AA‐012 242.AA‐012 242‐‐UT‐7 SCBR Kraft SDT (Kraft)

8196_2009 Source Compliance Test Report.pdf 243 NEI8196 R403 243.R403 243‐‐RSS5 SCBR Kraft SDT (Kraft)

8196_2009 Source Compliance Test Report.pdf 243 NEI8196 R408 243.R408 243‐‐RSS6 SCBR Kraft SDT (Kraft)

P_P_ICR Part III_RTI531_InternationalPaper‐ Savnnah Mill (4).pdf 531 NEI8186 RF10 531.RF10 531‐‐AP15 SCBR Kraft, Secondary SDT (Kraft)RTI600_InternationalPaper‐CourtlandMill‐NEI18357NOV 10 1‐3L.pdf 600 NEI18357 G0805 600.G0805 600‐‐08‐CD‐02‐004 SCBR Kraft SDT (kraft)

RTI600_InternationalPaper‐CourtlandMill‐NEI18357JUN 10 3RF .pdf 600 NEI18357 G0807 600.G0807 600‐‐08‐CD‐03‐003 SCBR Kraft SDT (kraft)ODEQ‐Final‐Report‐SDT‐TSP‐TRS‐10‐20‐09.pdf 615 NEI40554 25 615.25 615‐‐SDTSC1 SCBR Kraft SDT (Kraft)

2011_0315‐17.1.pdf 617 NEI42695 P21 617.P21 617‐‐C08 PBSCBR Kraft SDT (Kraft)NEI18373_002_Particulate_2010.pdf 208228535 NEI18373 002 208228535.002 208228535‐‐X002 SCBR Unknown (Kraft) SDT (Kraft)

NEI18373_002_Particulate_2011.pdf 208228535 NEI18373 002 208228535.002 208228535‐‐X002 SCBR Unknown (Kraft) SDT (Kraft)

NEI18373_008_Particulate_2010.pdf 208228535 NEI18373 008 208228535.008 208228535‐‐X013 SCBR Unknown (Kraft) SDT (Kraft)

2007_PE_Lime_Kiln_ESP,_No_4_Rec_Boiler_ESP_and_Smelt_Dis_Tank.pdf 105 NEI45182 EU445D 105.EU445D 105‐‐CD 445‐447 SCBR Kraft, Secondary SDT (Kraft)2008_PM_No_3_Rec_Furnace_and_No_3_Smelt_Dis_Tank_Vents.pdf 105 NEI45182 EU445BEast 105.EU445BEast 105‐‐CD445‐164 SCBR Kraft, Secondary SDT (Kraft)

2008_PM_No_3_Rec_Furnace_and_No_3_Smelt_Dis_Tank_Vents.pdf 105 NEI45182 EU445BWest 105.EU445BWest 105‐‐CD445‐162 SCBR Kraft, Secondary SDT (Kraft)

TempleInland‐OrangeMill_NEI12492_PPTestReport‐

2002TestReport.pdf 121 NEI12492 000009 121.000009 121‐‐C‐REVB1, C‐REVB2 SCBR Kraft, Secondary SDT (Kraft)

TempleInland‐OrangeMill_NEI12492_PPTestReport‐

2002TestReport.pdf 121 NEI12492 000010 121.000010 121‐‐C‐REVB1, C‐REVB2 SCBR Kraft, Secondary SDT (Kraft)

TempleInland‐OrangeMill_NEI12492_PPTestReport‐

2004MACTIIReport.pdf 121 NEI12492 000009 121.000009 121‐‐C‐11 SCBR Kraft, Secondary SDT (Kraft)

TempleInland‐OrangeMill_NEI12492_PPTestReport‐

2004MACTIIReport.pdf 121 NEI12492 000010 121.000010 121‐‐C‐13 SCBR Kraft, Secondary SDT (Kraft)

NEI42341A_PIII_D2a_2011‐Q1 LK‐RB10‐SDTV10‐

HFB11.pdf 102 NEI42341A SDTV10 102.SDTV10 102‐‐SDTV‐S SCBR Kraft SDT (Kraft)

IP PENSACOLA 2011 RF‐SDTV COMP REPORT.pdf 178 NEI26309 08T014 178.08T014 178‐‐08C014 SCBR Kraft SDT (Kraft)

IP PENSACOLA 2011 RF‐SDTV COMP REPORT.pdf 178 NEI26309 08T015 178.08T015 178‐‐08C015 SCBR Kraft SDT (Kraft)Georgia‐Pacific Cedar Springs NEI26491 P3 RB1 PM

& SDTV1 PM, TRS 09‐24‐2009 Compliance Test.pdf 190 NEI26491 R404 190.R404 190‐‐C400 SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

2008_PM_Lime_Kiln,_No_4_Rec_Boiler_and_No_4_Smelt_Dis_Tank.pdf 105 NEI45182 EU445D 105.EU445D 105‐‐CD 445‐447 SCBR Kraft, Secondary SDT (Kraft)

Test_data_memo_appendices.xlsx App C SDT PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

Generic ProcessType

2008_PM_Lime_Kiln_Exh,_No_4_Rec_Boiler_and_No_4_Smelt_Dis_Tank.pdf 105 NEI45182 EU445D 105.EU445D 105‐‐CD 445‐447 SCBR Kraft, Secondary SDT (Kraft)2009_PM_No_3_Lime_Kiln,_No_4_Rec_Boiler_and_No_4_Smelt.pdf 105 NEI45182 EU445D 105.EU445D 105‐‐CD 445‐447 SCBR Kraft, Secondary SDT (Kraft)2009_PM_No_3_Lime_Kiln_and_No_4_Smelt_Dis_Tank.pdf 105 NEI45182 EU445D 105.EU445D 105‐‐CD 445‐447 SCBR Kraft, Secondary SDT (Kraft)IP PENSACOLA SEPT 04 PM COMP REPORT.pdf 178 NEI26309 08T015 178.08T015 178‐‐08C015 SCBR Kraft SDT (Kraft)

IP PENSACOLA SEPT 04 PM COMP REPORT.pdf 178 NEI26309 08T014 178.08T014 178‐‐08C014 SCBR Kraft SDT (Kraft)2011 Stack Report‐AIR.pdf 130 NEI18338 11 130.11 130‐‐11SD3S SCBR Kraft SDT (Kraft)2011 Stack Report‐AIR.pdf 130 NEI18338 6 130.6 130‐‐6SD1S SCBR Kraft SDT (Kraft)2011 Stack Report‐AIR.pdf 130 NEI18338 7 130.7 130‐‐7SD2S SCBR Kraft SDT (Kraft)2011 RB & ST PM #103.pdf 135 NEI33118 007‐1, 007‐2 135.007‐1, 007‐2 135‐‐007‐4, 007‐5 SCBR Kraft SDT (Kraft)

2010‐08‐31 4SD PM Eng Test Report.pdf 137 NEI26581 157 137.157 137‐‐PC(157) SCBR Kraft SDT (Kraft)

2010‐09‐16 4SDT PM Test Report.pdf 137 NEI26581 157 137.157 137‐‐PC(157) SCBR Kraft SDT (Kraft)Mill code 139 part 4.pdf 139 NEI42357 03 139.03 139‐‐SDTSCBR SCBR Kraft, Secondary SDT (Kraft)SDT EPA5 102010.pdf 140 NEI13340 57 140.57 140‐‐461‐213 PBSCBR Kraft SDT (Kraft)

SDT OM5 032011.pdf 140 NEI13340 57 140.57 140‐‐461‐212 PBSCBR Kraft SDT (Kraft)SDT OM5 032011.pdf 140 NEI13340 57 140.57 140‐‐461‐212 PBSCBR Kraft SDT (Kraft)RTI1#CGM.pdf 142 NEI41552 P7236 142.P7236 142‐‐CD‐7236 SCBR Kraft, Secondary SDT (Kraft)

NEI26504_RTI143_PCA Valdosta Mill_1,2,3 SDT

PM_November 2009.pdf 143 NEI26504 7005 143.7005 143‐‐C012 SCBR Kraft SDT (Kraft)

NEI26504_RTI143_PCA Valdosta Mill_1,2,3 SDT

PM_November 2009.pdf 143 NEI26504 7015 143.7015 143‐‐C014 SCBR Kraft SDT (Kraft)

NEI26504_RTI143_PCA Valdosta Mill_1,2,3 SDT

PM_November 2009.pdf 143 NEI26504 7025 143.7025 143‐‐C016 SCBR Kraft SDT (Kraft)

NEI11338_WPC ‐ RF_SDT_LK ‐ Mar 2007.pdf 152 NEI11338 04 152.04 152‐‐04‐SCBR SCBR Kraft SDT (Kraft)

NEI46739 RB2, SDT1, SDT2 and SDT3 PM March

2004.pdf 154 NEI46739 P32 ‐ Smelt Dissolving Tank 1

154.P32 ‐ Smelt

Dissolving Tank 1 154‐‐C07 SCBR Kraft SDT (Kraft)

NEI46739 SDT1 and SDT2 PM May 2004.pdf 154 NEI46739 P32 ‐ Smelt Dissolving Tank 1

154.P32 ‐ Smelt

Dissolving Tank 1 154‐‐C07 SCBR Kraft SDT (Kraft)

NEI46739 RB2, SDT1, SDT2 and SDT3 PM March

2004.pdf 154 NEI46739 P35 ‐ Smelt Dissolving Tank 2

154.P35 ‐ Smelt

Dissolving Tank 2 154‐‐C09 SCBR Kraft SDT (Kraft)

NEI46739 SDT1 and SDT2 PM May 2004.pdf 154 NEI46739 P35 ‐ Smelt Dissolving Tank 2

154.P35 ‐ Smelt

Dissolving Tank 2 154‐‐C09 SCBR Kraft SDT (Kraft)

NEI33104‐SDT 2005 PM Compliance.pdf 157 NEI33104 SDT 157.SDT 157‐‐SDRMST OTH Kraft SDT (Kraft)

RTI167 NEI340702011_IPVicksburg_StackTestReport_(PB,LK,RB,SDT,SS).pdf 167 NEI34070 007SDT 167.007SDT 167‐‐SDSCBR SCBR Kraft, Secondary SDT (Kraft)9‐0224C Evergreen F.pdf 171 NEI18658 006 171.006 171‐‐MESDT2 OTH Kraft SDT (Kraft)9‐0224C Evergreen F.pdf 171 NEI18658 007 171.007 171‐‐VSSDT3 SCBR Kraft SDT (Kraft)9‐0224C Evergreen F.pdf 171 NEI18658 008 171.008 171‐‐VSSDT4 SCBR Kraft SDT (Kraft)RTI173 NEI 35908 IPTiconderoga SDT test 2‐01.pdf 173 NEI35908 SDT 173.SDT 173‐‐SDSCBR SCBR NA Kraft SDT (Kraft)

RTI173 NEI 35908 IPTiconderoga Subpart MM StackTest for RB‐SDT‐LK 10‐04.pdf 173 NEI35908 SDT 173.SDT 173‐‐SDSCBR SCBR NA Kraft SDT (Kraft)

P_P_ICR Part III_RTI175_InternationalPaper‐AugustaMill_N (5).pdf 175 NEI26514 ST3A 175.ST3A 175‐‐ST3B SCBR Kraft SDT (Kraft)

RecBoiler #1_SmeltTank#1‐

ComplianceTest2004_Part1.pdf 184 NEI46817 SDT1 184.SDT1 184‐‐7 SCBR Kraft SDT (Kraft)RecBoiler #1_SmeltTank#1‐

ComplianceTest2004_Part1.pdf 184 NEI46817 SDT1 184.SDT1 184‐‐7 SCBR Kraft SDT (Kraft)RecBoiler #1_SmeltTank#1‐

ComplianceTest2004_Part1.pdf 184 NEI46817 SDT2a 184.SDT2a 184‐‐8 SCBR Kraft SDT (Kraft)RecBoiler #1_SmeltTank#1‐

ComplianceTest2004_Part1.pdf 184 NEI46817 SDT2a 184.SDT2a 184‐‐8 SCBR Kraft SDT (Kraft)

SmeltTank#2E ComplianceTest2004.pdf 184 NEI46817 SDT2a 184.SDT2a 184‐‐8 SCBR Kraft SDT (Kraft)

RecBoiler #1_SmeltTank#1‐

ComplianceTest2004_Part1.pdf 184 NEI46817 SDT2b 184.SDT2b 184‐‐9 SCBR Kraft SDT (Kraft)RecBoiler #1_SmeltTank#1‐

ComplianceTest2004_Part1.pdf 184 NEI46817 SDT2b 184.SDT2b 184‐‐9 SCBR Kraft SDT (Kraft)SmeltTank#2W ComplianceTest2004.pdf 184 NEI46817 SDT2b 184.SDT2b 184‐‐9 SCBR Kraft SDT (Kraft)

2011.0606‐0609.2Q.tests.pdf 188 NEI40600 015SD1 188.015SD1 188‐‐62‐056 SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

2011.0606‐0609.2Q.tests.pdf 188 NEI40600 017SD2 188.017SD2 188‐‐62‐256 SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

Georgia‐Pacific Cedar Springs NEI26491 P3 SDTV2

PM 10‐15‐2009 Compliance Test.pdf 190 NEI26491 R405 190.R405 190‐‐C405 SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

2004 Method 5 Testing ‐ part 1 of 3.pdf 196 NEI18660 SN‐15 196.SN‐15 196‐‐SN‐15 SCBR Scrubber Kraft SDT (Kraft)

NEI18390_002_004_PM_2011.pdf 199 NEI18390 004 199.004 199‐‐Z006 SCBR Kraft SDT (Kraft)NEI7559Smelt‐87‐02 Comp2004 SubprtMM.pdf 201 NEI7559 SR0034 201.SR0034 201‐‐SDTS SCBR

Kraft, Mechanical,

Secondary SDT (Kraft)

NEI8601_Unit 010_2010.pdf 205 NEI8601 010 205.010 205‐‐SDTS SCBR Kraft, Secondary SDT (Kraft)

RTI206_BRPPSDTV10COMPPM012505.pdf 206 NEI40282 G‐35 206.G‐35 206‐‐SDT10 DEM OTH Kraft SDT (Kraft)

RTI206_BRPPSDTV10PM111705.pdf 206 NEI40282 G‐35 206.G‐35 206‐‐SDT10 DEM OTH Kraft SDT (Kraft)

Test_data_memo_appendices.xlsx App C SDT PM 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

Generic ProcessType

RTI206_BRPPSDTV11COMPPM012605.pdf 206 NEI40282 G‐36 206.G‐36 206‐‐SDT11 DEM OTH Kraft SDT (Kraft)

RTI206_BRPPSDTV11PM102005.pdf 206 NEI40282 G‐36 206.G‐36 206‐‐SDT11 DEM OTH Kraft SDT (Kraft)47091_006_2010A_PM.pdf 606 NEI47091 SDT2 606.SDT2 606‐‐SCRB2 SCBR Kraft SDT (Kraft)

47091_006_2011_PM.pdf 606 NEI47091 SDT2 606.SDT2 606‐‐SCRB2 SCBR Kraft SDT (Kraft)47091_007_2005_PM_TRS.pdf 606 NEI47091 SDT3 606.SDT3 606‐‐SCRB3 SCBR Kraft SDT (Kraft)47091_007_2010_PM.pdf 606 NEI47091 SDT3 606.SDT3 606‐‐SCRB3 SCBR Kraft SDT (Kraft)47091_011_2006_PM_TRS.pdf 606 NEI47091 SDT4 606.SDT4 606‐‐SCRB4 SCBR Kraft SDT (Kraft)47091_011_2010_PM.pdf 606 NEI47091 SDT4 606.SDT4 606‐‐SCRB4 SCBR Kraft SDT (Kraft)610 Verso 2009 SDT 1&2 Report.pdf 610 NEI6261 10 610.10 610‐‐SDT2WS SCBR Kraft, Mechanical SDT (Kraft)610 Verso 2009 SDT 1&2 Report.pdf 610 NEI6261 10 610.10 610‐‐SDT2WS SCBR Kraft, Mechanical SDT (Kraft)

610 Verso 2009 SDT 1&2 Report.pdf 610 NEI6261 9 610.9 610‐‐SDT1WS SCBR

stacked air installed in recovery boiler No. 1

in 2007 Kraft, Mechanical SDT (Kraft)

610 Verso 2009 SDT 1&2 Report.pdf 610 NEI6261 9 610.9 610‐‐SDT1WS SCBR

stacked air installed in recovery boiler No. 1

in 2007 Kraft, Mechanical SDT (Kraft)

2009 #1 SDTV.pdf 613 NEI11172 005 613.005 613‐‐1LSCRB SCBR Kraft, Secondary SDT (Kraft)

2009 #1 SDTV.pdf 613 NEI11172 006 613.006 613‐‐1RSCRB SCBR Kraft, Secondary SDT (Kraft)2009 #2 SDTV.pdf 613 NEI11172 007 613.007 613‐‐2LSCRB SCBR Kraft, Secondary SDT (Kraft)2009 #2 SDTV.pdf 613 NEI11172 008 613.008 613‐‐2RSCRB SCBR Kraft, Secondary SDT (Kraft)No.2 SDT Part Testing.pdf 145 NEI33135 56 145.56 145‐‐PR009‐01C OTH Kraft SDT (Kraft)

2009 4 SDT.pdf 132 NEI42357 4SDT 132.4SDT 132‐‐SCBR1 SCBR Kraft, Secondary SDT (Kraft)

Green rows were not used in the NSPS review.

Test_data_memo_appendices.xlsx App C SDT PM 
atter

RTI+EUID105.EU445D107.09‐P2

109.SDT3109.SDT4109.SDT3111.G‐127

166.ST01166.ST02174.G‐63B

174.G‐63C

174.G‐63C

174.G‐63B

174.G‐63C

174.G‐63C

124.020124.021340.007340.007100.109112.AA‐101114.U508115.SM01115.SM01116.004116.004119.EQT005119.EQT011120.M3126.SDT127.SDT1131.SDT4N131.SDT4S131.SDT5132.4SDT132.5SDT136.EU 031137.204138.003

Configuration General Test Report Information Production Rate Inlet/OutletHas the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date

(mm/dd/yyyy)

Emission Test

Method

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet dataprovided?

no PM 2010 #4 Smelt Dissolving Tank unspecified 10/13/2010 M5 59.05 ton BLS/hr Outlet

PM 2011 Smelt Dissolving Tanks unspecified 6/9/2011 M5 94.5 ton BLS/hr Outlet

No PM 2008 Smelt Dissolving Tank # 3 unspecified 7/31/2008 M5 49.51 ton BLS/hr Outlet

No PM 2008 No. 4 Smelt Dissolver unspecified 8/13/2008 M5 83.92 ton BLS/hr Outlet

No PM 2006 No. 3 Smelt Dissolver unspecified 5/12/2006 M5 44.35725 ton BLS/hr

Report provided 88714.5 "tonsBLS/hr" but it appears that this

was really "lb BLS/hr". Used

corrected production rate. Outlet

No PM 2011 South Smelt Tank unspecified 1/29/2011 M5 45.3 ton BLS/hr Outlet

No PM 2009 No. 1 Smelt Dissolving Tank unspecified 7/14/2009 M5 68.5 ton BLS/hr Outlet

No PM 2009 No. 2 Smelt Dissolving Tank unspecified 7/17/2009 M5 82.5 ton BLS/hr Outlet

PM 2005 No. 4 SDT unspecified 2/3/2005 M5 50.5 ton BLS/hr Outlet

PM 2005 No. 5 SDT ‐ East Stack unspecified 2/1/2005 M5 139 ton BLS/hr OutletPM 2005 No. 5 SDT ‐ West Stack unspecified 2/1/2005 M5 139 ton BLS/hr OutletPM 2004 No. 4 SDT unspecified 10/27/2004 M5 45.5 ton BLS/hr Outlet

PM 2004 No. 5 SDT ‐ East Stack unspecified 10/22/2004 M5 139.7 ton BLS/hr OutletPM 2004 No. 5 SDT ‐ West Stack unspecified 10/22/2004 M5 139.7 ton BLS/hr Outlet

No PM 2010 No. 1 Smelt Dissolver Fuel oil 11/3/2010 M5 58.3 ton BLS/hr outlet

No PM 2010 No. 2 Smelt Dissolver Fuel oil 11/4/2010 M5 58.05 ton BLS/hr outletNo PM 2005 Smelt Dissolving Tank unspecified 6/21/2005 M5 48.03333333 ton BLS/hr outlet

No PM 2004 Smelt Dissolving Tank unspecified 7/23/2004 M5 49.73 ton BLS/hr outlet

No PM 2001 Smelt Dissolving Tank 8/9/2001 M5 57.5 ton BLS/hr Outlet

Yes

smelt dissolving tank

rebuilt in 2009 followingtesting. PM 2009 Smelt Dissolving Tank 3/18/2009 M5 117.18 ton BLS/hr Outlet

No PM 2008 Smelt Dissolving Tank 12/18/2008 M5 105.83 ton BLS/hr Outlet

no PM 2010 SDT West 9/9/2010 M5 87.5 ton BLS/hr Outlet

no PM 2010 SDT East 9/9/2010 M5 87.5 ton BLS/hr Outlet

No PM 2004 Smelt Dissolving Tank Vent 7/20/2004 M5 95.41 ton BLS/hr Outlet

No PM 2010 Smelt Dissovling Tank Vent 9/2/2010 M5 95 ton BLS/hr Outlet

No PM 2007 No. 20 SDT 1/3/2007 M5 unspecified OutletNo PM 2007 No. 21 SDT 3/21/2007 M5 unspecified OutletNo PM 2009 #5 SDT 7/22/2009 M5 102.5 ton BLS/hr OutletNo PM 2009 SDT 12/10/2009 M5 51.6 ton BLS/hr Outlet

No PM 2005 SDT Vent 2/15/2005 M5 71.16 ton BLS/hr Outlet

No PM 2004 SDT 4N 3/8/2004 M5 63.58639583 ton BLS/hr Outlet

No PM 2004 SDT 4S 3/8/2004 M5 63.58639583 ton BLS/hr Outlet

No PM 2003 SDT 5 12/9/2003 M5 62.91416667 ton BLS/hr Outlet

PM 2010 4 SDT 5/20/2010 M5 63.49 ton BLS/hr OutletPM 2010 5 SDT 5/18/2010 M5 74.18 ton BLS/hr Outlet

no PM 2010 SDT 5/19/2010 M5 113.5 ton BLS/hr Outlet

No PM 2010 No. 5 SDT 9/15/2010 M5 95.01 ton BLS/hr Outlet

No PM 2010 Smelt Dissolving Tank 9/23/2010 M5 57.01388889 ton BLS/hr Outlet

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

142.P7413146.10146.10146.17147.161147.244148.002148.008149.P005150.CREC‐2b

150.CREC‐2a

154.P38 ‐ Smelt

Dissolving Tank 3

155.SDT156.SMEL18156.SMEL18156.SMEL19156.SMEL19156.SMEL19156.SMEL19156.SMEL19156.SMEL22156.SMEL22156.SMEL22156.SMEL22156.SMEL22162.381C162.382B163.SD1902163.SD1903

Has the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date

(mm/dd/yyyy)

Emission Test

Method

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet dataprovided?

No

New stack and scrubber

specific to SDT‐1 installedduring 2011. PM 2004 No. 1 and No. 2 SDTs 7/22/2004 M5 73.45733333 ton BLS/hr Outlet

No PM 2008 No. 1 SDT (upriver vent) 10/16/2008 M5 76.66666667 ton BLS/hr OutletNo PM 2008 No. 1 SDT (downriver vent) 10/16/2008 M5 76.875 ton BLS/hr OutletNo PM 2008 No. 2 SDT 10/16/2008 M5 114.375 ton BLS/hr Outlet

no NA PM 2004 SDT3 7/28/2004 M5 57.6 ton BLS/hr Outlet

no NA PM 2004 SDT2 7/28/2004 M5 37.9 ton BLS/hr Outlet

no PM 2010 No. 1 SDT 7/21/2010 M5 58.6 ton BLS/hr Outlet

no PM 2010 No. 2 SDT 7/20/2010 M5 81.3 ton BLS/hr Outlet

no PM 2009 No. 9 SDT 4/3/2009 M5 68.35 ton BLS/hr Outlet

No PM 2007 Smelt Tank East 8/29/2007 M5 87.3 ton BLS/hr Outlet

No PM 2007 Smelt Tank West 8/29/2007 M5 87.3 ton BLS/hr Outlet

No PM 2006 SDT3 8/1/2006 M5 33.77333333 ton BLS/hr Outlet

No PM 2011 Smelt Dissolving Tank 3/3/2011 M5 77.7 ton BLS/hr Outlet

No PM 2010 SDT 18 3/17/2010 M5 42.467 ton BLS/hr Outlet

No PM 2010 SDT 18 8/4/2010 M5 42.5085 ton BLS/hr Outlet

No PM 2010 SDT 19 4/6/2010 M5 59.521 ton BLS/hr Outlet

No PM 2010 SDT 19 9/20/2010 M5 55.4085 ton BLS/hr Outlet

No PM 2010 SDT 19 10/27/2010 M5 66.31 ton BLS/hr Outlet

No PM 2010 SDT 19 11/9/2010 M5 57.5065 ton BLS/hr Outlet

No PM 2010 SDT 19 12/7/2010 M5 55.0005 ton BLS/hr Outlet

No PM 2010 SDT 22 1/26/2010 M5 88.5 ton BLS/hr Outlet

No PM 2010 SDT 22 2/11/2010 M5 86.5 ton BLS/hr Outlet

No PM 2010 SDT 22 4/8/2010 M5 83 ton BLS/hr Outlet

No PM 2010 SDT 22 9/10/2010 M5 60 ton BLS/hr Outlet

No PM 2010 SDT 22 11/18/2010 M5 68.5 ton BLS/hr Outlet

No PM 2007 No. 1 SDT 10/25/2007 M5 50 ton BLS/hr Outlet

No PM 2009 No. 2 SDT 5/21/2009 M5 106 ton BLS/hr Outlet

No PM 2011 No. 1 SDT South 6/1/2011 M5 51.5 ADTP/hr ton BLS/hr not provided Outlet

No PM 2011 No. 1 SDT North 6/1/2011 M5 51.5 ADTP/hr ton BLS/hr not provided Outlet

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

163.SD2906164.P08164.P10165.000008165.000014169.06169.07172.ST01175.ST2A177.EU0805179.SDT179.SDT180.D002, D907

181.11181.11181.11181.51181.51181.51181.51182.110185.05185.05185.05185.05185.05185.05186.RB17186.RB17189.SN27189.SN28190.R404190.R406196.SN‐08North

196.SN‐08South

198.020

Has the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date

(mm/dd/yyyy)

Emission Test

Method

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet dataprovided?

No PM 2011 No. 2 6/2/2011 M5 65.20833333 ton BLS/hr Outlet

PM 2004 No. 8 SDT 6/14/2004 M5 unspecified OutletPM 2004 No. 10 SDT 6/16/2004 M5 unspecified Outlet

No PM 2004 No. 2 Smelt Tank Scrubber 7/21/2004 M5 91.4 ton BLS/hr Outlet

No PM 2004 No. 1 Smelt Tank Scrubber 7/27/2004 M5 49.53 ton BLS/hr Outlet

No PM 2010 Smelt Dissolving Tank No. 1 9/21/2010 M5 76.8 ton BLS/hr Outlet

No PM 2010 Smelt Dissolving Tank No. 2 9/21/2010 M5 79.1 ton BLS/hr Outlet

no PM 2010 No. 1 SDT 10/27/2010 unspecified 35.83 ADTP/hr Outletno PM 2010 No. 2 SDT 4/13/2010 M5 30.9 ton BLS/hr Outlet

No PM 2011 SDT 3/29/2011 M5 83.6 ton BLS/hr

Converted from kpph BLS

(thousand lb/hr) Outlet

No PM 2010 No. 3 SDT Vent 6/2/2010 M5 93.17 ton BLS/hr OutletNo PM 2009 No. 3 SDT Vent 5/27/2009 M5 86.8 ton BLS/hr Outlet

No PM 2009 No. 3 SDT Vent 3/17/2009 M5 73.81 ton BLS/hr Outlet

No PM 2006

No. 4 RB SDT (condition 1: P‐dop = 6.9 in

H2O) 11/2/2006 M5 58 ton BLS/hr Outlet

No PM 2006

No. 4 RB SDT (condition 3: P‐drop = 7.7 in

H2O) 11/3/2006 M5 57 ton BLS/hr Outlet

No PM 2005 No. 4 RB SDT 1/25/2005 M5 57.73 ton BLS/hr Outlet

No PM 2006

No. 5 RB SDT ‐ (condition 1: P‐drop = 5.9

in H2O) 10/31/2006 M5 51 ton BLS/hr Outlet

No PM 2006

No. 5 RB SDT ‐ (condition 2: P‐drop = 7.0

in H2O) 11/1/2006 M5 46 ton BLS/hr

Summary sheet had 50, but testreport appendix had 46 ton

BLS/hr. Used 46. Outlet

No PM 2006

No. 5 RB SDT ‐ (condition 3: P‐drop = 7.1

in H2O) 11/1/2006 M5 50 ton BLS/hr Outlet

No PM 2005 No. 5 RB SDT 1/25/2005 M5 48.25 ton BLS/hr Outlet

no PM 2005 Smelt Dissolving Tank Vent 4/12/2005 M5 66.38333333 ton BLS/hr Outlet

No PM 2009 No. 4 Smelt Dissolver 2/4/2009 M5 53.15277778 ton BLS/hr

provided TBLS/day‐‐divided by24 to get hourly Outlet

No PM 2009 No. 4 Smelt Dissolver 3/11/2009 M5 52.01388889 ton BLS/hr

provided TBLS/day‐‐divided by24 to get hourly Outlet

No PM 2009 No. 4 Smelt Dissolver 8/26/2009 M5 51.94444444 ton BLS/hr

provided TBLS/day‐‐divided by24 to get hourly Outlet

No PM 2009 No. 4 Smelt Dissolver 11/12/2009 M5 52.33333333 ton BLS/hr

provided TBLS/day‐‐divided by24 to get hourly Outlet

No PM 2009 No. 4 Smelt Dissolver 1/2/2009 M5 52.375 ton BLS/hr

provided TBLS/day‐‐divided by24 to get hourly Outlet

No PM 2009 No. 4 Smelt Dissolver 6/3/2009 M5 53.77777778 ton BLS/hr

provided TBLS/day‐‐divided by

24 to get hourly Outlet

No PM 2009 No. 4 Smelt Tank 7/13/2009 M5 128.31 ton BLS/hr Outlet

No PM 2008 No. 4 Smelt Tank 7/22/2008 M5 127.2 ton BLS/hr Outlet

no PM 2010 SDT East 12/2/2010 M5 115.4166667 ton BLS/hr

provided BLS MM#/day,converted to TBLS/hr Outlet

no PM 2010 SDT West 11/30/2010 M5 114.9375 ton BLS/hr

provided BLS MM#/day,converted to TBLS/hr Outlet

No PM 2010 No. 1 SDT 4/21/2010 M5 46.5 ton BLS/hr Outlet

No PM 2010 No. 3 SDT 3/23/2010 M5 74.5 ton BLS/hr Outlet

no PM 2010 No. 2 North Smelt Tank Vent 4/20/2010 M5 79.16666667 ton BLS/hr

provided MM#/day (appears to

be BLS), converted to ton/hr Outlet

no PM 2010 No. 2 South Smelt Tank Vents 4/20/2010 M5 79.16666667 ton BLS/hr

provided MM#/day (appears to

be BLS), converted to ton/hr Outlet

No PM 2004 No. 3 SDT 7/27/2004 M5 111.95 ton BLS/hr Outlet

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

200.007_8, 007_9

202.Smelt DissolvingTank EU322

203.2DTScr

203.3DTScr207.108226.SDT1N226.SDT1S226.SDT2240.RF02240.RF05240.RF06242.AA‐012243.R403243.R408531.RF10600.G0805600.G0807615.25617.P21208228535.002208228535.002208228535.008105.EU445D105.EU445BEast105.EU445BWest121.000009121.000010121.000009121.000010102.SDTV10178.08T014178.08T015190.R404105.EU445D

Has the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date

(mm/dd/yyyy)

Emission Test

Method

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet dataprovided?

No PM 2009 Nos. 2 and 3 SDT Vent 7/29/2009 M5 118.6 ton BLS/hr Outlet

no

Particulate matter testincludes condensable as

well as method 5

filterable PM 2011 SDT EU322 7/19/2011 M5 57.3 ton BLS/hr Outlet

No PM 2010 No. 2 DT Scrubber Vent Stack 10/12/2010 M5 55.7 gpm Black Liq. Flow Outlet

No PM 2010 No. 3 SDT 10/26/2010 M5 68.30208 ton BLS/hr

Calculated based on avg of 308

gpm @ 66% solids and 11.2

lb/gal provided in report. Outlet

no NA PM 2003 Smelt Tank 9/24/2003 M5 20.2 ton BLS/hr Outlet

no PM 2004 No. 2 SDT North 1/19/2004 M5 82.3 ton BLS/hr Outlet

no PM 2004 No. 2 SDT South 1/20/2004 M5 83.96 ton BLS/hr Outlet

no PM 2004 No. 3 SDT 1/17/2004 M5 52.6 ton BLS/hr Outlet

No PM 2010 No. 5 SDT 5/25/2010 M5 67.4 ton BLS/hr Outlet

No PM 2010 No. 6 SDT East 3/17/2010 M5 119.6 ton BLS/hr Outlet

No PM 2010 No. 6 SDT West 3/17/2010 M5 119.6 ton BLS/hr Outlet

No PM 2010 SDT 9/15/2010 M5 125.2 ton BLS/hr

RF PM, TRS, Nox, CO, SO2; LK

PM, TRS, Nox, CO, SO2; INC TRS,Nox, CO, SO2, THC; O2 delig THC

and CO; pet coke BH PM; bleach

plant Cl2 and ClO2 Outlet

No PM 2009 No. 5 SDT 10/29/2009 M5 35.37 ton BLS/hr Outlet

No PM 2009 No. 6 SDT 10/28/2009 M5 120.1 ton BLS/hr Outlet

No PM 2011 No. 15 SDT 5/4/2011 M5 150 ton BLS/hr Outlet

no PM 2010 No. 2 SDT 11/2/2010 M5 85.56 ton BLS/hr Outlet

no PM 2010 No. 3 SDT 6/8/2010 M5 104 ton BLS/hr Outlet

no PM 2009 SDT 10/20/2009 M5 64.05 ton BLS/hr

Provided production in lb BLS

fired/min‐‐converted to TBLS/hr Outlet

no PM 2011 S21 SDT 3/16/2011 M5 35 ton BLS/hr Outlet

No PM 2010 No. 1 SDT 4/28/2010 M5 105.7 ton BLS/hr

Did not specify tons of BLS,ADTP, etc. Assumed tons "BLS"since this value is similar to

other tests labeled as BLS Outlet

No PM 2011 No. 1 SDT 5/27/2011 M5 104.79 ton BLS/hr

Did not specify tons of BLS,ADTP, etc. Assumed tons "BLS"since this value is similar to

other tests labeled as BLS Outlet

No PM 2010 No. 2 SDT 8/19/2010 M5 122.93 ton BLS/hr

Did not specify tons of BLS,ADTP, etc. Assumed tons "BLS"since this value is similar to

other TRS and PM test thatlabeled as BLS Outlet

No PM 2007 No. 4 Smelt Dissolving Tank 05/16/2007 EPA\ODEQ M5 64.4 ton BLS/hr

Units in test report provided in

"MPPH" which was interpreted

as thousand pounds per hour Outlet

no PM 2008 Smelt dissolving tanks, #3 East Vent Unspecified 2/20/2008 ODEQ M5 60.5 ton BLS/hr

Interpreted "MPPH" as thousandpounds per hour BLS firing rate Outlet

no PM 2008 Smelt dissolving tanks, #3 West Vent Unspecified 2/20/2008 ODEQ M5 60.5 ton BLS/hr

Interpreted "MPPH" as thousandpounds per hour BLS firing rate Outlet

No PM 2002 No. 1 Smelt Dissolving Tank Unspecified 10/29/2002 M5 34.3 ton BLS/hr Outlet

No PM 2002 No. 2 Smelt Dissolving Tank Unspecified 10/30/2002 M5 34.2 ton BLS/hr Outlet

No PM 2004 No. 1 Smelt Dissolving Tank Unspecified 8/20/2004 M5 39 ton BLS/hr Outlet

No PM 2004 No. 2 Smelt Dissolving Tank Unspecified 8/18/2004 M5 39 ton BLS/hr Outlet

No PM 2011 Smelt Dissolver Tank Vent unspecified 1/5/2011 M5 121.25 ton BLS/hr

Converted from klbs/hr to

tons/hr Outlet

No PM 2011 Smelt Dissolving Tank No. 1 unspecified 6/21/2011 M5 51.78 ton BLS/hr Outlet

No PM 2011 Smelt Dissolving Tank No. 2 unspecified 6/22/2011 M5 51.8 ton BLS/hr Outlet

No PM 2009 SDTV NO. 1 unspecified 9/24/2009 M5 47.2733 ton BLS/hr Outlet

no PM 2008 No. 4 Smelt Dissolving Tank unspecified 05/20/2008 EPA\ODEQ M5 64.4 ton BLS/hr Outlet

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

105.EU445D105.EU445D105.EU445D178.08T015178.08T014130.11130.6130.7135.007‐1, 007‐2

137.157137.157139.03140.57140.57140.57142.P7236143.7005143.7015143.7025152.04154.P32 ‐ Smelt

Dissolving Tank 1

154.P32 ‐ Smelt

Dissolving Tank 1

154.P35 ‐ Smelt

Dissolving Tank 2

154.P35 ‐ Smelt

Dissolving Tank 2

157.SDT167.007SDT171.006171.007171.008173.SDT173.SDT175.ST3A184.SDT1184.SDT1184.SDT2a184.SDT2a184.SDT2a184.SDT2b184.SDT2b184.SDT2b188.015SD1188.017SD2190.R405196.SN‐15

199.004201.SR0034205.010206.G‐35

206.G‐35

Has the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date

(mm/dd/yyyy)

Emission Test

Method

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet dataprovided?

no PM 2008 No. 4 Smelt Dissolving Tank unspecified 10/22/2008 EPA\ODEQ M5 59.2 ton BLS/hr Outlet

no PM 2009 No. 4 Smelt Dissolving Tank unspecified 06/03/2009 EPA\ODEQ M5 57.8 ton BLS/hr Outlet

no PM 2009 No. 4 Smelt Dissolving Tank unspecified 09/23/2009 EPA\ODEQ M5 53.8 ton BLS/hr Outlet

No PM 2004 No. 2 Smelt Dissolving Tank unspecified 09/08/2004 M5 60.25 ton BLS/hr Outlet

No PM 2004 No. 1 Smelt Dissolving Tank unspecified 09/07/2004 M5 60.29 ton BLS/hr Outlet

No PM 2011 No. 3 Smelt Dissolving Tank 06/21/2011 M5 48.48 ton BLS/hr Outlet

No PM 2011 No. 1 Smelt Dissolving Tank 06/23/2011 M5 30.30 ton BLS/hr Outlet

No PM 2011 No. 2 Smelt Dissolving Tank 06/22/2011 M5 29.83 ton BLS/hr Outlet

No PM 2011 Smelt Dissolving Tank 02/16/2011 M5 110.80 ton BLS/hr Outlet

No PM 2010 No. 4 Recovery Smelt Dissolver 08/31/2010 M5 27.50 ton BLS/hr Outlet

No PM 2010 No. 4 Recovery Smelt Dissolver 09/16/2010 M5 27.19 ton BLS/hr Outlet

Yes

Scrubber design reviewedand improvements madeto scrubber damper andspray nozzle locations. PM 2004 Smelt Dissolving Tank 09/10/2004 M5 45.09 ton BLS/hr Outlet

Yes PM 2010 Smelt Dissolving Tank 10/06/2010 M5 52.71 ton BLS/hr Outlet

No PM 2011 Smelt Dissolving Tank 03/31/2011 ODEQ M5 52.92 ton BLS/hr Outlet

No PM 2011 Smelt Dissolving Tank 03/31/2011 ODEQ M5 52.92 ton BLS/hr Outlet

No PM 2003 No. 3 Smelt Dissolving Tank Vent 06/30/2003 M5 66.50 ton BLS/hr Outlet

no PM 2009 No. 1 Smelt Dissolving Tank 11/05/2009 M5 16.85 ton BLS/hr Outlet

no PM 2009 No. 2 Smelt Dissolving Tank 11/05/2009 M5 17.72 ton BLS/hr Outlet

no PM 2009 No. 3 Smelt Dissolving Tank 11/04/2009 M5 26.90 ton BLS/hr Outlet

No PM 2007 Smelt Dissolving Tank 03/07/2007 M5 66.30 ton BLS/hr Outlet

No PM 2004 No. 1 Smelt Dissolving Tank 03/09/2004 M5 35.46 ton BLS/hr Outlet

No PM 2004 No. 1 Smelt Dissolving Tank 05/05/2004 M5 35.41 ton BLS/hr Outlet

No PM 2004 No. 2 Smelt Dissolving Tank 03/10/2004 M5 35.68 ton BLS/hr Outlet

No PM 2004 No. 2 Smelt Dissolving Tank 05/06/2004 M5 35.10 ton BLS/hr Outlet

No PM 2005 Smelt Dissolving Tank 08/23/2005 M5 32.40 ton BLS/hr Outlet

no NA PM 2011 Smelt Dissolving Tank 01/17/2011 M5 72.03 ton BLS/hr Outlet

no PM 2009 No. 2 Smelt Dissolving Tank 07/08/2009 M5 27.19 ton BLS/hr Outlet

no PM 2009 No. 3 Smelt Dissolving Tank 07/07/2009 M5 27.64 ton BLS/hr Outlet

no PM 2009 No. 4 Smelt Dissolving Tank 07/06/2009 M5 84.05 ton BLS/hr Outlet

No NA PM 2001 Smelt Dissolving Tank 12/19/2000 M5 41.67 ton BLS/hr Outlet

No NA PM 2004 Smelt Dissolving Tank 09/30/2004 M5 44.30 ton BLS/hr Outlet

no PM 2009 No. 3 Smelt Dissolving Tank 03/24/2009 M5 116.57 ton BLS/hr Outlet

No PM 2004 Smelt Tank No. 1, West 08/27/2004 M5 44.58 ton BLS/hr OutletNo PM 2004 Smelt Tank No. 1, West 08/31/2004 M5 61.46 ton BLS/hr OutletNo PM 2004 Smelt Tank No. 2, East 08/25/2004 M5 31.46 ton BLS/hr Outlet

No PM 2004 Smelt Tank No. 2, East 08/26/2004 M5 45.42 ton BLS/hr OutletNo PM 2004 Smelt Tank No. 2, East 10/26/2004 M5 45.42 ton BLS/hr OutletNo PM 2004 Smelt Tank No. 2, West 08/25/2004 M5 31.46 ton BLS/hr OutletNo PM 2004 Smelt Tank No. 2, West 08/26/2004 M5 45.42 ton BLS/hr OutletNo PM 2004 Smelt Tank No. 2, West 10/21/2004 M5 45.42 ton BLS/hr OutletNo PM 2011 No. 1 Smelt Dissolving Tank 06/06/2011 M5 29.45 ton BLS/hr Outlet

No PM 2011 No. 2 Smelt Dissolving Tank 06/06/2011 M5 30.14 ton BLS/hr Outlet

No PM 2009 Smelt Dissolving Tank No. 2 10/15/2009 M5 44.95 ton BLS/hr Outlet

no PM 2004 No. 3 Smelt Dissolving Tank 09/03/2004 M5 110.14 ton BLS/hr Outlet

No PM 2011 No. 3 Smelt Dissolving Tank 06/15/2011 M5 76.25 ton BLS/hr

converted from 3.66 millionlb/day Outlet

No PM 2004 Smelt Dissolving Tank 08/19/2004 M5 92.59 ton BLS/hr Outlet

No PM 2010 Smelt Dissolving Tank 07/20/2010 M5 50.51 ton BLS/hr Outlet

no PM 2005 No. 10 Smelt Dissolving Tank 01/25/2005 M5 53.57 ton BLS/hr Outlet

no PM 2005 No. 10 Smelt Dissolving Tank 11/17/2005 M5 unspecified Production values are reserved Outlet

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

206.G‐36

206.G‐36

606.SDT2606.SDT2606.SDT3606.SDT3606.SDT4606.SDT4610.10610.10610.9610.9613.005613.006613.007613.008145.56132.4SDT

Has the configuration of

the emission unit,

combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date

(mm/dd/yyyy)

Emission Test

Method

AverageHourly Production

Rate(value)

Hourly Production

Rate(units) Production comment

Are inlet or

outlet dataprovided?

no PM 2005 No. 11 Smelt Dissolving Tank 01/26/2005 M5 57.16 ton BLS/hr Outlet

no PM 2005 No. 11 Smelt Dissolving Tank 11/20/2005 M5 unspecified Production values are reserved Outlet

no PM 2010 No. 2 Smelt Dissolving Tank 03/19/2010 M5 47.70 ton BLS/hr Outlet

no PM 2011 No. 2 Smelt Dissolving Tank 04/05/2011 M5 44.00 ton BLS/hr Outlet

no PM 2005 No. 3 Smelt Dissolving Tank 10/25/2005 M5 40.90 ton BLS/hr Outlet

no PM 2010 No. 3 Smelt Dissolving Tank 07/25/2010 M5 39.00 ton BLS/hr Outlet

no PM 2006 No. 4 Smelt Dissolving Tank 07/20/2006 M5 66.00 ton BLS/hr Outlet

no PM 2010 No. 4 Smelt Dissolving Tank 10/25/2010 M5 62.50 ton BLS/hr Outlet

no PM 2009 No. 2 Smelt Dissolving Tank 07/09/2009 M5 64.20 ton BLS/hr Outlet

no PM 2009 No. 2 Smelt Dissolving Tank 07/09/2009 M5 64.40 ton BLS/hr Outlet

no PM 2009 No. 1 Smelt Dissolving Tank 07/08/2009 M5 46.00 ton BLS/hr Outlet

no PM 2009 No. 1 Smelt Dissolving Tank 07/08/2009 M5 45.80 ton BLS/hr Outlet

No PM 2009 No. 1 Smelt Dissolving Tank ‐ Left Side 10/29/2009 M5 unspecified no production data given Outlet

No PM 2009 No. 1 Smelt Dissolving Tank ‐ Right Side 10/29/2009 M5 unspecified no production data given Outlet

No PM 2009 No. 2 Smelt Dissolving Tank ‐ Left Side 10/29/2009 M5 unspecified no production data given Outlet

No PM 2009 No. 2 Smelt Dissolving Tank ‐ Right Side 10/29/2009 M5 unspecified no production data given OutletNo PM 2005 No. 2 RB SDT 10/26/2005 M5 37.9 ton BLS/hr Outlet

PM 2009 SDTV No. 4 6/15/2009 M5 66.76 ton BLS/hr Outlet

Test_data_memo_appendices.xlsx App C SDT PM 
atter

RTI+EUID105.EU445D107.09‐P2

109.SDT3109.SDT4109.SDT3111.G‐127

166.ST01166.ST02174.G‐63B

174.G‐63C

174.G‐63C

174.G‐63B

174.G‐63C

174.G‐63C

124.020124.021340.007340.007100.109112.AA‐101114.U508115.SM01115.SM01116.004116.004119.EQT005119.EQT011120.M3126.SDT127.SDT1131.SDT4N131.SDT4S131.SDT5132.4SDT132.5SDT136.EU 031137.204138.003

Inlet ‐ Testing Methodology Data Inlet ‐ Average Stack Gas Parameters Inlet ‐ Average Emissions DataAverage Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

142.P7413146.10146.10146.17147.161147.244148.002148.008149.P005150.CREC‐2b

150.CREC‐2a

154.P38 ‐ Smelt

Dissolving Tank 3

155.SDT156.SMEL18156.SMEL18156.SMEL19156.SMEL19156.SMEL19156.SMEL19156.SMEL19156.SMEL22156.SMEL22156.SMEL22156.SMEL22156.SMEL22162.381C162.382B163.SD1902163.SD1903

Average Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

163.SD2906164.P08164.P10165.000008165.000014169.06169.07172.ST01175.ST2A177.EU0805179.SDT179.SDT180.D002, D907

181.11181.11181.11181.51181.51181.51181.51182.110185.05185.05185.05185.05185.05185.05186.RB17186.RB17189.SN27189.SN28190.R404190.R406196.SN‐08North

196.SN‐08South

198.020

Average Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

200.007_8, 007_9

202.Smelt DissolvingTank EU322

203.2DTScr

203.3DTScr207.108226.SDT1N226.SDT1S226.SDT2240.RF02240.RF05240.RF06242.AA‐012243.R403243.R408531.RF10600.G0805600.G0807615.25617.P21208228535.002208228535.002208228535.008105.EU445D105.EU445BEast105.EU445BWest121.000009121.000010121.000009121.000010102.SDTV10178.08T014178.08T015190.R404105.EU445D

Average Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

105.EU445D105.EU445D105.EU445D178.08T015178.08T014130.11130.6130.7135.007‐1, 007‐2

137.157137.157139.03140.57140.57140.57142.P7236143.7005143.7015143.7025152.04154.P32 ‐ Smelt

Dissolving Tank 1

154.P32 ‐ Smelt

Dissolving Tank 1

154.P35 ‐ Smelt

Dissolving Tank 2

154.P35 ‐ Smelt

Dissolving Tank 2

157.SDT167.007SDT171.006171.007171.008173.SDT173.SDT175.ST3A184.SDT1184.SDT1184.SDT2a184.SDT2a184.SDT2a184.SDT2b184.SDT2b184.SDT2b188.015SD1188.017SD2190.R405196.SN‐15

199.004201.SR0034205.010206.G‐35

206.G‐35

Average Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

206.G‐36

206.G‐36

606.SDT2606.SDT2606.SDT3606.SDT3606.SDT4606.SDT4610.10610.10610.9610.9613.005613.006613.007613.008145.56132.4SDT

Average Sampling RunLength_Inlet(mins)

Average Fraction ofIsokinetic SamplingRate_Inlet(%)

AverageAirflowRate_Inlet(acfm)

AverageAirflow Rate_Inlet(dscfm)

AverageGasMoisture_Inlet(%)

AverageGas Temp_Inlet(F)

Average GasPressure_Inlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Inlet(%)

Average_Inletconcentration

Average Inletconcentrationunits

Number of

Inlet Test Runs

Count Inlet

Non‐Detect

Runs

Average_Inlet(lb/hr)

Average_Inlet(lb/production)

AverageLb/Productiounits

Test_data_memo_appendices.xlsx App C SDT PM 
atter

RTI+EUID105.EU445D107.09‐P2

109.SDT3109.SDT4109.SDT3111.G‐127

166.ST01166.ST02174.G‐63B

174.G‐63C

174.G‐63C

174.G‐63B

174.G‐63C

174.G‐63C

124.020124.021340.007340.007100.109112.AA‐101114.U508115.SM01115.SM01116.004116.004119.EQT005119.EQT011120.M3126.SDT127.SDT1131.SDT4N131.SDT4S131.SDT5132.4SDT132.5SDT136.EU 031137.204138.003

Outlet ‐ Testing Methodology Data Outlet ‐ Average Stack Gas Parameters Outlet ‐ Average Emissions Data 

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic Sampling

Rate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐Detect

Runs

Average_Outlet(lb/hr)

Average_(lb/produ

76 108 24663 10215 49.3 179.28 29.6 0.03 20.95 0.0751 gr/dscf 3 0 6.58 60 102.4 21808 4934 71.6 197.6 29.676 unspecified unspecified 0.309 gr/dscf 3 0 13.03 

60 99.37 17287 8689.67 38.97 169.9 29.4 0 21 0.0524 gr/dscf 3 0 3.9 

61.3 99.3 27746.67 11488 49.03 179.5 29.4 0 21 0.0493 gr/dscf 3 0 4.89 

65 107 15696.67 7576 40.93 170.92 29.23 0 21 0.057 gr/dscf 3 0 3.72 

62 97.83 26630 20899 29.82 183.7 29.69 0 20.7 0.0218 gr/dscf 3 0 3.91 60 100.2 42564 24297 32.8 159.2 29.53 0 20.9 0.048 gr/dscf 3 0 9.9 60 101.8 31171 13241 48.6 176.5 29.44 0 20.9 0.114 gr/dscf 3 0 12.9 60 102.1 31058 20165 24.7 152.1 29.91 0 20.9 0.057 gr/dscf 3 0 9.9 60 97.1 29005 17125 35.8 158.3 30.08 0 20.9 0.04 gr/dscf 3 0 5.8 60 103.9 27430 16752 29 158.8 30.2 0 20.9 0.029 gr/dscf 3 0 4.2 60 100.4 29487 18229 28 155.9 30 0 20.9 0.073 gr/dscf 3 0 11.5 60 100.7 29625 15171 38.9 169 29.91 0 20.9 0.0384 gr/dscf 3 0 5 60 98.5 28472 16983 32.2 157.1 29.91 0 20.9 0.0293 gr/dscf 3 0 4.26 66 95.1 47994 30916 24.6 156.4 29.84 0 20.9 0.0209 gr/dscf 3 0 5.541 

68 99.7 47828 30980 24.8 146.8 29.63 0 20.9 0.0203 gr/dscf 3 0 5.393 60 107 21177 10517 40.57 174 30.03 0 20.9 0.086 gr/dscf 3 0 7.74 

60 105 23025 12115 37 170 29.872 0 20.9 0.078 gr/dscf 3 0 8.19 

92 95.53333333 12566.66667 4590 53.2 179.3333333 28.32 0.4 19.7 0.078566667 gr/dscf 3 0 3.066666667 0.05

62 95.82 85119 47483 34.46 165.8 30.23 0 20.5 0.0321 gr/dscf 3 0 12.98 0.1

61.33333333 94.6 34685 19715 33.46666667 159.3333333 30.00666667 0 21 0.0818 gr/dscf 3 0 13.82 

77.66666667 99.5 19046 9545 40.5 167.6 29.94 0 20.9 0.044 gr/dscf 3 0 3.608 0.04

77 98.7 18998 10564 34.4 162.9 29.94 0 20.9 0.0316 gr/dscf 3 0 2.86 0.03

60 95.7 47368 28533 29.8 157.6 30 0 20.9 0.02971602 gr/dscf 3 0 7.28 

61 104 43008 25031 31.8 161 30.06 0 20.9 0.041 gr/dscf 3 0 8.81 

64.33333333 101.2 30237 21233 20.1 144 0 20.73 0.05327 gr/dscf 3 0 9.998 unspecifie

63 96.33 33161 15754 43.3 173 0 20.77 0.09041 gr/dscf 3 0 12.209 unspecifie60 100.1 26374 7529 64.2 190.2 29.41 0.5 20 not provided 3 0 not provided 

60 96.21666667 42308 30776 18.11 134.31 29.36 0 20.77 0.0323 gr/dscf 3 0 8.355 0.16

60 100.3 24923 14886 30.3 157.8 30.02 0 20.9 0.0306 gr/dscf 3 0 3.89 0.05

65 97.6 17400 11900 21.2 144 29.73 0 20.8 0.018 gr/dscf 3 0 1.8 0.02

65 99.1 20200 12000 31.6 157 29.72 0 20.8 0.041 gr/dscf 3 0 4.2 0.0665 100.2 29300 16200 36.7 163 29.98 0 20.8 0.028 gr/dscf 4 0 3.8 0.06

60 92.93 40442 26802 22.65 154.64 29.83 0.0091 gr/dscf 3 0 2.079 

60 98.77666667 31913 17033 36.92 166.53 29.88 0.0699 gr/dscf 3 0 10.141 

76.33333333 105.4 34300 11500 57.01333333 183.6666667 28.57 0.233333333 19.73333333 0.116 gr/dscf 3 0 11.5 

72 101 29000 11400 51.2 179 29.24 0.03 20.95 0.097 gr/dscf 3 0 9.5 60 104.0433333 5928.966667 55.96 199.9966667 30.1 1.1 19 0.0886 gr/dscf 3 0 4.48 0.07

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

142.P7413146.10146.10146.17147.161147.244148.002148.008149.P005150.CREC‐2b

150.CREC‐2a

154.P38 ‐ Smelt

Dissolving Tank 3

155.SDT156.SMEL18156.SMEL18156.SMEL19156.SMEL19156.SMEL19156.SMEL19156.SMEL19156.SMEL22156.SMEL22156.SMEL22156.SMEL22156.SMEL22162.381C162.382B163.SD1902163.SD1903

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐Detect

Runs

Average_Outlet(lb/hr)

Average_(lb/produ

180 94 30089 17286 31.4 160 29.45 0 20.9 0.054 gr/dscf 3 0 7.97 

67.66666667 101.8 25775 13962 34.9 145.9 28.54 0 20.9 0.0231 gr/dscf 3 0 2.767 0.03

64.33333333 107.5 24615 14234 30.1 148.8 28.55 0 20.9 0.0152 gr/dscf 3 0 1.848 0.02

67.66666667 101 36256 16907 41.6 175.6 28.76 0.2 20.6 0.0456 gr/dscf 3 0 6.578 0.05

45 106.3 21046 9740 165.33 29.91 0 20.9 0.0684 gr/dscf 2 0 5.71 

45 92.9 16996 9625 159.33 29.91 0 20.9 0.062 gr/dscf 2 0 5.15 

66 95.1 25147 12449 41.3 171.66 30.14 0 20.9 0.0499 gr/dscf 3 0 5.3 

74.33333333 99.1 24502 7384 61.8 190 29.11 0 20.9 0.1904 gr/dscf 4 0 12.04 0.1462.66666667 99.9 17100 6680 50.2 178 28.37 0 20.8 0.122255489 gr/dscf 3 0 7 0.10

60 103.7 16222 6791 48.9 187 30.02 0 20.9 0.0637 gr/dscf 3 0 3.7 

60 107.2 14429 5173 56 190 30.03 0 20.9 0.104 gr/dscf 3 0 4.6 

62 111.7 13869 7159 37.1 175.9 29.59 0.2 20.4 0.0206 gr/dscf 4 0 1.265 

62 103.2 34390 15416 44.7 191.33 29.92 0.1 20.6 0.054 gr/dscf 5 0 6.95 

60 103.1 24168 17618 19 133 30.57 0.1 20.9 0.0249 gr/dscf 3 0 3.77 

60 103.1 24329 17185 19.6 137 30.06 0.1 20.9 0.0257 gr/dscf 3 0 3.83 

60 106.4 23424 15631 23.9 141 30.12 0.1 20.9 0.0253 gr/dscf 3 0 3.4 

60 110.3 22834 13087 32.9 156 29.86 0.1 20.9 0.0394 gr/dscf 3 0 4.42 

60 108.6 24038 14251 31.5 159 30.12 0.1 20.9 0.0476 gr/dscf 3 0 6.34 

60 116.6 19118 10666 34.1 156 29.87 0.1 20.9 0.0595 gr/dscf 3 0 5.54 

60 113 22697 12568 34.3 158 30.01 0.1 20.9 0.0359 gr/dscf 3 0 3.79 

60 131.8 18347 7806 49 166 29.94 0.1 20.9 0.0701 gr/dscf 3 0 4.63 

60 108.3 17225 9113 36.6 161 29.94 0.1 20.9 0.0555 gr/dscf 3 0 4.32 

60 119.6 17245 8392 41.5 171 30.17 0.1 20.9 0.0484 gr/dscf 3 0 3.48 

60 105.9 14795 7011 43.2 169 30.11 0.1 20.9 0.0483 gr/dscf 3 0 2.89 

60 106.1 17811 9603 35.8 158.6666667 29.94 0.1 20.9 0.0469 gr/dscf 3 0 3.85 

64 99 33126 16543 39.2 172.8 29.52 0 20.9 0.0506 gr/dscf 3 0 7.2 

60 100 53063 26930 41.9 171.1 29.88 0 20.9 0.0493 gr/dscf 3 0 11.4 

65.66666667 102.6 16534 10801 24.3 151.3333333 29.94 0 20.9 0.019 gr/dscf 3 0 1.78 unspecifie65.66666667 102.6 24170 16563 21.6 144.3333333 29.94 0 20.9 0.02 gr/dscf 3 0 2.82 unspecifie

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

163.SD2906164.P08164.P10165.000008165.000014169.06169.07172.ST01175.ST2A177.EU0805179.SDT179.SDT180.D002, D907

181.11181.11181.11181.51181.51181.51181.51182.110185.05185.05185.05185.05185.05185.05186.RB17186.RB17189.SN27189.SN28190.R404190.R406196.SN‐08North

196.SN‐08South

198.020

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐Detect

Runs

Average_Outlet(lb/hr)

Average_(lb/produ

62 100.8 42577 23498 34.9 164 30.02 0 20.9 0.0482 gr/dscf 3 0 9.69 0.14

61 99.5 8678 5025 30 160.9 29.1 0 20.8 0.04724 gr/dscf 3 0 2.0373 unspecifie

61 99.06666667 12317 6273 38 169.2 29.3 0 20.8 0.05742 gr/dscf 3 0 3.0941 unspecifie

63.66666667 103 43333 27737 25.1 148.8 29.52 0 20.9 0.036 gr/dscf 3 0 8.64 

67 99 26406 16183 28.4 154.5 29.85 0 20.9 0.039 gr/dscf 3 0 5.38 

60 99.3 36073 21506 29.3 156.1 29.52 0 20 0.052 gr/dscf 3 0 9.605 0.12

60 100.4 41381 24713 29.6 156.7 29.61 0 20 0.0618 gr/dscf 3 0 13.06 0.16

66.33333333 96.4 15678 9349 30.3 158 29.96 0 20.9 0.042 gr/dscf 3 0 3.33 unspecifie62.33333333 99.3 45138 32927 18.1 85 30.28 0 20.9 0.0213 gr/dscf 4 0 6.03 63.66666667 94.2 33735 16415 40 171.9 29.03 0.1 20.3 0.0204 gr/dscf 3 0 2.864 

60 97.7 36585 17457 42.1 171.3 29.5 0 20.9 0.049 gr/dscf 3 0 7.33 0.07

60 98.5 36744 17473 42 173 29.51 0 20.9 0.044 gr/dscf 3 0 6.56 0.07

60 98.3 22043 10922 40.8 170.2 29.82 0 21 0.037 gr/dscf 3 0 3.5 

75.66666667 103.7 26072 11400 51 180.3 30.24 0 20.9 0.1082 gr/dscf 3 0 10.6 

68 100.4 21433 9613 46 180 30.31 0 20.9 0.0872 gr/dscf 3 0 6.9 

60 94 23217 11021 42.1 177 29.5385 0 20.9 0.066 gr/dscf 3 0 6.202 

68 105.3 16162 8294 38.4 174.4 29.94 0 20.9 0.1632 gr/dscf 3 0 11.6 

64 103 17840 9761 35 169 29.98 0 20.9 0.088 gr/dscf 3 0 7.4 

60 101.9 18899 9922 37 172 29.98 0 20.9 0.1252 gr/dscf 3 0 10.7 

60 97 23193 13228 31.3 166 29.46 0 20.9 0.046 gr/dscf 3 0 5.24 

72 99.23333333 17507 8676.333333 40.5 169.3333333 29.74 0.133333333 19.76666667 0.0624 gr/dscf 3 0 4.6491 

60 96.4 7126 40.93333333 170.33 29.99 0.03 20.95 0.057333333 gr/dscf 3 0 3.474 0.06

60 95.03333333 7542 45.85333333 177.33 30.25 0.03 20.95 0.071666667 gr/dscf 3 0 4.588 0.08

60 95.76666667 8305.666667 45.6 176 30.01 0.03 20.95 0.059666667 gr/dscf 3 0 4.264333333 

60 97.63333333 6511.666667 42.2 172.663 29.84 0.03 20.95 0.046 gr/dscf 3 0 2.571 0.04

60 97.33333333 7486.333333 40.91666667 170.33 29.72 0.03 20.95 0.046333333 gr/dscf 3 0 2.968666667 0.05

60 93.7 8583.666667 43.12666667 173.663 29.9 0.03 20.95 0.057333333 gr/dscf 3 0 4.161666667 0.07

60 105.18 51663 28407 34.86 166.8 29.99 0 20.5 0.0422 gr/dscf 3 0 10.28 0.08

73.66666667 101.1 50848 24161 43 172 29.7 0.1 20 0.058 gr/dscf 3 0 12 53.33333333 94.35666667 20263 9488.783333 44.52 166 29.94 0 20 0.0715 gr/dscf 3 0 5.8 62.66666667 108 27722 12852.91667 45.44 165 30.01 0 20 0.1054 gr/dscf 3 0 11.41 

65 100.2 24666 13726 34 162.66 29.7 0 20.9 0.0209 gr/dscf 3 0 2.45 

65 97.3 33008 20704 25.5 149.33 29.08 0.3 20.6 0.0598 gr/dscf 3 0 10.6 

60 103.1 23769 12116 39.1 169.5 29.89 0 21 0.0687 gr/dscf 3 0 7.12 0.08

60 104.9 25487 13678 36.3 165.6 29.86 0 21 0.0487 gr/dscf 3 0 5.61 0.07

60 102.1 28463 9400 58.3 187.4 29.024 0.44 19.54 0.1302 gr/dscf 3 0 10.42 

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

200.007_8, 007_9

202.Smelt DissolvingTank EU322

203.2DTScr

203.3DTScr207.108226.SDT1N226.SDT1S226.SDT2240.RF02240.RF05240.RF06242.AA‐012243.R403243.R408531.RF10600.G0805600.G0807615.25617.P21208228535.002208228535.002208228535.008105.EU445D105.EU445BEast105.EU445BWest121.000009121.000010121.000009121.000010102.SDTV10178.08T014178.08T015190.R404105.EU445D

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐Detect

Runs

Average_Outlet(lb/hr)

Average_(lb/produ

64 95.1 53607 27322 37.9 168 29.21 0 20.9 0.0279 gr/dscf 3 0 6.5 

60 102.8 28600 16200 30.8 158 28.73 0.1 20.7 0.033 gr/dscf 3 0 4.55 

60 91 9829 19.1 141 30.43 0 20.9 0.007 gr/dscf 1 0 0.6 unspecifie60 97 30906 24.5 152 29.93 0 20.9 0.019 gr/dscf 3 0 5.1 

80 99.64 8381 4596 35.21 166.81 30.12 0 20.5 0.0486 gr/dscf 3 0 1.92 

60 99.9 19843 12917 24.9 150.6 29.98266667 0 20.9 0.0458 gr/dscf 3 0 5.028 

60 101.6 15039 8559 33 162.5 29.941 0 20.9 0.0784 gr/dscf 3 0 5.71 

60 105 22486 10899.66667 41.63333333 173.6 29.816 0 20.9 0.0482 gr/dscf 3 0 4.4981 0.08

60 100.3 46166 30312 23.9 147.5 29.72 0 20.9 0.0244 gr/dscf 3 0 6.3 

60 96 31313 17080 34.7 165 29.59 0 20.9 0.051 gr/dscf 3 0 7.51 60 101 32674 17508 36 164.2 29.59 0 20.9 0.047 gr/dscf 3 0 7.08 72 108.1 27704 9085 59.2 191.1 29.76 0 20.9 0.1361 gr/dscf 3 0 10.6 

60 98.6 35600 19548 34.7 166.5 29.87 0 20.9 0.031 gr/dscf 3 0 5.17 

60 100.5 24431 12046 40.5 172.4 29.71 0 20.9 0.181 gr/dscf 3 0 18.77 

60 101.3 36176 13841 53.4 181.9 29.89 0 20.9 0.0549 gr/dscf 3 0 6.5 

60 96.4 23980 9855 49.1 180.7 29.41 0 20.9 0.057 gr/dscf 3 0 4.81 

60 98.5 31970 7627 69.3 195.8 29.06 0 20.9 0.074 gr/dscf 3 0 4.782 

60 100.2 33330 22241 23.3 147.3 29.96 0.02 20.54 0.0345 gr/dscf 3 0 6.58 

65 103.2666667 20793.66667 10676.66667 39.36666667 164.8333333 28.99 0.166666667 20.4 0.0182 gr/dscf 3 0 1.6562 

61 99.3 37174 18322 40.7 179.6666667 30.1 0 20.9 0.044 gr/dscf 3 0 6.9 

64 105 29124 10076 57.3 192 29.9 0 20.9 0.043 gr/dscf 3 0 3.74 

60 100.5 57601 31721 34.7 163.3333333 29.85 0 20.9 0.0178 gr/dscf 3 0 8.81 

63 96.0 26490 11921 45.14 174.25 29.50 0.03 20.95 0.0686 gr/dscf 3 0 7.01 0.1060 94 12661 7594 25.92 160.86 29.25 0.03 20.95 0.063 gr/dscf 3 0 4.12 60 90.9 21268 13844 22.81 153.14 29.26 0.03 20.95 0.0416 gr/dscf 3 0 4.84 60 102 16625 8510 39 167 29.63 0 20.8 0.03 gr/dscf 3 0 2.2 0.0660 103 20428 11900 32 160 29.86 0 20.8 0.032 gr/dscf 3 0 3.3 0.0960 102 19705 10700 36 168 30.47 0 20.8 0.047 gr/dscf 3 0 4.3 0.160 100 22024 13900 28 157 30.57 0 20.3 0.021 gr/dscf 3 0 2.5 0.0660 101 37092 21902 31.17 161 30.21 13.9 7 0.025 gr/dscf 3 0 4.71 0.0360 96 28285 14436 38 170 29.49 0 20.9 0.068 gr/dscf 3 0 8.3 

60 95 27512 12667 44 178 29.49 0 20.9 0.071 gr/dscf 3 0 7.7 60 97.5 31294.3 18467.7 30.5 157.8 29.71 0 20.9 0.02 gr/dscf 3 0 3.158 

67.3 99.4 25397 11266 45.79 173.14 29.36 0.03 20.95 0.0867 gr/dscf 3 0 8.4 

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

105.EU445D105.EU445D105.EU445D178.08T015178.08T014130.11130.6130.7135.007‐1, 007‐2

137.157137.157139.03140.57140.57140.57142.P7236143.7005143.7015143.7025152.04154.P32 ‐ Smelt

Dissolving Tank 1

154.P32 ‐ Smelt

Dissolving Tank 1

154.P35 ‐ Smelt

Dissolving Tank 2

154.P35 ‐ Smelt

Dissolving Tank 2

157.SDT167.007SDT171.006171.007171.008173.SDT173.SDT175.ST3A184.SDT1184.SDT1184.SDT2a184.SDT2a184.SDT2a184.SDT2b184.SDT2b184.SDT2b188.015SD1188.017SD2190.R405196.SN‐15

199.004201.SR0034205.010206.G‐35

206.G‐35

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐Detect

Runs

Average_Outlet(lb/hr)

Average_(lb/produ

76.7 102.4 23382 10871 43.98 174.17 29.83 0.03 20.95 0.073 gr/dscf 3 0 6.79 

65.7 100.5 25386 10659 48.62 178.53 29.58 0.03 20.95 0.0714 gr/dscf 3 0 6.51 

63 96.1 28244 12796 44.58 176.39 29.50 0.03 20.95 0.0523 gr/dscf 3 0 5.73 

60 98.5 21700 11117 44.6 166.6 29.44 0 20.9 0.032 gr/dscf 3 0 3.06 

60 93.2 20004 8915 56.6 174.3 29.49 0 20.9 0.075 gr/dscf 3 0 5.78 

63.33 97.80 22731 14142 27.80 153.3 29.96 0.10 21.10 0.0597 gr/dscf 4 0 7.24 

63.33 97.70 16505 10208 28.00 154.3 29.99 0.05 21.50 0.0522 gr/dscf 3 0 4.56 

63.33 100.00 20585 12256 30.30 157.7 29.89 0.07 20.80 0.0675 gr/dscf 3 0 7.1 75.67 97.80 30371 11297 55.20 185.3 30.34 0.30 19.90 0.05 gr/dscf 3 0 4.8 

60.00 100.50 16800 10800 24.70 152.0 29.49 0.03 20.95 0.011 gr/dscf 2 0 1.005 

64.00 101.00 16452 9750 30.90 151.0 29.16 0.03 20.95 0.0103 gr/dscf 3 0 0.862 80.00 104.00 unspecified 8054 40.95 176.5 unspecified 0.00 18.80 0.107 gr/dscf 3 0 7.4 

71.00 93.00 19727 8902 45.67 176.9 unspecified 0.10 20.47 0.051 gr/dscf 3 0 3.85 

78.33 96.40 20885 9506 46.27 175.3 unspecified 0.10 20.40 0.051 gr/dscf 3 0 4.16 78.33 96.40 20885 9506 46.27 175.3 unspecified 0.10 20.40 0.068 gr/dscf 3 0 5.55 63.33 97.67 35038 22259 24.97 155.0 29.51 0.00 20.90 0.054 gr/dscf 3 0 10.31 62.67 105.00 12816 9413 17.00 136.0 30.07 0.00 20.90 0.0077 gr/dscf 3 0 0.6 

61.00 101.33 12698 9458 16.00 136.7 30.07 0.00 20.90 0.0084 gr/dscf 3 0 0.7 61.00 104.00 21369 16528 14.00 130.0 30.05 0.00 21.00 0.0062 gr/dscf 3 0 0.9 64.33 99.80 34007 20199 30.30 156.9 29.70 0.00 21.00 0.086 gr/dscf 3 0 14.87 

66.00 99.40 19433 11500 28.20 158.0 28.90 0.00 20.90 0.037 gr/dscf 3 0 3.7 

65.33 101.77 20300 10800 33.90 161.0 28.46 0.00 20.90 0.059 gr/dscf 3 0 5.5 66.33 100.70 17900 10100 31.90 158.0 unspecified 0.00 20.90 0.049 gr/dscf 3 0 4.2 62.67 99.30 20200 9800 38.90 166.0 28.25 0.00 20.90 0.074 gr/dscf 3 0 6.2 67.00 100.03 10655 3961 54.50 183.0 29.76 1.50 21.00 0.1416 gr/dscf 4 0 4.8 

63.67 93.26 48779 26486 34.97 264.4 29.94 0.00 20.90 0.0423 gr/dscf 3 0 9.63 

60.00 101.80 7656 3731 41.40 170.9 29.73 0.00 21.00 0.2208 gr/dscf 3 0 7.06 

60.00 99.40 14514 8103 33.90 162.3 29.79 0.00 21.00 0.0366 gr/dscf 3 0 2.52 60.00 97.90 33417 15882 42.70 173.3 29.75 0.00 21.00 0.0659 gr/dscf 3 0 8.97 73.00 105.50 17148 10732 28.60 136.0 unspecified 0.00 20.90 0.0928 gr/dscf 3 0 8.5 

63.33 101.13 15416 9046 32.00 156.7 unspecified 0.00 20.90 0.103 gr/dscf 3 0 7.95 60.00 95.30 31536 17996 33.00 161.7 30.23 0.00 19.90 0.0520 gr/dscf 3 0 8 64.33 98.82 23573 13475 32.90 162.0 30.01 0.50 19.90 0.0635 gr/dscf 3 0 7.344 62.33 102.96 22883 11933 38.20 169.0 30.09 0.40 20.00 0.0832 gr/dscf 3 0 8.368 64.00 101.89 20400 12984 25.96 157.0 30.07 0.40 20.50 0.0655 gr/dscf 3 0 7.325 62.00 106.41 22431 12032 36.38 168.7 30.03 0.40 20.60 0.1082 gr/dscf 3 0 11.146 62.00 99.69 19835 9888 40.17 174.3 29.94 0.50 20.20 0.0935 gr/dscf 3 0 7.811 

63.00 101.47 24196 15367 26.00 157.0 30.07 0.50 20.40 0.1279 gr/dscf 3 0 16.788 

62.67 104.64 25472 15109 30.45 161.0 30.02 0.40 20.40 0.1406 gr/dscf 3 0 18.208 62.67 101.72 20865 11433 35.05 166.0 29.81 0.40 19.90 0.0506 gr/dscf 3 0 4.955 

73.33 104.40 20494 11753 32.91 161.2 30.09 0.10 20.34 0.029 gr/dscf 3 0 2.96 

72.67 98.40 19215 11406 30.67 158.5 30.09 0.10 20.51 0.029 gr/dscf 3 0 2.85 65.33 99.70 31226 19113 27.20 158.5 29.46 0.00 20.90 0.0199 gr/dscf 3 0 3.256 74.33 104.80 25400 8381 58.90 195.3 29.85 0.00 20.90 0.2152 gr/dscf 3 0 15.5 

70.00 96.67 26331 10017 55.90 180.7 29.39 0.00 20.90 0.145 gr/dscf 3 0 12.28 

65.00 91.41 59246 32913 34.45 162.6 29.90 0.00 20.90 0.0535 gr/dscf 3 0 15.09 65.00 98.80 22855 12504 35.30 165.0 unspecified 0.00 20.90 0.052 gr/dscf 3 0 5.6 

67.00 107.00 17912 10183 26.70 159.6 27.23 0.10 21.00 0.1173 gr/dscf 3 0 10.245 66.00 105.60 20862 11911 27.40 155.3 27.41 0.50 20.70 0.1064 gr/dscf 3 0 10.794 unspecifie

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

206.G‐36

206.G‐36

606.SDT2606.SDT2606.SDT3606.SDT3606.SDT4606.SDT4610.10610.10610.9610.9613.005613.006613.007613.008145.56132.4SDT

Average Sampling RunLength_Outlet(mins)

Average Fraction ofIsokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average GasPressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outletconcentration units

Number of

Outlet Test Runs

Count Outlet

Non‐Detect

Runs

Average_Outlet(lb/hr)

Average_(lb/produ

71.50 99.70 16406 7178 42.20 168.9 26.97 0.40 21.00 0.2502 gr/dscf 4 0 15.417 

64.00 100.40 22036 11115 35.50 155.9 27.28 0.20 20.80 0.114 gr/dscf 3 0 10.864 unspecifie

67.00 101.10 17146 9428 35.30 164.1 20.07 0.00 21.00 0.0527 gr/dscf 3 0 4.257 

60.00 101.32 17852 10232 32.30 164.0 29.90 0.00 20.90 0.0578 gr/dscf 4 0 5.0723 

62.67 98.33 21903 13608 29.20 154.0 29.98 0.00 20.90 0.0306 gr/dscf 3 0 3.6 

64.67 96.44 15401 10849 17.70 157.0 29.91 0.00 20.90 0.0323 gr/dscf 3 0 3.013 63.00 100.30 33283 19776 30.10 163.0 30.02 0.00 20.90 0.0385 gr/dscf 3 0 6.5 62.33 94.69 19148 18643 25.50 157.0 29.91 0.00 20.90 0.067 gr/dscf 3 0 10.8 

76.67 105.60 14602 7993 35.10 163.0 29.83 0.13 19.76 0.074 gr/dscf 3 0 5.04 64.00 102.80 13459 7790 32.80 160.9 30.00 0.21 19.60 0.052 gr/dscf 3 0 3.5 

66.00 95.00 14573 8399 31.70 160.8 29.70 0.04 20.04 0.078 gr/dscf 3 0 5.59 

63.00 96.40 16268 9877 28.60 155.7 29.69 0.10 20.08 0.066 gr/dscf 3 0 5.61 62.33 101.67 16448 7583 44.70 174.0 29.92 0.00 20.90 0.04 gr/dscf 3 0 2.69 unspecifie

62.00 99.00 17066 8859 38.10 169.0 29.91 0.00 20.90 0.027 gr/dscf 3 0 2.01 unspecifie61.67 102.00 17068 8592 39.80 172.0 29.94 0.00 20.90 0.037 gr/dscf 3 0 2.76 unspecifie62.67 97.00 18369 10404 33.10 164.0 29.93 0.00 20.90 0.021 gr/dscf 3 0 1.84 unspecifie

60 97.1 20180 12936 23 152.33 28.83 0 20.9 0.217 gr/dscf 3 0 24.1 60 97.32666667 30482 17566 31.67 163.86 29.8 unspecified unspecified 0.0198 gr/dscf 3 0 2.964 

Test_data_memo_appendices.xlsx App C SDT PM 
atter

RTI+EUID105.EU445D107.09‐P2

109.SDT3109.SDT4109.SDT3111.G‐127

166.ST01166.ST02174.G‐63B

174.G‐63C

174.G‐63C

174.G‐63B

174.G‐63C

174.G‐63C

124.020124.021340.007340.007100.109112.AA‐101114.U508115.SM01115.SM01116.004116.004119.EQT005119.EQT011120.M3126.SDT127.SDT1131.SDT4N131.SDT4S131.SDT5132.4SDT132.5SDT136.EU 031137.204138.003

Suspect Data Exclude Comment Data analysis notes Multi‐stack sums

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

105.EU445D.PM 6.58 0.1114 107.09‐P2.PM 13.03 0.1380 

109.SDT3.PM different years 3.9 0.0790 

109.SDT4.PM 4.89 0.0580 109.SDT3.PM different years 3.72 0.0840 

SDT operates with SCBR/INC_RF normally, but onlythe SDT bypass with the SCBR alone was tested as

an alternative condition. 111.G‐127.PM 3.91 0.0863 

166.ST01.PM 9.9 0.1441 166.ST02.PM 12.9 0.1568 174.G‐63B.PM different years 9.9 0.1953 174.G‐63C.PM separate stacks 

174.G‐63C.PM separate stacks 10 0.071717172 

174.G‐63B.PM different years 11.5 0.2519 

174.G‐63C.PM separate stacks 

174.G‐63C.PM separate stacks 9.26 0.066284896 

124.020.PM 5.541 0.0951 124.021.PM 5.393 0.0929 340.007.PM different years 7.74 0.1611 

340.007.PM different years 8.19 0.1647 

Stack moisture: AVERAGE(65.1,60.6,59.8)=61.83,

but used lower 53.2 at sat. 100.109.PM 3.066666667 0.0533 

smelt dissolving tank rebuilt in 2009 following

testing. 112.AA‐101.PM 12.98 0.1108 

114.U508.PM 13.82 0.1300 115.SM01.PM separate stacks 

115.SM01.PM separate stacks 6.468 0.07392 

116.004.PM different years 7.28 0.0763 

116.004.PM different years 8.81 0.0930 

pdf pg 37 references unit‐operating data, but no

data are included; however, they did provide

"Normal Operating Rate" on pdf pg. 52 but it is

dated 7/8/03 119.EQT005.PM 9.998 unspecified 

pdf pg 37 references unit‐operating data, but no

data are included; however, they did provide

"Normal Operating Rate" on pdf pg. 52 but it is

dated 7/8/03. Test report summary said "gr/dscf

@ 8% O2" but the calculations in in the appendix

confirmed actual %O2. 119.EQT011.PM 12.209 unspecified 

No concentration data provided 120.M3.PM not provided 0.0500 

126.SDT.PM 8.355 0.1619 127.SDT1.PM 3.89 0.0547 

SDT 4 has two stacks (north and south) 131.SDT4N.PM 

SDT 4 has two stacks (north and south) 131.SDT4S.PM 6 0.0944 

(1) 2003 report not found‐‐used 2004 report

instead. (2) "After completion of Run 3, filterdestroyed during transfer to trailer. Run 3 sample

invalid" (pdf pg 524) Run 3 data not included in

report 131.SDT5.PM 3.8 0.0604 

132.4SDT.PM 2.079 0.0328 132.5SDT.PM 10.141 0.1370 136.EU 031.PM 11.5 0.1000 137.204.PM 9.5 0.1000 138.003.PM 4.48 0.0786 

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

142.P7413146.10146.10146.17147.161147.244148.002148.008149.P005150.CREC‐2b

150.CREC‐2a

154.P38 ‐ Smelt

Dissolving Tank 3

155.SDT156.SMEL18156.SMEL18156.SMEL19156.SMEL19156.SMEL19156.SMEL19156.SMEL19156.SMEL22156.SMEL22156.SMEL22156.SMEL22156.SMEL22162.381C162.382B163.SD1902163.SD1903

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

New stack and scrubber specific to SDT‐1 installed

during 2011. Emissions are from 2 SDTs with a combined stack. 142.P7413.PM 7.97 0.1080 

SDT has 2 stacks. Test report has 0.0722 lb/TBLS ‐ 

twice the value calculated here. However, thetotal for both vents 0.0602 lb/TBLS matches ourcalculated totals. Use our calculated emission

factors. 146.10.PM separate stacks 

SDT has 2 stacks. Test report has 0.0480 lb/TBLS ‐ 

twice the value calculated here. However, the

total for both vents 0.0602 lb/TBLS matches ourcalculated totals. Use our calculated emissionfactors. 146.10.PM separate stacks 4.615 0.060130329 

146.17.PM 6.578 0.0575 

Yes

Facility performed 2 45‐minute runs for each, and

did not provide detailed report (only provided

summary tables) 147.161.PM 5.71 0.0993 

Yes

Facility performed 2 45‐minute runs for each, and

did not provide detailed report (only providedsummary tables) 147.244.PM 5.15 0.1358 

148.002.PM 5.3 0.0909 

4 runs were condcued but Run #2 was not included

in results average due to expectation of finalcalculated isokinetic sample rate exceeding 110%. 148.008.PM 12.04 0.1481 

149.P005.PM 7 0.1024 

150.CREC‐2b.PM

Separate stacks: The smelt dissolving tank

emission unit id CREC‐2 has two identical

stacks (CREC‐2a and CREC‐2b) and each

stack has an identical scrubber (SCRBSTaand SCRBSTb). 

150.CREC‐2a.PM

Separate stacks: The smelt dissolving tank

emission unit id CREC‐2 has two identical

stacks (CREC‐2a and CREC‐2b) and each

stack has an identical scrubber (SCRBSTaand SCRBSTb). 8.3 0.096 

Yes Failed isokinetics

"Test 1 was not included in the average results due

to the scrubber being down" 154.P38 ‐ Smelt Dissolving Tank 3.PM 1.265 0.0370 

"Runs 1 and 3 were voided due to sub‐isokinetic

sampling rates. Additional test runs werecompmleted in order to obtain three acceptable

isokinetic sampling rate test runs" 155.SDT .PM 6.95 0.0890 

156.SMEL18.PM different dates within same year 3.77 0.0889 

156.SMEL18.PM different dates within same year 3.83 0.0901 

156.SMEL19.PM different dates within same year 3.4 0.0572 

Yes Failed isokinetics 156.SMEL19.PM different dates within same year 4.42 0.0800 

156.SMEL19.PM different dates within same year 6.34 0.0954 

Yes Failed isokinetics 156.SMEL19.PM different dates within same year 5.54 0.0963 

Yes Failed isokinetics 156.SMEL19.PM different dates within same year 3.79 0.0689 

Yes Failed isokinetics 156.SMEL22.PM different dates within same year 4.63 0.0522 

156.SMEL22.PM different dates within same year 4.32 0.0501 

Yes Failed isokinetics 156.SMEL22.PM different dates within same year 3.48 0.0419 

156.SMEL22.PM different dates within same year 2.89 0.0483 

156.SMEL22.PM different dates within same year 3.85 0.0564 

162.381C.PM 7.2 0.1435 162.382B.PM 11.4 0.1071 

(1) Only provided portion of test report, could not

determine filter temperature. (2) Did not have BLS

throughput to calculate emission factor. 163.SD1902.PM 1.78 unspecified 

(1) Only provided portion of test report, could not

determine filter temperature. (2) Did not have BLS

throughput to calculate emission factor. 163.SD1903.PM 2.82 

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

163.SD2906164.P08164.P10165.000008165.000014169.06169.07172.ST01175.ST2A177.EU0805179.SDT179.SDT180.D002, D907

181.11181.11181.11181.51181.51181.51181.51182.110185.05185.05185.05185.05185.05185.05186.RB17186.RB17189.SN27189.SN28190.R404190.R406196.SN‐08North

196.SN‐08South

198.020

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

Only provided portion of test report, could not

determine filter temperature 163.SD2906.PM 9.69 0.1486 

No production data provided 164.P08.PM 2.0373 

No production data provided 164.P10.PM 3.0941 

165.000008.PM 8.64 0.0945 165.000014.PM 5.38 0.1086 

In summary, gr/dscf were listed at 8% O2. Pulled

uncorrected gr/dscf from appendix. 169.06.PM 9.605 0.1251 

In summary, gr/dscf were listed at 8% O2. Pulleduncorrected gr/dscf from appendix. 169.07.PM 13.06 0.1651 Only provided portion of test report (3 of 37

pages), could not determine test method or filtertemperature from those 3 pages. Emission factor

in desired units of measure could not be

developed. 172.ST01.PM 3.33 4 runs total‐‐runs 2‐4 used for averages (no

explanation included for exclusion of run 1) 175.ST2A.PM 6.03 0.1951 

177.EU0805.PM 2.864 0.0343 179.SDT.PM different years 7.33 0.0787 

179.SDT.PM different years 6.56 0.0756 

EmissionUnitID: No. 3 SDT (D002) and salt cake

mix tank (D907) have combined exhausts 180.D002, D907.PM 3.5 0.0471 Compliance test. "Run 1 isokinetic was out of

range and an additional run was made. The "AVG"

column excludes the Run1. A high isokinetic

sample tends to be biased low" 181.11.PM Separate conditions 10.6 0.1830 

Test condition 2 included only 1 run and was not

included in test report. 181.11.PM Separate conditions 6.9 0.1220 

Avg diff. pressure during testing was 7.6. 181.11.PM different year 6.202 0.1080 

M

Exceeds NSPS limit of 0.2 lb/ton BLS. Installed in

1990 and subject to NSPS. Achieved compliancewith condition 2. Target P‐drop for condition 1 was 6.0. 181.51.PM Separate conditions 11.6 0.2288 

Compliance test. Target P‐drop for condition 2

was 7.0 (avg as measured). Used production rate

and emission factor from appendix (different ‐ 

slightly higher EF ‐ than in summary sheet). 181.51.PM Separate conditions 7.4 0.1600 

M

Exceeds NSPS limit of 0.2 lb/ton BLS. Installed in

1990 and subject to NSPS. Achieved compliance

with condition 2.

Target P‐drop for condition 3 was 6.5 (but 7.1 was

the average) 181.51.PM Separate conditions 10.7 0.2140 

Avg diff. pressure during testing was 7.8. 181.51.PM different year 5.24 0.1090 

A 4th run was performed to "establish the unit

operating range." The 4th run was not included inthe calculation of the averages. 182.110.PM 4.6491 0.0700 

185.05.PM different dates within same year 3.474 0.0653 

185.05.PM different dates within same year 4.588 0.0883 

185.05.PM different dates within same year 4.264333333 0.0820 185.05.PM different dates within same year 2.571 0.0493 

185.05.PM different dates within same year 2.968666667 0.0567 185.05.PM different dates within same year 4.161666667 0.0773 

186.RB17.PM different years 10.28 0.0801 

186.RB17.PM different years 12 0.0900 

M 1 run <60 min 189.SN27.PM 5.8 0.0500 

189.SN28.PM 11.41 0.0990 190.R404.PM different years 2.45 0.0527 

190.R406.PM 10.6 0.1440 

There are 2 separate RB #2 SDTs (North and South)

per flow diagram, not separate stacks 196.SN‐08North.PM 7.12 0.089936842 There are 2 separate RB #2 SDTs (North and South)per flow diagram, not separate stacks 196.SN‐08South.PM 5.61 0.070863158 

198.020.PM 10.42 0.0930 

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

200.007_8, 007_9

202.Smelt DissolvingTank EU322

203.2DTScr

203.3DTScr207.108226.SDT1N226.SDT1S226.SDT2240.RF02240.RF05240.RF06242.AA‐012243.R403243.R408531.RF10600.G0805600.G0807615.25617.P21208228535.002208228535.002208228535.008105.EU445D105.EU445BEast105.EU445BWest121.000009121.000010121.000009121.000010102.SDTV10178.08T014178.08T015190.R404105.EU445D

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

Emissions are from 2 SDTs with a combined vent. 200.007_8, 007_9.PM 6.5 0.0548 

Reported filterable PM only in this table (did not

include CPM) 202.Smelt Dissolving Tank EU322.PM 4.55 0.0790 

Only 1 run

Emission factor could not be calculated in desired

units. 203.2DTScr .PM 0.6 unspecified 

203.3DTScr.PM 5.1 0.0700 

Did not provide handwritten data sheets and did

not report filter temperature 207.108.PM 1.92 0.0900 

226.SDT1N.PM 5.028 0.0611 

226.SDT1S.PM 5.71 0.0680 226.SDT2.PM 4.4981 0.0855 240.RF02.PM 6.3 0.0942 240.RF05.PM 7.51 0.0628 240.RF06.PM 7.08 0.0592 242.AA‐012.PM 10.6 0.0846 

yes

Report stated TRS and PM tests were concurrent,

but production data is much higher for TRS than

for PM 243.R403.PM 5.17 0.1463 

243.R408.PM 18.77 0.1563 531.RF10.PM 6.5 0.0434 600.G0805.PM 4.81 0.0562 600.G0807.PM 4.782 0.0460 615.25.PM 6.58 0.1170 617.P21.PM 1.6562 0.0473 208228535.002.PM different years 

208228535.002.PM different years 10.64 0.101 

208228535.008.PM 8.81 0.0720 

M ODEQ M5 test 105.EU445D.PM 7.01 0.1089 M ODEQ M5 test Separate stacks: 3 East Smelt Tank Vent. 105.EU445BEast.PM Separate stacks 

M ODEQ M5 test Separate Stacks: 3 West Smelt Tank Vent. 105.EU445BWest.PM Separate stacks 8.96 0.1481 

121.000009.PM different years 2.2 0.0641 121.000010.PM different years 3.3 0.0965 121.000009.PM different years 4.3 0.1103 121.000010.PM different years 2.5 0.0641 102.SDTV10.PM 4.71 0.0388 178.08T014.PM 8.3 0.1600 178.08T015.PM 7.7 0.1500 190.R404.PM different years 3.158 0.0668 

M ODEQ M5 test 105.EU445D.PM different dates within same year 8.4 0.1304 

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

105.EU445D105.EU445D105.EU445D178.08T015178.08T014130.11130.6130.7135.007‐1, 007‐2

137.157137.157139.03140.57140.57140.57142.P7236143.7005143.7015143.7025152.04154.P32 ‐ Smelt

Dissolving Tank 1

154.P32 ‐ Smelt

Dissolving Tank 1

154.P35 ‐ Smelt

Dissolving Tank 2

154.P35 ‐ Smelt

Dissolving Tank 2

157.SDT167.007SDT171.006171.007171.008173.SDT173.SDT175.ST3A184.SDT1184.SDT1184.SDT2a184.SDT2a184.SDT2a184.SDT2b184.SDT2b184.SDT2b188.015SD1188.017SD2190.R405196.SN‐15

199.004201.SR0034205.010206.G‐35

206.G‐35

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

M ODEQ M5 test

Recalculated emission factor. Emission factor in

the test report was erronously based on the steam

production rate rather than BLS firing rate (both

provided in MPPH) 105.EU445D.PM different dates within same year 6.79 0.1147 

M ODEQ M5 test 105.EU445D.PM different dates within same year 6.51 0.1126 

M ODEQ M5 test 105.EU445D.PM different dates within same year 5.73 0.1065 

178.08T015.PM 3.06 0.0508 

178.08T014.PM 5.78 0.0959 

Run 1 was excluded due to sub‐isokinetic samplingduring test run. 130.11.PM 7.24 0.1494 

130.6.PM 4.56 0.1505 130.7.PM 7.1 0.2380 

Combined East and West stack values only given. 135.007‐1, 007‐2.PM Combined stacks given 4.8 0.0400 

Only 2 runs in report 137.157.PM 1.005 0.0370 

137.157.PM appears to be retest 0.862 0.0317 

Qa and Ps were not found in report. 139.03.PM 7.4 0.1600 

140.57.PM Different dates and methods (M5) 3.85 0.0730 

M ODEQ M5 test 140.57.PM Different dates and methods (ORDEQ5) 4.16 0.0790 

M ODEQ M5 test 140.57.PM 5.55 0.1049 

142.P7236.PM 10.31 0.1550 143.7005.PM 0.6 0.0356 143.7015.PM 0.7 0.0400 143.7025.PM 0.9 0.0300 152.04.PM 14.87 0.2243 154.P32 ‐ Smelt Dissolving Tank 1.PM different dates within same year 3.7 0.1000 

154.P32 ‐ Smelt Dissolving Tank 1.PM different dates within same year 5.5 0.1500 

Parameters for No. 2 Smelt Dissolving Tank were

missing from appendix. Values given are from

summary table. 154.P35 ‐ Smelt Dissolving Tank 2.PM different dates within same year 4.2 0.1200 

154.P35 ‐ Smelt Dissolving Tank 2.PM different dates within same year 6.2 0.1800 

157.SDT.PM 4.8 0.1480 167.007SDT.PM 9.63 0.1337 171.006.PM 7.06 0.2600 171.007.PM 2.52 0.0900 171.008.PM 8.97 0.1100 173.SDT.PM different dates 8.5 0.2040 173.SDT.PM different dates 7.95 0.1800 

175.ST3A.PM 8 0.0686 184.SDT1.PM

different dates (test report did not indicate

why each tank was tested twice) 7.344 0.1647 

184.SDT1.PM

different dates (test report did not indicate

why each tank was tested twice) 8.368 0.1362 

184.SDT2a.PM

different dates (test report did not indicatewhy each tank was tested twice) 7.325 0.2328 

184.SDT2a.PM

different dates (test report did not indicatewhy each tank was tested twice) 11.146 0.2454 

184.SDT2a.PM different dates 7.811 0.1720 

184.SDT2b.PM

different dates (test report did not indicatewhy each tank was tested twice) 16.788 0.5337 

184.SDT2b.PM

different dates (test report did not indicatewhy each tank was tested twice) 18.208 0.4009 

184.SDT2b.PM different dates 4.955 0.1091 

188.015SD1.PM 2.96 0.1010 188.017SD2.PM 2.85 0.0950 190.R405.PM 3.256 0.0724 196.SN‐15.PM 15.5 0.1406 

199.004.PM 12.28 0.1613 201.SR0034.PM 15.09 0.1770 205.010.PM 5.6 0.1110 206.G‐35.PM different dates 10.245 0.1912 

206.G‐35.PM different dates 10.794 unspecified 

Test_data_memo_appendices.xlsx App C SDT PM 
RTI+EUID

206.G‐36

206.G‐36

606.SDT2606.SDT2606.SDT3606.SDT3606.SDT4606.SDT4610.10610.10610.9610.9613.005613.006613.007613.008145.56132.4SDT

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

206.G‐36.PM different dates 15.417 0.2697 

206.G‐36.PM different dates 10.864 unspecified 

606.SDT2.PM different dates 4.257 0.0892 

Yes

boiler main safetyvalve opened during

run 2 and boiler had

to reduce operation

rate. Run 2 was not

used in thecalculations and an

additional run was

conducted atpermitted capacity. 606.SDT2.PM different dates 5.072333333 0.1153 

606.SDT3.PM different dates 3.6 0.0880 606.SDT3.PM different dates 3.013 0.0770 

606.SDT4.PM different dates 6.5 0.0985 

yes

Run 1 probe rinse was discolored, high wt of the

rinse was likely due to impacting something in the

stack. 606.SDT4.PM different dates 10.8 0.1728 

Weak wash scrubber flow 610.10.PM Separate conditions: weak wash scrubber 5.04 0.0790 Water wash scrubber flow 610.10.PM Separate conditions: water scrubber 3.5 0.0540 

Weak wash scrubber flow 610.9.PM Separate conditions: weak wash scrubber 5.59 0.1210 Water wash scrubber flow 610.9.PM Separate conditions: water scrubber 5.61 0.1230 

No TRS data given 613.005.PM 2.69 unspecified No TRS data given 613.006.PM 2.01 unspecified No TRS data given 613.007.PM 2.76 unspecified No TRS data given 613.008.PM 1.84 unspecified summary pages only 145.56.PM 24.1 0.6360 

132.4SDT.PM 2.964 0.0444 

Test_data_memo_appendices.xlsx App C SDT PM 
Appendix D

Total Reduced Sulfur Emissions Data for Smelt Dissolving Tanks
Appendix D: Pulp and Paper Emissions Test Data Spreadsheet for NSPS Review ‐ SDT Total Reduced Sulfur

General Information

Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

Generic ProcessType

2010_TRS_Source_Test_IP_No_4_Smelt_Disolving_Tank_Springfield.pdf 105 NEI45182 EU445D 105.EU445D

105‐‐CD 456‐110, CD445‐480, and

CD 445‐447 SCBR Kraft, Secondary SDT (Kraft)

SECTION 2.pdf 107 NEI47074 09‐P2 107.09‐P2 107‐‐09‐P2 SCBR Kraft SDT (Kraft)

H, I.pdf 109 NEI32869A SDT3 109.SDT3 109‐‐ST3SBR SCBR Kraft SDT (Kraft)

NEI32869 TRS EMISSION TEST OCT 2008 ‐ APP F, G,

H, I.pdf 109 NEI32869A SDT4 109.SDT4 109‐‐ST4SBR SCBR Kraft SDT (Kraft)

NEI45206_P&P Survey_2‐2011 Recovery Furnace &

Smelt Dissolvi.pdf 111 NEI45206 G‐127 111.G‐127 111‐‐STWS and ES 455‐001 SCBR NA Kraft SDT (Kraft)

P_P_ICR Part III_RTI166_InternationalPaper‐GeorgetownMill_NEI_41314_LK1and2_RB1and2_ST1and2_PM_July 2009.PDF 166 NEI41314 ST01 166.ST01 166‐‐ST1 Scrubber SCBR Kraft SDT (Kraft)

P_P_ICR Part III_RTI166_InternationalPaper‐GeorgetownMill_NEI_41314_LK1and2_RB1and2_ST1and2_PM_July 2009.PDF 166 NEI41314 ST02 166.ST02 166‐‐ST2 Scrubber SCBR Kraft SDT (Kraft)

P_P ICR Part III_RTI174_International Paper‐

Riegelwood M (1)2.pdf 174 NEI40247 G‐63C 174.G‐63C 174‐‐G‐63C EWSCRUB SCBR Kraft SDT (Kraft)

P_P ICR Part III_RTI174_International Paper‐

Riegelwood M (1)2.pdf 174 NEI40247 G‐63C 174.G‐63C 174‐‐G‐63C EWSCRUB SCBR Kraft SDT (Kraft)

SDTV No. 1 2010 Update 124 NEI8278 020 124.020 124‐‐sdtsbr020 SCBR Kraft SDT (Kraft)

0910‐29 SDTV No. 2 124 NEI8278 021 124.021 124‐‐sdtsbr021 SCBR Kraft SDT (Kraft)

NEI40686_RTI100_DomtarJohnsonburgMill_Smelt

DissolvingTank Test_August2001.pdf 100 NEI40686 109 100.109 100‐‐C109 SCBR Kraft SDT (Kraft)

112_TR2009_Weyerhaeuser Final Report.pdf 112 NEI34064 AA‐101 112.AA‐101 112‐‐Scrubber SCBR Kraft SDT (Kraft)

NEI26506_SDT_December_2009.pdf 114 NEI26506 U508 114.U508 114‐‐CDU5 SCBR Kraft SDT (Kraft)

Smelt Dissovlving Tank and Recovery Boiler Part

1.pdf 115 NEI26476 SM01 115.SM01 115‐‐SMO1 SCBR SCBR Good Combustion Practices Kraft SDT (Kraft)

Smelt Dissovlving Tank and Recovery Boiler Part

1.pdf 115 NEI26476 SM01 115.SM01 115‐‐SMO1 SCBR SCBR Good Combustion Practices Kraft SDT (Kraft)

NEI8619_July 2004 Stack Test Report.pdf 116 NEI8619 004 116.004 116‐‐SDTSCR SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

No 20 SDT Dec 2010.pdf 119 NEI46814 EQT005 119.EQT005 119‐‐SCBR04 SCBR Kraft, Secondary SDT (Kraft)

NEI 42317 Hopewell VA Dec 2009 SDT PM and

TRS.pdf 126 NEI42317 SDT 126.SDT 126‐‐SDTScr SCBR Kraft SDT (Kraft)

NEI7933_PIII ‐ Smelt Dissolving Tank Vent ‐ TRS ‐ 

October 26, 2010.pdf 127 NEI7933 SDT1 127.SDT1 127‐‐E111A SCBR Kraft, Secondary SDT (Kraft)

2010 ‐ SDT(PM‐TRS) + RB10(PM‐Hg).pdf 136 NEI12368 EU 031 136.EU 031 136‐‐CE 017 SCBR Kraft SDT (Kraft)

2010‐09‐15 5SDT PM‐TRS Test Report.pdf 137 NEI26581 204 137.204 137‐‐PC(204) SCBR Kraft SDT (Kraft)

TRS and PM Smelt Dissolving Tank SN‐03

September 2010.pdf 138 NEI18652 003 138.003 138‐‐SCRB SDT1, SCRB SDT2 PBSCBR Kraft SDT (Kraft)

RTI1#QKT.PDF 142 NEI41552 P7413 142.P7413 142‐‐CD7217 SCBR Kraft, Secondary SDT (Kraft) (2)

NEI759 TSP Testing 2008 part 1.pdf, NEI759 TSP

Testing 2008 part 2.pdf 146 NEI759 10 146.10 146‐‐SDT101 SCBR Kraft SDT (Kraft)

NEI759 TSP Testing 2008 part 1.pdf, NEI759 TSP

Testing 2008 part 2.pdf 146 NEI759 10 146.10 146‐‐SDT101 SCBR Kraft SDT (Kraft)

NEI759 TSP Testing 2008 part 1.pdf, NEI759 TSP

Testing 2008 part 2.pdf 146 NEI759 17 146.17 146‐‐SDT201 SCBR Kraft SDT (Kraft)

NEI46931_12 17 2010 1SDT Compliance Test

Report.pdf 148 NEI46931 002 148.002 148‐‐SDT1SCB SCBR Kraft, Secondary SDT (Kraft)

Test_data_memo_appendices.xlsx App D SDT TRS 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

Generic ProcessType

NEI46931_8 31 2010 & 9 28, 30 2010 No. 1 & No.

2 SDT Compliance Test Report.pdf 148 NEI46931 008 148.008 148‐‐SDT2SCB SCBR Kraft, Secondary SDT (Kraft)

NEI40488 B011, P001, P005 ‐ 2009 Title V

Compliance Test Rep.pdf 149 NEI40488 P005 149.P005 149‐‐SC‐502 SCBR Kraft SDT (Kraft)

NEI40488 B011, P001, P005 ‐ 2009 Title V

Compliance Test Rep.pdf 149 NEI40488 P005 149.P005 149‐‐SC‐502 SCBR Kraft SDT (Kraft)

150 NewPage Rumford TRC 2011 Report_Smelt

Tank_TRS.pdf 150 NEI6273 CREC‐2a 150.CREC‐2a 150‐‐SCRBSTa SCBR Kraft, Mechanical SDT (Kraft)

150 NewPage Rumford TRC 2011 Report_Smelt

Tank_TRS.pdf 150 NEI6273 CREC‐2b 150.CREC‐2b 150‐‐SCRBSTb SCBR Kraft, Mechanical SDT (Kraft)

NEI46739 SDT3 TRS April_May 2008.pdf 154 NEI46739 P38 ‐ Smelt Dissolving Tank 3

154.P38 ‐ SmeltDissolving Tank 3 154‐‐C12 PBSCBR Kraft SDT (Kraft)

NEI33883 ‐ Smelt Dissolving Tank ‐ March 3, 2011 ‐ 

Compliance Test Report.pdf 155 NEI33883 SDT 155.SDT 155‐‐SDT SCRUBBER PBSCBR Kraft, Mechanical SDT (Kraft)

P_P ICR Part III_RTI162_InternationalPaper‐

EastoverMill_NEI46760_no 1 smelt dis tank total

sulfur.pdf 162 NEI46760 381C 162.381C 162‐‐381CSCRUB SCBR Kraft SDT (Kraft)

P_P ICR Part III_RTI162_InternationalPaper‐

EastoverMill_NEI46760_no 2 smelt dis tank total

sulfur.pdf 162 NEI46760 382B 162.382B 162‐‐382BSCRUB SCBR Kraft SDT (Kraft)

RTI163_International Paper ‐ PrattvilleMill_NEI8560_No 1 Recovery Furnace and Smelt

Dissolving Tanks testing.pdf 163 NEI8560 SD1902 163.SD1902 163‐‐SD1SC1 SCBR Kraft, Secondary SDT (Kraft)

RTI163_International Paper ‐ PrattvilleMill_NEI8560_No 1 Recovery Furnace and Smelt

Dissolving Tanks testing.pdf 163 NEI8560 SD1903 163.SD1903 163‐‐SD1SC2 SCBR Kraft, Secondary SDT (Kraft)

P_P_ICR Part III_RTI175_InternationalPaper‐AugustaMill_N (6).PDF 175 NEI26514 ST2A 175.ST2A 175‐‐ST2B SCBR Kraft SDT (Kraft)

RecBoiler_WasteBoiler_SmeltTank_LimeKiln_Compliancetest2011_Part1.pdf 177 NEI33887 EU0805 177.EU0805 177‐‐CD0801 SCBR Kraft SDT (Kraft)

RTI179_Rock‐TennDemopolis_NEI45474_PP

Survey_RFSDTTest2009.pdf 179 NEI45474 SDT 179.SDT 179‐‐SDTSCR SCBR Kraft SDT (Kraft)

NEI26471_No3_Smelt_Tank_PM_TRS_2009‐0317[2].pdf 180 NEI26471 D002, D907 180.D002, D907 180‐‐D02S SCBR Kraft, Secondary SDT (Kraft)

Source 110 Test Report Feb 2010.pdf 182 NEI7181 110 182.110 182‐‐C10/SCR1 SCBR Kraft SDT (Kraft)

Smelt.pdf 186 NEI18334 RB17 186.RB17 186‐‐SMSCR SCBR Kraft SDT (Kraft)

GP Crossett Paper Smelt Dissolving Tank

Compliance 2010.pdf 189 NEI54342 SN27 189.SN27 189‐‐SN27S SCBR Kraft SDT (Kraft)

GP Crossett Paper Smelt Dissolving Tank

Compliance 2010.pdf 189 NEI54342 SN28 189.SN28 189‐‐SN28S SCBR Kraft SDT (Kraft)

Georgia‐Pacific Cedar Springs NEI26491 P3 SDTV2 &

SDTV3 TRS 03‐23‐2010.pdf 190 NEI26491 R405 190.R405 190‐‐C405 SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

Georgia‐Pacific Cedar Springs NEI26491 P3 SDTV3

TRS 03‐25‐2011 Compliance Test.pdf 190 NEI26491 R406 190.R406 190‐‐C406 SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

2010 Domtar Compliance Testing Part 1 of 6.pdf

and 2010 Domtar Compliance Testing Part 2 of

6.pdf 196 NEI18660 SN‐08North 196.SN‐08North 196‐‐SN‐08 SCBR Scrubber Kraft SDT (Kraft)

2010 Domtar Compliance Testing Part 1 of 6.pdf 196 NEI18660 SN‐08South 196.SN‐08South 196‐‐SN‐08 SCBR Scrubber Kraft SDT (Kraft)

2010 Domtar Compliance Testing Part 1 of 6.pdf 196 NEI18660 SN‐15 196.SN‐15 196‐‐SN‐15 SCBR Scrubber Kraft SDT (Kraft)

NEI41565 Smelt Tank Particulate Sampling March

1995.pdf 198 NEI41565 020 198.020 198‐‐020_CD SCBR

Kraft, Mechanical,Secondary SDT (Kraft)

NEI47077 BOWATER CATAWBA MAY 11 COMP

REPORT.pdf 200 NEI47077 007_8, 007_9 200.007_8, 007_9 200‐‐2511C SCBR Kraft, Mechanical SDT (Kraft)

1106‐104_Boise White Paper_SDT Report.pdf 202 NEI12411 Smelt Dissolving Tank EU322

202.Smelt Dissolving

Tank EU322 202‐‐CE322 SCBR

5 gph 50% caustic to reduce TRS; started

recycling scrubber overflow in 2010 to SDT

to reduce caustic and energy losses tosewer. Kraft SDT (Kraft)

2010 12 2SDTV TRS.pdf 203 NEI42410 2DTScr 203.2DTScr 203‐‐2DTScr‐Scr SCBR none Kraft, Sulfite‐Na SDT (Kraft)

Test_data_memo_appendices.xlsx App D SDT TRS 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

Generic ProcessType

NEI33023_SDT3_1992_TRS.pdf 226 NEI33023 SDT2 226.SDT2 226‐‐SDT3S SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

Rayonier Jesup SDT5 PM &TRS test 05_25_10.pdf 240 NEI26526 RF02 240.RF02 240‐‐RFC2 SCBR Kraft SDT (Kraft)

Rayonier Jesup SDT6 PM &TRS test 03_17_10.pdf 240 NEI26526 RF05 240.RF05 240‐‐RFC4 SCBR Kraft SDT (Kraft)

Rayonier Jesup SDT6 PM &TRS test 03_17_10.pdf 240 NEI26526 RF06 240.RF06 240‐‐RFC5 SCBR Kraft SDT (Kraft)

NEI 34066 Emission Test RB‐LK‐ SDT 2010.pdf 242 NEI34066 AA‐012 242.AA‐012 242‐‐UT‐7 SCBR Kraft SDT (Kraft)

8196_2009 Source Compliance Test Report.pdf 243 NEI8196 R403 243.R403 243‐‐RSS5 SCBR Kraft SDT (Kraft)

8196_2009 Source Compliance Test Report.pdf 243 NEI8196 R408 243.R408 243‐‐RSS6 SCBR Kraft SDT (Kraft)

P_P_ICR Part III_RTI531_InternationalPaper‐ Savnnah Mill (6).pdf 531 NEI8186 RF10 531.RF10 531‐‐AP15 SCBR Kraft, Secondary SDT (Kraft)

RTI600_InternationalPaper‐CourtlandMill‐NEI18357

NOV 07 2RF‐.pdf 600 NEI18357 G0805 600.G0805 600‐‐08‐CD‐02‐004 SCBR Kraft SDT (kraft)

RTI600_InternationalPaper‐CourtlandMill‐NEI18357

MAY 08 3RF‐.pdf 600 NEI18357 G0807 600.G0807 600‐‐08‐CD‐03‐003 SCBR Kraft SDT (kraft)

ODEQ‐Final‐Report‐SDT‐TSP‐TRS‐10‐20‐09.pdf 615 NEI40554 25 615.25 615‐‐SDTSC1 SCBR Kraft SDT (Kraft)

2011_0315‐17.2.pdf 617 NEI42695 P21 617.P21 617‐‐C08 PBSCBR Kraft SDT (Kraft)

NEI18373_002_Particulate,SO2,andTRS_2007.pdf 208228535 NEI18373 002 208228535.002 208228535‐‐X002 SCBR Unknown (Kraft) SDT (Kraft)

NEI18373_008_Particulate,SO2, and TRS_2006.pdf 208228535 NEI18373 008 208228535.008 208228535‐‐X013 SCBR Unknown (Kraft) SDT (Kraft)

NEI42341A_PIII_D2a_2011‐Q1 LK‐RB10‐SDTV10‐

HFB11.pdf 102 NEI42341A SDTV10 102.SDTV10 102‐‐SDTV‐S SCBR Kraft SDT (Kraft)

2010 RB & SDT TRS #102.pdf 135 NEI33118 007‐1, 007‐2 135.007‐1, 007‐2 135‐‐007‐4, 007‐5 SCBR Kraft SDT (Kraft)

EPA M16A 052011.pdf 140 NEI13340 57 140.57 140‐‐461‐213 PBSCBR Kraft SDT (Kraft)

RTI1#CGM.pdf 142 NEI41552 P7236 142.P7236 142‐‐CD‐7236 SCBR Kraft, Secondary SDT (Kraft)

NEI26504_RTI143_PCA Valdosta Mill_1,2,3SDT

TRS_July 2009 143 NEI26504 7005 143.7005 143‐‐C012 SCBR Kraft SDT (Kraft)

NEI26504_RTI143_PCA Valdosta Mill_1,2,3SDT

TRS_July 2009 143 NEI26504 7015 143.7015 143‐‐C014 SCBR Kraft SDT (Kraft)

NEI26504_RTI143_PCA Valdosta Mill_1,2,3SDT

TRS_July 2009 143 NEI26504 7025 143.7025 143‐‐C016 SCBR Kraft SDT (Kraft)

NEI33104‐SDT 2011 TRS Compliance.pdf 157 NEI33104 SDT 157.SDT 157‐‐SDRMST OTH Kraft SDT (Kraft)

RTI163_International Paper ‐ PrattvilleMill_NEI8560_No 2 Recovery Furnace and Smelt

Dissolving Tank.pdf testing 163 NEI8560 SD2906 163.SD2906 163‐‐SD2SCR SCBR Kraft, Secondary SDT (Kraft)

RTI167 NEI34070

2011_IPVicksburg_StackTestReport_(PB,LK,RB,SDT,SS).pdf 167 NEI34070 007SDT 167.007SDT 167‐‐SDSCBR SCBR Kraft, Secondary SDT (Kraft)

9‐0224C Evergreen F.pdf 171 NEI18658 006 171.006 171‐‐MESDT2 OTH Kraft SDT (Kraft)

10‐0102 Evergreen Compliance_F.pdf 171 NEI18658 006 171.006 171‐‐MESDT2 OTH Kraft SDT (Kraft)9‐0224C Evergreen F.pdf 171 NEI18658 007 171.007 171‐‐VSSDT3 SCBR Kraft SDT (Kraft)10‐0102 Evergreen Compliance_F.pdf 171 NEI18658 007 171.007 171‐‐VSSDT3 SCBR Kraft SDT (Kraft)9‐0224C Evergreen F.pdf 171 NEI18658 008 171.008 171‐‐VSSDT4 SCBR Kraft SDT (Kraft)10‐0102 Evergreen Compliance_F.pdf 171 NEI18658 008 171.008 171‐‐VSSDT4 SCBR Kraft SDT (Kraft)RTI173 NEI 35908 IPTiconderoga SDT test 2‐01.pdf 173 NEI35908 SDT 173.SDT 173‐‐SDSCBR SCBR NA Kraft SDT (Kraft)

P_P_ICR Part III_RTI175_InternationalPaper‐AugustaMill_N (6).pdf 175 NEI26514 ST3A 175.ST3A 175‐‐ST3B SCBR Kraft SDT (Kraft)

NEI46599_4SD TRS 2007.pdf 185 NEI46599 05 185.05 185‐‐SD4SCB PBSCBR Kraft SDT (Kraft)

2011.0606‐0609.2Q.tests.pdf 188 NEI40600 015SD1 188.015SD1 188‐‐62‐056 SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

Test_data_memo_appendices.xlsx App D SDT TRS 
Test report electronic file name RTI Plant ID NEI Site ID Emission Unit ID(s) RTI+EUID APCD_ID(s) Test report APCD type

Combustion modifications or controls used

to reduce air pollution (from combustion

sources) Pulping Process Type

Generic ProcessType

2011.0606‐0609.2Q.tests.pdf 188 NEI40600 017SD2 188.017SD2 188‐‐62‐256 SCBR

Kraft, Secondary,

SemiChem SDT (Kraft)

NEI18390_004_TRS_2009.pdf 199 NEI18390 004 199.004 199‐‐Z006 SCBR Kraft SDT (Kraft)

NEI7559SmeltDisTank‐87‐

02TRSSO2Comp1987PartI.pdf 201 NEI7559 SR0034 201.SR0034 201‐‐SDTS SCBR

Kraft, Mechanical,Secondary SDT (Kraft)

NEI8601_Unit 010_TRS_2009.pdf 205 NEI8601 010 205.010 205‐‐SDTS SCBR Kraft, Secondary SDT (Kraft)

RTI206_BRPSDTV10TRS11.15.2007.pdf 206 NEI40282 G‐35 206.G‐35 206‐‐SDT10 DEM OTH Kraft SDT (Kraft)RTI206_BRPSDTV11TRS11.14.2007.pdf 206 NEI40282 G‐36 206.G‐36 206‐‐SDT11 DEM OTH Kraft SDT (Kraft)47091_021_2011_TRS.pdf 606 NEI47091 SDT2 606.SDT2 606‐‐SCRB2 SCBR Kraft SDT (Kraft)

47091_007_2005_PM_TRS.pdf 606 NEI47091 SDT3 606.SDT3 606‐‐SCRB3 SCBR Kraft SDT (Kraft)

47091_011_2006_PM_TRS.pdf 606 NEI47091 SDT4 606.SDT4 606‐‐SCRB4 SCBR Kraft SDT (Kraft)

610 Verso 2009 SDT 1&2 Report.pdf 610 NEI6261 10 610.10 610‐‐SDT2WS SCBR Kraft, Mechanical SDT (Kraft)610 Verso 2009 SDT 1&2 Report.pdf 610 NEI6261 10 610.10 610‐‐SDT2WS SCBR Kraft, Mechanical SDT (Kraft)

610 Verso 2009 SDT 1&2 Report.pdf 610 NEI6261 9 610.9 610‐‐SDT1WS SCBR

stacked air installed in recovery boiler No. 1

in 2007 Kraft, Mechanical SDT (Kraft)

610 Verso 2009 SDT 1&2 Report.pdf 610 NEI6261 9 610.9 610‐‐SDT1WS SCBR

stacked air installed in recovery boiler No. 1

in 2007 Kraft, Mechanical SDT (Kraft)

SDT TRS Source Tests 2004.pdf 133 NEI13363 12a 133.12a 133‐‐SDT4TE SCBR Kraft SDT (Kraft)

SDT TRS Source Tests 2004.pdf 133 NEI13363 12b 133.12b 133‐‐SDT4TW SCBR Kraft SDT (Kraft)

2009 4 SDT.pdf 132 NEI42357 4SDT 132.4SDT 132‐‐SCBR1 SCBR Kraft, Secondary SDT (Kraft)

NEI46931_3 24‐26 2004 No. 1 & No. 2 SDT

Compliance Test Report.pdf 148 NEI46931 002, SCMT1 148.002, SCMT1 148‐‐SDT1SCB SCBR Kraft, Secondary

SDT (Kraft), Salt

Cake Tank

NEI46931_3 24‐26 2004 No. 1 & No. 2 SDT

Compliance Test Report.pdf 148 NEI46931 008, SCMT2 148.008, SCMT2 148‐‐SDT2SCB SCBR Kraft, Secondary

SDT (Kraft), Salt

Cake Tank

NEI46931_8 31 2010 & 9 28, 30 2010 No. 1 & No.

2 SDT Compliance Test Report.pdf 148 NEI46931 002 148.002 148‐‐SDT1SCB SCBR Kraft, Secondary SDT (Kraft)

2008 11 2SDTV TRS.pdf 203 NEI42410 2DTScr 203.2DTScr 203‐‐2DTScr‐Scr SCBR none Kraft, Sulfite‐Na SDT (Kraft)

2007 10 2SDTV TRS.pdf 203 NEI42410 2DTScr 203.2DTScr 203‐‐2DTScr‐Scr SCBR none Kraft, Sulfite‐Na SDT (Kraft)

2003 12 2SDTV TRS.pdf 203 NEI42410 2DTScr 203.2DTScr 203‐‐2DTScr‐Scr SCBR none Kraft, Sulfite‐Na SDT (Kraft)

610 Verso 2005 Smelt Tank #2 IPT.pdf 610 NEI6261 10 610.10 610‐‐SDT2WS SCBR Kraft, Mechanical SDT (Kraft)

610 Verso 2005 Smelt Tank #2 IPT.pdf 610 NEI6261 10 610.10 610‐‐SDT2WS SCBR Kraft, Mechanical SDT (Kraft)

610 Verso 2005 Smelt Tank #2 IPT.pdf 610 NEI6261 10 610.10 610‐‐SDT2WS SCBR Kraft, Mechanical SDT (Kraft)

610 Verso 2007 Smelt Tank #1 and #2.pdf 610 NEI6261 9 610.9 610‐‐SDT1WS SCBR Kraft, Mechanical SDT (Kraft)

610 Verso 2007 Smelt Tank #1 and #2.pdf 610 NEI6261 9 610.9 610‐‐SDT1WS SCBR Kraft, Mechanical SDT (Kraft)

610 Verso 2007 Smelt Tank #1 and #2.pdf 610 NEI6261 10 610.10 610‐‐SDT2WS SCBR Kraft, Mechanical SDT (Kraft)

610 Verso 2007 Smelt Tank #1 and #2.pdf 610 NEI6261 10 610.10 610‐‐SDT2WS SCBR Kraft, Mechanical SDT (Kraft)

Green rows were not used in the NSPS review.

Test_data_memo_appendices.xlsx App D SDT TRS 
RTI+EUID

105.EU445D107.09‐P2

109.SDT3109.SDT4111.G‐127

166.ST01166.ST02174.G‐63C

174.G‐63C

124.020124.021100.109112.AA‐101

114.U508115.SM01115.SM01116.004119.EQT005126.SDT127.SDT1136.EU 031

137.204138.003142.P7413146.10146.10146.17148.002

Configuration General Test Report Information Production Rate Inlet/OutletHas the configuration of

the emission unit,combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date

(mm/dd/yyyy)

Emission TestMethod

AverageHourly ProductionRate(value)

Hourly ProductionRate(units) Production comment

Are inlet oroutlet data

provided?

no TRS as H2S 2010 #4 Smelt Dissolving Tank unspecified 9/28/2010 M16A 60.33 ton BLS/hr Outlet

TRS as H2S 2011 Smelt Dissolving Tanks unspecified 6/9/2011 M16A 94.5 ton BLS/hr Outlet

No TRS as H2S 2008 Smelt Dissolving Tank # 3 unspecified 9/9/2008 M16 50.27 ton BLS/hr Outlet

No TRS as H2S 2008 No. 4 Smelt Dissolver unspecified 9/10/2008 M16 78.65 ton BLS/hr Outlet

No TRS as H2S 2011 South Smelt Tank unspecified 1/29/2011 M16 45.3 ton BLS/hr Outlet

No TRS as H2S 2009 No. 1 Smelt Dissolving Tank unspecified 7/14/2009 M16 68.5 ton BLS/hr Outlet

No TRS as H2S 2009 No. 2 Smelt Dissolving Tank unspecified 7/17/2009 M16 82.5 ton BLS/hr Outlet

TRS as H2S 2004 No. 5 SDT ‐ East Stack unspecified 10/22/2004 M16 139.7 ton BLS/hr Outlet

TRS as H2S 2004 No. 5 SDT ‐ West Stack unspecified 10/22/2004 M16 139.7 ton BLS/hr Outlet

No TRS as H2S 2010 No. 1 Smelt Dissolver Fuel oil 11/3/2010 M16A 58.3 ton BLS/hr outlet

No TRS as H2S 2010 No. 2 Smelt Dissolver Fuel oil 11/4/2010 M16A 58.05 ton BLS/hr outlet

No TRS as H2S 2001 Smelt Dissolving Tank 8/9/2001 M16 57.5 ton BLS/hr Outlet

Yes

smelt dissolving tank

rebuilt in 2009 following

testing. TRS as H2S 2009 Smelt Dissolving Tank 3/18/2009 M16A/M6C 117.18 ton BLS/hr Outlet

No TRS as H2S 2009 Smelt Dissolving Tank 12/2/2009 M16A 107.3 ton BLS/hr Outlet

no TRS as H2S 2010 SDT West 9/9/2010 M16A 87.7 ton BLS/hr Outlet

no TRS as H2S 2010 SDT East 9/9/2010 M16A 87.7 ton BLS/hr Outlet

No TRS as H2S 2004 Smelt Dissolving Tank Vent 7/20/2004 M16A 95.41 ton BLS/hr Outlet

No TRS as H2S 2010 No. 20 SDT 12/1/2010 M16 57.2 ton BLS/hr Outlet

No TRS as H2S 2009 SDT 12/10/2009 M16A 51.6 ton BLS/hr Outlet

No TRS as H2S 2010 SDT Vent 10/26/2010 M16A 77.45 ton BLS/hr Outlet

no TRS as H2S 2010 SDT 5/19/2010 M16A/M16B 113.5 ton BLS/hr Outlet

No TRS as H2S 2010 No. 5 SDT 9/15/2010 M16A/M6C Outlet

No TRS as H2S 2010 Smelt Dissolving Tank 9/23/2010 M16B 57.01388889 ton BLS/hr Outlet

No

New stack and scrubber

specific to SDT‐1 installed

during 2011. TRS as H2S 2004 No. 1 and No. 2 SDTs 7/22/2004 M16A 73.45733333 ton BLS/hr Outlet

No TRS as H2S 2008 No. 1 SDT upriver 10/14/2008 M16A 75.90277778 ton BLS/hr Outlet

No TRS as H2S 2008 No. 1 SDT downriver 10/14/2008 M16A 75.90277778 ton BLS/hr Outlet

No TRS as H2S 2008 No. 2 SDT 10/16/2008 M16A 99.93055556 ton BLS/hr Outlet

no TRS as H2S 2010 No. 1 SDT 12/17/2010 M16C 58.7 ton BLS/hr Outlet

Test_data_memo_appendices.xlsx App D SDT TRS 
RTI+EUID

148.008149.P005149.P005150.CREC‐2a

150.CREC‐2b

154.P38 ‐ Smelt

Dissolving Tank 3

155.SDT162.381C162.382B163.SD1902163.SD1903175.ST2A177.EU0805179.SDT180.D002, D907

182.110186.RB17189.SN27189.SN28190.R405190.R406196.SN‐08North

196.SN‐08South

196.SN‐15

198.020200.007_8, 007_9

202.Smelt Dissolving

Tank EU322

203.2DTScr

Has the configuration of

the emission unit,combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date

(mm/dd/yyyy)

Emission TestMethod

AverageHourly ProductionRate(value)

Hourly ProductionRate(units) Production comment

Are inlet oroutlet data

provided?

no TRS as H2S 2010 No. 2 SDT 9/30/2010 M16C 83.3 ton BLS/hr Outlet

no TRS as H2S 2009 No. 9 SDT (test 1) 4/3/2009 M16 68.37 ton BLS/hr Outlet

no TRS as H2S 2009 No. 9 SDT (test 2) 4/8/2009 M16 68.87 ton BLS/hr Outlet

No TRS as H2S 2011 Smelt Tank East 3/16/2011 M16B 88.7 ton BLS/hr Outlet

No TRS as H2S 2011 Smelt Tank West 3/16/2011 M16B 88.7 ton BLS/hr Outlet

No TRS as H2S 2008 SDT3 4/29/2008 M16A 35.13 ton BLS/hr Outlet

No TRS as H2S 2011 Smelt Dissolving Tank 3/3/2011 M16C 77.7 ton BLS/hr Outlet

No TRS as H2S 2008 No. 1 SDT 8/7/2008 M16 52.5 ton BLS/hr Outlet

No TRS as H2S 2007 No. 2 SDT 3/15/2007 M16 107 ton BLS/hr Outlet

No TRS as H2S 2009 No. 1 SDT South 7/16/2009 M16A 54.47072277 ton BLS/hr Outlet

No TRS as H2S 2009 No. 1 SDT North 7/16/2009 M16A 54.47182508 ton BLS/hr Outlet

no TRS as H2S 2010 No. 2 SDT 8/10/2010 M16C 29.6 ton BLS/hr Outlet

No TRS as H2S 2011 SDT 3/29/2011 M16C 82.5 ton BLS/hr Outlet

No TRS as H2S 2009 No. 3 SDT Vent 5/27/2009 M16 86.8 ton BLS/hr Outlet

No TRS as H2S 2009 No. 3 SDT Vent 3/17/2009 M16 73.98 ton BLS/hr Outlet

no TRS as H2S 2010 Smelt Dissolving Tank Vent 1/12/2010 M16 63.65 ton BLS/hr Outlet

No TRS as H2S 2008 No. 4 Smelt Tank 7/22/2008 M16 127.2 ton BLS/hr Outlet

no TRS as H2S 2010 SDT East 12/2/2010 M16B 115.2083333 ton BLS/hr

provided BLS MM#/day,

converted to TBLS/hr Outlet

no TRS as H2S 2010 SDT West 11/30/2010 M16B 114.7916667 ton BLS/hr

provided BLS MM#/day,

converted to TBLS/hr Outlet

No TRS as H2S 2010 No. 2 SDT 3/24/2010 M16A 54.1 ton BLS/hr Outlet

No TRS as H2S 2011 No. 3 SDT 3/25/2011 M16C 71.6 ton BLS/hr Outlet

no TRS as H2S 2010 No. 2 North Smelt Tank Vent 4/20/2010 M16A 79.16666667 ton BLS/hr

provided MM#/day (appears to

be BLS), converted to ton/hr Outlet

no TRS as H2S 2010 No. 2 South Smelt Tank Vents 4/20/2010 M16A 79.16666667 ton BLS/hr

provided MM#/day (appears to

be BLS), converted to ton/hr Outlet

no TRS as H2S 2010 No. 3 Smelt Tank Vents 4/21/2010 M16A 106.25 ton BLS/hr

provided MM#/day (appears to

be BLS), converted to ton/hr Outlet

No TRS as H2S 1995 No. 3 SDT 2/21/1995 M16A 106.25 ton BLS/hr Outlet

No TRS as H2S 2011 Nos. 2 and 3 SDT Vent 4/14/2011 M16 119.9 ton BLS/hr Outlet

no

Control TRS with 5 gph

50% caustic to ensure

compliance beginning in

2004 TRS as H2S 2011 SDT EU322 7/19/2011 M16A 57.3 ton BLS/hr Outlet

No TRS as H2S 2010 No. 2 DT Scrubber Vent Stack 12/6/2010 M16A 11.304 ton BLS/hr Outlet

Test_data_memo_appendices.xlsx App D SDT TRS 
RTI+EUID

226.SDT2240.RF02240.RF05240.RF06242.AA‐012

243.R403243.R408531.RF10600.G0805600.G0807615.25617.P21208228535.002208228535.008102.SDTV10135.007‐1, 007‐2

140.57142.P7236143.7005143.7015143.7025157.SDT163.SD2906167.007SDT171.006171.006171.007171.007171.008171.008173.SDT175.ST3A185.05188.015SD1

Has the configuration of

the emission unit,combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date

(mm/dd/yyyy)

Emission TestMethod

AverageHourly ProductionRate(value)

Hourly ProductionRate(units) Production comment

Are inlet oroutlet data

provided?

no TRS as H2S 1992 No. 3 SDT 9/11/1992 M16 53.75 ton BLS/hr Outlet

No TRS as H2S 2010 No. 5 SDT 5/25/2010 M16 67.4 ton BLS/hr Outlet

No TRS as H2S 2010 No. 6 SDT East 3/17/2010 M16 119.6 ton BLS/hr Outlet

No TRS as H2S 2010 No. 6 SDT West 3/17/2010 M16 119.6 ton BLS/hr Outlet

No TRS as H2S 2010 SDT 9/30/2010 M16 128.4 ton BLS/hr Outlet

No TRS as H2S 2009 No. 5 SDT 10/29/2009 M16 81.6 ton BLS/hr Outlet

No TRS as H2S 2009 No. 6 SDT 10/28/2009 M16 121.8 ton BLS/hr Outlet

No TRS as H2S 2010 No. 15 SDT 4/14/2010 M16 155 ton BLS/hr Outlet

no TRS as H2S 2007 No. 2 SDT 10/23/2007 M16 85.39 ton BLS/hr Outlet

no TRS as H2S 2008 No. 3 SDT 5/7/2008 M16 99.92 ton BLS/hr Outlet

no TRS as H2S 2009 SDT 10/20/2009 M16A 64.05 ton BLS/hr

Provided production in lb BLS

fired/min‐‐converted to TBLS/hr Outlet

no TRS as H2S 2011 S21 SDT 3/16/2011 M16A 34.2 ton BLS/hr Outlet

No TRS as H2S 2007 No. 1 SDT 4/23/2007 M16A 109 ton BLS/hr Outlet

No TRS as H2S 2006 No. 2 SDT 12/14/2006 M16A 126.9 ton BLS/hr Outlet

No TRS as H2S 2011 No. 10 Smelt Dissolving Tank 01/05/2011 M16A/M6C 121.20 ton BLS/hr Outlet

No TRS as H2S 2010 Smelt Dissolving Tank 12/01/2010

M16(modified) 93.30 ton BLS/hr Outlet

Yes TRS as H2S 2011 Smelt Dissolving Tank 05/17/2011 M16A 52.92 ton BLS/hr Outlet

No TRS as H2S 2003 No. 3 Smelt Dissolving Tank Vent 06/30/2003 M16A 66.50 ton BLS/hr Outlet

no TRS as H2S 2009 No. 1 Smelt Dissolving Tank 07/30/2009 M16 17.79 ton BLS/hr Outlet

no TRS as H2S 2009 No. 2 Smelt Dissolving Tank 07/30/2009 M16 10.03 ton BLS/hr Outlet

no TRS as H2S 2009 No. 3 Smelt Dissolving Tank 07/31/2009 M16 25.97 ton BLS/hr Outlet

No TRS as H2S 2011 Smelt Dissolving Tank 04/06/2011 M16B 33.52 ton BLS/hr Outlet

No TRS as H2S 2003 No. 2 Smelt Dissolving Tank 12/08/2003 M16A 76.16 ton BLS/hr Outlet

no NA TRS as H2S 2011 Smelt Dissolving Tank 01/17/2011 M16A 72.03 ton BLS/hr Outlet

no TRS as H2S 2009 No. 2 Smelt Dissolving Tank 07/08/2009 M16A/M6C 27.22 ton BLS/hr Outlet

no TRS as H2S 2010 No. 2 Smelt Dissolving Tank 07/14/2010 M16A/M6C 27.31 ton BLS/hr Outlet

no TRS as H2S 2009 No. 3 Smelt Dissolving Tank 07/07/2009 M16A/M6C 27.68 ton BLS/hr Outlet

no TRS as H2S 2010 No. 3 Smelt Dissolving Tank 07/13/2010 M16A/M6C 27.83 ton BLS/hr Outlet

no TRS as H2S 2009 No. 4 Smelt Dissolving Tank 07/06/2009 M16A/M6C 84.66 ton BLS/hr Outlet

no TRS as H2S 2010 No. 4 Smelt Dissolving Tank 07/15/2010 M16A/M6C 83.41 ton BLS/hr Outlet

No NA TRS as H2S 2001 Smelt Dissolving Tank 02/08/2001 M16 41.70 ton BLS/hr Outlet

no TRS as H2S 2009 No. 3 Smelt Dissolving Tank 08/10/2009 M16 115.67 ton BLS/hr Outlet

No TRS as H2S 2007 No. 4 Smelt Dissolver 01/31/2007 M16A/M6C 36.67 ton BLS/hr Outlet

No TRS as H2S 2011 No. 1 Smelt Dissolving Tank 06/06/2011 M16A/M6C 29.45 ton BLS/hr Outlet

Test_data_memo_appendices.xlsx App D SDT TRS 
RTI+EUID

188.017SD2199.004201.SR0034205.010206.G‐35

206.G‐36

606.SDT2606.SDT3606.SDT4610.10610.10610.9610.9133.12a133.12b132.4SDT148.002, SCMT1148.008, SCMT2148.002203.2DTScr203.2DTScr203.2DTScr610.10610.10610.10610.9610.9610.10610.10

Has the configuration of

the emission unit,combustion controls,

collection system, orAPCD changed since the

test was conducted? If yes, please explain Pollutant

Year of

emissionstest General Description Fuels Burned During Test

Test Date

(mm/dd/yyyy)

Emission TestMethod

AverageHourly ProductionRate(value)

Hourly ProductionRate(units) Production comment

Are inlet oroutlet data

provided?

No TRS as H2S 2011 No. 2 Smelt Dissolving Tank 06/06/2011 M16A/M6C 30.14 ton BLS/hr Outlet

No TRS as H2S 2009 No. 3 Smelt Dissolving Tank 02/11/2009 M16 71.10 ton BLS/hr Outlet

No TRS as H2S 1987 Smelt Dissolving Tank 10/28/1987 M16A 82.52 ton BLS/hr Outlet

No TRS as H2S 2009 Smelt Dissolving Tank 01/14/2009 M16A 51.50 ton BLS/hr Outlet

no TRS as H2S 2007 No. 10 Smelt Dissolving Tank 11/15/2007 M16A unspecified Production values are reserved Outlet

no TRS as H2S 2007 No. 11 Smelt Dissolving Tank 11/14/2007 M16A unspecified Production values are reserved Outlet

no TRS as H2S 2011 No. 2 Smelt Dissolving Tank 12/15/2011 M16 43.97 ton BLS/hr Outlet

no TRS as H2S 2005 No. 3 Smelt Dissolving Tank 10/25/2005 M16 40.90 ton BLS/hr Outlet

no TRS as H2S 2006 No. 4 Smelt Dissolving Tank 07/20/2006 M16 66.00 ton BLS/hr Outlet

no TRS as H2S 2009 No. 2 Smelt Dissolving Tank 07/14/2009 M16 63.70 ton BLS/hr Outlet

no TRS as H2S 2009 No. 2 Smelt Dissolving Tank 07/14/2009 M16 64.00 ton BLS/hr Outlet

no TRS as H2S 2009 No. 1 Smelt Dissolving Tank 07/14/2009 M16 45.90 ton BLS/hr Outlet

no TRS as H2S 2009 No. 1 Smelt Dissolving Tank 07/15/2009 M16 45.90 ton BLS/hr Outlet

No TRS as H2S 2004 No. 4 Smelt Dissolving Tank ‐ East 12/01/2004

M16(modified) unspecified no production data given Outlet

No TRS as H2S 2004 No. 4 Smelt Dissolving Tank ‐ West 12/01/2004

M16(modified) unspecified no production data given Outlet

TRS as H2S 2009 SDTV No. 4 6/15/2009 M16A 66.66 ton BLS/hr Outlet

no TRS as H2S 2004 No. 1 SDT 3/24/2004 M16A 59.17 ton BLS/hr Outlet

no TRS as H2S 2004 No. 2 SDT 3/24/2004 M16A 74.58 ton BLS/hr Outlet

no TRS as H2S 2010 No. 1 SDT 8/31/2010 M16C 60.7 ton BLS/hr Outlet

No TRS as H2S 2008 No. 2 SDT 11/21/2008 M16A unspecified unspecified

BLS mass rate not provided (only

gpm) Outlet

No TRS as H2S 2007 No. 2 SDT 10/30/2007 M16A unspecified unspecified

BLS mass rate not provided (only

gpm) Outlet

No TRS as H2S 2003 No. 2 SDT 12/3/2003 M16A unspecified unspecified Outlet

no TRS as H2S 2005 No. 2 Smelt Dissolving Tank 8/1/2005 M16 50.2 ton BLS/hr Outlet

no TRS as H2S 2005 No. 2 Smelt Dissolving Tank 8/3/2005 M16 56.2 ton BLS/hr Outlet

no TRS as H2S 2005 No. 2 Smelt Dissolving Tank 8/4/2005 M16 57.5 ton BLS/hr Outlet

no TRS as H2S 2007 No. 1 Smelt Dissolving Tank 7/30/2007 M16 43.7 ton BLS/hr Outlet

no TRS as H2S 2007 No. 1 Smelt Dissolving Tank 7/31/2007 M16 43.7 ton BLS/hr Outlet

no TRS as H2S 2007 No. 2 Smelt Dissolving Tank 7/17/2007 M16 62.5 ton BLS/hr Outlet

no TRS as H2S 2007 No. 2 Smelt Dissolving Tank 7/19/2007 M16 63.9 ton BLS/hr Outlet

Test_data_memo_appendices.xlsx App D SDT TRS 
RTI+EUID

105.EU445D107.09‐P2

109.SDT3109.SDT4111.G‐127

166.ST01166.ST02174.G‐63C

174.G‐63C

124.020124.021100.109112.AA‐101

114.U508115.SM01115.SM01116.004119.EQT005126.SDT127.SDT1136.EU 031

137.204138.003142.P7413146.10146.10146.17148.002

Outlet ‐ Testing Methodology Data Outlet ‐ Average Stack Gas Parameters Outlet ‐ Average Emissions Data 

Average Sampling Run

Length_Outlet(mins)

Average Fraction of

Isokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average Gas

Pressure_Outlet(in. Hg)

AverageGas CO2_Inlet

(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outlet

concentration units

Number ofOutlet Test Runs

Count OutletNon‐Detect

Runs

Average_Outlet(lb/hr)

Average_O(lb/product

60 unspecified 27076 11855 46.09 180 29.45 0.13 20.19 7.23 ppmdv 3 0 0.446 

60 102.4 21808 4934 71.6 197.6 29.676 unspecified unspecified 5.72 ppm as SO2 3 0 0.921 

180 unspecified 16923 8630 38.6 167 29.52 0 20.9 4.93 ppm 3 0 0.23 

180 unspecified 22355 9325 49 177 29.51 0 20.9 3.02 ppm 3 0 0.15 

62 97.83 26630 20899 29.82 183.7 29.69 ‐0.03 20.7 5.82 ppm 3 0 0.6342 

60 100.2 42564 24297 32.8 159.2 29.53 0 20.9 3.71 ppm 3 0 0.48 

60 101.8 31171 13241 48.6 176.5 29.44 0 20.9 16.4 ppm 3 0 1.2 

60 100.7 29625 15171 38.9 169 29.91 0 20.9 3.75 ppm 3 0 0.3 

60 98.5 28472 16983 32.2 157.1 29.91 0 20.9 14.4 ppm 3 0 1.2 

180 unspecified 40751 unspecified unspecified unspecified unspecified unspecified 2.999333333 ppm as SO2 3 0 0.647933333 0.011

180 unspecified 30980 unspecified unspecified unspecified unspecified unspecified 5.441333333 ppm as SO2 3 0 0.893033333 0.015

92 12567 4590 53.2 179 28.33 0.4 19.56666667 14.15666667 ppm 3 0 0.344883071 0.005

unspecified 95.82 85119 47483 34.46 166 0 20.5 3 0 0.335160787 0.002

193 36087 19390 24.97666667 166.33 29.22333333 0 21 5.7 ppmdv as H2S 3 0 0.58 

180.0447 19046 9545 40.5 167.6 29.94 0 20.9 4.874 ppm as SO2 3 0 0.247 

180.067 18998 10564 34.4 162.9 29.94 0 20.9 3.856 ppm as SO2 3 0 0.2159 

60 95.7 47368 28533 29.8 157.6 30 0 20.9 2.45 ppmd 3 0 0.4 

180 32163.33333 22139 21.43333333 145.23 30.08 0 20.9 7.07 ppmv 3 0 0.831 

180 96.21666667 42308 30881.66667 18.11 134.31 29.36 0 20.77 1.47 ppm as SO2 3 0 0.2404 0.004

180 26880.33333 14638 33 161.9333333 29.81 0 20.9 1.631 ppm as SO2 3 0 0.1265 

76.33333333 105.4 34300 11500 57.01333333 183.6666667 28.57 0.233333333 19.73333333 8.15 ppm as H2S 3 0 0.5 

0.008

60 104.0433333 unspecified unspecified 55.96 199.9966667 30.1 1.1 19 1.5 ppm 3 0 0.05 

180 30089 17286 31.4 160 29.45 0 20.9 3.1 ppm 3 0 0.282 

180 101.8 25931.33333 14744 31.6 148.0666667 28.64333333 0 20.9 1.822 ppm as SO2 3 0 0.1427 0.001

180 107.5333333 24716.66667 14369 29.86666667 149.8 28.65 0 20.9 1.878333333 ppm as SO2 3 0 0.143233333 0.001

180 101 36921 17321.66667 41.23333333 175.7 28.82 0.2 20.8 1.500333333 ppm as SO2 3 0 0.1379 0.001

66.33333333 26619 15240 32.4 163.9966667 29.93 0 20.9 13.02 ppm as SO2 3 0 1.04 

Test_data_memo_appendices.xlsx App D SDT TRS 
RTI+EUID

148.008149.P005149.P005150.CREC‐2a

150.CREC‐2b

154.P38 ‐ Smelt

Dissolving Tank 3

155.SDT162.381C162.382B163.SD1902163.SD1903175.ST2A177.EU0805179.SDT180.D002, D907

182.110186.RB17189.SN27189.SN28190.R405190.R406196.SN‐08North

196.SN‐08South

196.SN‐15

198.020200.007_8, 007_9

202.Smelt Dissolving

Tank EU322

203.2DTScr

Average Sampling Run

Length_Outlet(mins)

Average Fraction of

Isokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average Gas

Pressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outlet

concentration units

Number ofOutlet Test Runs

Count OutletNon‐DetectRuns

Average_Outlet(lb/hr)

Average_O(lb/product

60.33333333 26760 9763 55.3 183.9966667 29.78 0 20.9 33.8 ppm as SO2 4 0 1.72 

180 15900 7030 45.03333333 173 28.31 0 20.8 26 ppmd 3 0 0.96 0.014

180 13800 5930 46.33333333 174 28.9 0 20.8 28 ppmd 3 0 0.89 0.012

60 16704 5982 56.6 185 30.16 0 20.9 17.5 ppm as SO2 3 0 0.6 

60 16923 6125 56.2 184 30.16 0 20.9 11.3 ppm as SO2 3 0 0.4 

60 13372 6845 37.2 176.1 29.46 1 19 2 ppmvd as SO2 12 0 0.073 

62 103.2 34390 15416 44.7 191.33 29.92 0.1 20.6 11.41 ppm as SO2 5 0 0.917 

90 25921 11780 44.5 177.8 29.62 0 20.9 7.3 ppm 3 0 0.45 

95.33333333 46210 23668.33333 38.5 167 29.62 0.07 20.23 9.4 ppm 3 0 1.184 0.011

60 21470 13851 25.3 152 29.98 0 20.9 3.2 ppmd as SO2 3 0 0.237 

60 26147 18772 18.7 138.3333333 29.98 0 20.9 0.933333333 ppmd as SO2 3 0 0.093 

59 31890 23481 17.3 135.6633333 30.05 0 21 0.86 ppm as SO2 3 0 0.108 

180 unspecified 16477 unspecified unspecified unspecified unspecified unspecified 1.9 ppmd as SO2 3 0 0.17 0.002

90.33333333 36585 17457 42.2 173 29.5 0 20.9 9.6 ppm 3 0 0.88 179.6666667 21972 10863 40.7 170.4666667 29.82 0 21 6.61 ppm 3 0 0.38 

60 19321.66667 9456 42 167.0333333 30.04 0.1 20.4 10.4 ppmvd 3 0 0.5 77 50221 24161 42.05 171 29.7 0 20.9 20.6 ppm 4 0 2.67 

192 20263 9488.783333 44.52 166 0 20 0.1141 ppmvd 3 0 0.006 

192 27722 12852.91667 45.44 165 0 20 2.72 ppmvd 3 0 0.19 

62.66666667 31148 18348 28.9 155.66 28.89 0 20.9 4.22 ppm 3 0 0.379 

60 29536 18787 26.1 154.33 29.94 0.073333333 20.66 6.63 ppm 3 0 0.647 

180 23769 12116 39.1 169.5 29.87 0 21 0.8 ppmvd as H2S 3 0 0.05 0.000

180 25487 13678 36.3 165.6 29.86 0 21 0.7 ppmvd 3 0 0.05 0.000

180 unspecified 8613 unspecified unspecified unspecified unspecified unspecified 0.7 ppmvd 3 0 0.03 0.000

60 29832 14414 40.603 177 29.04 0.2 20.5 15.51 ppm 3 0 1.19 

90 55688 25843 43.3 172 29.3 0 20.9 3.26 ppm 3 0 0.45 60 28600 16200 2.8 ppmvd 3 0 0.24 

61 12100 7630 26.6 156 29.98 0.03 20.95 5.43 ppmv 1 0 0.22 

Test_data_memo_appendices.xlsx App D SDT TRS 
RTI+EUID

226.SDT2240.RF02240.RF05240.RF06242.AA‐012

243.R403243.R408531.RF10600.G0805600.G0807615.25617.P21208228535.002208228535.008102.SDTV10135.007‐1, 007‐2

140.57142.P7236143.7005143.7015143.7025157.SDT163.SD2906167.007SDT171.006171.006171.007171.007171.008171.008173.SDT175.ST3A185.05188.015SD1

Average Sampling Run

Length_Outlet(mins)

Average Fraction of

Isokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average Gas

Pressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outlet

concentration units

Number ofOutlet Test Runs

Count OutletNon‐DetectRuns

Average_Outlet(lb/hr)

Average_O(lb/product

180 26590.93333 13094 38 166.66 29.92933333 1 19.5 14.4 ppm 3 0 0.3117 

60 46166 30312 23.9 147.5 29.72 0 20.9 4.1 ppm 3 0 0.654 

90 31313 17080 34.7 165 29.59 0 20.9 10.3 ppm 3 0 0.93 0.00

90 32674 17508 36 164.2 29.59 0 20.9 2.19 ppm 3 0 0.2 0.001

180 35976 16424 44.4 173 29.48 0 21 18.6 ppm 3 0 1.626 

90 35600 19548 34.7 166.5 29.87 0 20.9 9.63 ppm 3 0 0.99 

90 24431 12046 40.5 172.4 29.71 0 20.9 6.11 ppm 3 0 0.39 

90 40737 14483 56.6 185 29.99 0 20.9 10.53 ppm 3 0 0.81 

120 28559 9703 57.1 184 28.93 0 20.9 21 ppm 3 0 1.1 

70 13200 47.3 11.4 ppm 3 0 0.8 

60 33330 22241 23.3 147.3 29.96 0.02 20.54 2.33 ppmvd 3 0 0.28 

180 10677 29.03 7.86 ppmvd 3 0 0.4446 

60 18150 39.8 28.4 ppmd 3 0 2.7 

64.33333333 46491 37.2 6.1 ppmd 3 0 1.5 

60.00 N/A 37092 21902 31.17 161.0 30.21 13.90 7.00 7.02 ppm 3 0 0.816 

90.00 N/A 33600 15833 43.83 173.3 30.07 0.00 20.80 14.05 ppm 3 0 1.1806 

180.00 N/A 20361 9852 41.90 173.2 29.87 0.07 20.46 15.41 ppmd 3 0 0.81 

63.33 97.67 35038 22259 24.97 155.0 29.51 0.00 20.90 7.1 ppm 3 0 0.8417 

90.00 N/A 10499 7357 18.73 148.3 unspecified 0.00 20.90 1.4 ppm 3 0 0.0547 

90.00 N/A 9833 6340 24.93 151.1 29.72 0.00 20.90 0.22 ppm 3 0 0.0074 

90.00 N/A 24320 15919 23.03 158.0 29.77 0.00 20.90 1.9 ppm 3 0 0.16 

60.00 N/A 3675 3001 10.20 115.3 29.60 0.00 20.90 0.5 ppm 3 0 0.008 

60.00 N/A 33406 19071 31.90 156.6 unspecified 0.00 20.90 6.5 ppmd 3 0 0.66 

63.67 93.26 48779 26486 34.97 264.4 29.94 0.00 20.90 3.3 ppm 3 0 0.4639 

180.00 N/A 7656 3731 41.40 170.9 29.73 0.00 21.00 3 ppmvd 3 0 0.06 

180.00 N/A 9318 4506 41.87 171.3 29.80 0.00 21.00 21.5 ppmvd 3 0 0.51 

180.00 N/A 14514 8103 33.90 162.3 29.79 0.00 21.00 3 ppmvd 3 0 0.13 

180.00 N/A 12853 7678 29.37 155.2 29.66 0.00 21.00 18.6 ppmvd 3 0 0.76 

180.00 N/A 33417 15882 42.70 173.3 29.75 0.00 21.00 4.1 ppmvd 3 0 0.35 

180.00 N/A 28637 12103 47.77 177.0 29.79 0.00 21.00 16.9667 ppmvd 3 0 1.0867 

175.00 N/A 17135 10615 30.00 138.0 29.99 0.00 20.90 7.4 ppm 3 0 0.4169 

60.67 N/A 38309 17821 44.00 173.3 29.83 0.00 20.90 1.53 ppm 3 0 0.1433 

60.00 N/A 13127 7194 35.27 165.0 30.00 0.03 20.95 5.12 ppmvd 3 0 0.196 

73.33 N/A 20494 11753 32.91 161.2 30.09 0.10 20.34 1.9172 ppm 3 0 0.1196 

Test_data_memo_appendices.xlsx App D SDT TRS 
RTI+EUID

188.017SD2199.004201.SR0034205.010206.G‐35

206.G‐36

606.SDT2606.SDT3606.SDT4610.10610.10610.9610.9133.12a133.12b132.4SDT148.002, SCMT1148.008, SCMT2148.002203.2DTScr203.2DTScr203.2DTScr610.10610.10610.10610.9610.9610.10610.10

Average Sampling Run

Length_Outlet(mins)

Average Fraction of

Isokinetic SamplingRate_Outlet(%)

AverageAirflowRate_Outlet(acfm)

AverageAirflowRate_Outlet(dscfm)

AverageGasMoisture_Outlet(%)

AverageGasTemp_Outlet(F)

Average Gas

Pressure_Outlet(in. Hg)

AverageGas CO2_Inlet(%)

AverageGasOxygen_Outlet(%)

Average_Outletconcentration

Average Outlet

concentration units

Number ofOutlet Test Runs

Count OutletNon‐DetectRuns

Average_Outlet(lb/hr)

Average_O(lb/product

72.67 N/A 19215 11405 30.87 158.5 30.09 0.10 20.51 2.055 ppm 3 0 0.12436 

93.00 N/A 21005 11003 37.20 166.0 29.59 0.00 21.00 12.6 ppm 3 0 0.73 

60.00 N/A 51824 28613 34.88 164.7 29.86 0.00 20.80 7.9 ppm 3 0 1.2 

60.00 N/A 28378 18828 24.10 151.0 unspecified 0.00 20.90 1.5 ppm 3 0 0.1467 

66.67 N/A 19176 6578 55.21 179.0 27.10 0.00 20.90 0.936 ppm 3 0 0.0328 unspecified70.00 N/A 16990 8334 36.93 157.3 27.23 0.00 20.90 0.988 ppm 3 0 0.0436 unspecified

180.00 N/A 17411 9386 36.30 165.0 30.00 0.00 21.00 8.16 ppm 3 0 0.404 

179.00 N/A 21545 13151 28.60 158.0 29.98 0.00 20.90 5.5 ppm 3 0 0.381 

63.00 N/A 33283 19776 30.10 163.0 30.02 0.00 20.90 8.6 ppm 3 0 0.903 

60.00 N/A 11920 6888 31.20 165.6 29.83 0.13 20.90 19.1133 ppmvd 3 0 0.72 

60.00 N/A 12902 7575 30.20 165.0 30.00 0.21 20.90 31.9467 ppmvd 3 0 1.32 

60.00 N/A 15768 9311 30.90 159.7 30.00 0.00 20.90 10 ppmvd 3 0 0.52 

60.00 N/A 12817 7613 30.50 159.1 30.00 0.00 20.90 4.7 ppmvd 3 0 0.2 

30.00 N/A 16821 12689 16.00 136.6 30.36 unspecified unspecified 0.063 ppm 1 0 0.004 unspecified30.00 N/A 19682 14363 18.00 142.0 30.36 unspecified unspecified 2.7 ppm 1 0 0.205 unspecified

60 unspecified 30482 17566.7 31.67 163.86 29.8 unspecified unspecified unspecified 3 0 0.507633333 0.007

60 28718 18876 24.6 150.3333333 30.16 0.2 20.7 7.527333333 ppm 3 0 0.696 

60 21003 10970 38.5 172 30.42 0.133333333 20.76666667 26.19333333 ppm 3 0 1.35 

60 27964 13225 43.7 175 unspecified 0 20.9 23.795 ppm 3 0 1.64 

unspecified unspecified 11441 unspecified unspecified unspecified unspecified unspecified 4.432 ppmdv 1 0 unspecified 

unspecified unspecified 12266 unspecified unspecified unspecified unspecified unspecified 5.241 ppmdv 1 0 unspecified 

60 unspecified unspecified unspecified unspecified unspecified unspecified unspecified 14.2725 ppmv 4 0 unspecified unspecified 60 101.3 12179 7211.476667 31 158.7 unspecified 0.08 20.4 25.9 ppmvd 3 0 1.02 

60 100 13716.9 8723.348333 26.3 156.3 unspecified 0.04 20.05 35.3 ppmvd 3 0 1.689 

60 107.2 13347.8 8266.775 28.5 155.2 unspecified 0.25 20.4 32 ppmvd 3 0 1.43 

60 100.4 9791 4233.616667 47.5 179 unspecified 0.04 20.11 47.6 ppmdv 3 0 1.1 

60 92.6 10323 5039.133333 41.4 171.9 unspecified 0.14 19.99 47 ppmdv 3 0 1.29 

60 101.8 10708 6709.083333 27.2 152.1 unspecified 0.18 20.11 34.9 ppmdv 3 0 1.28 

60 99.4 16826 8419.916667 40 168.6 unspecified 0.17 20.09 41.1 ppmdv 3 0 1.99 

No inlet data were provided for SDT TRS.

Test_data_memo_appendices.xlsx App D SDT TRS 
RTI+EUID

105.EU445D107.09‐P2

109.SDT3109.SDT4111.G‐127

166.ST01166.ST02174.G‐63C

174.G‐63C

124.020124.021100.109112.AA‐101

114.U508115.SM01115.SM01116.004119.EQT005126.SDT127.SDT1136.EU 031

137.204138.003142.P7413146.10146.10146.17148.002

Suspect Data Exclude Comment Data analysis notes Multi‐stack sums

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

Slightly caustic boiler blowdwon is used as the

scrubbing liquid. 105.EU445D.TRS as H2S 0.446 0.0074 

107.09‐P2.TRS as H2S 0.921 0.0100 

109.SDT3.TRS as H2S 0.23 0.0040 

109.SDT4.TRS as H2S 0.15 0.0020 

SDT operates with SCBR/INC_RF normally, but only

the SDT bypass with the SCBR alone was tested as

an alternative condition. Re‐calculated mass

emission rate to determine that it was "as H2S"

because eqns not provided and not specified in

report. 111.G‐127.TRS as H2S 0.6342 0.0140 

Checked calculation to ensure mass reported as

H2S 166.ST01.TRS as H2S 0.48 0.0070 

Checked calculation to ensure mass reported as

H2S 166.ST02.TRS as H2S 1.2 0.0140 

174.G‐63C.TRS as H2S separate stacks 

174.G‐63C.TRS as H2S separate stacks 1.5 0.010737294 

124.020.TRS as H2S 0.647933333 0.0111 

124.021.TRS as H2S 0.893033333 0.0154 

(1) Only H2S was detected. Test report did not

provide detection limits, but instead treated other

TRS compounds as zero in calculatons. (2)

Recalculated TRS lb/hr and lb/ton using subpart BB

eqn. 100.109.TRS as H2S 0.344883071 0.0060 

smelt dissolving tank rebuilt in 2009 following

testing. TRS as SO2 provided. Converted to as H2S basis. 112.AA‐101.TRS as H2S 0.335160787 0.0029 

Don’t need M16A concentration (different units);

however can use mass rate

Modified version of M16A used to provide TRS as

H2S. 114.U508.TRS as H2S 0.58 0.0054 

There are 2 SDTs supporting 1 RF. 115.SM01.TRS as H2S separate stacks 

There are 2 SDTs supporting 1 RF. 115.SM01.TRS as H2S separate stacks 0.4629 0.0053 

116.004.TRS as H2S 0.4 0.0039 

119.EQT005.TRS as H2S 0.831 0.0150 126.SDT.TRS as H2S 0.2404 0.0047 

127.SDT1.TRS as H2S 0.1265 0.0016 

Test report labels method as 16A/B. 136.EU 031.TRS as H2S 0.5 0.0044 

Only 1 run Yes Only 1 run 137.204.TRS as H2S 0 0.0090 

Did not provide H2S, MeSH, DMDS, or DMS values.

Using eqn on p. 12 of pdf report, could see that

testers used MW of H2S for mass calculations (so

TRS was reported as H2S). 138.003.TRS as H2S 0.05 0.0009 

New stack and scrubber specific to SDT‐1 installed

during 2011.

Emissions are from 2 SDTs with a combined stack.

Did not provide H2S, MeSH, DMDS, or DMS values.

Confired as H2S by reviewing equation used for

mass calculation. 142.P7413.TRS as H2S 0.282 0.0040 

Test report multiplies lb/ton values for upriver and

downriver SDTs by 2, then averages them to get

total; same as just adding the upriver and

downriver lb/ton values together. Test report uses

parameters from PM Runs 1 and 2 for TRS Runs 1

and 2 and provides parameters for TRS Run 3;

does not provide isokinetic for Run 3 of TRS test;

used number from Run 3 of PM test (assuming

overlap between PM and TRS Run 3). 146.10.TRS as H2S separate stacks 

Test report multiplies lb/ton values for upriver and

downriver SDTs by 2, then averages them to get

total; same as just adding the upriver and

downriver lb/ton values together. Test report uses

parameters from PM Runs 1 and 2 for TRS Runs 1

and 2 and provides parameters for TRS Run 3;

does not provide isokinetic for Run 3 of TRS test;

used number from Run 3 of PM test (assuming

overlap between PM and TRS Run 3). 146.10.TRS as H2S separate stacks 0.285933333 0.003777667 

Test report uses parameters from PM run 3 for

TRS Run 3 and provides parameters for TRS Runs 1

and 2; does not provide isokinetic for Runs 1 and 2

of TRS test; used numbers from Runs 1 and 2 of

PM test (assuming overlap between PM and TRS

test runs). 146.17.TRS as H2S 0.1379 0.0014 

148.002.TRS as H2S different dates 1.04 0.0176 

Test_data_memo_appendices.xlsx App D SDT TRS 
RTI+EUID

148.008149.P005149.P005150.CREC‐2a

150.CREC‐2b

154.P38 ‐ Smelt

Dissolving Tank 3

155.SDT162.381C162.382B163.SD1902163.SD1903175.ST2A177.EU0805179.SDT180.D002, D907

182.110186.RB17189.SN27189.SN28190.R405190.R406196.SN‐08North

196.SN‐08South

196.SN‐15

198.020200.007_8, 007_9

202.Smelt Dissolving

Tank EU322

203.2DTScr

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

Run 1 not included in averages; used Runs 2‐4. 148.008.TRS as H2S different dates 1.72 0.0206 

Separate tests conducted on SDT on different days ‐

report provided no reason for the separate tests.

H2S was the only TRS compound detected; others

treated as zero. 149.P005.TRS as H2S reason unspecified 0.96 0.0140 

Test included 4 runs, but "Integrator paper

jammed during run. Illegible data from 1020‐1040

hours (5 injects)." Run 1 was not included in the

averages. 2 of the 4 TRS were non‐detect in all

runs; only H2S and MeSH were detected. 149.P005.TRS as H2S reason unspecified 0.89 0.0129 

150.CREC‐2a.TRS as H2S

Separate stacks: The smelt dissolving tank

emission unit id CREC‐2 has two identical

stacks (CREC‐2a and CREC‐2b) and each

stack has an identical scrubber (SCRBSTa

and SCRBSTb). 

150.CREC‐2b.TRS as H2S

Separate stacks: The smelt dissolving tank

emission unit id CREC‐2 has two identical

stacks (CREC‐2a and CREC‐2b) and each

stack has an identical scrubber (SCRBSTa

and SCRBSTb). 1 0.01 

"Runs 1, 2, and 3 were not included in the average

results due to failed validations." Derived

parameters for each run by averaging the

parameters measured at the start of that run and

the next run.

154.P38 ‐ Smelt Dissolving Tank 3.TRS

as H2S 0.073 0.0021 

"Runs 1 and 3 were voided due to sub‐isokinetic

sampling rates. Additional test runs were

completed in order to obtain three acceptable

isokinetic sampling rate test runs." Report

calculated TRS as S; revised to calculate TRS as H2S

and added my calculated values here. 155.SDT .TRS as H2S 0.917 0.0118 

162.381C.TRS as H2S 0.45 0.0087 

Only H2S was detected. Concentration averages

were calculated using 0 for non‐detect TRS

compounds. 162.382B.TRS as H2S 1.184 0.0111 

Although report presents ppmd TRS "as H2S,"

calculations indicate it is actually "as SO2."Inconsistency in moisture content between two

tables in report; went with number in lab report

table. Converted kg BLS/hr process rate to ton

BLS/hr. 163.SD1902.TRS as H2S 0.237 0.0043 

Although report presents ppmd TRS "as H2S,"

calculations indicate it is actually "as SO2."Converted kg BLS/hr process rate to ton BLS/hr. 163.SD1903.TRS as H2S 0.093 0.0017 

Report calculated TRS as S; revised to calculate TRS

as H2S and added my calculated values here. 175.ST2A.TRS as H2S 0.108 0.0037 

Test report emission factor of 0.0038 lb/TBLS was

on an as SO2 basis; recalcuated as H2S. 177.EU0805.TRS as H2S 0.17 0.0021 

179.SDT.TRS as H2S 0.88 0.0102 

EmissionUnitID: No. 3 SDT (D002) and salt cake

mix tank (D907) have combined exhausts 180.D002, D907.TRS as H2S 0.38 0.0050 

182.110.TRS as H2S 0.5 0.0080 

TRS runs 1‐3 correspond to PM runs 1‐3. Averages

calculated using PM runs 1‐3 and TRS run 4 data 186.RB17.TRS as H2S 2.67 0.0210 

189.SN27.TRS as H2S 0.006 0.0001 189.SN28.TRS as H2S 0.19 0.0017 190.R405.TRS as H2S 0.379 0.0070 

190.R406.TRS as H2S 0.647 0.0090 

Flow data used were from con‐current PM testing

(3 60‐min runs) 196.SN‐08North.TRS as H2S 0.05 0.0006 

Flow data used were from con‐current PM testing

(3 60‐min runs) 196.SN‐08South.TRS as H2S 0.05 0.0006 

Flow data not provided 196.SN‐15.TRS as H2S 0.03 0.0003 

198.020.TRS as H2S 1.19 0.0110 200.007_8, 007_9.TRS as H2S 0.45 0.0040 202.Smelt Dissolving Tank EU322.TRS as

H2S 0.24 0.0041 

Yes Only 1 run 203.2DTScr .TRS as H2S 0.22 0.0190 

Test_data_memo_appendices.xlsx App D SDT TRS 
RTI+EUID

226.SDT2240.RF02240.RF05240.RF06242.AA‐012

243.R403243.R408531.RF10600.G0805600.G0807615.25617.P21208228535.002208228535.008102.SDTV10135.007‐1, 007‐2

140.57142.P7236143.7005143.7015143.7025157.SDT163.SD2906167.007SDT171.006171.006171.007171.007171.008171.008173.SDT175.ST3A185.05188.015SD1

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

Reported non‐detect for all three runs for MeSH,

DMDS, and DMS‐‐could not find any information

on MDL 226.SDT2.TRS as H2S 0.3117 0.0058 

H2S was the only TRS compound measured. Test

report provided detcection limits but used 0 for

determining the TRS concentration. 240.RF02.TRS as H2S 0.654 0.0097 

Concentration averages were calculated using 0

for non‐detect TRS compounds (DMS and DMDS

were all ND) 240.RF05.TRS as H2S 0.93 0.0078 

Concentration averages were calculated using 0

for non‐detect TRS compounds (DMS and DMDS

were all ND) 240.RF06.TRS as H2S 0.2 0.0017 

yes

TRS data included a dilution factor, which was not

accounted for in values reported here

Concentration averages were calculated using 0

for non‐detect TRS compounds (only H2S was

detected) 242.AA‐012.TRS as H2S 1.626 0.0130 

Flow rates are from concurrent PM test. 243.R403.TRS as H2S 0.99 0.0122 

Concentration averages were calculated using 0

for non‐detect compounds (DMS and DMDS were

all ND). Flow rates are from concurrent PM test. 243.R408.TRS as H2S 0.39 0.0032 

DMDS was all ND. Used 0 for values for DMDS. 531.RF10.TRS as H2S 0.81 0.0050 

Run 1 was 3 hrs. Runs 2‐3 were 1.5 hrs. 600.G0805.TRS as H2S 1.1 0.0130 

Did not provide all stack conditions‐‐PM tests were

not concurrent. Non‐detect TRS compounds

treated as 0. 600.G0807.TRS as H2S 0.8 0.0080 

615.25.TRS as H2S 0.28 0.0050 617.P21.TRS as H2S 0.4446 0.0130 208228535.002.TRS as H2S 2.7 0.0250 

208228535.008.TRS as H2S 1.5 0.0119 

102.SDTV10.TRS as H2S 0.816 0.0067 

TRS as MeSH, DMS, and DMDS were all non‐

detects. Combined East and West stack values only

given. 135.007‐1, 007‐2.TRS as H2S Combined stacks given 1.1806 0.0127 

TRS as H2S is the only pollutant given. 140.57.TRS as H2S 0.81 0.0153 

142.P7236.TRS as H2S 0.841666667 0.0130 

TRS as MeSH, DMS, and DMDS were all non‐

detects. 143.7005.TRS as H2S 0.0547 0.0031 

TRS as MeSH, DMS, and DMDS were all non‐

detects. 143.7015.TRS as H2S 0.0074 0.0007 

TRS as MeSH, DMS, and DMDS were all non‐

detects. 143.7025.TRS as H2S 0.16 0.0062 

157.SDT.TRS as H2S 0.008 0.0002 

163.SD2906.TRS as H2S 0.66 0.0086 

167.007SDT.TRS as H2S 0.4639 0.0064 171.006.TRS as H2S different dates 0.06 0.0022 

171.006.TRS as H2S different dates 0.51 0.0188 

171.007.TRS as H2S different dates 0.13 0.0047 

171.007.TRS as H2S different dates 0.76 0.0272 

171.008.TRS as H2S different dates 0.35 0.0041 

171.008.TRS as H2S different dates 1.086666667 0.0130 

173.SDT.TRS as H2S 0.4169 0.0100 

Concentration is TRS as DMS. TRS as H2S, MeSH

and DMDS were all non‐detects 175.ST3A.TRS as H2S 0.143333333 0.0012 

185.05.TRS as H2S 0.196 0.0053 

188.015SD1.TRS as H2S 0.119583333 0.0041 

Test_data_memo_appendices.xlsx App D SDT TRS 
RTI+EUID

188.017SD2199.004201.SR0034205.010206.G‐35

206.G‐36

606.SDT2606.SDT3606.SDT4610.10610.10610.9610.9133.12a133.12b132.4SDT148.002, SCMT1148.008, SCMT2148.002203.2DTScr203.2DTScr203.2DTScr610.10610.10610.10610.9610.9610.10610.10

Suspect Data? Cause for suspicion Exclude Data? Reason for excluding Test Report Comment

Duplicate check:

RTICode+EmissionUnitID+Pollutant Duplicate_Emission_Unit_Poll_notes Unit total lb/hr

Unit total EF,

lb/production So

188.017SD2.TRS as H2S 0.12436 0.0041 

TRS as MeSH, DMS, and DMDS were all non‐

detects. 199.004.TRS as H2S 0.73 0.0100 

TRS runs were taken within the runs of the other

pollutants. The summary sheet for TRS did not

have all the parameters needed for this

spreadsheet. Therefore many points came for thesummary sheet of the other pollutants. 201.SR0034.TRS as H2S 1.2 0.0145 

205.010.TRS as H2S 0.146666667 0.0029 

206.G‐35.TRS as H2S 0.032766667 unspecified 206.G‐36.TRS as H2S 0.043633333 unspecified 

TRS as MeSH, DMS, and DMDS were all non‐

detects. 606.SDT2.TRS as H2S 0.404 0.0090 

TRS as MeSH, DMS, and DMDS were all non‐

detects. 606.SDT3.TRS as H2S 0.381 0.0093 

TRS as MeSH, DMS, and DMDS were all non‐

detects. 606.SDT4.TRS as H2S 0.903 0.0137 

Weak wash scrubber flow 610.10.TRS as H2S Separate conditions: weak wash scrubber 0.72 0.0110 

Water wash scrubber flow 610.10.TRS as H2S Separate conditions: water scrubber 1.32 0.0210 

Weak wash scrubber flow 610.9.TRS as H2S Separate conditions: weak wash scrubber 0.52 0.0110 

Water wash scrubber flow 610.9.TRS as H2S Separate conditions: water scrubber 0.2 0.0040 

yes

Modified Method 16 uses many other forms of

Sulfur to calculate total TRS. Yes

30‐min sample;

modified method

One thirty minute integrated sample. Modified

Method 16 Total TRS includes TRS as Hydrogen

Sulfide, Carbonyl Sulfide, Methyl Mercaptan, Ethyl

Mercaptan, Dimeththyl Sulfide, Carbon Disulfide,

Isopropyl Mercaptan, Ter‐Butyl Mercaptan, n‐

Propyl Mercaptan, Ethyl Methyl Sulfide,

Thiophene, Isobutyl Mercaptan, Dimethyl

Disulfide, 3‐Merhylthiophene,

Tetrahydrothiophene, 2‐Ethylthiophene, 2,5‐

Dimethylthiophene, and Diethyl Disulfide. 0.004 unspecified 

yes

Modified Method 16 uses many other forms of

Sulfur to calculate total TRS. Yes

30‐min sample;

modified method

One thirty minute integrated sample. Modified

Method 16 Total TRS includes TRS as Hydrogen

Sulfide, Carbonyl Sulfide, Methyl Mercaptan, Ethyl

Mercaptan, Dimeththyl Sulfide, Carbon Disulfide,

Isopropyl Mercaptan, Ter‐Butyl Mercaptan, n‐

Propyl Mercaptan, Ethyl Methyl Sulfide,

Thiophene, Isobutyl Mercaptan, Dimethyl

Disulfide, 3‐Merhylthiophene,Tetrahydrothiophene, 2‐Ethylthiophene, 2,5‐

Dimethylthiophene, and Diethyl Disulfide. 0.205 unspecified 

Flow rate from PM test was used in TRS test. TRS

emission rates provided in lb/K# BLS ‐ converted. 132.4SDT.TRS as H2S 0.507633333 0.0077 

The PIII emissions test data tab indicated the salt

cake tank was included in the test; however, the

test report does not specify whether the SCMT

enhausts into the SDT 148.002, SCMT1.TRS as H2S different dates 0.696 0.0118 

The PIII emissions test data tab indicated the salt

cake tank was included in the test; however, the

test report does not specify whether the SCMT

enhausts into the SDT 148.008, SCMT2.TRS as H2S different dates 1.35 0.0181 

A separate test of the SDT was performed on

9/28/10 but was discarded because it exceeded

the limit (0.0458 > 0.033 lb/ton BLS); only the

repeat test is provided for compliance. 148.002.TRS as H2S different dates 1.64 0.0270 

Engineering test. Plant personel provided CEMS

data for emission factor. Yes Only 1 run

Engineering test. Plant personel provided CEMS

data for emission factor. 203.2DTScr .TRS as H2S different dates unspecified 0.0250 

Engineering test. Plant personel provided CEMS

data for emission factor. Yes Only 1 run

Engineering test. Plant personel provided CEMS

data for emission factor. 203.2DTScr .TRS as H2S different dates unspecified 0.0320 

No flow data. Engineering test. Yes No flow data

4 runs were conducted: 2 as found (~19 ppm

each), 1 with caustic on (10.88 ppm), and 1 with

caustic on and pH increase (7.57 ppm) 203.2DTScr .TRS as H2S different dates unspecified unspecified 

Normal weak wash scrubber flow 610.10.TRS as H2S

Different dates and Separate conditions:

Normal weak wash scrubber flow 1.02 0.0200 

Low weak wash scrubber flow 610.10.TRS as H2S

Different dates and Separate conditions:

Low weak wash scrubber flow 1.689 0.0290 

Low water wash scrubber flow 610.10.TRS as H2S

Different dates and Separate conditions:

Low water wash scrubber flow 1.43 0.0240 

Weak wash scrubber flow 610.9.TRS as H2S

Different dates and Separate conditions:

Weak wash scrubber flow 1.1 0.0250 

Water scrubber flow 610.9.TRS as H2S

Different dates and Separate conditions:

Water scrubber flow 1.29 0.0290 

Weak wash scrubber flow 610.10.TRS as H2S

Different dates and Separate conditions:

Weak wash scrubber flow 1.28 0.0200 

Water scrubber flow 610.10.TRS as H2S

Different dates and Separate conditions:

Water scrubber flow 1.99 0.0310 

Test_data_memo_appendices.xlsx App D SDT TRS