DAQ-2024-011517

1

DAQC-1098-24
Site ID 10327 (B4)

MEMORANDUM

TO: STACK TEST FILE – INTERMOUNTAIN POWER SERVICE CORPORATION

THROUGH: Harold Burge, Major Source Compliance Section Manager

FROM: Paul Morris, Environmental Scientist

DATE: October 28, 2024

SUBJECT: Sources: Unit 1 and Unit 2 Boiler Stacks
Contact: Mike Utley – 435-864-6489
Location: Delta, Millard County, UT
Test Contractor: Intermountain Power In-House Staff
FRS ID# UT0000004902700010
Permit#: Title V Permit #2700010006, dated November 21, 2023
Action Code: TR
Subject: Review of Stack Test Report dated October 9, 2024

On October 21, 2024, DAQ received a test report for Unit 1 and Unit 2 PM10 emissions. Testing was
performed on August 27 and 28, 2024, to demonstrate compliance with the emission limits found in
Condition II.B.2.b. The DAQ-calculated test results are:

Source Test Date Test Method Pollutant Result Limit

Unit 1 9/27/2024 RM 5B PM10 0.0027* 0.0184*

Unit 2 9/28/2024 RM 5B PM10 0.0026* 0.0184*

* lbs/MMBtu

DEVIATIONS: No deviations were noted.

CONCLUSION: Units 1 and 2 PM10 emissions were within limits at the time of testing.

RECOMMENDATION: No further action required.

HPV: Not Applicable

ATTACHMENT: Stack test report dated October 9, 2024, DAQ generated spreadsheets

6 , 3
October 9,2024
Mr. Bryce Bird, Director
Utah Division of Air Quality
P.O. Box L4482O
Salt Lake City, Utah 84L1.4-4820
Attention: Compliance Section
Reference: Operating Permit #2700010006
Dear Director Bird:
-- -
U-",,, l, it..Pru-,;f'rFl, i .,i'
E rtv I l? () N tJ fl-T4:!:9-Llil-l IJ
OCT 21
I ._
-ltrl\/lSlON OF AIR Ol lAl' ITY
1.
2.
3.
Annual Compliance Particulate Testins of lntermountain Generating Station
lntermountain Power Service Corporation (IPSC) is submitting the results of the 2024 particulate testing
of Units 1 and 2 boiler stacks. Annual testing is required by our Title V Operating Permit, Section
11.8.2.b.1(b)(1). The testing was performed on August2T and28,2024 by IPSC personnel.
I certify that:
Testing was conducted while each applicable Unit was operating at conditions specified in IPSC's
operating permit for testing and under conditions indicated in the report.
During testing, the source combusted fuels used raw materials and maintained process
conditions representative of normal operations.
Based on information and belief formed after reasonable inquiry, the statements and
information in the document are true, accurate and complete.
lf you have any questions or comments, please contact Mr. Mike Utley, IPSC's Environmental Engineer,
at [phone], or [e-mail].
Cordially,
fur q V///'*,
Jon A. Finlinson
President and Chief Operations Officer
I rl:\ *lL
VL/HBl:he
Attachment
cc: Kevin Peng Greg Huynh
Tamer Ellyahky Mike Utley
850 West Brush Wellman Road, Delta, Utah, 84524 / Telephone: [phone] I FAX: [phone] / Fed. l.D. #87-0388573
UTAFi iJFPART
F.ll\/l R ol'.1 it.I f NTAL Q t JAI_lTy
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Executive Summary
The Intermountain Power Service Corporation (IPSC) has performed stack testing to determine
particulate matter emissions (PMro) from the Intermountain Power Project (IPP) boiler Units
I SGA and 2SGA. The testing occurred on August 2'7 and28,2024, and was required under
IPSC's Title V Operating Permit, #2700010006, Condition II.B.2.b.l(b).
The results of that testing indicate that IPSC is in compliance with the permit condition and other
regulatory requirements. The permit limit for PMro for each stack is 0.0184 pounds PM'o per
million British Thermal Unit heat input (lb/mmbtu). The actual average PMro emissions during
testing were as follows:
2SGA
Emission Rate
0.0025 lb/mmbtu
0.0023lb/mmbtu
Content Outline
1.0 lntroduction
2.0 Summary of Compliance Results
3.0 Test Conditions
4.0 Sampling and Analysis Procedures
5.0 Quality Control / Quality Assurance
6.0 Observations
Appendix A
Appendix B
Appendix C
Appendices Dr and Dz
Appendix E
Appendix F
Appendix G
Tables and Figures
Pre-Test Protocol
Production Data
Unit-Specific Field and Laboratory Data
Emissions and Test Formulae
Field Flow Data
Calibrations and Standards
1.0 Introduction
l.l Overview
IPSC operates under the authority of a Title V Operating Permit, #2700010006, issued
November 21,2023. PM;s compliance testing is required by this permit at Condition
II.B.2.b.l (b). That permit condition requires particulate emissions testing on Boiler Units
l SGA and 2SGA using EPA Method 58. It also requires that the production rate during
testing be no less than 90 percent of the maximum production achieved in the previous
three (3) years. The particulate emission limit established in the operating permit is
0.0184 lb/mmBtu for each boiler, as specified at Condition II.B.2(b).
1.2 TestingOrganization
Testing was performed by IPSC personnel organized along lines of authority and
responsibility:
Plant Owner: Intermountain Power Agency
10653 S. River Front Parkway, Suite 120
South Jordan, UT 84095
Operating Agent: Los Angeles Department of Water and Power
lllHopeSt.
Los Angeles, CA 90012
Plant Operations and Contact:
President and COO:
Project Manager:
Test Coordinator:
QA/QC Data:
QA/QC Analytical:
Team Members:
Regulatory Oversight:
Intermountain Power Service Corporation
850 W. Brush Wellman Rd
Delta, UT 84624
435-8644414
Jon A. Finlinson
Mike Utley
VickiLyman
Kirk Stevens
VickiLyman
Kirk Stevens
Vicki Lyman
Kyle Church
Trevor Johnson
Rick Moody
Kirk Stevens
Utah Deparunent of Environmental Quality
Utah Division of Air Quality
P.O. Box 144820
Salt Lake City, UT 841144820
1.3 Source Description
The IPP is a coal fueled steam electric generating station consisting of two (2) identical
Babcock & Wilcox steam generator boilers. Each boiler is capable of producing 6.9
million pounds of steam per hour at2,975 psi and 1,005 degrees F to matching turbine-
generator sets. Each Unit is rated at 950 MW (megawatt).
Each Unit has associated pollution control devices to capture combustion products.
These devices include a high efficiency fabric filter for PMro emissions, and a limestone
scrubber for acid gases. Flue gas discharges from a 710 foot chimney after passing
through these devices.
Testing occurred at the mid-point of the chimney. The sampling point is located so as to
minimize interferences from disturbances upstream or downstream of the sampling point.
Test Description
The following sources were tested as per the operating permit:
- Intermountain Unit ISGA Boiler Stack
- Intermountain Unit 2SGA Boiler Stack
The testing was conducted on August2T and28,2024. A pretest protocol was
submitted to the UDAQ on June 17,2024. A copy of that protocol is attached in
Appendix B.
To evaluate compliance with the stipulated permit conditions, IPSC performed
emissions testing as set forth in the Code of Federal Regulations (CFR), Title 40,
Chapter I, Part 60, Appendix A.
t.4
The following methods were used to evaluate compliance:
Method 1 -
Method 2 -
"Sample and Velocity Traverses for Stationary Sources"
"Determination of Stack Gas Velocity and Volumetric Flow Rate
(type AS@ Pitot tube)"
2.0
Method 38 - "Gas Analysis for Carbon Dioxide, Oxygen, Excess Air and Dry
Molecular Weight"
Method 4 - "Determination of Moisture Content in Stack Gases"
Method 58 - "Determination of Nonsulfuric Acid Particulate Matter Emissions
from Stationary Sources"
Summary of Compliance Results
2.1 Particulate Emissions
The results of the emission testing by EPA Method 58 are summarized in the tables
below.
Unit I SGA Boiler Stack
Test
Run No.
DSCF
Collected
Emissions Rates
lb/hr lb/mmBtu
I
2
J
73.287
74.322
73.834
18.7
21.1
22.6
0.0022
0.0025
0.0027
Average:73.814 20.8 0.002s
Test
Run No.
DSCF
Collected
Emissions Rates
lb/hr lb/mmBtu
I
2
3
74.796
75.760
77.464
21.6
18.6
18.7
0.0025
0.0023
0.0021
Average =76.007 19.6 0.0023
Unit 2 SGA Boiler Stack
3.0 Test Conditions
3.1 Source Operations
Unit I SGA and Unit 2SGA boilers are each rated at 950 megawatts. Both Units are
coal-fired boilers. The stack gas vents through a fabric filter baghouse and a
limestone wet scrubber. Source operations were normal, steady state, full load, at or
above 90 percent ofrated capacity.
Production data during the testing period are attached as Appendix C.
Unit I SGA and Unit 2SGA boilers are permitted to burn bituminous, sub-
bituminous, and refined coal for steam-electric generation. Fuel analyses
representing the fuel bumed during testing are attached in Appendix C.
4.0 Sampling and Analysis Procedures
4.1 Emissions Testing
A.EPA Method 1: Sample and velocity traverses for stationary sources.
Figures 1a and lb are diagrams of Unit ISGA and 2SGA boiler stacks (both
stacks are identical). This reference method requires the tester, due to stack
geometry, to sample for particulate and velocity at twelve ( l2) separate
locations in the stack, six (6) per traverse. The locations of these points
relative to the stack are given in Table l.
EPA Method 38: For gas analysis of carbon dioxide, oxygen, excess air,
and dry molecular weight.
This reference method requires that a gas sample be extracted from the stack
for analysis currently with each of the three (3) EPA Method 58 runs. The
integrated gas sample is then analyzed via an Orsat for carbon dioxide and
oxygen. The nitrogen value is obtained by difference.
Results by Unit from these determinations are included in Appendices Dr
and D: with field and laboratory data forms.
EPA Methods 2,4, and 58 combined: For the determination of velocity,
volumetric flow rate, moisture content, and filterable particulate matter from
stationary sources.
IPSC tested using methodology consistent with EPA Methods 2,4, and 58.
Data from the three (3) separate runs for each Unit, which constitute a single
compliance test for filterable particulate matter, is summarized in Table 2
for Unit l SGA boiler stack and Table 3 for Unit 2SGA boiler stack. The
original laboratory and field data accumulated at the test site are presented
by Unit in Appendices Dr and Dz.
B.
C.
Impinger
Number
I
2
J
4
Data forms were used to record readings from the tests. These were blank
forms from the computer program to calculate the Method 58 sampling.
The data was entered into the program 1o calculate the Method 58 test
results. The data forms and the computer generated results are included by
Unit in Appendices Dr and D:. The computer progTam used is:
IsoCALC Workbook (MS EXCEL) for lsoKinetic Sampling
(By Apex lnstruments Version l.l4b (1998))
Figure I is a schematic of the sample train used to obtain the field data. A
stainless steel probe liner was used for the testing. The glass fiber filters
used in the train are 99.999 percent efficient on 0.3 micron particles and
have no organic binders (Whatman 934AH). These filters are tared before
use and re-weighed after the test to determine particulate loading. Air
filtration properties of the filter material is shown in the calibration
Appendix G. Because this is a Subpart Da source, filters were prepared by
being oven dried at 320' F for three (3) hours, desiccated for two (2) hours
and weighed to a constant tare.
During testing, the probe and filter were kept at 320o F + 25o F during
sampling.
A thermocouple was installed on the outlet of the filter to assure an outlet
temperature above the dew point of the stack gas. These readings are
recorded by Unit on the field sheets in Appendices Dr and D:. After
analysis was completed, the probe washings were evaporated and then
desiccated along with the filter. Afterwards, samples were conditioned at
320'F for at least six (6) hours. cooled in a desiccator for two (2) hours and
weighed until the final weight was constant. In addition, at least 60 DSCF
were collected over 120 minute time period.
Moisture in the stack gases was determined by Method 4. The "back-half'
of the moisture sampling train contained the following impingers:
Contents
Deionized water
Deionized water
Empty
Silica Gel
Amount
100 ml
100 ml
200 g
Parameter Collected
Moisture
Moisture
Moisture
Moisture
5.0
Prior to performing each day's EPA Method 58 tests, IPSC ran a pretest
cyclonic flow determination in the exhaust stacks per EPA Method I criteria
as shown in Appendix F. The stacks are testable if the average flow rate
varies less than 20 degrees from parallel to the vertical stack. The average
angles were found to satisfu this requirement.
The sampling train and Pitot tube lines were leak tested before and after
each run at a pressure or vacuum greater than that at any point during the
test. This was to assure the sample was not diluted or a false reading in the
manometer. The leak tests are shown on the data sheets by Unit in
Appendices Dr and D:.
Quality Control / Quality Assurance
Compliance Testine
The testing at the Intermountain Generating Station Boiler Stacks I and 2 were
conducted by IPSC personnel in compliance with EPA Method 58 criteria and our
pretest protocol. No deviations from the prescribed testing procedures were noted.
Calibrations
Pre- and post-test calibrations of the instruments used are attached in Appendix G.
5.1
5.2
IO
5.3 Regulations
The Intermountain Generating Station is a Subpart Da source. Consequently,
40CFR 60.48a(b) applies to our testing.
The following items for the test meet the regulation:
Dry basis F factor was used to calculate the emission rate.
Method 58 as required for a wet stack.
Sample run time was at least 120 minutes/run.
Greater than 60 ft3 of volume was collected per run.
Sample train was run at 320'F (+ 25' F).
Integrated l2 point Method 38 sampling was used to obtain diluent
gases.
Opacity was obtained using certified Continuous Opacity Monitors
(COM=s).
Plant operating and production data is found in Appendix C.
6.0 Observations
6.1 Compliance
Testing results indicate that IPP emissions meet regulatory standards and permit
limits as required.
11
APPENDIX A
Tables & Figures
Intermountain Power Service Corp.
850 W. Brushwellman Road
Delta, Utah 84624
Traverse Point Calculations
Plant: Intermountain Generating Station
Date: Augu st 27th through 281h, 2024
Sampling Location: unit #sGA-l and unit #SGA-2 Main Boiler Stacks
Port Size: 6"
Port Length (inside stack wall to outside flange): 9"
Port Length Total: 9"
Port Projection into Stack: 0"
Stack lnside Diameter: 336" = 615.75 sq ft
Point Calculation Basis: 40 CFR Pt. 60, App. A, Method l, Table 1-2.
Traverse Percent of Stack LD. Product of Port Traverse point
Points Stack I.D. inches Columns 2&3 Length location from
outside port
| &.7 04.4 336 14.784
2 &.8 14.6 336 49.056
3 &.9 29.6 336 99.4s6
4 & t0 70.4 136 236.544
5 & 11 8s.4 336 286.944
6 & 12 9s.6 336 321.216
Since each flue has 4 ports 90 degrees around the stack, sampling occurs from each port instead
of going all the way tluough the stack for the far points. Traverses were made at the following
points:
Traverse Point Number Tmverse point location
Port A Port B Port C Port D from outside port. (inches)
1 4 7 l0 23.784 =23 314"
2 5 8 11 58.056=58"
3 6 9 17 108.456 = 108 2"
9" 23.784"
9" 58.056"
9" 108.456"g" 245.544"g" 295.944"
9" 330.216"
D 5. DETERMINAT]ON OF PARTICULATE EMISSIONS. RESULTS
Plant Name INTERMOUNTAIN GENERATING STATION Date En1n024
Sampllns Location UNIT 1 STACK Prolect #)M Performance
0pelator Vicki Lvman Stack Type ]ircular
Historical Data
Run Number ,|2 3 Averaqe
Run Start Time 7:4O 1U: 1U 12:34 Runs 1,2,
and 3
hh:mm
Run Stoo Tlme 9:45 12:15 14:38 hh:mm
Meter Calibration Factor rY)1.001 1.001 1.001
Pitot Tube Coefflclent (c")0.840 0.840 0.840
Actual Nozzle Dlsmeter (DJ 0.1 93 0.193 0.193 tn
St ck Te3t Data
lnitial Meter Volume (V.),261.571 352.501 446.601 fl"
Final Meter Volume (V^)t 351.665 444.609 538.596
lotal Meter Volume (v-)90.094 92.1 08 91.995 91.399 fr"
Totel Sampllnq Time (o)120.0 120.0 120.0 120.0 min
Avsraoo Meter Temoerature (t-).,o 83.0 89.0 92.0 88.0
Avcrage Stack Tcmpcrature (1").,o 118.0 119.0 1 19.0 118.7 .F
Barometric Prcssure (P")24.9U 24.97 24.9(24.95 in Ho
Stack Static Prsssure (P.t.'i")1.00 -1.00 -1.O0 1.00 in HrO
Absolute Stack Pressure (P.)24.E3 24.90 24.90 24.88 in Hq
Average Orifice Prcssure Drop (aH)*1.56 1.60 1.63 1.60 in H"O
Absolute Meter Prcssure (P-)z5.o1 25.09 25.09 25.06 in Hg
{vo Square Root Pltot Pressure (aptu)*1.18 1.19 1.18 1.18 (in HzO)tz
MolBture Content Data
mplnoers 1-3 Water Volume Galn (v")224.0 244,2 248.1 238.8 ml
molnoer 4 Silica Gsl Weioht Galn u")21.6 21.9 20.8 21.4 I
Total Water Volume Collected (Vu)245.6 256.1 268.9 260.2 ml
Standard Water Vapor Volums (V*),,'1 1 550 12,525 12.657 12.247 scf
St ndard Meter Volume (v,),,73.287 74.322 73.834 73.814 dscf
]alculated Stack Moicture (B*rr.rrr)'t 3.6 14.4 14.6 14.2 Vc
laturated Stack Moisture (Bwrrror)13.1 13.4 13.4 13.3 olo
loported Stack Moisture Contont (8".)13.'1 13.4 13.4 13.3 Yc
Gas Analvsis Date
Carbon Dioxide Percentase (o/oCOz')13.6 13.6 13.6 13.6 oln
Oxygen Percentagc (oho,\5.4 5.3 5.4 5.4 ok
Carbon Monoxldc Porcenlaoe ("6CO)0.0 0.0 0.0 0.0
Nitrogen P€rcenteEe (%trtr1 81.0 81.1 81"0 81.0 Yo
Dry Gas Molecular Weiqht (Ma)30.39 30.39 30.39 30.39 lbilb.mole
Wct Stack Gas Molecular llYeisht (M.)28.70 28.61 28.58 28.63 lb/lb-mole
Calculated Fuel Factor (F.)1,140 1.147 1.140 1.142
Fuel F-Factor (F")9780 9780 9780 9780 dscf/mmBlu
Percent Excass Air (%EA)33.8 32.9 33.8 33.5 Yo
Volumetric Flow Rate Data
Averloe Stack Gas Vclocltv (v.)76.32 77.O4 76.43 76.60 ftlsec
Stack Cross€ectional Aroa (A.)615.75 615.75 615.75 615.75 ft'
Actual Stack Flow Rate (Q.)2819642 2U6243 2823706 2829864 acfm
Drv Standard Stack Flow Rate (Q*)1846839 1849008 1 830082 1 841 976 dsc-fm
Percent of lsoklnatlc Rate fl)100.3 101 .6 102.O 101.3 oli
Emission Rate Oata
Mass of Particulats on Fllter (m)-1 .1 000 -0.3000 {).5000 {.633 m0
Mass of Particulate ln Acetone (m.')6,7000 6.7000 7.4000 6.933 mg
Mass due to Acetone Blank (W.)0.0000 0.0000 0.0000 0.0000 m9
Iotal Mass of Particulates (m")5.6 6.4 6.9 6.3 m0
Stack Partlculate Concentration (cJ 0.0001 0.0001 0.0001 0.0001 0/dscf
(c.)0.0015 0.0015 0.0015 0.0015 gr/dscf
Particulate Emlssion Rale (E)11.08 11.09 10.98 11.05 kE/hr
(E)18.7 21.1 22.6 20.8 lb3/hr
(E)0.0022 0.0025 0.0027 0.0025 lbYmmBtu
Table 3
METHOD 5. DETERMINATION OF PARTICULATE EM]SSIONS. RESULTS
Plant Nams NTERMOUNTAIN GENERATING STATION )ate EtzEt2024
Sampllnq Locatlon JNIT 2 STACK ,rolect #PM Performance
Operator y'icki Lyman Stack Type lircular
Historical Data
Run Number 1 2 3 Average
Run Start Tlme 7:17 9:,12'.AO Runs 1 ,2,
and 3
hh:mm
Run Stop Time 9:22 'l:44 14:05 hh:mm
Metar Calihration Factor (Y)1.001 1.001 1.O01
Pitot Tube Coefflcient (c")0.840 0.840 0.840
Actual Nozzle Dlamater (D".)0.1 93 0,1 93 0.193 ln
itack Test Data
lnitial Meter Volume (V')i 539.012 632.675 728.202 ft"
Final Meter Volume (V.)r 632.1s3 727.864 825.858 fl"
fotal Metor Volume (v-)93.'141 95.189 97.656 95.32S ff
Total Samollno Time (o)120.0 120.0 120.O 120.0 mtn
Averaoe Motor TemDerature (t-),*88.0 93.0 95.0 92.0 "F
Averagg Stack Temperature (^)^""117.O 118.0 119.0 118.0 I
Barometrlc Prsssure (Po)24.80 24.80 24.80 24.80 in Ho
Stack Static Pressure (Po*J 1.00 -1.00 1.00 -1.00 in H,O
Absolute Stack Pressure (P.)24.73 24.73 24.73 24.73 in Ho
Average Orifice Pressure Drop (AH).""1.66 1.71 1.80 1.72 in H,O
Absolute Meter Pressure (P,)24.92 24.93 24.93 24.93 in Ho
Avo Sou.re Root Pltot Pressure (ap"').*1.20 1.22 1.24 1.22 (in H,O)"z
Moisture Contsnt Data
mpinqers 1-3 Water Volume Gain N")225.2 239.8 253,9 239.633 ml
moinoer 4 Silica Gel Wcioht Gain (w,)19.2 221.8 20.5 87.167 q
Total Water Volume Collected (v,.)244.4 462.0 274.4 326.933 ml
3tandard Water Vaoor Volume (V.)*1 't.504 21.746 12.916 15.389 scf
itandard Meter Volume (v-)."74,796 75.760 77.4U 76.007 dscf
:alculated Stack Moisturc (B*"-"J 13.3 22.3 14.3 16.6 o/o
Saturated Stack Moisture (B*.r.-t)12.8 13.2 13.5 't3.2 o/o
leDorted Stack Moisture Content (8.,)12.8 13.2 13.5 13.2 o,/a
Gas Analysls Data
larbon Dioxide Percentage (%co,l 13.6 134 13.6 13.5 c/o
Jxygen Percentage (o/oOzl 5.4 5.4 5.4 5.4 c,/o
larbon Monoxlde Percentaoe (%co)0.0 0.0 0.0 0.0 o/o
{ltrogen PercentaEe (7oNz)U].U 81.2 81.0 81.1 o/c
)ry Gas Molecular Weight (Ma)30.39 30.36 30.3e 30.380 lb/lb-mole
n et Stack Gas Molecular Weisht (M.)28.74 2t.6U 28.62 28.320 lb/lb-mole
]alculated Fuel Factor (F.) '1.140 1.157 1.140 .145
Fuel F-Factor (Fd)9780 9780 9780 9780 dscf/mmBtu
Psrcont Excess Air (o/oEA\33.8 33.7 33.8 33.8 c/o
Volumetric Flow Rate Data
Averaoe Stack Gas Velocltv (vJ 77.U 80.62 80.54 79.60 fUsec
Stack Cross-Ssctional Area (A.)615.75 615.75 615.75 615.750 ft'
Actual Stack Flow Rate (Qo)28684 1 0 2978506 2975550 2940822 acfm
Drv Slandard Stack Flow Rate (Q.,)1 880966 1747343 1 922056 1 850135 dscfm
Porcont of lEoklnotic Rete fl) 100.5 109.6 101.8 104.0 o/L
Emission Rate Data
lllass of Particulate on Fllter (mr)-1.6000 -0.2000 -o.6000 -0.800 mg
Uass of Parliculate in Acetone (mr')8.1000 6.3000 6.3000 6.900 mE
\llass due to Acetone Blank (w.)0.0000 U.UUUU 0.0000 0.0000 mg
Total Masi of Particulates (m")6.5 6.1 5.7 6.1 mg
Stack Particulate Concentration (c.)0.0001 0.0001 0.0001 0.0001 g/dscf
(c.)0.0015 0.0015 0.0015 0.00't5 gr/dscf
Particulato Emlsslon Rate (E 11.29 10.48 11.53 11.10 ko/hr
(E 21.6 18.6 18.7 19.6 lbsihr
(E 0.0025 0.0023 0.0021 0.0023 lbVmmBtu
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APPENDIX B
Pre-Test Protocol
Department of
Environmental Quality
Kimberly D. Shelley
Executive Director
DTVISION OF AIR QUALITY
Bryce C. Bird
Dit'ector
RECEIVED
JUL O B 2024
JAFState
SPENCERJ. COX
Oovenor
DEIDRE TTENDERSON
Lieulenanl Governor
Re:
July 2,2024
DAQC-613-24
Site ID t0327 @4)
Jon A. Finlinson
Intermountain Power Service Corporation
850 West Bnrsh Welhnan Road
Delta, UT 84624
Dear Mr. Finlinson:
Intennountain Power Service Corporation - Intermountain Generating Station (IGS) Unit
I and Unit 2 - Protocol Review and Test Date Confirmation - Millard County
The source testing protocol for PM compliance testing of the Intermountain Power Service
Corporation IGS Unit 1 and Unit 2 boiler stacks dated June 17.2024, has been reviewed and found
acceptable. The agreed upon testing will be held on August 27 and28,2024.
Acceptance of a protocol does not relieve the owner/operator and the testing contractor from strict
adherence to all applicable EPA methods, Utah Division of Air Quality (DAQ) policies, Utah Air
Qualiry Rules (UAQR), and methods approved by the Director. Any deviation from EPA
methods, DAQ policies, UAQR, and methods approved by the Director must be addressed
separately and express written consent given prior to commencement of testing.
The DAQ requires that all test reports include a statement signed by a responsible of[rcial
certifying that:
A. Testing was conducted while the source was operating at the rate and/or conditions
specified in the applicable approval order, operating permit, or federal regulation.
B. During testing, the source combusted fuels, used raw materials, and maintained
process conditions representative ofnormal operations, and operated under such
other relevant conditions specified by the Director.
C. Based on information and belief formed after reasonable inquiry, the statements
and inforrnation contained in the report are true, accurate, and complete.
195 North 1950 West . Satt Lake City, UT
Mailiog Address: P.O. Box 144820 . Satt Lakc City, UT 841144820
Telephonc (80 l) 5364000 . Fax (801 ) 5364099 . T.D.D. (80 l) 903-3978
rlMe.dcq.illah.gov
Printcd on 1009'c rccyclcd prper
Iti, 1,
"' .tl
DAQC-613-24
Page2
If you have any questions, call me at (801) 5364165 or e-mail me at [e-mail]'
Sincerely,
?ail fi4owil
P.ul Morns(Jul 1,2024 09n6 MoTJ
Paul Morris, Environmental Scientist
Division of Air Qualtty
PFMjI
cc: Cenhal Utah Public Health Department
Pretest Protocol
EPA Gompliance Testing for Particulate Emissions at
lntermountain Power Generating Station
Proposed for IGS Unit 1 and Unit 2 Boiler Stacks
The tests will be conducted by lntermountain Power Service Corporation's
Environmental Group on August 27 and August 28,2024.
INTERMOUNTAIN POWER SERVICE CORPORATION
850 West Brush Wellman Road
Delta, Utah 84624-9546
[phone]
Pretest lnformation Form and Attachments
SOURCE INFORMATION
Company Name: lntermountain Power Service Corporation (lPSC)
Facility Name: lntermountain Generating Station (lGS)
Unit to be tested: A. Unit 1 Boiler Stack (1SGA)
B. Unit 2 Boiler Stack (2SGA)
Mailing Address: 850 West Brush Wellman Road, Delta, Utah 84624
Plant Address: Same
Phone: [phone]
Plant Technical Contact: Mr. Mike Utley, Environmental Engineer [phone]
Proposed Test Date: August 27 and28,2024
Testing to be done by: IPSC personnel
OPERATING PERMIT EMISSION LIMITATIONS AND REASON FOR TESTING
On November 21, 2A23, the Utah Department of Environmental Quality (UDEO) Division of Air
Quality (UDAO) issued IPSC a Title V Operating Permit for a coalfired, steam electric
generation station in Millard County, Permit Number 2700010006. A copy of that permit is
available at UDAQ's website.
(See htto://168.178.3.241:8080/DAQ NOI/DocViewer?lntDoclD=69712&contentTvpe=application/pdf)
Compliance testing is required as per Title V permit requirements on Boiler Units 1 and 2 for
particulate emissions. The lntermountain Generating Station is a subpart Da power plant with a
wet scrubber. As per 40 CFR part 60.48 (b)(2), we are required to use Method 58 for filterable
particulate matter emissions. Condensable particulate matter testing is not required and will not
be performed. Testing will be conducted on the boilers at 90 percent load or greater of normal
operating capacity as required by the rules. The particulate emission limitation is 0.0184 lb/MM
BTU for each boiler.
SOURCE TEST SUMMARY
Methodoloqv
EPA Method 1
EPA Method 2
EPA Method 38
EPA Method 4
EPA Method 58
Parameter Determined
Location of Samples and Velocity
Traverses from Stationary Sources
Determination of Stack Gas Velocity
and Volumetric Flow Rate
(Type S Pitot Tube)
Gas Analysis for the Determination
of Dry Molecular Weight
Determination of Moisture Content
in Stack Gases
Determination of Non-sulfuric Acid
Particulate Matter from Stationary
Sources
Units to Test
BoilerUnitsl&2
BoilerUnitsl&2
BoilerUnitsl&2
BoilerUnitsl&2
BoilerUnitsl&2
CALIBRATION DATA
The EPA and State agencies require various calibrations for speciflc equipment used during
testing. Calibration data is not yet available but will be obtained before the testing starts. These
calibrations will be available for inspection at the time of the test and will be appended to the
final report. A sample of all field data forms will be made available at the job site.
PROCESS DESCRIPTION AND POLLUTION CONTROL EQUIPMENT
Both boilers are coal fired boilers. The stack gas passes through a fabric filter baghouse for
particulate control and a limestone wet scrubber for acid gas and SO2 control. Each Unit has a
dedicated flberglass flue suspended within a concrete chimney. Stack testing is done inside the
chimney support structure at the 352 foot level, There are over eight diameters ftom the last
flow restriction either side of the test point.
Operational parameters, coal BTU analysis, and tons of coal burned will be recorded during the
testing period and reported in the formal compliance test report.
SAMPLE TRAIN AND ANALYSIS INFORMATION
Figure 1 is a schematic of the sample train to be used to obtain the field data during testing using
a stainless steel probe liner. The glass fiber filters used for Method 58 in the train are 99.95
percent etficient on 0.3 micron particles and have no organic binders (Whatman 93+AH), These
filters are tarred before use and after the test to determine particulate loading.
Because this is a Subpart Da source and Method 58 is used, the filtered particulate (FP) fraction
filters will be oven dried at 320 degrees F for three hours, desiccated for two hours and weighed
to a constant tare. The probe and FP filter will be kept at 320 degrees F t 25 degrees F during
sampling. After analysis is completed, the probe wash and filter samples will be conditioned at
320 degrees F for at least six hours, cooled in a desiccator for two hours and weighed until the
finalweight is constant. To facilitate a preliminary result while the testing is in progress, the probe
wash acetone will be heated below boiling point on a hot plate to accelerate evaporation. ln
addition, at least 60 DSCF will be withdrawn over a time of 120 minutes.
Moisture in the stack gases will be collected by keeping the impingers in the sample train below
68 degrees F with an ice bath. The Method 4 section of the moisture sampling train willcontain
the following impingers:
lmpinger
Number
1
2
3
4
Contents
Deionized Water
Deionized Water
Empty
Silica Gel
Amount
100 m!
100 m!
200 g
Parameter
Collected
Moisture
Moisture
Moisture
Moisture
All impingers will be weighed before and after each test to determine the moisture content of the
gases. Pitot tubes and the meter system will be leak checked before and after sampling.
STACK SCHEMATIC AND TRAVERSE POINT LOCATIONS
The location of sampling and velocity traverse points are determined by EPA Method 1 with
respect to the stack diameter and the distance from the sampling ports to upstream and
downstream interferences to laminar flow. A drawing of the exhaust duct and stack showing the
sampling locations and their relationship to the interferences to flow are shown in Figure 1a. The
exact tocation of each of the traverse points of the stack diameter (90 degrees apart from one
another at the sample port locations) are given in Table 1. Figure 1b shows the port detailand
the sampling levelwith the port orientation.
Table I
Traverse Point Calculations
Plant: lntermountain Generating Station
Date: August 27 and28, 2024
Sampling Location: Unit 1 and Unit 2 Main Boiler Stack
Port Size: 6"
Port Length (inside stack wall to outside flange): 9"
Port Length Total: 9"
Port Projection into Stack: 0"
Stack lnside Diameter: 336" => 615.75 sq. ft. in area
Point Calculation Basis: 40 CFR Pt. 60, App. A, Meth. 1, Table 1-2.
Traverse
Point
Number
1&7
2&8
3&9
4&10
5&11
6&12
Percent
of
Stack l.D.
04.4
14.6
29.6
74.4
85.4
95.6
Product of
Column
2 and 3 Lenqth
14.784
49.056
99.456
236.544
286.944
321.216
Traverse Point
Location From
Outside Port
23.784',
58.056"
108.456"
245.544"
295.944"
330.216"
Stack
t.D.
lnches
336
336
336
336
336
336
Port
9"
9"
9t'
gr'
9"
9t'
Since we have four poils 90 degrees around the stack, we will be sampling from each port
instead of going all the way through the stack for the far points.
Traverse Point Number
1,4,7,&1A
2,5,8, & 11
3,6,9, &'12
Traverse Point Location
From Outside Port (lnghes)
23.784 = 23-314
58.056 = 58"
108.456 = 108-112
1.
2.
3.
4.
Other Comments, Recommendations, or Proposed Modifications
Each of the Method 58 tests will be 120 minutes or longer as per 40 CFR 60.48a(2Xi).
Nozzle diameter will be selected after the pretest velocity data is collected.
As required by 40 CFR Part 60.48(b)(2xii), Method 38 will be used to determine the dry
molecular weight of the gas stream. Gas analysis will be conducted using an Orsat and
be performed at the sampling site.
The moisture content of the gas stream willbe measured using EPA Method 4 and
weighed at the test site or in the Environmental Lab. The filterable particulate will be
measured using EPA Method 58. A minimum of 60 DSCF will be collected over the
duration of the test at a rate greater than 0.5 DSCFM as required in 40 CFR Part
60.48(bX2Xi).
An ,'S" type Pitot tube will be used to measure the velocity of the gas stream using EPA
Method 2. An inclined manometer will be used to measure the velocity head. The
manometer shall have marks allowing it to detect a 0.01 inch of water column from the
zero point.
Barometric pressure will be measured using a mercury barometer. A correction shall be
made for the difference in elevation fiom the barometer location and the testing location,
Prior to testing and while the boiler is at the test load, a pretest cyclonic flow
determination in the exhaust stack will be done as per Method 2 criteria. The test will
proceed only if the average cyclonic flow angle is less than 20 degrees from parallel to
the stack.
Testing of the condensable particulate matter in the water collected in the impingers
(back half) will not be performed.
5.
7.
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6" DIA.i.D.
TYPICAL PORT DETAlL
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APPENDIX C
Test Period Production Data
Particulate Testing: Production Data
Dates of Testing:
UNIT ONE
Et2712024Begin: 7:40
6 min 6m
End:14:46
PI TAGS
Load
Fuel Flow
Opacity
IPP UNIT ONE
27-Aug-24 09:58:00
10:O4:00
27-Aug-24 12:16:00
27-Aug-24 12:22:00
27-Aug-24 12:28:00
Tesi Time:
Averaging Period
'tcoAxt027A
lCOAXIOOlB
lSAAAZOO1E
MWh-e
tons/hr-coal
Stack Particulate Teet Production / Monitorino Data
950 391
391950
1.6
1.6
1
1,6
1.5
27-Aug-24 07:46:00
27-Aug-24 07:52:00
27-Aug-24 07:58:00
27-Aug-24 08:04:00
27-Au9-24 08:10;00
27-Aug-24 08:16:00
27-Aug-24 08:22:00
27-Aug-24 08:28:00
27-Aug-24 08:34:00
27-Aug-24 08:40:00
27-Aug-24 08:46:00
27-Aug-24 08:52:00
27-Aug-24 08:58:00
27-Aug-24 09:M:00
27-Aug-24 09:10:00
27-Aug-24 09:16:00
27-Aug-24 09:22:00
27-Aug-24 09:28:00
27-Aug-24 09:34:00
27-Aug-24 09:40:00
950
950
950
950
950
950
949
950
950
950
950
950
950
951
950
950
950
950
949
950
951
390
392
392
390
391
389
390
390
391
391
390
391
393
392
389
389
390
390
394
394
393
1.7
1.7
1.7
1.7
1.7
1.7
1.7
1.7
1.7
1.7
1.7
1.6
1.6
27-Aug-24 1O:22:OO
27-Aug-24 10:28:00
27-Aug-24 10:34:00
27-Aug-24 10:40:00
27-Aug-24 10:46:00
27-Aug-24 10:52:00
27-Aug-24 10:58:00
27-Aug-24 1'l:M:00
27-Aug-24 11:10:00
27-Aug-24 11:'16:00
27-Aug-24 11:22:J0
27-Aug-24 11:28:00
27-Aug-24 11:34:00
27-Aug-24 1 1:40:00
27-Aug-24 1 1:46:00
27-Aug-2,4 1 1:52:00
27-Aug-24 1 1:58:00
27-Aug-24 12:04:00
950
9s0
950
950
949
9s0
950
950
949
949
950
951
950
950
950
950
950
950
950
950
394
395
391
391
395
397
395
392
392
395
398
397
396
396
396
395
396
395
395
395
Particulate Testing: Production Data
Dates of Testing:
UNIT ONE
8t27t2024
Begin:
6 min
7:40 End:
6m
14:46
PI TAGS
Load
Fuel Flow
Opacity
IPP UNIT ONE
Test Time:
Averaging Period
1COM|027A MWh-e
1COAX|001 B lons/hr-coal
1SAAAZ0018 %
Stack Particulate Test Production / Monitorinq Data
27-Aug-24 12:40:00
27-Aug-24 12:46:00
27-Aug-24 12:52:00
27-Aug-24 12:58:00
27-Aug-24 13:04:00
27-Aug-24 13:10:00
27-Aug-24 13:16:00
27-Aug-24 13:22:00
27-Aug-24 13:28:00
27-Aug-24 13:34:00
27-Aug-24 13:40:00
27-Aug-24 13:46:00
27-Aug-24 13:52:00
27-Aug-24 13:58:00
27-Aug-24 14:04:00
27-Aug-24 14:10:00
27-Aug-24 14:16:00
27-Aug-24 14:22:00
27-Aug-24 14:28:00
27-Aug-24 14:34:00
949
950
951
950
950
950
950
950
950
950
951
9s0
950
950
950
951
950
950
951
9s0
950
394
396
394
396
393
396
396
396
396
3S6
396
396
396
397
398
396
396
397
396
396
397
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.5
1.527-Aus-24 14:40:00
Particulate Testing:
Dates of Testing:
PI TAGS
Load
Fuel Flow
Opacity
Production Data
Test Time:
Averaging Period
2COAXr027A
2COAxt001B
2SAAMOO18
UNIT TWO
8128t2024
Begin:7:12
6 min
End: 14:'12
6m
MWh-e
tons/hr-coal
o/o
Stack Particulate Test Production / Monitorinq DataIPP UNIT TWO
28-Aug-24 07:18:00
28-Au9-24 O7:24:00
28-Aug-24 07:30:00
28-Aug-24 07:36:00
28-Aug-?4 07:42:00
28-Aug-24 07:48:00
28-Aug-24 07:54:00
28-Aug-24 08:00:00
28-Aug-24 08:06:00
28-Aug-?4 08:12:00
28-Aug-24 08:'t8:00
28-Aug-24 08:24:00
28-Aug-24 08:30:00
2B-Aug-24 08:36:00
28-Aug-24 08:42:00
28-Aug-24 08:48:00
28-Aug-24 08:54:00
28-Aug-24 09:00;00
28-Aug-24 09:06:00
28-Aug-24 09:12:00
949
949
951
951
950
950
951
949
950
949
951
951
949
950
951
948
951
950
948
952
950
390
393
392
392
392
391
390
390
391
391
392
390
389
392
387
392
390
390
393
390
389
5.
5.
5.
4.
4.
4.
4
4
4
4
4
28-Aug-24 09:42:00
28-Aug-24 09:48:00
28-Aug-24 09:54:00
28-Aug-24 10;00:00
28-Aug-24 10:06:00
28-Aug-24 10:'12:00
28-Aug-24 10:18:00
28-Aug-24 10:24:00
28-Aug-24 10:30:00
28-Aug-24 10:36:00
28-Aug-24 10:42:00
28-Aug-24 10:48:00
28-Aug-24 10:54:00
28-Aug-24 11:00:00
28-Aug-24 11:06;00
28-Aug-24 '11:12:00
28-Aug-24 1 1 :18:00
28-Aug-24 11:24:0A
28-Aug-24 11:30:00
28-Aug-24 11:36:00
951
949
951
949
951
949
949
951
949
949
951
950
9s0
951
950
949
950
951
951
950
950
391
390
391
390
392
390
390
392
391
392
395
393
393
394
392
392
394
395
394
393
393
393
28-Aug-24 11:54:00
Particulate Testing: Production Data
Dates of Testing:
UNIT TWO
8t2812024
Begin',7:12
5 min
End: 14:12Test Time:
Averaging Period
2COAxl027A
2COAXl001B
2SAAAZOOls
6m
PI TAGS
Load
Fuel Flow
Opacity
IPP UNIT TWO
MWh-e
tons/hr-coal
Yo
28-Aug-2412:06:00
28-Aug-24 12:12:00
28-Aug-24 '12:18:00
28-Aug-24 12:24:00
28-Aug-24 12:30:00
28-Aug-24'12:36:00
28-Aug-24 12:42:00
28-Aug-2412:48:00
28-Aug-24 12:54:00
28-Aug-24 13:00:00
28-Aug-24 13:06:00
28-Aug-2413:12:00
28-Aug-24 1 3:1 8:00
28-Aug-24 13:24:00
28-Aug-24 13:30:00
28-Aug-24 '13:36:00
28-Aug-24 13:42:00
28-Aug-24 13:48:00
2E-Aug-24 13:54:00
28-Aug-24 14:00:00
949
950
950
951
949
952
949
950
949
951
950
950
949
949
952
948
951
950
950
952
948
396
396
396
394
397
393
393
393
396
394
395
393
393
396
391
39s
395
393
396
393
39328-Auo-2414:06:00
FWFMo002
Date Sampled:
Lab Sample Number:
Analyst Init.ials:
Date Analyzed:
As Fired Sample Final Report
IPSC Fuels Lab
08 /25 /2024
69555
RGC/C.'
08 /27 /2024
14:00
1of2
t Total MoisEure
t Ash
t Sulfur
BTU/Lb
Short Proximate
As Received
10.98 t
]-2.04 *
0.78 t
10736
Analys is
Drv Ba$is
xxxx
1,3.52 *
0.88 r
r.2050
Moisture Ash Free BTU/Lb ),3946
t Residual MoisEure 2.43 8
Sample operated properly during sampling period.
Comments:
Prod 09: l-3:23 AM Int.ermounEain Power Service Corp 09/L0/2024 13959
t Air Drv Loss
Cont.ainer weight - 629.9
As Received Sample + Cont,ainer Weight - L659. I
Dry Sample + ConEainer weighE - 1559.5
B Air Dry Loss
t Residual Moisture in Dupficate (1) (2)
L4.9207 14.8728
15.9231 15. 8719
15.8987 15.8476
B Residual Moistrure -
Dry Constant -t Total Moisture -
(1) (2t
2t.3584 19.0956
22.354L 20.0961
2L.4898 ]-9.2215
FWFMo0 01
Date Sampled:
Lab Sample Nunrlcer:
Analyst Initials:
DaEe Analyzed:
Crucible Weight -Total Wec Weight -
Tot,a1 Dry Weight -
t Ash in Duplicate
Crucible Weighc -
TocaL wet weights -
ToEal Dry Weight -
BTU in Duplicate
As DeEermined BTU/Lb -
Sul-fur in Dru>licate
I As DeEermined Su1fur
As Fired Sample Worksheet
IPSC Fuels Lab
08/25/2024 14:00
696s5
RGC/C,J
08 /27 /2024
8.76 t
(1)
2.43 \
a .97 5'7
10.98 t
(2)
2.43 *
0.9'?57
1"0.98 t
2of2
(Ave)
2.43 S
0.9't57
10.98 t
(Ave)
13.19 t
13.52 tDeLermined Ash -t Dry Ash -
(1) (2\
Lt'164 tl11 0
Dry BTU/Lb -
M. A. F. BTU/Lb
(1) (21
t3 .20 t 13.18
r.3.53 t 13.51
(Ave)
1!7 6't
(1) 12)L2057 t2053
- 13 944 1394?
tt
(Ave)
12050
13946
(1) (21 (Ave)
0.86 0.85 0.85 t
(1)
t Dry Sulfur - 0.88 t
(2t
0,88 *
(Ave)
0.88 *
13959 09:13:23 AI'l fnEermountain Power Service Corp 09/lO/2024 Prod
FWF.Mo002
Date Sampled:
Lab Sample Number:Analyst Initials:
Date Analyzed:
08 /27 /2024
69558
RGC/CJ
08 /29 /2024
As Fired Sample Final Report
IPSC Fuels Lab
]-of2
14:00
t Total MoisEure
t Ash
* Sulfur
BTU/Lb
Short Proximat,e
As Received
10 .71 t
11.67 *
0.80 B
10838
Analys i s
Drv Basis
xxxx
13.07 I
0.90 t
r_2 r-3 I
Moisture Ash Free BTU/Lb 13963
t Residual Moisture 2.80 I
Sample operatsed properly during sampling period.
CommenEs:
Prod 09:13:50 AM Intermountain Power Service Corp 09/10/2024 13959
FWFMo001
Date Sampled:
Lab Sample Number:Analyst Initials:
Date Analyzed:
Crucible Weight -Total Wet Weigrht -Tot.al- Dry Weight -
Crucible Weight. -Tot,al Wet WeighE -Tot,a] Dry Weight -
BTU in Duplicare
As Det.ermined BTU/Lb -
Sulfur in Dupli-cate
t As Determined Sulfur
As Fired Sample Worksheet
IPSC Fuels Lab
2of2
t Air Dry Loss
Cont.ainer Weight, - 629.6As Received Sarnple + ConEainer Weight - 1076.3Dry Sample + ConLainer Weight - 1591.1
t Air Dry Loss
I Residual Moisture in Duplicate
t Ash in Duplicate
(1) (2)
L3 .426'7 l-4 . 92 t 0
t6.421"1 t5.9235
16.3937 15.8955
Residual Moisture -Dry Const.ant. -t ToLal MoisE,ure -
(1) (2t
2L.3].54 21.3583
22.3]-54 22 .3560
21 .4424 21 . 48s0
08/27 /2024
69 658
RGC/C.T
08 /29 /2024
L4:00
As DeE,ermined Ash -t Dry Ash -
(]. ) (2J
11801 11795
8.14 t
(1) (21 (Ave )2.81 t 2.79 * 2.80 r0.97L9 0.972t 0.9720
1,0.'72 t t0.70 $ 10.71 t
(1)
12.10
13.0?
(Ave)
11798
12) (Ave)
z L2.70 \ L2.70 *t 13.06 t 13 .0? r
(2) (Ave)
12134 121381-3957 13963
Dry BTU/Lb -M. A. F. BTU/Lb
(1)
t2t42
13968
(Ave)
0.87 $
(1)
0. 87
(2t
0.87
(1)
0.90 t
(2J
0.89 t (Ave)
0.90 tt Dry Sulfur -
L3959 09:13 : 50 AM fnEermounf,ain Power Service Corp 09/L0/2024 Prod
FWFMo002
Dat.e Sampled.:
Lab Sample Number:Analyst Initials:
Date Analyzed:
As Fired Sample Final Report,
IPSC Fuels Lab
08/28/2024
69651
RGC/CJ
08 /29 /2024
14:00
Lof2
* Total Moisture
t Ash
I Su1fur
BTU/Lb
Short Proximate
As Received
10.88 r
1_0.17 t
0.59 t
11065
Analys is
Dry Basis
xxxx
11.41 t
0.56 I
]-2415
Moisture Ash Free BTU/Lb L4016
t Residual Moisture 2.92 *
Sample operated properly during sampling period.
Comnents:
Prod 09 :14: l-4 AM IntermounEain Power Service Corp a9/t0/2024
I
rwFMo001 As Fired Sample
IPSC Fuels
Worksheet
Lab
2of2
(Ave)
11.08 t
11.41 t
Date Sampled:
Lab Sample Nurnber:
Ana1yst. tnit.ials:
Date Analyzed:
08 /28 /2024 l-4: 00
6966r
RGC/CJ
08 /29 /2024
t Air Drv. Loss
Container Weight - 535.9
As Received Sarnple + Cont,ainer Weight - L667.0
Dry Sample + Container Weight - L582.5t Air Dry Loss
I Bgsidual Moisture in Duplicate
Crucible Weight -Total wet WeighE -Total Dry Weight -
(1) (2)
74 .7 6"t3 15 .0729
1s,7531 t6.0107
1s.7341 r.5.04r.4
8.19 t
(1) (2) (Ave)
2.9L * 2.94 * 2.92 *
0.9709 0.9705 0.9708
10.86 t r.0.89 t 10.88 t
t Ash in DupliqEle
Crucible Weight -Total wet Weight -Total Dry WeighE -
BTU in Duplicate
As Determined BTU/Lb -
Sulfur in-Duplicate
t As DeEermined Sulfur
Determined Ash -tDryAsh-
(1) (2)
t2054 L2052
Dry BTU/Lb -
M. A. F. BTU/IJb
(1) (2)
11.04 t 1t_.L1
11.37 t 11.45
(Ave)
12 053
(1 ) (2)
12415 L24L't
- 14008 r.4023
Residual Moisture -Dry ConsCant -t Tot.al Moisture -
(1) (2)
t6.61't6 16.9423
t7.5t'74 t'7.9441
t5 ."1280 17 . 05 3 5
t
*
(Ave)
1_2475
L4015
(1) (2) (Ave)
0.54 0.63 0.54 t
(1)
t Dry Sulfur - 0.65 I
(2\
0.5s t
(Ave)
0.55 t
13959 09:14 :14 AII fnEermountain Power Service Corp 09/L0/2024 Prod
APPENDIX
Field & Laboratory Da
UNIT 1SGA
I
ta
STATIONARY SOURGE SAtlIIPLING TITLE PAGE
Stationarv Source Information
Plant Name INTERMOUNTAIN GENERATING STATION
Fuel Type COAL. BITUMINOUS
Samolino Location UNIT 1 STACK
Cperator VickiLvman
Date 812712024
Prolect #PM Performance
Base Run Number I
I of Ports Available 4
I of Ports Used 4
Port lnside Diameter o
ircular Stack?
Rectanoular Stack?
Fuel F-Factor 9780 9780 9780
Test Equipment lnformation
Meter Box Number 1 508035 Apex
Meter Calibration Factor (Y)1.0006
Drilice Meter Coefficient (AHa)1.850 in H2O
Pitot ldentification tPP 007
Pitot Tube Coefficient (c")0.840
)rsat ldentification 39-507
Nozzle Number 11
Itlozzle Diameter (D.)0,1 93 tn
Probe Number 1
Probe LenEth 114.00 tn
Liner Material SS
Samole Case / Oven Number 522-14
lmoinoer Case Number s22-1C
Acetone Lot Number 248735
Testinq Comoanv lnformation
Comoanv Name lntermountain Power Service Coro
Address 850 W Brush Wellman Rd
Citv State Zio Countrv Delta. UT 84624
Phone Number 435-8644414
Fax Number 435-864-U70
Plant Name NTERMOUNTAIN GENERATING STATION Date 8127t2024
Samplino LocaUon UNIT 1 STACK ?roiect #PM Performance
Operator /icki Lyman I of Ports Avallable
Stack Tvpe 3ircular $ of Ports Ussd
Stack Size !arge rort lnside Diameter f,
lDlameter of Stack (=Lr* - L*) I tol I SS0.OO I in I
L'FL-r -I Lnw
D
..\
--\
Distance from Port to Disturbances
Distance Uostream (B)3012.00 tn
Diameterc Upstream (=B/D)(Bo)8.96 diameters
Dlstance Downstream (A)4274.00 ln
Diameters Downstream (=A,/D)(Ao)12.72 diameters
Number of Traverce Points Required
Diameters to
Flow Disturbance
Mlnlmum Number of'
Traverce Points
Up
Stream
Down
Stream
Particulate
Points
Velocity
Polnts
2.004.99 0.50-1.24 24 16
5.00-5.99 1.25-1.49 20 16.
6.00-6.99 1.50-1.74 16 12
7.00-7.99 1.75-1.99 12 12
>= 8.00 >=2.00 8 or 1?'8 or 12'
Upstream Spec 12 12
Downstream SDec 12 12
Iraverse Pts Required 12 12
Check Minimum Number of Points for the Upslream
and Downstream conditions, than use the largest.
I tor Circular Stacks 12 to 24 inches
12 for Circular Stacks over 24 inches
--r-
I
Downstr€.'3r-n
Disturb)once
t
IVe,:SLt r-er11 en
Sjte
A I up'sireorrrI t_-[ (L,,SiurL,onCe
Number of Traverse Points Used
4 Ports bv 3 Across
12 Pts Used 12 Required
Particulate n Velocitv
Tre'el*
Po itl {6 IO I
I!
3I
5
6
7
8
9
l0II
t,
.tt6
.85.r
.067
.2S0
.750
.933
.0.r{
.l J6
.296
.70{
.85{
.956
.032
.r0s
. l9{
,323
.G77
.806
.E95
.968
.026
.082
.116
.?:6
JJ2
.658
.771
.85r
.918
.97!
.02 r
.067
.r 18
,177
.2S0
356
.6{J
.7S0
.823
.882
.933
Traverce Point Locations
Traverse
Point
Number
Fraction
of
Stack
Dlameter
Distance
from
lnside
Wall
Distance
lncluding
Nlpple
Lenoth
tn tn
1 0.044 14 618 23 618
2 0.146 49 58
3 0.296 99 4/8 108 4/8
4
5
6
7
8
9
10
11
12
Plant Name INTERMOUNTAIN GENERATING STATION Date 8t27t2024
Samolino Location UNIT 1 STACK Proiect #)M Performance
Jperator Vicki Lyman # of Ports Used
Stack Tvoe Circular Pitot ldentiflcation PP OO7
Pitot Leak Check Pl lPreTestl lq lPostTest Pitot Coefficient (C.)0.8400
Stack Dimensions Velocltv Traverce Data
Dlameter or Lenqth of Stack (D)336.00 ln Run Number 1-V1
Width of Stack (w)tn Run Time
Area of Stack (A.)615.75 ff Traverse
Point
Veloclty
Head
(^p)
Stack
Temp
(t.)
Local
Veloclty
(v")rPressures
Barometric Pressure (Pn)24.97 in Ho in H,O oF fUsec
Static Pressure (Prt"rr")1.00 in HrO A-1 1.35 117.00 74.9
Absolute Stack Pressure (P")24.90 in Hg A-2 1.50 1 17.00 79.0
A-3 1.55 117.00 80.3
Stack Gas Composition B-1 1.20 117.00 70.7
Composition Data: I Actual tl Estimate lrl B-2 1.45 117.00
Carbon Dioxide Concantratlon (%COz)13.0 %B-3 1.50 118.00 79.1
Oxvoen Goncentration (o/oOz)6.0 o/o c-1 1.15 117.00 69.2
Carbon Monoxide Concentration (ToCO\0.0 Yo v-z 1.40 118.00 76.4
Nitrogen ConcentraUon (%N,)81.0 %c-3 1.45 118.00 77.7
Stack Moisture Content (B*)0.130 % (O.xx)D-1 1.30 118.00 73.6
Stack Dry Molecular Weisht (Mu)30.32 lb/lb-mole D-2 1.50 '1 18.00 79.1
Stack Wet Molecular Weight (M.)28.72 lb/lb-mole D-3 1.55 118.00 80.4
Results
Avq Stack Gas Velocity (vJ 76.8 fUsec
Avg Stack Dry Std Flow Rate (a'a)129254905 dscf/hr
Avg Stack Dry Std Flow Rate (Q"a)2154248 dscf/min
Avq Stack Wet Flow Rate (Q.*)2837376 acflmin 1.41
Stack Cross Section Schematic
Average'1.19 118
Please report lhe average of lhe square rools of
ap, or, (ap)12,* = t/.r(apta)
Formulas Used
A, = DW/K, for Rectangular Stacks Ts(evc) = '/nIt, + 1,
A, = (r(D/2)2)/K, for Circular Stacks where T, = 273oK for metric units
where ( = 1 for metric units where T, = 460 oR for English units
where ( ='144 (in2lftz) for English units v, = Kpcp(ap)r'2,,e (T,1n,e/(P,M,))rr2
P" = Pu., + P.r"riJl 3.6 where Ko = 34.97 for metric units
%N2 = 1gg - %CO2 - o/oO2 - o/oCO where Ko = 85.49 for English units
Mo = .44(%CO) + .32(o/oOz) + .28(%N2 + %CO) Q'6 = 3600(1 - Bo.)v,A,(T,s6/Ts(."0))(Ps/P6rd)
M. = M6('l - B*) + 188*. where T3rd = 293 oK, P.,o = 760 mm Hg, for metric units
)tn",o = t/nr(apl/2)where T",o = 528 oR, P",6 = 29.92 in Hg, for English units
Plant Name NTERMOUNTAIN GENERATING STATION Date 8t27t2024
SamDllno Location JNIT 1 STACK Prolect #PM Performance
Operatot Vlike Utlev E of Ports Used
Fuel Tvpe ]OAL. BITUMINOUS l/linimum Fuel Factor 1.083 lMaxlmum Fuel Factor 11.230
Orsat Leak Check lvl I PreTsst lll I PostTest )rsat ldentification 39-507
Gas Analysls Data
Run Number I lun Start Tlme 7'.40 Run Stop Time 9:45
Sample
Analysis
Time
Carbon
Dioxide
Volume
ru^^")
Oxygen
Volume
(V^.)
Carbon
Monoxide
Volume
(V".)
Carbon
Dloxlde Oxygan
Carbon
Monoxide Nitrogen
Concentra.
(7oN,)
Dry
Molecular
Weight
(M,)
Molecular
Weight
Deviation
(^MJ(o/oCOe\{o/oO2)(o/oCO)
hh:mm ml ml ml percent percent psrcent Defcent lb/lb-mole lb/lb-mole
'11:25 13.6 19.0 13.6 5.4 0.0 81.0 30.39 0.00
'11:,40 13.5 18.9 '13.5 5.4 0.0 81_'l 30.38 -0.01
11:50 13.6 18.9 13.6 5.3 0.0 81 30.39 0.00
Results Averages 13.6 b.4 0.0 E1 30.39
[voraoo Calculatod Fuel Factor (Fo).*1.140 Molecular Wt Devlatlon < 0,3?4
{veraoe Excess Air (%EA).*33.7 percent Fuel Factor in Handbook Ranoe?4
Gas AnalvslB Data
Run Number 2 Run Start 'lme 1O:1O Run Stop Time 12i15
Sample
Analysis
Time
Carbon
Dioxide
Volume
(v^^.)
Oxygen
Volume
(V.,)
Carbon
Monoxlde
Volume
(V^^)
Carbon
Dloxlde
Concentra
(o/oCOz)
Oxygen
Carbon
Monoxide Nitrogen
Concentra
(%N,)
Dry
Molecular
Weight
ru")
Molecular
Weight
Deviation
(AM")(o/oO,l (%co)
hh:mm ml ml ml percent percent percent percent lb/lb-mole lbilb-mole
14:15 13.6 't8.9 13.6 5.3 0.0 81.1 30.39 0.00
14:26 13.6 '19.0 13.6 5.4 0.0 81.0 30.39 0.00
14:38 13.6 18.9 13.6 5.3 0.0 81.1 30.39 0.00
Results Averaqes 13.6 b.3 0.0 81.1 3U.39
Averaoe Calculated Fuel Factor (F").""-141 Molecular Wt Deviatlon < 0.3?lrl
Average Excess Alr (%EA).,.32.9 percent Fuel Factor in Handbook Ranqe?lvl
Gas Analysls Data
Run Number Run Start Time 12:.34 Run Stop Time 14:38
Sample
Analysis
Time
Carbon
Dioxlde
Volume
(Vcor)
Oxygen
Volume
(v^,)
Carbon
Monoxlde
Volume
(Vco)
Carbon
Dioxide Oxygen
Concentra
(o/oO"\
Carbon
Monoxide Nitrogen
Dry
Molecular
Weight
rM,)
Molecular
Weight
Deviation
(AMa)(o/oCOr)(%co)(0/6N")
hh:mm ml ml ml Dercenl oercent Dercent oercenl lbflb-mole lb/lb-mole
17:00 13.6 18.9 't3.6 5.3 0.0 81.1 30.39 0.00
17:14 13.5 18.S 13.5 5.4 0.0 81.1 30.38 .0.01
17,.25 13.6 19.0 13.6 5.4 0.0 81.0 30.39 U.UU
Results Averaqes 13.6 5.4 0.0 6't _'l 30.39
Averaoe Calculated Fuel Factor (F"),""t.14U Ulolecular Wt Devlatlon < 0.3?lvl
dveraqe Excess Alr (%EA)"*33.7 percent :uEl Factor ln Handbook Ranoe?lvl
Fuel Factor Fo
:uel Type Minimum Maximum
loal. Anthraclte 1 .016 1.130
loal. Lionite 1 .016 1.130
loal, Bituminous 1.083 1.230
lll, Distillate 1.260 1.413
Oil, Resldual 1.210 1.370
Gas, Natural 1.600 1.836
Gas. Propane 1.434 1.586
Gas, Butane 1.405 1.553
Wood 1.000 1.120
Wood Bark 1.003 't.130
Formulas Used
%CO2 = V6e2
%O2=V62-V6e2
%CO=V66-V6,
%Nz = 1gg -o/oCO2-o/oO2-ohCO
Mo = .44(%COz)+ .32(%Oa )+ .28(%N2 + %CO)
AM6 = M6'M6.,e
Fo = (20.9 - o/oO2- ,S%CO)I(%CO2 + o/oCO)
0,6EA= 1 O0(%O-. SoloCOV(.264% NO
Plant Name I NTERMOUNTAIN GENEMTING STATION Date 8127t2024
Sampllnq LocaUon UNIT 1 STACK Proiect #PM Performance
Operator r'icki Lyman # of Ports Used 4
Stack Tvoe ircular Meter Box Number '1508035
fraln Leak Check lvl lPreTestl lvl lPostTest Meter Cal Factor U)1.0006
Molsture Content Data
Run Number Run Start Tlme 7:40 Run Stop Tlme 9:45
fotal Mater Volume ry-)90.094 dcf Barometric Pressure (Po)24.90 in Hq
Avg Meter Temp (t.).,o 83 OF Stack Static Pressure (P.ro)'1.00 in H"O
Avg Stack Temp (L)oo 118 -l-Avg Orilice Pressure (aH).,c 1.56 in H2O
lmolnoer I lmplnger 2 lmplnser 3 lmpinqer 4 lmplnqer 5 lmplnoer 6 lmplnqer 7
ml ml ml q ml ml ml
Contents 100 Watel 100 Water 0.00 200 SiGel
Final Value (V'),(W)890.25 728.82 633.1 8 828.63
lnltial Value M),(W,)716.96 685.14 626.24 806.98
Net Value (v"),(w")'173.3 43.7 6.9 21.7
Results
Total Volume (VJ 223.90 ml Water Vol Condensed (V*r.*)10.539 scf
Total Weisht (w)21.70 I Water Vol Welqhed (V*.o,.,0,)1,023 scf
Std Meter Volume (V-rrrar)73.257 dscf Sat Moisture Content (B*.".)13.1 o/o
Calc Molsture Content (B-.-o)13.6 Yo Flnal Molsture Content (B*.)13.'l o/o
Moisture Content Data
Run Number 2 Run Start tme 10:10 Run Stoo Tlme 12:15
Total Meter Volume (v^)92.1 08 dcf Barometric Pressure (Pr)24.97 in Ho
Avo Meter Temo (t-).""89 OF Stack Statlc Pressure (P.,.,,.)-1,00 in H,O
Avg Stack Temp (tr)o,e 119 -F Avg Orifice Pressure (AH)o,o 1.60 in H2O
lmoinoer 1 lmpinqer 2 lmpinqer 3 lmoinoer 4 lmolnoer 5 lmolnoer 6 lmolnoer 7
ml ml ml a ml ml ml
Contents 100 Water 100 Water 0.00 200 SiGel
Fina! Value (v),(w,905.16 717.12 601.34 828.61
nitial Value (v,),(w)705.14 678.94 595.36 806.71
Met Value (v"),(w")200.0 38.2 6.0 21.9
Results
lotal Volume (V,)244.21)ml Water Vol Condensed (VwaruJ 11.494 scf
Iotal Weioht (w)21 90 s Water Vol Weiohed (v*..,.'|1.033 scf
Std Meter Volume (V-,.,r')t4.zvz dscf Sat. Molsture Content (8,13.4 o/o
Calc Moisture Content (B*)14.4 %Final Moisture Content (B*)'t3.4 Yo
Moisture Content Data
Run Number Run Start Time 12:34 Run Stoo Time 14:38
Total Meter Volume (v.)91 .995 dcf Barometric Pressure (P.)24.97 in Hs
Avg Meter Temp (t-).".92 ,F Stack Static Pressure (P 1.00 in HrO
Avg Stack Temp (tr)",0 119 'F Avg Orlfice Pressure (AH)",e 1.63 in H2O
lmDinoer 1 lmpinqer 2 lmpanqer 3 lmoinqer 4 lmplnqer €lmplnqer 6 lmolnoer 7
ml ml ml q ml ml ml
Contents 100 Water 100 Water 0.00 200 SiGel
Flnal Value (v),(w)920.93 729.25 633.21 830.81
nitial Value M),(W)719.51 687.93 627.90 810.00
tlet Value (v"),(w.)201.4 4',1.3 5.3 20.8
Results
Total Volume (VJ 248.00 ml lVater Vol Condensed (V*,r"r)11.673 scf
Total Weioht (w)20.80 q iVater Vol Weished (V*o,",o')0.981 scf
Std Meter Volume (V*.'r)73.844 dscf !at. Moisture Content (B*.*^)13.4 Yo
Calc Moisture Content (B*)14.6 ol Flnal Molsture Contenl (B*,)13.4 To
It cf Polnt3 Acror. 13 l* o! PorE U3.d 14 |
ld..l Nozzl. Dlrmatcr.nd lroKln.tlc Factor Satuo
rltot Tub! Coelflclrnt (c")0.840
lvq Strck T.mD (L)118
Wr Grr Mr!.r Tomp (L)82
\H A 0.75 SCFi'(AH@)1.85 in H,o
\vo Pltot Tub! Dlll. Pruriun (ap*)1.41 ln H"O
lltck lroltlult Contrni (B-)13.0 9t (u.x)
itrcl Drv Mol.culrrW.loht (M-)30.32 lMb-mol(
:3tlmrt d Orlfic. Flow Rttr (Q-)0.730 actm
, to AH l3okln.ilc Frcior (K)1.14
SrmDllno Eoulomrnl
tlrtor *1508035
ll.trr Crllbntlon Frctot (n I 1.0006
[ozzl. I 1'l
lctu.l l{o2rlc Olrm.tcr (D-t10.193 I in
d.rl Nozlr Dlrmrt r to-llo.tgol in
Probr *, L.[oih 1 114.00 | in
Llnrt Mrt rlll SS
Srmola Crla , Ovan *52i2-14
mDlno.rC.3o t 522-1C
AVr Lo.k Ch.c*3
Pra 0 ftlmin @ 8.5 in Ho
Mtd ft"/mln @ in Ho
Po3t 0 ft'/mln @ 6.E in Hq
!v- < 0.020 at"rmin IJ )k?
Pltor oK?,l
TrrvarrG
Polntt
Srmpllng
Tlmo
tel
Clock
Tlm.
ury (,r3
Mctor
R.rdln!
ru_l
V!loclty
Hord
IADI
uaatrao
Odflct
AH
(AHI
Actu.l
O.lflca
AH
IAHI
Strck
T.mp
lL'l
Mat.r
lnl.t
Tcmp
lr_,1
ir.t r
Oull.t
T.mp
Ir_ -l
Flltrr
T.mp
lnplng.r
Exit
T.mp
Pump
Vacuum
Squ.rt
Root
AP
(aptnl
Locrl
Stlck
V.loclty
lv-1,
Cumuhdv.
t .trr
Volum.
fv_r--
Cumulatlvo
Parcrnt
EoKln.tlc
fll
min hh:mm:sE n'in H,O in H,O ln H,O "F .F in Ho (io H,Ol"'lusrc 3d ch
A-l 0.0 7:40:00 261.571 1.30 .48 1.51 119 74 71 305 73 4.5 1.14 73.70 6 112 103 3
A-2 10.0 7:50:00 268.964 1.40 .60 1.55 1r8 76 76 a2a 50 a.s 118 76.50 12.219 10't _3
A-3 200 8:00:00 276.37e 1.55 77 1,70 118 7A 7A 319 46 4.7 1.24 80.49 18.572 100.2
B-1 30.0 8:12:00 284.115 1_30 .48 1_48 119 80 BO 316 50 4.s 1.14 73.78 24.503 100 2
B-2 40.0 8:22:OO 291.372 1.40 .60 1.50 119 82 82 319 53 4.6 1.18 76.56 30_661 100.2
B-3 50.0 8:32:00 298.931 1.50 .71 'l 70 11S 8d a4 320 s2 50 1.22 79.25 37 _062 100_3
1 600 8:43:00 306.81 1 120 37 1.35 119 85 85 316 55 4_4 1.10 70.89 42.738 '100.2
c-2 70.0 8:53:00 31 3-828 1.35 .54 1.52 119 86 86 320 55 4.6 1.16 75.19 48.750 1rl0 2
c-3 80.0 9:03:00 321.265 1.45 .65 1.62 114 87 a7 319 58 4.8 120 7?.54 51.972 1 00.1
D-1 90.0 9:15:00 328.970 1.25 .43 140 115 88 88 3'.ta 5S 45 112 72.10 60.781 100.0
D-2 100.o g:25:0O 336.188 1.45 .65 1.64 115 88 88 319 55 5_0 1.20 77.65 67.016 100.0
D-3 110.O 9:35:00 313.922 1.50 .71 1.70 116 89 89 319 57 5.0 1.22 79.05 73.247 998
Last Pt 120.O 9:45:00 351.665
I Vrlua 120.O 9:45:00 351.665 num vacuum 5.0 Flnrl Vrluit 73.247 s9.E
\vrrloa Vrluaa 139 ,r 56 118 83 83 318 55 1.18 76.O7
83
t-
IFEiiurrno ltnrenmourretxceruenertruGstrttol
lsFpllng Lccruon IUNTT T STACK
l^ri..^. lni.X Moodv lKunt 14 If.jrji#El7i,il15- -lrorPori.t[.d I1 I
trd Narrrr hhartar .^d lroxlnallc Frctd SatUD
,ltot Tubo Coamcl.ni rc-I 0.840
{vqSt ckTamp (L)118 'F
avo G[ lrltar T.mp {r-}8S .F
tH O 0.75 SCFi!(AH@)1.85 ln H,O
AYo Pliot Tub! Dlfl. Prttturo (aD.-)1.39 in H,O
S(.ck Molrtura Conlont (8-)13.0 %
itrct Dry Molsul.r W.lght (Mi)30,39 lb/b{ol.
irilmrtod Ormco Flow Rai!(o-)0.751 aclrn
\P to AH lrokln.tlc Frctoi (Kt
SrmDllns Equlpm.nt
[.tar #r 506035
lr.l.r Crllbnllon Frstor Nl t1.0006
{ozlt *1
lctu.l Nrla Olrmottt (0-) I 0.193 tn
d.rl Nozlo DlrmlLr (D")10.1921 tn
Prob. t, Lmot r 114.00 I h
Llncr U.t rirl 3S
S.mol! Crtt , OY.n ,t22-1A
molnqtr cac I i22-1C
^v L.rk Chiclr
trc 0 Ir'/mh @ s.2 in Ho
ltd ft"/rnin @ hHo
,61 0 ft'lmin @ s.5 in Ho
rv- < 0.020 It'/min f,k )l?
,ltot OX?Crilt OX?IJ
Ttlvorto
Polnt #
S.mpllng
Timo
Clock
Tlma
Dry Ga3
M.t!r
RGrdlnC
rv-)
V.loclty
Hold
lAol
DIlrod
Orflis
AH
(AH)
Aclurl
Orlflcc
AH
(^H)
Strek
Tomp
ttl
lr.ter
lnltt
Tcmp
lr_t
lrstot
Ouu!t
T.mp
lr-^l
Flll.r
T!mp
lmPrncol
EIIt
Tomp
Pump
Vrcuum
6qurn
Rool
AP
{aoral
Loc.l
Strck
V.loclly
cumulrdvc
l,lit r
volum!
Cumul.tivo
Porcont
lroKlnollc
Ill
min hh:mm:BE It'in HrO rn H,O in H,O .F .F hHo (ur H,Ol",Ut.c scl
D-l 0.0 10:10:0C 352.501 1.30 1.51 a5 18 84 a4 306 58 5.?14 73_53 6.224 '105.1
o-2 100 l0:20:0C 360.1 51 1.a5 'r.68 .60 19 84 a4 324 a1 5-4 1.20 77.71 12.113 101.9
D-3 200 lO:30:00 367.754 150 1.71 70 a 85 85 319 44 5_8 1.22 78.99 18.788 101.3
c-1 30,0 10:42:00 375.598 1.25 1.45 rl0 19 a7 a7 311 50 5.0 1.12 72.'t7 24.615 1 01.1
c-2 .10.0 10:52:0(382.802 1.40 1.62 55 119 87 a7 421 55 5.5 .r 18 76.38 30.641 100 5
c-3 50.0 1 1:O2:00 390.248 1.50 1.74 70 119 89 89 421 56 5.9 1.22 7e.o6 36.974 100.3
8.1 60.0 1 'l: t 3:00 39E.096 't 30 1.51 .50 110 90 90 917 59 5.5 1.14 73.60 12.976 100.5
B-2 70.0 l l:23:00 405.554 t-40 1_62 .5S 119 90 90 320 59 5.0 1.18 75.3E a9 118 100.4
B-3 80.0 11:33:00 41 3.183 1.50 171 .70 '120 91 01 318 61 6.2 1.22 7S.1 3 55.444 t 00.3
A.'t 90.0 'l l:45:OC .r21.051 1.30 I 5l .17 119 9'l 91 316 51 5.6 1.14 73.60 61.405 100.4
a-2 't 00.0 1 1:55:0[a28.474 1-50 1.74 73 119 92 92 122 61 6.5 122 79.O6 a7.794 100.4
A-3 10.0 12:05:00 436.432 1.60 1_86 .80 119 s2 92 322 63 6.8 1.26 al 65 74 360 't 00.3
Lest Pt 120.0 l2: 'l 5:O!444.609
nrl Vrlur 120.0 .la.t 609 Vacuum 6.6 Finrl Valu.r 74.360
lvcruot Vrlu!a 112 1.50 t9 89 89 318 56 1.19 76.77
E9
'l.nt N.ma NTERMOUNTAIN GENERATING STATION )!tr el27l202A
rmDllno Locrton JNIT 1 STACK )rclrct {)M Padomrnm
oeralor lirt Mnndv Qun ,
I of Polntr Acmrs I ol Podr tlmd
ldatl Nozb Dhm.i.r rnd lroKln.tlc lct6r Salu6
,ltot Tub. Cosftlol.nt (c.)0.840
Avg Strch T.mD (L]119 .F
Avq Gr3 iilltcr TemD (L)94 .F
It g 0.76 scFM (AH@)1.E5 irl HrO
Avo Pltot Tubc Dlff. Pr.rtur.(AD-)1.12 h H,o
St ck Mol3tur. Contanl (B-)13.0 %
St.ck Ory ilol.cul.r Wrliht (M&)30.39 lbrlb-moh
Erlimrt.d Orlllcr Flow Rrtc (o-)0.768 .dm
AP to AH ltokln.0c Frctor rKl 1
SrmDllno EoulDm.nt
lrrl.r *t508035
[rt ] C.llbrlffon Frctor ft1 I 1.0006
{ozzli t 11
tctu.l Nozzlr Ol.matcr (D^.)l 0.193 I in
derl Nozzlc Dlamet r (D",) I 0.192 n
)rob. #, Linotr 1 114.00 n
.lnor Hrtcrhl )J
lr Cri. / Ovin *tzt-'tA
mplntar Crrr #t22-1C
Prar3u rca
Brrcmairlc Pr.r3ure {P*)24.97 in Ho
Strck St tlc Pr.tiuri aP.*r 1.00 h H.o
Abiolulo St.ck Pror3uri (P.)24.90 in Ho
Abtoluta tlatar Pra!3ur.(P-)25.11 in Ho
AV- LerkChrcks
trG 0 ft'/mh @ 8 in Ha
f,ld tt'lmh @ in H0
,o3t 0 ft'/mh a g in Ho
rv- < 0.020 ll'/mh ck 3k?
,ltoi OK?4
Currul.tlvc
Perccnt
EoKln.tlc
100.2
t 00.3
100.4
1
1
METHOD 5 . SAMPLE RECOVERY AND INTEGRITY DATA SHEET
Plant Name INTERMOUNTAIN GENERATING STATION Date 8t27t2024
Samplino Location UNIT 1 STACK Proiect #PM Performance
)perator Vicki Lvman Acetone Lot Number 248735
Run History Data
Run Number 1 2 3
Run Start Time 7:40 10:10 12:34 (hh:mm)
Run Stop Time 9:45 12:15 14:38 (hh:mm)
Irain Preoared Bv VL VL VL
lrain Recovered Bv VL VL VL
Recoverv Date 8t2712024 8127t2024 8t27t2024 (mm/dd/w)
Relinquished Bv nla nla nla
Received Bv
Relinouished Date (mm/dd/yy)
Relinquished Time (hh:mm)
Equipment ldentification Numbers
Fllter 1 2 3
Acetone Wash C1 c2 C3
Silica Gel DRP.12.1OB DRP.12.1OB DRP.12.1OB
lmpinqer Case 522-1C 522-1C 522-1C
Samole Box 522-1A 522-14 522-1A
Oven 1350G 1350G 1350G .*,a,n* oF AIR 6galtTY
Formulas Used
V. = V1 -V1 Wn = Wr - Wi V," = Vn + Wn/p* where p* = ,9982
Moisture Content Data
lmoinoers 1,2, and 3 - Water Volume
Final Volume (V')2252.3 2223.6 2283.4 q
lnitial Volume (v)2028.3 1979.4 2035.3 s
Net Volume (v^)224.0 244.2 248.1 s
Comments
lmpinqer 4 - Silica Gel Weioht
Final Weioht (w)828.6 828.6 830.8 s
lnitialWeisht (Wi)807.0 806.7 810.0 s
Net Weight (w^)21.6 21,9 20.8 s
Comments
Total Water Collected
Total Volume (Vr")245.6 266.1 268.9 s
IPP_PM_U 1_8_27 _2024 - M5 - Recovery Page 1 Printed 911312024
METHOD 5. SAMPLE ANALYTICAL DATA SHEET
)lant Name INTERMOUNTAIN GENERATING STATION Date 8n7no24
iamollno Locstion UNIT 1 STACK ,roiect #)M Performance
)perator r'icki Lyman Acetone Lot Number 248735
Formulas Used
rTtx = irvofillc of last two filter measurem€nls fi11 = lI1x - ITln Wn = Comn* mo=mf + fr.', - W.
mrr' = average of last two acelone measurements ' = mro' - m,"' l[]n* = lYlu, * Ihrr ' lrt
Analvtlcal Data
Placed in Desiccator Run Number 1
Number Date Tlme Run Start Tlme 7:40
:llter 1 08127t24 10:43 Leakaoe Evldent?lvl no
{cetons Wash Beaker c'l 08t28t24 10:09 Estimated Volume 125 ml
Fllter Acotone Dats Tlme Humldlty Temp Cal Audlt
o o mm/ddlw hh:mm %RH OF q
Uleasurement I (mr),(mt.)0.6161 130.6239 o8t31124 9:01 25 72
Usasuroment 2 (m2?),(m?J 0.6161 130.6243 09t01124 8:41 28 72
Ueasuremont 3 (mv),(mr.)130.6242 o9to3l24 5:19 38 72
lllsasuremont 4 (mr),(mr.)
Results Acetone Blank
:lnal Welsht (mn),(mr.')0.6161 130.6243 s Final Weioht (Ca')129.8972 s
Iare Welsht (mr),(m.')o.6172 130.6176 s Tare Weioht (C"')129.8966 s
rtVeloht Galn (mr),(m"')1.1 6.7 mg 3lank Concentratlon (c.)0.0000 mg/9
3lank AdJustmcnt (w.)0.0000 mg
lotal Partlculates (m")5.6 mg
Analvtical Data
Placed ln Deslccator Run Number z
Number Date Time lun Start Tlme 10:10
silter 2 08t27t24 13:08 -eakase Evident?Jl no
Acatone Wash Beaker c2 o8r28n4 10:09 tutlmated Volume 100 ml
Filter Acetone Date Time Humldlty Temp Cal Audlt
a q mm/dd/w hh:mm %RH OF q
Measurement'l {m'J,(m,.)0.6157 105.9972 o8t31t24 9:01 25 72
Measurement 2 (m2r),(m2J 0.6157 105.9973 09to'U24 8:41 28 72
Meaiuremant 3 (m.r),(m3o)105,9972 09to3t24 5:19 38 72
ILleasurement 4 (mrr),(mr.)
Results Acetone Blank
Final Weisht (mn),(mt')u.615 /'105.9973 s :inal Weight (c,,)129.8972 g
lare Weight (m,r),(m"')U,OlOU 1U5.99Ub s Tare Weiqht (c,.)129.8966 s
Weioht Gain (mr),(m.')-0.3 6.7 mg Slank Concentration (c^)0.0000 mg/g
Blank Adiustment (w.)0.0000 mg
Total Particulates (mn)6.4 mq
Analytical Data
Placed ln Dosiccator Run Number 3
Number Oate Time Run Start Tlme 12:34
Filter 3 o8t27t24 15:10 lsakaqo Evident?lJl no
Acetono Wash Beaker c3 08t28t24 10:09 Estlm.tod Volume 120 ml
Filter Acstone Date Time Humidity Temo Cal Audit
q q mm/dd/w hh:mm %RH OF a
Measurement 1 (m,r),(mlJ 4.6232 130.6420 08t31t24 9:01 25 72
Measurement 2 (mzr),(mr,)0.6233 130.6426 o9to1t24 8:41 28 72
Measurement 3 (m:),(m:.)130.6/.27 09to3l24 5:'19 38 72
Measuremenl 4 (m.),{mro)
Rssults Acetons Blank
Flnal Weight (mr),(mr.')0.6233 130.6427 s Flnal Weight (Cr')129.8966 s
Tare Welght (mr),(m,.')0.6238 130.6353 s Iare Weight (C"')129.8966 s
Weiqht Galn (mJ,(m.')-0.5 7.4 mq Blank Concentratlon (c.)0.000c mg/g
Blank Adiustment (W.)0.0000 mq
Total Particulates (mn)6.9 mg
IPP_PM_U1_8 27 2024 - M5 - Analytical Page 1 Prinled 5h312024
Table 2
METHOD 5 - DETERM]NATION OF PARTICULATE EMISSIONS. RESULTS
Plant Name INTERMOUNTAIN GENERATING STATION Dete 8t27t2024
Samolinq Locatlon UNIT 1 STACK Prolect #)M Performance
Operator y'icki Lyman Stack Tyoe ]ircular
Hlstorlcal Data
Run Number 'l 2 3 Averaqe
Run Strrl Tlme 7'.40 10:10 12:34 Runs 1,2,
and 3
hh:mm
Run Stop Time 9:45 12:15 14:38 hh:mm
Meter Callbratlon Factor 01 1.001 1.OOl 1.001
Pltot Tube Coefticient (c")0.840 0.840 0.840
Actual Norzle Diameter (D",)0.193 0.193 0.193 in
Stack Test Data
nitlal Meter Volume (v-),26',t.571 352.501 446.601 n"
Flnal Mster Volume N-)r 351.665 444.609 538.596
fotal Meter Volume N-)90.094 92.108 91.995 91.399 ft"
fotal Samolino Time (o)120.0 120.0 120.0 120.0 mln
Averaqe Meter Temperature (L).""83.0 89.0 92.0 88.0 "F
Averaqe Stack Temperature (r.)*118.0 '119.0 119.0 1 18.7
Earometrlc ProsBure (Ph)24.90 24.97 24.91 24.95 in Ho
Stack Statlc Pressure (P.-*)1.00 -1.00 1.00 1.00 in H,O
Absolute Stack Pressura (P.)24_83 24.90 24.90 24.48 in Ho
Average Orlflce Pressure Drop (AH)."o 1.56 1.60 1.63 1.60 in H,O
Absolute Metsr Prassure (P-)25.O1 25.09 25.09 25.06 in Ho
AvE Square Root Pitot Pressure (apt").,.1.18 1.19 1.18 1.18 (in H,Olrz
Moisture Contont Data
lmpingerc 1-3 Water Volume Galn (v^)224.0 244.2 248.1 238.8 ml
lmpinqer 4 Silica Gcl Welsht Galn (w")21.6 21.9 20.8 21,4 o
Total Watcr Volume Collectod (Vn)245.6 266.'l 268.9 260.2 ml
Standard Water Vapor Voluma (V-)o"11.560 12.525 12.657 12.247 scf
Standard Meter Volurne (V.)oo 73.287 74.322 73.834 73.814 dsc'f
Calculated Stack Molsture (B-.13.6 14.4 14.6 14.2 %
Saturatod Stack Molsture (B.r*r)13.1 13.4 13.4 13.3 %
Reported Stack Moistura Content (B-.)13.1 13.4 13.4 13.3 %
Gas Analysis Data
Carbon Dioxide Percentaqe (%cor)13.6 13.6 13.6 13.6 clo
Oxygen Perceniage (%o,)5.4 5.3 5.4 5.4 c/a
Carbon Monoxide Percentaqe (06co)0.0 0.0 0.0 0.0 ',/o
NitroEen Percentase (%N")U1.U E1.1 81.0 81.0 %
Drv Gas Molecular Weioht (M.)30.39 30.39 30.39 30.39 lb/lb-mole
ffet Stack Gas Molecular Weiqht M.)28.70 28.61 28.58 28.63 lb/lb-mole
Salculated Fuel Factor (F")1140 1.147 1.140 1.142
Fuel F-Factor (Fd)9780 9780 9780 9780 dscf/mmBlu
Percent Excess Alr (%EA)33.8 32.5 33.8 33.5 c/a
Volumetric Flow Rats Data
Neraoe Stack Gas Veloclw (v,)76.32 77.O4 76,43 76.60 fUsec
Stack Cross-Sectional Area (A.)515.75 615.75 615.75 615.75 ft'
{ctual Stack Flow Rate (o.)2819642 2846243 2823706 2829864 acfm
Dry Standard Stack Flow Rate (Qro)1 846839 '1849008 1 830082 1841976 dscfm
,ercent of lsoklnelic Rate fl) 100.3 10'1.6 102.0 101 .3 Yo
Emission Rate Data
Vlass of Particulate on Fllter (m,-1.1000 -0.s000 -0.5000 -0.633 m0
Uass of Partaculate in Acetone (m,')6.7000 6.7000 7.4000 6.933 mg
llass due to Acetone Blank (w")0.0000 0.0000 0.0000 0.0000 m9
fotal Mass of Particulates (m,)5.6 6.4 6.9 6.3 m9
Stack Particulate Concentration (cJ 0.0001 0.0001 0.0001 0.0001 g/dscf
(c.)0,0015 0.0015 0.00 1 5 0.0015 or/dscf
Partlculate Emlsslon Rate G I 1.08 11.09 10.98 11.05 ks/hr
G 18.7 21.1 22.6 20.8 lbslhr
(E)0.0022 0.0025 0.0027 0.0025 lbE/mmBlu
LOCATION OF TRAVERSE POINTS IN STAGKS
The following two tables give the location of traverse points across the stack as a fraction of the
stack dimension from the inside wall, as a function of the number of traverse points across the stack.
Location of Traverse Points in Gircular Stacks
Travelse
Point
Number
(Fraction of Stack Dimonsion lrom lnside Wall to Traverse Point)
Number of Traverse Points Across the Stack
2 4 o I 't0 12
1 .'146
.854
.067
.250
.750
.933
o44
146
296
704
854
956
032
105
194
323
677
806
895
968
026
082
146
226
342
658
774
854
918
974
021
067
118
177
250
356
6M
750
82s
882
933
979
2
3
4
5
6
7
8I
10
11
12
IPP PM Ul 8 27 2024 - Fraction of Diameter Page 1 Printed 911312424
Location of Traverse Points in Rectanoular Stacks
Traverse
Point
Number
(Fraclion of Slack Dimension from lnside Wall to raverse Point)
Number of Traverse Points Across the Stack
2 3 4 5 6 7 8 9 10 11 12
1 .250
.750
167
500
833
.125
.375
.625
.875
.100
.300
.500
.700
.900
083
250
417
583
750
917
,071
.214
.357
.500
.643
.786
.929
.063
.188
.313
.438
.563
.688
.813
.938
.056
.167
.278
.389
.500
.611
.722
.833
.944
.050
.150
.250
.350
.450
.550
.6s0
.750
.850
.950
.045
.136
.227
.318
.409
.500
.591
.682
.773
.864
.955
.o42
.125
.208
.292
.375
.458
.542
.625
.708
.792
.875
.958
2
3
4
5
6
7I
I
10
11
12
isoCALC UNITS
lJnltr Nrmc Tlble
Unltt
Number
N.Uvr Engllsh
Nrme
1 Enolish Enolish
2 Metrac Metric
3 Blank Blank
lurrsnt Unlt l,lumbar 1
Unlt! Lookuo T.bl.
Engllch
I lnltc
Mct lc
Llnlt.
"F
OK
tn mm
tn cm
tn m
fr m
ff m'
tt'mo
dcf dcm
9Cf 3Cm
dsct dscm
c{m cmm
scfm aorm
n"/min m"/min
dscfm d3ctnm
dscrhin dscrn/min
dsc7hr dscm/ht
fusec m/sec
in H"O mm H"0
in Ho mm Hg
in Ho kPa
(ln HrO)(mm H2O)rr
lb/lb-mol.c/o-mole
o/dsc,o/dsm
drldscf orld8cm
lb/hr ko/ht
conrt nt! Lookuo TeblG
Conttant
Nrme
Con3tant
Svmbol
Currcnt
Vrlur
Currcnt
unltt
Engll.h
VrIn
Engllsh
lrnltr
,iletrlc
Valu.
MlEic
Units
Leroc Steck Dlamctcr (c.")24 in 24 tn 0.61 m
lnch8 Drr Foot tc-)12 in/n 12 in/fr 1 m/m
nchra prr Foot mm per llretcr (c.",12 in/ft 12 in/ft 1000 mm/m
tllxlmum Allowlblc LGrk R.tc (c*)0.02 cfm 0.02 crrn 0.00057 m'/mln
Iozzlc Dlemster Conrtrnt (c")0.03575 ?0.03575 ?607.1 ?
( Frctor Conrtrnt (cJ 849.8 ?849.8 ?6.03EE-05 I
)ltot TubE Conat!nt K"85.49 )laxin Ho))/85.49 ,axin Ho))/34.97
M.t€r Molsture Content (B*-)0.00 oh 0.00 %0.00 %
Meter Drv ilol.culsr Weloht (MoJ 29.00 lb/lb-mole z9.(x)lMFmole 29.00 g/q-mole
Prcriure Drop ln G.s MatGr (Pr')0.25 in H;O o.25 in HrO 6.35 llllll HrO
Abtolute Tomperrturc Ofract T 460 "R 460 273
Strnd.rd Absolutc PrcsruTc P.u 29.92 an Ho 29.92 in Ho 760.00 mm Ho
Itrnd.rd AbsolutG Temper.turc T 524 528 293
Itrndard Volume Corrcctlon Kr 17.64 "R/in Hg 17.64 "R/in Hg 0.38s8 'K/mm Hg
ir.t.r Volumc to Std Watcr Vepor Kc 0.04747 ft'/ml 0.04707 ft"/ml 0.001 333 mn/ml
ioklnatic Vrrlation - RevJ Dat Kr 0.002669 Hg-tl'/mF'0.002669 Hg-ft'/ml-'0.003454
roklnetlc Vrrhtlon . lntcrmcdlrte &0.09450 ?0.09450 ?4.320 ?
Wator Mrrs to Std Waiar Vrpor K5 0.0471s ft'ls 0.04715 It'/S 0.001 335 m'/g
Deoreo! F to D.qr.es C Multiplicr IG 1.000 "FfF 1.000 "FTF 1.800 "Frc
)lorcet F to Dcorccr C Otfset Kr 0.000 "F 0.000 -F 32.00 .F
ttllllmctors Der lnch K,1.OOO in/in I.OOO in/in 25.40 mm/in
irrmi Der Pound 1(1.000 in/ln 1.000 in/in 25.40 mrvin
)ensltv of W.tcr tu 0.9982 o/ml 0.9982 O/ml 0.9982 e/ml
I PP_PM_U 1 _8_27 -2024 - U nits Pinled 911312O24
rlant Name NTERMOUNTAIN GENERATING STATION Date tr,Z hzozLt
Samollno Locafon JNIT 1 STACK Prolcct #
)perator tick Moody Run *If of Polnts Across 3 f of Ports Used 4
ldsal Nozzle Diamstsr and lsoKlnetlc Fector SetuD
Pitot Tube Coefficlent (c")0.840
Avg Stack Temp (t.)F
Avg Gas Meter Temo (L)
aH @ 0.7s scFM ( H@)in H,O
Avo PltotTube Dlff. Pressure (Ap-")ln HzO
Stack Moisturo Content (B*.)o/o (9,.x\
Stack Drv Molecular Weloht (M..)lb/tb-molc
Estlmated Orilice Flow Rate (a-)acfm
lP to AH lsoklnetic Factor (K)
SampllnE Equioment
Meter #
Metsr Callbratlon Factor m
Nozzle #
Actual Nozzle Dlameter (D-)tn
ldeal Nozzls Dlametsr (D")tn
Probe # / Length 1 1'14.00 tn
Llner Materlal SS
Sample Case / Ovcn #522-1A
lmpinEer Caee #522-1C,
Prgssures
Barometrlc Pressure (P")in Hg
Stack Statlc Prosauro '(P."o)in HrO
Absoluta Stack Pressure (P,)in Ho
Absolute Mater Pressure (P-)in Ho
AV- Leak Checks
Pre d fi'/min @ n.?in Hq
Mid ft'/min @ in Hq
Post #ft'/min @ /o,b in Ho
rv- < 0.020 ftt/min tr ok?
Pltot OK?W f,rsatOK? Wf
Traverse
Polnt #
Sampllng
Tlme
(s)
Clock
:I'lme
Dry Gas
Meter
Reading
w-)
Velocity
Head
(Ap)
Desired
Orlfice
AH
(AH)
Actual
Oriflce
AH
(^H)
Stack
Temp
(L)
Meter
lnlet
Temp
(tJ
Metcr
Outlet
Temp
(L")
Filter
Temp
lmplnger
Exlt
Temp
Pump
Vacuum
mln hh:mm:ss fi-in H"O in H"O in HrO a OF in Ho
A-1 0.0 7:rn 2L1.5+
26,?rt
L7$.?71
1.1r)tGl 1..1,,tn 7q '1, !
A-2 10.0 7lH l-4D /,Ln /,-qtr tlF 7/-7{-o ?1./M,419
A-3 20.0 9,lt/')t.E5 r*T ItAb iln VE 73 3tq {b 1,7
B-1 30.0 9'.tL z.2.l,lll l'1D / lLf ffi)flo 9/L 47)7,7
B-2 40.0 t. ??t.qr,Lt)o l, Lo I,L il F2 3Z r?,,L
B-3 50.0 '.<2 ?.qt l,iD l,7l /,h z1 7q zla
"/{-
72 6-tD
c-1 60.0 ,.47 ,DL,qI l.rt)),7A l,?tr ') ll *E a,tr ,1.{
c-2 70.0 ,r<3rL,t "3{l,Ezl /,.62 'L #12D ,U,L
u-5 80.0 'fl<121,2t{
"8,11c731, tgLflP.qD
t.u.<tLr I .l^2 I t')JZ -?/q at l,r/, X
D-1 90.0 l5 ,2{It ,3 I,LID ,I *,5
D-2 100.0 g:L5 ,'Jtr t. /-_f /.L.-l t5 PR PT ?,6 5tD
D-3 1 10.0 qi<A ,g)t.o l:b tb 8?P??t FV 6tU
Last Pt 120.0 <4;45 ?{1,/"4
Einal Value 120.0 Maximum Vacuum
Averaoe Values
Plant Name INTERMOUNTAIN GENERATING STATION Date r.2-?.202.1
Samollno Locatlon UNIT 1 STACK Prolect #
Ooerator Rick Moody Run #z
# of Polnts Across #ofPorG Used
ldeal l{ozzle Dlameter and lsoKlnetic Factor Setup
Pitot Tube Coefliclent (c.)0.840
Avq Stack Tomp (L)r
Avq Gas Meter Temp (L)"F
aH @ 0.75 SCFM (^H@)in H,O
Avq Pltot Tubc Dlff. Preasure (AP.ro)in HrO
Stack Molstura Content (B-,)% (>o<.x)
Stack Drv Molscular Welqht (MaJ lb/lb-mole
Estimated Orlfice Flow Rate (o-)e6fm
lP to AH lsoklnetic Factor (K)
Sampllnq Equlpment
Meter #
Meter Calibratlon Factor (Y)
Nozzle #
Actual Nozzle Dlameter o",)tn
ldeal Nozzle Diameter (Dr)IN
Probe # / Lenoth I 114.00 rn
Llner llllaierial SS
Sample Case / Oven #522-14
molnoor Case #522-1C
Pressures
Baromgtrlc Pressure (Po)in Hq
Stack Static Pressure (Po.r")in H"O
dbsolute Stack Preesure (P,)in Hg
Absolute Meter Pressure (P-)in Ho
AV- Leak Checks
Pre -g ft'/min @ gz in Hq
Mld ft"/min @-in Hq
Post {fto/min @-q,E in Ho
rv- < 0.020 ft"/min n )k?
Pltot OK?iT OrsatOK? l[,{
Traveree
Point #
Sampllng
Time
(e)
Clock
Tlme
Dry Gas
Meter
Reading
(v-)
Veloclty
H6ad
(ap)
Desired
Orlfice
AH
(AH)
Actual
Orifice
AH
(AH)
Stack
Temp
(L)
Meter
lnlst
Temp
{L,l
Meter
Outlet
Tomp
(L")
Filter
Temp
lmpinger
Exit
Temp
Pump
Vacuum
min hh:mm:ss ft"in H,O in H"O in H"O "F "F r ,F r in Ho
A-1 0.0 !t ?fl.6ot .?o t.K Aqtr ,l3 .l I .gt2-
A-2 10.0 )ta 3IAJN \/,L,+#b I ,cl 6ta
A-3 20.o :?LV,7g{lt?d.gltTr?.fri
,TLI E!n .7t .l fr
B-1 30.0 '0,",,2 w n*57)m
B-2 40.0 /o;6L A rl^R€-\zl EF Ag
B-3 50.0 I.til'?qaL.fr '.fr lll srh t fr'1
c-1 60.0 .ll sqa.bq,l,3A LR l, CiO ll.7 7 -,Lc-2 70.0 /l ;7_.q *q$zllt7 t9S
41l.Agl
1,4 /, r lt 7 g2 3toTtr .Ct
c-3 80.0 ,t?t 7,fr :1.7'/, ',I I /.t 1o, )
D-1 90.0 I I:H(/ t ?^{)LC I t47 It(,I w l^l 6{o
D-2 100.0 :(5 {8911 l,{o t7"1 t7a z bt LtE
D-3 110.0 :hq 41tuti2 l^60 t, P[^t, xD ,L :172 b?/^x
Last Pt 120.0 ln-'15
Final Valut 120.O Maxlmum Vacuum
Average Values
I lcattatttE?tr- cAlrEir rlra n^?a I, ISOKTNETIC SAMPLING DATA I
,lant Name NTERMOUNTAIN GENERATING STATION Dats 9.27,ru4
amplino Location JNIT 1 STACK Prolect *
)perator Rick Moodv Run #j
I of PolnB Across 3 # ofPorts Used
ldeal Nozzle Diameter and lsoKinetic Factor Setup
Pltot Tube Coefiiclent (c")0.840
Avo Stack Temo (t.)"F
Avg Gas MotGr Temp (t,)"F
aH @ 0.75 SCFM (^H@)ln H2O
Avs Pltot Tube Dlff. Pressur.(Ap-)ln H"O
Stach Molrtqre Content (Br.)% (p<x)
Stack Drv Molecular Weloht (MaJ lblb-mole
Estlmated Orlflce Flow Rato (o,)aofm
IP to AH lsoklnetic Factor (K)
Sampling Equipment
Meter #
Meter Calibration Factor .01
Nozle #
Actual Nozzle Dlameter (DJ tn
ldeal Nozzle Dlameter (D^r)rn
Probe # / Lenoth 1 114.00 I in
Llner Materlal SS
Sample Case / Oven *s22-14
mplnoer Cace #522-1C
Pressures
Barometric Prossure (Po)in Ho
Stack Static Pressure (Parr")in H"O
Absolute Stack Pressure (P.)in Ho
{bsolute Molor Prossure (P-)in Hq
AV- Leak Checks
,fO ,g ft'/min @ ,,o in Ho
trild ft'/min @ in Ho
,ost fl"/min @-t,o in Ho
!v- < 0.020 ft"/min U tk?
)itot OK?Z Crsat OK?a
Traverse
Point #
Sampling
Time
(e)
CIock
Tlme
Dry Gas
Meter
Reading
u-t
Velocity
Head
(ap)
Desired
Orffice
AH
(AH)
Actual
Orifice
AH
(AH)
Stack
Temp
(L)
Metor
lnlet
Temp
(L,)
Meter
Outlet
Temp
(L-l
Filter
Temp
lmplngor
Exit
T6mp
Pump
Vacuum
min hh:mm:ss fl'in H,o in H,O in H,O "F "F "F "F r in Hq
A-1 0.0 t7:3.41{,lfl l,l-{t4 llo ,',C,f)
A-2 10.0 ltt4 4A,Y)4tkm t,i a ?,t .L a, /
A-3 20.0 l7 ttrL ,1,l,g,t,D -qt fr
B-'r 30.0 l7 tnE \V"q,We
lvz.d
dQr.rQtat
Lar ,,t l.t C a r4
B-2 40.0 l7: tF r)l,l.t t/nL szL E ,, I
B-3 50.0 /3iz:l,€D ),'.,,rc It 3t?57 1.2
c-l 60.0 lfi-f/47 Llr l,.l a DD tilq*
c-2 70.0 ISirl,l:l ffiffi
t.n'.7 iq , t",
c-3 80-0 l.,y)
D-1 90.0 l.l:96 Z , 'll2 7 ZN #htTD-2 100.0 ,,).?O
a
,l
i ,€{
D-3 1 10.0 lq;2 ,5b l,r I
Last Pt 120.0 '21?
Final Valur 120.0 Maximum Vacuum
Avorage Values
Gas Analyols Data
lun Number Run Start Time Run Stoo Tlme
Sample
Analysls
Time
Carbon
Dloxide
Volume
ru"^")
Oxygen
Volume
(Vor)
Carbon
Monoxlde
Volume
ru"^)
Carbon
Dloxlde Oxygsn
Carbon
Monoxlde Nltrogen
Dry
Molecular
Weight
(Ma)
liolecular
Weight
Devlatlon
(AM,)(o/oCO2\(%oz)(%co)(%N,)
hhrmm ml ml ml DSrcent percent percent 0er@nl lb/lb-mole lb/lb-mole
t1. L,lq n
l'2.6 iR, (
i'SZ!13.6 ,l
Re3ults AveraEes
Avaraoe Calculated Fuel Factor (FJ,"O Molecular Wt Devlation < 0.3?U
Avsraoe Excess Air (%EA)o*percent Fuel Factor in llandbook Renge?U
Gas Analysis Data
Run Number 2 Run Start Time Run Stop Time
Sample
Analysls
Time
Carbon
Oioxide
Volume
(Vcor)
Orygen
Volume
(Vor)
Carbon
Monoxlde
Volume
(V-)
Carbon
Dloxide
Concentra
(o/oCOrl
Oxygen
Carbon
Monoxide Nltrogen
Concentra
(o/oN,)
Dry
Molecular
Weight
(M.)
molocular
Weight
Deviatlon
(AM,)(%o,)(YoCO)
hh:mm ml ml ml percent Dercent percent percent lb/lb-mole lb/lb-mole
4 "t),A lN t'1
UtkL ;<.6 l9.o
I Hl2..6 t*,q
Results Averaqes
Average Catculated Fuel Factor (Fo)."0 Molecular Wt Deviatlon < 0.3?
Averaqe Excess Air ,(%EA).*percent Fuel Factor ln Handbook Range?
Gas Analysis Data
lun Number 3 Run Start Time Run StoD Time
Sample
Analysis
Time
Carbon
Dloxide
Volume
(VcoJ
Orygen
Volume
(Vm)
Carbon
Monoxlde
Volume
(Vco)
Carbon
Dioxide Oxygcn
a
Carbon
Monoxlde Nltrogen
Concentra
(o/oNr)
Dry
Molecular
Welght
(M")
Molscular
Welght
Devlation
(AMa)(o/oCOr)(o/oOol (%co)
hh:mm ml ml ml percent Dercent Dercent percsnt lbflb-mole lb/lb-mole
-7 1An !<,6 le,,a.lu ?., <'
I ) :.)<'2. 6 ,(1
Results Averages
Averaqe Calculated Fuel Factor (Fo).*Molecular Wt Deviatlon < 0.3?U
Averaqe Excess Alr (7oEA).*percsnt Fuel Factor in Handbook Range?U
Fuel Factor Fo
Fuel Type Minimum Maximum
Coal, Anthracite 1.016 1.130
Coal, Lignlte 1.016 1 .130
Coal, Bitumlnous 1.083 1.230
Oil, Distillate 1.260 1.413
Oil, Residual 1.210 1.370
Gas, Natural 1.600 1.836
Gas. Propane 1.434 1.586
Gas, Butane 1.405 1.553
Wood 1.000 1120
/Vood Bark 1.003 130
= 100 - %COz 'o/oO2 - o/oCO
= .44(o/oCOt)+ .32(o/oO2)+ .28(%N2 + %CO)
F, = (20.9 - ohOz- .5o/oQQll(%COz + %CO)
soocjCa!E6o0,6q=
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Calc Moisture Conteni Final Moisture Content
Stack Statlc Pressure
Final Moisture Content
lA""t""tL"ffi
Formulas U"rd -
lmrr'=averagooflasttwoacelonemoasuremsnts 1qD t{L m.,=mrr,_mE, md=mhi+mr_mb - . I
Analvtlcal Data
Placed ln Dsriccrtor Run Number
Number Drte Tlrne Run Start Tlmr
Fllter I g.L'l-2 t0:*t Leakage Evldent?JNaACeIone Wash Beaket l't- I * -atQJ/lo:Dot Estlmated Volumr 125 m)-
Flltar Acatone Date Tlrne Humldltv Temo Cal Audlt
g o mm/dd/w hh:mm %RH oc
Moaiurerngnt,(mr),(mrJ h t^tt- t M.t lte|ailil1r4 Act. t\t 26 7LMeasurement 2 (ma),(me.)A.t^tal ttnttli blDtlrd.tc,*l a8, '12.
Measurometrt 3 (msr.(m!.)?9)-Lfr .t fal ol, ra ?92 't2Measure ment 4 (mrr),(mr.)
Rerultr Acetone WarhFinel Welghl (mr),(mr.)s Bottle Wtwlth Weth (mu.)q
r.rc tYetoht (mr),(m,')s Additlonsl Rlnge W (m.)sWclsht Gelr (mr),(m.')mg Bottle Trrc Welqht (mn)g
Blank Adlurtment (w.)mg NetftchWelshr (m*)sTotrl Partlcuhter (m")mg Blank Concontratlor (c.)ms/s
Alalytlcal Drta
Placed ln Derlccetor Run Number 2
Number Date Tlme Run Start TlmeFlltcl2*-zt-rt lg'.gq Lerkroo Evldont?tr rJoAcstona ttYerh Beeker Q.?-i-re-r/tn:0q Ertimated Volums tZD ruLFllterAcetone'Dltr Tlme Humldlty Temo Cal Audlt
s a mm/dd/w hh:mm %RH oc oMeasurement I (mrr),(m..)D Lt<?b6.qq'r2 ?Elsthmlollr,o.t..ol 2€'t2
Measurement I (mz),(mr.)D.ht t'7 n5.qE1etDeqql o9,41 ,Q '72Measurement 3 (ml),(mr")tlo*,'l qt ar. tO 1*'12Measurement 4 (mr),(m.,)
RetultB Acstone WethFinalWelohl(mn),(mn')o Bottle Wt with Wash (m*)s
Taro VYelohl (mr).(m.')q Addltlonal Rlnso W (m.)sWelght Geln (m),(m.')mq Bottle Trro Weiohl (mo)gt tent( Adlustmenl w.)mg Net Warh Welohl (m*)soltt Ftrucuttto!(mJ mg Blank Concentratlor (c.)mo/o
Antlyucel D.ta
Placed ln Derlccrtor Run Number 4
Number Date Time Run Stert Time
Fllter .3 A.2'l-2/)A! llt Leekrge Evldent?tl NaAcotone Wash Berker (9 O-se-tA .D-. oq Ertimatcd Volums tzo v^LFllterAcetoneDatoTlmeHumldltv Temo Cat Audlt
q a mm/dd/w hh:mm %RH oc oMeraurement 1 (mr),(m'.)0.0D2?2 t2b.irlrh I ltt 1 21Y Oq:Dl 25 72Measuremont i (mr),(mr.)D t-, l?ler) tirl,*t l^tlz4 aQ.Ll AE 72
Meesurement 3 (mrr),(mr.)lta tAz'na'lnllat oq: lq *n 72
Moa3urement {(mr),(mrJ
Rorulta Acetonc Wesh
Flnal Weloht (mr),(mr.')s Bottte Wt with Wesh (m*)sTare Weloht (mr),(m,.')s Additional Rinse W (m.)sWelght Galn (m),(m.')m9 Bottle Tare VYeiohl (mt)g
Blank Adlustment (w.)mg Net Wash Welohl (m*)oTotal Partlculates (m")m9 Blank Concentration (c.)ms/0
AfiQsffirrtrnffi,
APPENDIX D,
Field &Laboratory Data
UNIT 2SGA
STATIONARY SOURCE SAMPLING TITLE PAGE
Stationarv Source lnformation
Plant Name INTERMOUNTAIN GENERATING STATION
Fuel Tvoe COAL. BITUMINOUS
Sampling Location UNIT 2 STACK
Operator VickiLvman
Date 812812024
Proiect #PM Performance
Base Run Number 1
# of Ports Available 4
F of Ports Used 4
Port lnside Diameter 6
Circular Stack?
Rectanoular Stack?
Fuel F-Factor 9780 9780 9780
Test Eo uioment lnformation
Meter Box Number 1 508035 Apex
Meter Calibration Factor ff)'1.0006
Orifice Meter Coefficient (AH,a)1.850 in H,O
Pitot ldentlfication tPP 007
Pitot Tube Coefficient (c") 0.840
Orsat ldentification 39-507
Nozzle Number 11
Nozzle Diameter (D")0.1 93 tn
Probe Number 1
Probe Lenoth 114.00 in
Liner Material SS
Sample Case / Oven Number 522-14
lmoinqer Case Number 522-1C
Acetone Lot Number 248735
Testino Comoanv lnformation
Companv Name lntermountain Power Service Corp
Address 850 W Brush Wellman Rd
Citv State Zip Countrv Delta, UT 84624
Phone Number 435-864-4414
Fax Number 435-864-6470
Plant Name INTERMOU NTAIN GENERATING STATION Date 8128t2024
Sampllns Location UNIT 2 STACK Proiect #PM Performance
Operator r'icki Lyman # of Ports Avallable 4
Stack Tvpe Circular # of Ports Used 4
Stack Slze Larqe Port lnside Diameter 6
relarstackorDuctot"ril t-
Fr;\l
t.. l.
lDlstance from Portto Disturbances
Dlstance Upstream (B)3012.00 tn
Dlamelerc Upstr€am (=B/D)(Bo)8.96 diameters
Distance Downstream (A)4274.O0 ln
DiameteB Downstream (=A,tD) (An)12.72 diameters
Number of Traverce Points Required
Diamotens to
Flow Disturbance
Mlnlmum Number of1
Traverse Polnts
Up
Stream
Down
Stream
Particulate
Points
Velocity
Points
2.004.99 0.50-1.24 24 16
5.00-5.99 1.25-1.49 20 16
6.00-6.99 1.50-1.74 16 12
7.00-7.99 1.75-1.99 12 12
>= 8.00 >=2.00 8 or 12'I or 122
Upstream Spec 12 12
fownstroam Spec 12 12
fraverse Pts Required 12 12
' Gheck Minimum Number of Points for the Upstream
and Downstream conditions, then use lhe largest.I 8 for Circular Stacks 12 to 24 inches
'12 for Circular Stacks over 24 inches
-rl
i
-Fl
IEIii_t
Number of Traverse Polnts Used
4 Ports bv 3 Across
12 Pts Used 12 Requlred
tl Particulate n Velocity
Trs'csc
Poirr
J 6 TO t:
I
7
3t
6
7
8
9
t0ll
.I {6
.85{
,067
.250
,750
.933
.0J{
. l.t6
-296
.701
.8Sr
.956
.033
.105
.l9J
.313
.677
.806
.895
.968
.036
.082
.t16
.t16
.3.11
.658
.7 71
.85J
.9r8
.97t
.031
.067
.r l8
.177
.1t0
J56
.6{{
.750
.823
.88!
.r33
Traverse Point Locetions
Traverse
Point
Number
Fractlon
of
Stack
Diameter
Dlstance
from
lnside
Wall
Distance
lncludlng
Nipple
Lensth
tn tn
1 0.044 14 6t8 23 6/8
2 0.145 49 58
3 0.296 99 4/8 108 4t8
4
5
6
7
8
I
10
11
12
Plant Name INTERMOUNTAIN GENERATING STATION Date 8t2812024
Samolino Locatlon UNIT 2 STACK Proiect #PM Performance
0perator r/icki Lyman # of Ports Used
Stack Type Circular Pitot ldentification tPP 007
Pitot Leak Check E lPreTestl lJ lPostTest Pitot Goefficient (C")1.8400
Stack Dimensions Velocitv Traverse Data
Diameter or Lenqth of Stack (D)336.00 tn Run Number 1-V1
Width of Stack (w)tn Run Time 6:20
Area of Stack (AJ 615.75 ft'Traverse
Point
Velocity
Head
(ap)
Stack
Temp
(t.)
Local
Velocity
(vJ,Pressures
Barometric Pressure (Po)24.87 in Hg in H2O OF fUsec
Static Pressure (P.,o,'.)-1.00 in HrO A-1 1.25 114.00 72.1
Absolute Stack Pressure (P.)24.80 in Hg A-2 1.55 114.00 80.3
A-3 1.60 114.00 81.6
Stack Gas Composition B-1 1.25 114.00 72.1
Comoosltion Data: I Actual Estimate lvl B-2 1.50 114.00 79.0
Garbon Dioxide Concentration (%cor\12.9 oh B-3 1.70 114.00 84.1
Oxvoen Concentration (%or)5.6 o/o c-1 1.30 114.00 73.5
Carbon Monoxide Concentration (%co)0.0 oa c-2 1.35 114.00 74.9
Nitrogen Concentration (%N'81.5 o/o c-3 1.50 114.00 79.0
Stack Moisture Content (B*)0.'130 % (0.n)D-1 1.35 114.O0 74.9
Stack Dry Molecular Weight (Ma)30.29 lb/lb-mole D-2 1.45 114.00 77.7
Stack Wet Molecular Weight (MJ 28.69 lb/lb-mole D-3 1.55 114.00 80.3
Results
Avg Stack Gas Velocity (vJ 77.4 fUsec
Avq Stack DrY Std Flow Rate (Q"a)1 30645680 dscf/hr
Avq Stack Dry Std Flow Rate (Q.o)2177428 dscf/min 1.45
Avq Stack Wet Flow Rate (Qn,)2859543 acf/min
Stack Gross Section Schematic
Average 1.20 114
' Please report the average oflhe square rools o,
ao. or. (ap)r'2,* = t/^x(ap'/2)
Formulas Used
= DW/K, for Rectangular Stacks
= (n(Dt2)2)lK"for Circular Stacks
where K, = 'l for metric units
where l(. = 144 (in2lft2) for English unils
P.=Po"r+Prrrt"/13.6
%N, = 1gg -o/oCO2'YoO2-o/oCO
Mo =.44(%COz) + .32(o/ooz) +.28(%N2+ o/oco)
M"=M6(1 -Bs) +1888
(ap)t'2",o = t/n:(apt')
Ts(avg)='/nEt.+1u
where T, = 273oK for metric units
where T, = 460 oR for English units
v, = KrCo(AF)rn""e (T,1.,sy'(PrM.))'/2
where K, = 34.97 for metric units
where Kp = 85.49 for English units
Qso = 3600( 1 - B*")vrAr(T.,0/T"(n"s)XPs/Pttd)
where T"16 = 293 oK, P",o = 760 mm Hg, for metric units
where T",6 = 528 oR, Psro = 29.92 in Hg, for English units
N TNTERMOUNTAIN GENEMTING STATION Date 8t2812024
rllan JNIT 2 STACK Prolect #PM Performance
llika I lllev # of Ports Used
Fuel Type ]OAL. BITUMINOUS Mlnlmum Fuel Factot 1 .083 lMaxlmum Fusl Factor ll .230
Orsat Leak Check f4 I PreTest vl I PostTest Orsat ldentlficatlon 39-507
Gas Analysis Data
Run Number 1 lun Start Tims 7:17 Run Stoo Time 9:22
Sample
Analysls
Time
Carbon
Dloxide
Volume
(V..r)
Oxygen
Volume
(Vor)
Carbon
Monoxide
Volume
(V"a)
Carbon
Dioxide Oxygen
Carbon
Monoxide Nitrogen
Dry
Molecular
Weight
(M,)
Molecular
Welght
Devlation
(^MJ(%cor)(%o,)(%co)(%Nr)
hh:mm ml ml ml percent percent percent oercent lb/lb-mole lb/lb-mole
10:10 '13.6 19.0 13.6 5.4 0.0 81.0 30.39 0.00
10:26 13,6 19.0 13.6 5.4 0.0 81,0 30.39 0.00
10:44 13.6 19.0 13.6 5.4 0.0 81.0 30.39 0.00
Results Averages 13.6 5.4 U.U 81.0 30.39
qveraoe Calculated Fuel Factor (Fo)r,o 1.140 Molecular Wt Deviatlon < 0.3?
:00 (%EA).,.33.8 percent Fuel Factor In Handbook Range?IJ
:10
Gas Analysis Pata
Run Number Run Start Tlmo 9:39 Run Stoo Time 11:44
Sample
Analysis
Time
Carbon
Dioxide
Volume
{v.^,)
Oxygen
Volume
(Vor)
Carbon
Monoxida
Volume
(Vco)
Garbon
Dloxide Oxygen
Concentra
(o/oOr)
Carbon
Monoxide
Concsntra
(%col
Nitrogen
Dry
Molecular
Weight
(Ma)
Molecular
Welght
Deviation
(^Ma)(%co,(%N,)
hh:mm ml ml ml percent D6rcent perc€nt pefcenl lb/lb.mole lb/lb-mole
14:1O 13.5 18.9 13.5 5.4 0.0 81.1 30.38 0.01
14:2O 13.4 18.8 13.4 5.4 0.0 81.2 30.36 -0.01
14:30 13.4 18.8 13.4 5.4 0.0 81.2 30.36 -0.01
Results Averages 13.4 5.4 0.0 81.2 30.37
Avoraqe Calculated Fuel Factor (Fo)"ro 1.151 Molecular Wt Deviatlon < 0.3?lvl
Average Excess Air (%EA)ow 33.7 percent =uel Factor in Handbook Range?lvl
Gas Analysis Data
Run Numbel 3 Run Start Tlme '12:00 lun Stop Tlme 14:05
Sample
Analysis
Time
Carbon
Dioxlde
Volume
(V^^,)
Oxygen
Volume
(V.r)
Carbon
Monoxide
Volume
N.^)
Carbon
Dioxide
Concontra
(%co,\
Oxygen
Carbon
Monoxide Nitrogsn
Concentra
(%t'tr1
Dry
Molecular
Weight
(M,)
Molecular
Wclght
Devlation
(^MJ(%Or)
,Ul lUgllt
(%co)
hh:mm ml ml ml percent percent porcent peroent lb/lb-mole lbflb-mole
14:46 13.6 19.0 13.6 5.4 0.0 81.0 30,39 0.00
15:00 13.6 19.0 13.6 5.4 0.0 81.0 30.39 0.00
15:13 13.6 1S.0 13.6 5.4 o_o 81.0 30.39 0.00
Results Averages '13.6 5.4 U.U 81.0 30.39
AvGraoe Calculated Fuel Factor (Fo).,o 1.140 Molecular Wt Deviatlon < 0'3?E
Average Excess Alr (7oEA).,.33.8 percenl :uel Factor in Handbook Range?lrl
Fuol Factor Fo
Fuel Type Minimum Maximum
Coal, Anthracite 1.016 1.130
Coal, Llgnite 1.016 1.130
Coal, Bituminous 1.083 1.230
Oil, Distillate 1.260 1.413
f,ll, Residual 1.210 1.370
3as, Natural 1.600 1.836
3as. Propane 1.434 r.586
3as. Butane 1.405 1.553
/llood 1.000 1.120
rll/ood Bark 1 003 1 .130
= Voz'Vcoz
= Vco - Vo:
%N, = 1 gg - %CO2 - o/oO2 - o/oCO
Mc = .44(%COzl+ .32(ohOz)+.28(o/oN2 + %CO)
AM6=M6-M60,
Fo = (20.9 - o/oO2' .5o/oCO)l(o/oCO2 + %CO)
Plant Name NTERMOUNTAIN GENEMTING STATION Date 8t28/2024
SamDIlnq Location UNIT 2 STACK Proiect #PM Performance
0perator y'icki Lvman # of Ports Used 4
Stack Type lircular Meter Box Number 1 508035
Train Leak Check l.zl I PreTest I lvl lPostTest Meter Cal Factor {Yl 1,0006
Moisture Content Data
Run Number Run Start Time 7:17 Run Stop Time 9:22
fotal Metor Volume (v.)93.141 dcf Barometric Pressure (Pr)24.80 in Ho
Avq Meter Temo (t-),,o 88 Stack Static Pressure (P.to")1.00 in H,O
Avg Stack Temp (L)",o 117 -F Avq Orifice Pressure (AH).'o 1,66 in HzO
lmoinoer'l lmpinger 2 lmoinoer 3 lmpinqer 4 lmoinoer 5 lmoinoer 6 lmoinser 7
ml ml ml q ml ml ml
Contents 100 Water 100 Water 0.00 200 SiGel
Fina! Value (v),(w)862.52 738.90 607.26 824.50
lnitial Value (v,),(w,)680.08 702.24 601.1 3 805.25
Net Value (v"),(w.)182.4 36.7 6.1 19.3
Results
Total Volume (V')225.20 ml Water Vol Condenged (V*,o"t)10.600 scf
Total Weloht (w,)'19.30 s Water Vol Weiohed (V*.ot.raJ 0.910 scf
Std Meter Volume (Vnrrrar)74.766 dscf Sat Molsture Content (B*.,^')12.8 oa
Calc Moisture Content (B*.r.l.r)13.3 o/o Final Moisture Content (B*.)12.8 o/o
Molsture Content Data
Run Number Run Start Time 9:39 Run Stop Time 11:44
Total Meter Volume (v-)95.1 89 dcf Barometric Pressure (Po)24.80 in Ho
Avq Meter Temo (t^).,o 93 OF Stack Statlc Pressure (P".ort)1.00 in HrO
Avg Stack Temp (t.)oro 118 .F Avg Orlfice Pressure (AH).,q 1.71 in H2O
lmolnoer 1 lmoinqer 2 lmolnqer 3 lmolnqer 4 lmpinqer 6 lmpinqer 6 lmoinoer 7
ml ml ml 0 ml ml ml
Contents 100 Water 100 Water 0.00 200 SiGel
Flnal Value (vr),(W)914.30 729.4E 634.41 832.44
lnitial Value (v),(w,)721.08 688.46 628.85 610.57
Net Value (v"),(w")193.2 41.0 5.6 221.9
Results
Total Volume (v,)239.UU ml Water Vol Condensed (V*r.rar)11.2E7 scf
Total Weioht (WJ 221 .9t)g Water Vol Weighed (v*10.463 scf
Std Meter Volume (V.r.,o)/5. / JU dscf Sat. Moisture Content (B*rrror)13.2 o/o
Galc Moisture Content (B-.)22.3 o/o Fina! Molsture Content (B*)13.2 To
Molsture Contont Oata
Run Number Run Start Tlme 12:00 Run Stoo Tlme 14:05
fotal Meter Volume (V,) s7.656 dcf Barometric Pressure (Po)24.80 in Hq
Avg Meter Temp (t-)*o 95 OF Stack Static Pressure (P 1.00 in H,O
Avg Stack Temp (t,)",s 119 .F Avo Orifice Pressure (AH)",c 1.80 in H2O
lmoinoer 1 lmoinoer 2 lmoinoer 3 lmoinqer 4 lmpinqer 6 lmpinqer 6 lmoinoer 7
ml ml ml o ml ml ml
Contents 100 Water 100 Water 0.00 200 SiGel
Final Value (v),(w)903.1 0 730.30 603.07 824.66
lnitlal Value (v,).(w,)703.77 681.57 597.29 804.21
Net Value (v"),(w")199.3 48.7 5.8 20.4
Results
Iotal Volume (VJ 253.80 ml Water Vol Condensed (V*,.'",)11.946 scf
fotal Weiqht (w)20.40 s Water Vol Weiohed (V 0.962 sc,
Std Meter Volume (V-r.,ar)77.433 dscf Sat, Moisture Content (B-,r,o,)'t3.s %
Calc Moisture Content (B*)14.3 %Final Moisture Content (B*.)13.5 o/o
Phnt Nrno NTERMOUNTAIN GENERATING STATION Drta ar2ana2l
irmollno Locrd.JNIY 2 STACK I.cl I M Pcttomrnca
)paralor lick Moody {un I
I ol Polntr Ador I I ol Pari3 lJr.d
ldarl N621. Dhfrrt.r rnd LoKlnallc Faeldr Saloo
tltol Tub! Cillrlclonl (c-)0.840
lvo Strck TomD (L)'t 14 .F
No Gat Hltrr TlmD (L)81 .F
tH e 0.75 scFtl (air@)1.65 in H,O
lvq Pltot Tub! Dltf, Pr.asura (aD.".)115 in H'O
ttrck lrolsurr Coni.nt (B-)t3 0 % (r.r)
Itrck Dry Molecul.r Wolqht (M-t 30.29 lbnb-fiolr
itdm.lcd Orlllc. Ro{, Rrt.(o-t 0.730 .c{m
\P to AH hokln.llc F.clor IKI 1_15
SrntDllno Eoulomlnt
lratar I 1 508035
5.1.r Crllbradon Frctor (Y) I 1.0006
{ozl. ,I
lclud Nozl. Dlmitrr lo--'l I 0.193 I in
dtal Nozzl. Oirmct.r (D^.)l 0.188 I in
,robo L L.nsth 114.00 I in
-lmr ilrtorlrl SS
rmpl. Grr. / OY.n t 522-14
cr.. J 1522-1C
Prottu;oa
ttromrlric Pr6ruro (PJ 24.80 in Hd
itrck Sl.llc Prarsurs (P.,*)-{ oo in H,O
lb3olutn Stack Pra$ure (P.l ?4.73 rn Ho
\baoluto ilal.r Prasruro (P-)24.91 in Ho
AV- Luk Chlckr
tr!0 tr'/mn d!7.5 in Ho
6td It'/min @ in Ho
tott 0 ll'/min 6 9.2 in Ho
tv- < o.o20 ll'/min L{)T?
Pllot OK?lJ )r.t OK?,!)
TnvortG
Point,
S.mpllng
TimC
lgl
Clock
Tlmo
Ory G..
lr.tor
R.rdlng
lv-l
Volmlty
Hs.d
IAD}
Do3lr0d
Orltlci
AH
{AHI
Aclurl
Orlrico
AH
IAHI
Stsck
Tomp
lrl
Mct.,
lnlit
Tomp
M.tor
OuUot
Tomp
Irt
Flllol
Trmp
lmpingot
Exlt
T.mp
Pump
Vlcuum
SquEra
Rool
AP
(Apra)
Loc.l
St.ck
V!lelty
Cumul.llvo
Motcr
Volumo
tv_l-_-
Cumul.Um
Porccnt
lroKlnodc
,il
mn lrh:mm:ac fl'rn H.O h H.O rn H"O "F "F "F nHo Itn H'O)ra lutrc !c,.A
A-l 0.0 7'.17:00 539.012 1.35 1.55 50 'l't6 80 80 306 55 5.6 r.16 75.18 6.077 100.7
4.2 10.0 7:27iOO 546.475 1.55 1.74 77 ''tt6 81 81 318 48 5.5 1.24 40.55 12,488 90.8
A-3 20.o 7:37:0O 55.1.354 155 1SO 93 'I l5 83 83 323 49 7.0 1.24 83.1r 19.233 too 3
B-1 30.0 7:49:OO s62 875 1.25 1.44 .44 117 85 85 314 53 5_8 1.12 72.tn 25 147 100.7*2 40.0 7:59:00 570.035 43 1.67 .62 117 a7 87 323 53 6.! 120 77 Et 3't.315 'to0.3
B-3 50.0 6:09:00 577.6A3 1.75 2.O1 1.97 117 89 89 322 54 7.1 1.52 85.67 38.033 9S_8
c-'t 60-0 8:21:O0 585.O55 .20 I _38 3B 117 90 90 316 56 5.6 L10 70 s4 43 77'l too 0
c-2 700 8'3'l:O0 593 242 t3s 1 55 .54 117 s0 90 322 55 6.1 1.15 75.21 49.709 99.8
c-3 aoo E:41:00 800.672 .50 73 .73 117 91 91 3't 9 s7 7.O 122 79 31 s6.095 99.9
D-l 900 8:52'OO 608.068 1.20 1.38 .3E 117 9t 91 315 5S 5.6 1.10 70 94 61 413 99.9d-2 100.0 9:02:00 6r 5.842 1.50 1.73 .71 1'17 92 92 321 57 68 12)79.31 08.164 99_9
D-3 't 10.0 9:1 2:00 623.808 1.60 1.84 .86 1',t?92 92 319 58 7.2 1.26 81.91 71.422 to0 0
Last Pt 120 0 E:22tOD a32 153
=16.1 Vrlur 9:22:OO 632.153 Mulmum Find Vrlurs 71.E22 ',o0.0
\varror Vllulr 1.45 6E 318 55 1.20 77 .71
68
I tsoxtNETtc SAMPLING DATA I
Is.mollno Locrtlon lUNf2 STAGK lProl.cr, I PM Prrtormrnc. I
ln^-,..* lEhL M*d. lRilh I l? I
ll ot Potnrr acro$ 13 l, ot Port! Ur.d 14 I
ldoal Norrl! Dlm.ia, lnd LoKinruc Etor Srluo
tltol TubE Co.t lclont (c")0.640
Na St ck TomD (L)117 .F
lvo Ou Hator TomD lL)90
tH o 0,75 scF]it (6H@)1,E5 h H,o
lvo Pllol Tubo Dlfl. Pr.3.urc (AD-.)I .il h H.O
It ck f,lolitsr. Cont nl (B-)13.%
itrck Dry lrol.culrr Wolqht (Mi)30.39 lbIb.md.
:adm.bd Ormc. Flow Rrto (o-)0.776 eclm
lo aH ltollarilc Frctor {K}'t.16
AV- L!.k Choc*t
,fa 0 fi'/m ln o s in Ho
'ttd ft"/min a in Ho
roBt o tt"rmin a 95 in Ho
tv- < o o20 lt'/min lk )k?
lllol OK?4 lrilt OK?ut
TravaBo Srmpllnq Clock
Tlmo
Dry Grlr.t!r
Rordlng
lv-)
voloclly
H..d
lAol
Darlrad
Ortlico
AH
l^Hl
Acturl
Odnco
AH
IAHI
3t.cl
T.mp
lLt
Mol.r
lnlcl
Tcmp
It-t
lr.tor
OuU.t
Tomp
It--l
Flllrr
T.mp
lmplngor
Exlt
Tomp
Pump
3qu.ra
Root
AP
l6pra)
Local
Strck
V.lelty
Gumulruv!
Mottr
Vol umo
tv-t-..
CumulrtlY!
Porconl
l3oXln!tlclIPolnl I Tlm
(o)
Vrcum
rnin hh:mm:34 tr'rn HrO in H.o in HrO -F I F in Hg (n HrO)"'rurft 3cf
D-1 oo 9:39:O0 832.675 1.30 1.Sl .45 ta t9 80 302 63 6.1 1.14 73.79 6 023 102.O
D.2 10.0 9:49i00 640 196 1.50 1.74 74 1't 8 89 a9 310 59 6_8 1.22 79.26 12.385 tol 1
D-3 20.0 9:59:00 648.135 160 '1.86 _86 't 18 90 90 321 63 7.2 1.26 81.86 1 8.984 101.0
1 30.0 10:'l 1:0C 556.381 1.30 151 50 117 90 90 316 58 6.1 I 7r72 25.014 101.2
c-2 /EO O I O:21:Ot 663.S24 1.50 1.74 .70 118 92 92 321 54 5.7 1.?2 79,26 31 2{2 100.6
c-3 50.0 tO:3t:Ot 671 738 r.55 1.80 .78 117 93 g3 320 56 7.O 1.41 80.50 37.642 100.4
B-1 60.0 t 0:/t2:O(679.781 r30 t51 .50 118 03 93 315 58 6a 114 73.79 43.622 100.5
B-2 70.0 10:52:00 887.303 1.45 1.68 55 1'.t?94 94 323 59 6.9 r20 77 A6 40.766 100.2
B-3 80.0 1:02:00 695.042 1.65 1.9r .89 '118 95 05 318 50 7.5 1.28 83.13 56.345 'to0.1
A-t 90.0 1 1:14:00 703 335 1.35 1.57 .57 116 95 9S 420 6l 6.7 1_16 75.19 62.384 1()0-1
A-2 100.0 11:24'.OO 710.S58 1.65 lgl .s0 118 95 95 318 60 7.5 124 83.'t 3 68.999 100.0
A-3 1 10_O 1:34:O0 719.2S6 1.70 1.97 99 '118 96 06 121 60 8.0 1.30 B/l38 75.7A7 1 00.1
Last Pt 120.0 1:a4:O0 727.864
Rnal Vtlut 1?O.O 1 1:44 727 t6!Hrr Vacuum 8_0 Flnrl Vdur.75 747 1 00.1
lvondo Vrlu!r 1.49 1 ,18 93 93 318 59 1_22 7a a2
93
,lrnt Nrma MOIIhITAIN GENERATING STATION ilr 9128t2024
irm6llnd Locallon JNIT 2 STACX Pml.ct4 PM P.rrormanc.
Joantor thk Moodv Run *3
I ol Polnt Acr63r , of Porlt l,J..d I
ld.rl Nozzlr Dhm.t r rnd lroKlnatlc rclar SaluE
,ltot Tub. Cortficl.nt (c")0.840
\vo Strck Tlmo (L)118 'F
\Yo Grs u.trr T.mD (L)99 ?
!H @ 0.75 SGFilI {AH@)1.85 in HrO
{va Pltot Tuba DIff. Prrs3ura (AD-)1.49 in HrO
St ck Moltturr Cont.nt (B-J 12.7 o/o
St ck Diy Mohculrrlvaioht (M-l 30.36 lbflb-moL
Eftlmrt.d orlflcr Flow Rrte (o-)0.793 .c'fm
lP to AH l3oklnrtlc Frctor tKt 1 _19
SrmDllno EoulDmant
ir.t r*l 508035
Matar Crllbrrtlon Frctor u) 11.0006
Nozrh,11
Actual Norzl. Dlam.t.r (D-) I 0.193 h
ldc.l Nor.2l. Dlrmrtll (D-) I 0.192 n
Probe # / Lrnoth 1 114.00 n
Lln.r lht.rirl 55
rmola Casr, Ovln # 522-1A
lmolnorr Crr I -'1C
Prci3ura3
Brtomatrlc Prtr3utla rP.) 24.80 hHo
Strck St ilc Pr.3turo (P -1.00 in H,o
Abrolutc Stlck Pr.srurr (P.)24.73 hHo
qbrolute Mttar Pra33ur.(P-)24.94 hHo
AV- L.rk Ch.cks
tra o ll'/min @ 9 in Ho
trlld ff'/min @ in Ho
,ort 0 It'/min (a 9.5 in Ho
Iv- < 0.020 fl'/mln )t lk?
,ltot OK?.t lnri Ok?t3
Po16rnt
l30KlnrUc
METHOD 5. SAMPLE RECOVERY AND INTEGRITY DATA SHEET
Plant Name INTERMOUNTAIN GENERATING STATION lDate I 8128/2024
Samollno Locatlon UNIT 2 STACK Proiect #PM Performance
0perator Vicki Lvman {cetone Lot Number 248735
Run Hlstorv Data
Run Number 1 2 3
Run Start Time 7:17 9:39 12:00 (hh:mm)
Run Stoo Tlme 9:22 11'.44 14:05 (hh:mm)
Traln Preoared Bv VL VL VL
Train Recovered Bv VL VL VL
Recovew Date 9t1412023 9t14t2023 9t14t2023 (mm/dd/vv)
Rellnoulshed Bv nla nla nla
Received Bv
Relinqulshed Date (mm/dd/yv)
Relinouished Time (hh:mm)
Eouioment ldentlflcation Numbors
Fllter 4 5 6
Acetone Wash 121715 E 121715 E 121715 E
Sllica Gel 0RP-12-108 DRP.1 2.1 OB DRP-1 2-1OB
impinoer Case 522-1c 522-1C s22-1C
Samole Box 522-14 522-14 522-14
Cven 1350G 1 350G 1350G
Formulas Used
Vn=Vr-Vi Wn = Wt-=V-+where P* = .9982
Molsture Content Data
lmolnoers 't. 2. and 3 - Water Volume
Final Volume (Vr)2208.7 2278.2 2236.5 q
lnitia! Volume M)1983.5 2038.4 1982.6 g
Net Volume (v.)225.2 239.8 253.9 q
Comments
lmpinqer 4 - Sllica Gel Weioht
Final Weioht (w)824.5 832.4 824.t s
lnltlal Weight (WJ 805.3 610.6 804.2 s
Net Weioht (w")19.2 221.8 20.5 s
Comments
Total Water Collected
Total Volume (v,.)244.4 462.0 274.4 g
IPP_PM_U2_8 28 2024- M5 - Recovery Page 1 Printed 912312024
Plant Name INTERMOUNTAIN GENEMTING STATION Date 8t28n024
SamplinE Location UNIT 2 STACK )roiect #PM Performance
Soerator r/icki Lvman {cetona Lot Number 248735
Analvtical Data
Placed in Deslccator Run Number 1
Number Date Time lun Start Tlme 7:17
tilter 5 o8t28t24 10:14 -eakaoe Evldent?lrl no
qcotone Wash Beaker c5 08129124 8:58 istlmated Volume 100 ml
Filter Acetone Date Tlme Humldlty 230 Cal Audit
a a mm/dd/yy hh:mm o/rRH r 0
Measurement I (mr),(mi,)0.6234 136.9904 o8t31D4 9:01 25 72
Measurement 2 (mrr),(mz.)u.t z33 136.9908 o9to1tz4 8:41 28 72
Measurement 3 (msr),(mr,)t30.99U9 09ta3n4 5:19 38 72
Measurement 4 (mr),(m.,)
Results Acetons Blank
Final Weisht (mn),(mh')0.6234 136.9909 I :inal Weioht (ch')129.8972 s
Iare Weight (mn),(m,.')0.62s0 136.9828 s Iare Weioht (c,.')129.8966 s
rllleioht Galn (m),(m"')1.6 8.1 mg 3lank Concentratlon (c.)0.0000 ms/g
Blank Adiustment (w.)0.0000 mq
fotal Partaculates (mn)6.5 m0
Analvtical Data
Placed ln Desiccator lun Numbsr 2
Date Time lun Start Time 9:39
FIlter 4 08t28124 12:58 -eakase Evident?rl no
Acetone Wash Beaker c4 08t29t24 8:58 =stlmated Volume 100 ml
Fllter Acotons Date Time Humlditv Temp Cal Audlt
s o mm/dd/w hh:mm %RH OF o
lllleasurement 1 (mtr),(mr.)0.622s 129.2814 o8t31n4 9:01 25 72
Meagurement 2 (m,),(mrJ o.6224 129.2818 ogtun4 8:41 28 72
Measurement 3 (m.),(m'.)129.2819 09to3t24 5:19 38 72
l\ileasurement 4 (m.r),(m.J
Results Acetone Blank
tlnal Weight (m'r),(mh')o.6225 't29.2815 I rlnal Weisht (Cr')129.8972 s
Tare Welght (mr).(m,.')0.6227 129.2756 s fare Weioht (C,.')129.8966 s
ffeisht Galn (m),(m.')-0.2 6.3 m9 3lank Concentration (c.)0.0000 ms/g
Blank Adiustment (w.)0.0000 mg
Iotal Particulates (m.)6.1 mg
Analvtical Data
Placed in Desiccator Run Number 3
Number Date Time lun Start Tlme 12;00
Fllter 6 o8r28/24 1432 -eakape Evident?lJl no
Acetone Wash Beaker c6 a8n9n4 E:58 AM :stlmatod Volume 130 ml
Flltar Acetone Date Time HumidlW Temo Cal Audit
E s mmidd/yy hh:mm %RH oF o
Measurement I (mt),(mt.)0.6261 '127.4140 08i31n4 9:01 25 72
Measurement 2 (mz),(mz.)0.6260 127.4146 09101t24 8:41 28 72
Measurement 3 (mJ,(ms.)'t27.4148 09tc'3n4 5:19 38 72
Measurement 4 (m.r),(m..)
Results Acetone Blank
f-lnal Woioht (mfl),(mr.')0.6261 127.4147 s --lnal Welght (c,"')129.8972 s
fare Weloht (m,{),(m*')g.bz6t 127.4084 s Iare Weight (C"')129.8966 I
/Veioht Gain (mr,(m.')-0.6 o.mg 3lank Concentratlon (c.)0.0000 mo/o
Blank Adjustment (w.)0.0000 mg
Total Particulates (mJ 5.;mg
Formulas Used
filx = itvor?lE of last two filter measurements fl1| = lTls - lTll w. = c.m* ]116=IT11 * fi.'- w.
mr.' = everage of last two acetone measurements tro' = mrr' - mu' fi1sy = tl'tsp * t'1111 -
IPP_PM_U2_8 28 2024 - M5 - Analytical Printed 912312024
r'rterHOO S -OerenUlNATION oF PARTICULATE EMISSIONS - RESULTS
Plant Name INTERMOUNTAIN GENERATING STATION Date a28n024
5amollnq Locadon UNIT 2 STACK Prolact #PM Per{ormance
Coarator y'icki Lyman Stack Type lircular
Historlc.l Data
Run Number 2 3 Average
Run Start Time 7:17 9:39 12:00 Runs 1 .2.
and 3
hh:mm
Run Stop Time 9:22 1'l:.44 14:05 hh:mm
Meter Callbration Factor (Y)1.001 1.001 1.001
Pltot Tube Coefflcisnt (c,)0.840 0.840 0.840
\ctual Nozzle Dlameter (D-)0.1 93 0.193 0.193 tn
Stack Test Data
lnltial Moter Volume (V.)i 539.012 632.675 728,202 fi'
:inal Meter Volume (V')r 632.1 53 727.864 825.858 flo
Iotal Moter Volume (v-)93.141 95.189 97.656 95.329 fi'
fotal Samolino Tlme (o)120.0 120.0 't20.o 120.0 min
Averaqe Meter Temp€reture (t.)*88.0 s3.0 95.0 92.0 "F
Avoraae Stack T€mperature (t.).,0 117.O 118.0 1 '19.0 118.0
Barometrlc Prcssure (Pu)24.80 24.80 24.80 24.80 in Hq
Stack Static Pressure (P..uJ 100 -1,00 -1.00 1.00 in H"O
Absolute Stack Pressure (P.)24.73 24.73 24.73 24.73 in Hq
Average Orlflce Pressure Drop (AH).*1.66 1.71 '1.E0 1.72 in H,O
Absolute Meter Pressure (P-)24.92 24.93 24.93 24.93 in Hq
Avo Souare Root Pltot Pressuro (aD"'),,"1.20 1.22 1.24 't.22 (in H2O)r"
Moisture Content Data
lmoinqers 'l-3 Water volume Galn (v")225.2 239.8 253.9 239.633 ml
moinaer 4 Silica Gel Welqht Galn (w.)19.2 221 .A 20.5 87.167 I
[otal Water Volume Collocted (Vr")244.4 462.0 274.4 326.933 ml
Standard Water Vapor Volume (V*L,,11.504 21.746 12.916 15.389 scf
Standard Meter Volume (V.).ra 74.796 75.760 77.464 76.00/dscf
:elculated Stack Molsture (B-.13.3 22.3 14.3 16.6 oh
Saturated Stack Molsture (B*.r.,or)12.8 13.2 13.5 13.2 %
Reported Stack Molsturo Content (Brt)12.8 13.2 13.5 13.2 oA
Gas Analysis Data
larbon Dioxlde Percentase (o/oCOzl 13.6 13.4 13.6 13.5 c/o
OxYqen Percentaoe (o/oOzl 5.4 5.4 5.4 5.4 c,/o
Barbon Monoxlde Percentaqe (o/oCO)0.0 0.0 0.0 0.0 c/a
Nitrogon Percentago (%Nr)81.0 81.2 81.0 81.1 %
)rv Gas Molecular Weight (M.)30.39 30.36 30.39 30.380 lbflb-mole
iret stack Gas Molecular Welqht ru.)28.74 27,60 28.62 28.320 lbflb-mole
:alculsted Fuel Factor (F,)1.140 1.157 1.140 1.146
:uel F-Factor (Fa)9780 9780 9780 9780 dscflmmBtu
Percent Excess Air (7oEA)33.8 JJ. I 33.8 33.8 ch
Volumotrlc Flow Rato Data
Averaoe Stack Gas Velocitv (v.)77 _64 80.62 80.54 79.60 fUsec
Stack Crors-Sectional Area (4.)615.75 615.75 615.75 615.750 ft'
Actual Stack Flow Rete (Q.)280841 0 2978506 2975550 2944822 acfm
Dry Standard Stack Flow Rate (Q.a)1880966 1747383 1 922056 I 8501 35 dscfm
Porcent of lsokinetic Ratc fl)100.5 109.6 101.8 104.0 o/o
Emission Rate Data
Mass of Partlculats on F|ltsr (mJ -1,6000 O.ZUUU -0.6000 -0.800 m0
Mass of Particulats in Acetone (m,')8.1000 6.3000 6.3000 6.900 mg
Mass due to Acetone Blank (W.)0.0000 0.0000 0.0000 0.0000 mg
Total Mass of Partlculates (m")6.5 6.1 5.7 6.'l m9
Stack Particulate Concentratlon (c.)0.0001 0.0001 0.0001 0.0001 g/dscf
(ca)0.0015 0.0015 0.0015 0.0015 gr/dscf
Particulate Emission Rate (E)11.29 10.48 1 '1.53 't1.10 ks/hr
(E)21.6 1E.6 18.7 19.6 lbs/hr
(E)0.0025 0.0023 0.0021 0.0023 lbs/mmBtu
LOCATION OF TRAVERSE POINTS IN STACKS
The following two tables give the location of traverse points across the stack as a fraction of the
stack dimension from the inside wall, as a function of the number of traverse points across the stack.
Location of Traverce Points in Circular Stacks
Traverse
Point
Number
(Fraction of Stack Dimension lrom lnside Wall to Traverse Point)
Number of Traverse Points Across the Stack
2 4 6 I 10 ,,2
1 .146
.854
.067
.250
.750
.933
.044
.146
.296
.704
.854
.956
.032
.105
.194
.323
.677
.806
.895
.968
.026
.082
.146
.226
,342
.658
.774
.854
.918
.974
.021
.067
.118
.177
.250
.3s6
.644
.750
.823
.882
.933
.979
2
3
4
5
6
7
8
0
10
11
12
Location of Traverse Points in Rectanoular Stacks
Traverse
Point
Number
(Fraction of Stack Oimension from lnside Wall to raverse Point)
Number of Traverse Points Across the Stack
2 3 4 5 6 7 8 9 10 11 12
1 .250
.7sa
167
500
833
125
375
625
875
.100
.300
.500
.700
.900
.083
.250
.417
.583
.750
.917
.071
.214
.357
.500
.643
.786
.929
.063
.188
.313
.438
.563
.688
.813
.938
.056
.167
.278
.389
.500
.611
.722
.833
.944
.050
.150
.250
.3s0
.450
.550
.650
.750
.850
.950
.045
.136
.227
.318
.409
.500
.591
.682
.773
.864
.955
.042
.125
.208
.292
.375
.458
.il2
.625
.708
.792
.875
.958
2
3
4
5
6
7
8
9
10
11
12
IPP PM UZ 8 28 2024 - Fraction of Diameter Page I Printed 912312024
isoCALC UNITS
Unlt! Nrmr TrblG
Unlt3
Numbrr
Natlvc
Name
EngliBh
Nrmg
1 Enqlish Enolish
2 Metric Metric
3 Blank tslank
Curreni llnlt Numbrt 1
UnlE Lookup Teble
Engllrh
Unlt3
Motrlc
Unlt3
L
in mm
in clTl
in m
ft m
1'm'
n"m"
dcf dcm
Jcl sc'n
d3cf dscm
c,fm cmm
acfm acmm
ft'/min m'/min
dscfm d3crnm
dsf/min dscm/min
dscflhr dscrn/hr
fUsec m/sBc
in H,O mm HrO
in Ho mm Ho
in Ho kPa
(in HaO)(mm H:O)rr
lbnb-.mol6 0/0-mole
o/d3cf o/dscm
or/dscf orldscm
lbr'hr ko/hr
Conrtrnt! LoohuD T.blc
Conitrnt
Nrme
Con3tant
Svmbol
Currcnt
Valuc
Currant
Unltt
Engllrh
ValuE
Engllsh
I lnlrr
Matrlc
Vrlue
M.trlc
Unltr
Lergo gt ck Dlamoter (Cru)24 tn 24 ln 0.61 m
lnchca pcr Foot (C.')12 in/tt 1?in/ft 1 m/m
nches pcr Foot mm pcr Matcr (c.12 in/lt 12 in/ft 1 000 mm/m
lllximum Allowrbl! L.rk Rrte (C*)0.02 cfm 0_02 cfm 0.00057 m"/min
{ozlc Olametar Conrtsnt )")0.03575 ?0.03575 607.'l ?
( Frstor Conitant (cr)849.8 7 M9,E ?8.038E-05 ?
,ltot Tubs Conrtrnt K.85.49 )le)fin Ho))r 85.49 ilexin Hg))34.97
u.tGr Molstur! Contcnt (B*.)0.00 %0.00 9/o 0.00 %
iilrter Dry llolGcul.r Wclght (tld^)29.00 lb/lb-mole 29.00 lb/lb.mol6 ?9.OO o/c-molG
,rca.ure Drop in Gil Me(cr (P"-)o.25 in HrO 0.25 in H"O 6.35 mm HrU
Ab3olute Trmorr.turr Offart T"460 460 273
Strnd.rd Ab3olut! Prcsrur€P 29.92 in Ho 29,92 in Ho 760.00 mm Ho
st nd.rd Absolute Tomoor.tur.T 528 528 .R 293
it nderd Volume Corractlon K1 17.u "RYin H0 17.64 "Riin Hg 0.3858 'K/mm Hg
rurter Volume to Std Wetor VePol K, 0.04707 fl'/ml 0.04707 fl'/ml 0.001333 mo/ml
roklnctlc Verlttion - Raw Drta K"0,002669 Hg-fi'/ml-0.002669 H9.lt'ht.'0.003454
3oklnotlc V.rl.tlon - lntermedlrte &0.09450 ?0.09450 7 4.320 ?
,Vatcr Ma3! to Std Wrtcr Vapor K"0.04715 n'/c 0.04715 It'/g 0.001335 m?
)core.. F to O.or.o3 C ilultloller K"1.000 .FfF 1.000 "FTF '1.800 'Ffc
).oreGs F to Ocorla3 C Offret Kr 0.000 "F 0.000 .F 32.00
\llllllmctars pe, lnch Kr 1.000 in/in 1.000 in/in 25.40 mm/in
3?rmr oar Pound l(1.000 in/in r.000 in/in 25.40 mm/in
)cn3ltv of Wat.r pD 0.9982 s/ml 0.9962 qhl 0.9982 o/ml
IPP_PM_U2_8-28-2024 - Unils Printed 912312024
L lsoKtNETtC SAMPL|NG
Plant Name INTERMOUNTAIN GENERATING STATION Date 8, Zl, ZDZ.I
SamDllno Location UNIT 1 STACK Proiect #Utc?tu0paratorRlck Moodv Run #'/I of Potnts Across 3 l of Ports Used
ldeal Nozzle Dlameter and lsoKlnctic Factor Setuo)ltot Tubo Coefficlent (c")0.840
fus $tack Temp (t.)"F
Avg Gas Meter Temp (1.)"F
aH @ 0,7s SGFM (AH@)in H.O
Avs Pltot Tubs Dlff, Pressure (Ap*)in H"O
Stack Molsture Content (B*.)% (n<.x)
Stack Dry Molecular Weiqht (MoJ lb/lb-mole
Estimatod Orifice Flow Rate (Q.)acfm
!P to AH lsoklnetic Factor ffi)
Sampllng Equlpment
Uetor #
Vleter Calibration Factor cn
{ozzle #
Actual Nozzle Dlameter (D,.)tn
ldeal Nozzle Dlameter (D",)in
Probo * / Lenoth 1 114,00 I in
Llner Material SS
Sampls Case / Oven #522-1A
rmDlnoer Crse #522-1C
Presgures
Barometric Pressure (Pn)ln Ho
Stack Statlc Pressure (Po"")in H"O
Absoluto Stack Presrure (P.)in Ho
Absoluie Meter Pressure (P.)in Ho
AV, Leak Checks
,fe D flo/min @ 7.r in Ho
Mid ft"lmin @ in Ho
Post 1.4 flolmin @ 3L in HE
av- < 0.020 fto/minf tr 0k?
Pltot OK?Drsat OK?lf
Traverse
Point #
Sampling
Time
(e)
Clock
Time
Dry Gas
Mcter
Roadlng
u-r
Voloclty
Head
(^p)
Doslred
Orlfice
AH
(alt)
Actual
Orifice
AH
(AH)
Staclr
Temp
(L)
Metor
lnlet
Temp
(t-,)
Meter
Outlet
Temp
(L^l
Fllter
Temp
lmpinger
Exit
Temp
Pump
Vacuum
mtn hh:mm:ss fi'in H"o in H.O in H,O OF "F OF "F "F in Ho
A-'t 0.0 u:I.:
$1.otxffu,tf$
,#L€,7 ,r&o toiT
,o in Et 616*
(At b7rO
A-2 10.0 t,i ,.?P tlb il L
A-3 20.0 '{1,ztry ,/-b 1,93 J]L I Pq 323<t4
e23
B-1 30.0 7-! 4 (/^7 L1s t,2l t 1,44 t)1.6 E:
B-2 40.0 v;4 l{7D.h21 l,+)+Itl 1_tl7 ?;g E
^qB-3 50.0 *irrn tmt.L9.t,.ot R'It YI M .&t a:tc-1 60.0 ,:2 w?c,65kq,\.luL
l,Ec iBn /,8 tl 7 0 //-7T frlzc-2 70.0 la lr 3{I,ES 1,5'l I )-f)27 W 6tlc-3 80.0 ':1t i@,&7 l.sb ,.71 i,1frt.l )7 +VtD
D-1 90.0 s/-It?,l^l?,20 I l)a gt 3tS at bt/z
D-2 100.0 ;OL 6tc,ncl)f,tt 7;7-T lt q C]L ffi qD-3 110.0 'l 7.%.ffiB l-Lt /,t{t&l i.q1 ?tt a7
Last Pt 120.0 ,ZZ l,lF
=inal Valuel 120.0 Maxlmum Vacuum\verage Values
Plant Name NTERMOUNTAIN GENERATING STATION Date Y.Zt.ao2t)
Samplinq Location JNIT 1 STACK Prolect #I lu .ti?-
)perator Rick Moody Run #
I of Polnts Across 3 B of Ports Used
ldeal Nozzle Dlameter and lsoKinetic Factor Setuo
Pitot Tube Coefficient (c.)0.840
Avq Stack Temp 0.)
Avg Gas Meter Temp (r-)
AH @ 0.75 SCFM (AH@)in HuO
Avq Pltot Tube Dlff. Pressurs (AP.*)in H,O
Stack Molsture Content (B*.)% (to<.x)
Stack Dry Molecular Weiqht (MaJ lb/lb-mole
Estlmated Orlflce Flow Rate (a-)acfrn
!P to AH lsoklnetic Factor (K)
Sampllns EqulDmont
Meter #
Moter Calibratlon Factor m
Nozzle #
{ctual Nozzle Diametor (D".)in
deal Nozzla Dlameter (D")ln
rrobe # / Lenoth 1 114.00 I in
-iner Materlal SS
Samplo Case / Oven #522-14
lmolnqer Case #522-1C
Pressules
Barometrlc Prorsure (Pu)in Ho
Stack Static Pressure (Po*)in H,O
Absolute Stack Pressure (P.)in Hg
Absolute Meter Prossure (P-)in Hq
AV- Leak Checks
Pre 6 fl'/min @ q.o in Hq
Mtd fi-lmin @ in Ho
Post g fl"/min @ ?,f,in Ho
tv- < 0.020 fto/min tr tk?
Pitot OK?U Orsat OK?w)
Traverse
Polnt #
Sampllng
Tlme
(o)
Clock
Time
Dry Gas
Meter
Readlng
ru-l
Veloclty
Head
(ap)
Deslred
Orlfice
AH
(AH)
Actual
Orifice
AH
(AH)
Stack
Temp
lLl
Meter
lnlet
Temp
{L,I
Meter
Outlet
Tomp
(L^)
Fllter
Temp
lmpinger
Exlt
Temp
Pump
Vacuum
mtn hh:mm:ss fl-in HoO in H,O in H"O "F r OF OF in Ho
A-1 0.0 ,7 l,30I,fD IS?,.rT=Ir 1 t)i
g,q 343n 5.<1r,l
A-2 10.0 ffi l,Tbl ?g ,fi LrF
A-3 20.0 t,t 'l,W;),n IT qn D t9l d_, 2z-
B-1 30.0 lfl,,l t l,1A ),cl l,l I t9 47,
?r-67 *+B-2 40.0 lb,zl b3,114ilt.*lfr b5lfr 1,71 t,I ,/-??l .d.l
B-3 50.0 aD't,/,*1 /-II Q2D rL 7,1)
c-1 60.0 lh:tt?-I t6l LLl,!q:,<,f,ri
c-2 70.0 .q.f 1,1.2 t.,q 22 rq'6'Y
c-3 80.0 ,I Lqt t.tx z(
D-1 90.0 /, ?r
,%
I oE* lt q ao Z,-
D-2 100.0 LqI t,lt 4t 3t9 /l)
D-3 110.0 t l.;"4 t,l)w qa ffi q,D
Last Pt 120.0 / l:t4t ,a1-1.qri
=inalValue 120.0 Maxlmum Vacuum
\veraoe Values
Plant Namo ruipnuouruTnIN GENERATING STATION Date z . ?1)24
Samollnq Locatlon UNIT 1 STACK Prolect #L -7-
Operator Rick Moodv Run #
#.of PointE Across 3 F of Porte Used 4
ldeal Nozzle Dlameter and lsoKlnetic Factorilolup
,itot Tubo Cocfficlent (C,)0.840
lvo Stack Temp (r)r
dvq Gas Meter TemP (h)r
LH @ 0.7s scFM (AH@)in HzO
Avq Pitot Tube Dlff. Pressure (ap*)in H"O
Stack Mol3ture Content G*.)% (p<.x)
stack Dry Molecular Weight (MaJ lblb-mole
Estimated Oriflce Flow Rate (Q.)acfm
AP to AH lsoklnetic Factor K)
SimpllnE Equlpment
Meter #
Meter Callbratlon Factor (Y)
Irlozzle #
\ctual Nozzle Dlameter (D".)tn
deal Nozzle Diameter (Dr)tn
Probe # / Lenoth I 114.00 I in
Llner Material SS
Sample Case / Ovon #s22-14
lmolnoer Case #522-1C
Plessures
Baromotrlc Pressure (P')in Ho
Stack Static Pressure (P.r.rr")in HrO
Absolute Stack Pressure (P.)in Ho
Absolute Moter Pressure (P.)in Hg
AV- Leak Checks
Pre I fl'/min @ qf)in Ho
tld fl'/min @ in Ho
rost ,g ft"/mln @ t7,{in Ho
tv- < 0.020 fl'/min tr ok?
Pitot OK?Y Orsat OK?t5
Trav6rsG
Polnt #
Sampling
Tlme
(s)
Clock
Tlme
Dry Gas
Metor
Reading
(v-)
Veloclty
Head
(Ap)
Desired
Orlflce
AH
(AH)
Actual
Orlflce
AH
IAH)
Stack
Temp
(L)
Moter
lnlet
Temp
(L,)
Mstor
Outlet
Temp
(L^)
Fllter
Temp
lmplnger
Exlt
Temp
Pump
Vacuum
mln hh:mm:ss fl'in HrO in HzO in HrO "F "F "F F F in Ho
A-1 0.0 lzt00 a-E2n)),7?h';r5 lt 4 alq <Na faA,
A-2 10.0 l, 'll,1a-,qolql.y/,1
l,b z07 b it.?5_J 32t I la 4.
A-3 20.0 /):20 l.7F 7^OR 2,0L //l q4 't)zitrJ+XrO
B-1 ,30.0 t2!TZ^ffi .30 lecl q.Ll 2D ,r Iot
B-2 40.0 tr;.rL l.fo l,{r y'll d {D h-7
B-3 50.0 tr:c )*-q,l ]W ,,ID Y o '(-3.a-gD
c-1 60.0 ,3',A1 ffiTE /. Lrri .e:l,t ll 4 ?4 9/L 57 /-, 10
c-2 70.0 t'7: l? lK,ti .ro ,?ilc "16 a2t T,J
c-3 80.0 f,<,'2L ffJ,{r .lol),),gDr-4Zt _78-,3t{L/fi-f
D-1 90.0 la:I 5 x -<r)Lbk n.
D-2 100.0 n;Ll,-?07,n,l,ftr?.,5r ),8L|l,8L tq a-t *t
D-3 110.0 l?'t'{t,a,h Aftf l, )I q 6l!I
Last Pt 't20.0 t.l!6 l91ri, E{
:inal Value 120.0 Maxlmum Vacuum
{veraoe Values
Plant Name INTERMOUNTAIN GENERATING STATION Date qfrlMal 4, /.tl</Ilu
Samplinq Locatlon UNIT *STACK Proloct #ll.n,? Z
Operator Thrtt- llil,av F of Ports Used
Fuel Tvoe 3OAL, BITUMINOUS Mlnlmum Fuel Factor 1.083 lMaxlmum Fuel Factor 11.230
Crsat Leak Check D( I PreTect W I PostTest Crsst ldontlficatlon 3S-507
Gas Analysls Data
Run Number lun Start Time Run Stop Tlme
Sample
Analy8is
Time
Carbon
Dioxlde
Volume
(V"-)
Oxygen
Volume
(Vor)
Carbon
Monoxlde
Volume
rv^^)
Carbon
Dloxido
Carbon
Monoxide Nltrogen
Concentra
(0/6N")
Dry
Molecular
Welght
(M,)
Molecular
Welght
Devlatlon
(aMd)(ohco"l (o/oO2)(7oCO)
hh:mm ml ml ml Dercenl perc€nt percent Dercent lb/lb-mole lb/lb-mole
u\,. I t)t?.
A:2 I i'qi1:ull 1.
Results Averaqes
Averaoe Calculated Fuel Factor (FJ.*Molecular Wt Deviation < 0.3?
Average Excess Air (YoEA).*Dercent Fuel Factor ln Handbook Ranoe?
Gas Analvsls Data
Run Number Run Start Tlme Run Stoo Tlme
Sample
Analysis
Time
Carbon
Dloxlde
Volume
(V"^J
Oxygen
Volume
(V^J
Carbon
Monoxide
Volume
(V" )
Carbon
Dioxlde Oxygen
Carbon
Monoxide Nltrogen
Dry
illolecular
Welght
(M,)
Molocular
Weight
Devlation
(AM.)(o/oCO,)(o/oO)(o/oCO)(%N?)
hh:mm ml ml ml Dercent Dercent Derc€nt Dercent lb/lb-mole lb/lb-mole
11'. I t\t?<K,q
iU ia^ la. U :9,cRitl: ?A l7"Ll i 7.q
Results Averages
Average Calculated Fuel Factor (FJ'*Molocular Wt Devlation < 0,3?U
Averaqe Excoss Alr (%EA).*percent Fual Factor ln Handbook Ranoe?U
Gas Analvsls Data
Run Number 3 Run Start Tlme Run Stoo Time
Sample
Analysls
Tlme
Carbon
Dioxide
Volume
(V..r)
Oxygen
Volume
(V.r)
Carbon
Monoxlde
Volume
(Vco)
Carbon
Dloxlde
concentra
(%cor)
Oxygen
Carbon
Monoxide
Concentra
(o/oCO)
Nltrogen
Dry
Molecular
Weight
(Mo)
Molecular
Weight
Deviatlon
(aMa)(o/oOz\(%Nr)
hh:mm ml ml ml 9ercent percent Dercant percent lb/lb-mole lb/lb-mole
ta._ub i.(,,ot<|4n i?,-ni1:-13 [3,q.A
Results AYeraqes
Averaqe Calculatod Fuel Factor (F")","Molecular Wt Daviation < 0.3?
Averaoe Excess Air (o/oEA).*pBrcenl Fuel Factor in Handbook Ranoe?
Fuel Factor Fo
Fuel Type Minimum Maximum
Coal, Anthraclte 1.016 1.'130
Coal, Lignlte 1.016 1 .130
Coal, Bitumlnous 1.083 1.230
Oil, DlstJllate 1.260 1.413
Oil, Residual 1.210 1.370
Gas, Natural 1.600 1.836
Gas. Propans 1.434 1.585
Gas. Butane 1.405 1.553
Wood 't.000 1.120
9Vood Bark 1.003 1.130
7oCO2 = V6e2
%O2=V62-V662
ToCO=Vco-Vo:
%N2 = 199 - %COz' o/oo2' %CO.
= .44(o/oCOzl+ .32{o/oO2)+.28(%N2 + %CO)
Fo = (20.9 - o/oO2- .5o/o0O)l(o/oCOz + %CO)
sooc;cr!=qo0,ottofz
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Molsture Gontent Data
Run Start Time
Total Meter Volume
lnitial Value
Final Moisture Content
Plant Namc Date B-29-z
Semollno Locatlon Proiect i llrrrrf 2 M
Operator Acetone Lot Numbet 2AF,ZA
Anelytical Dat.
Placed ln Desiccator Run Number
Number Date Tirne Run St rt Tlmr
Fllter 6 e-rQ-ra ln:.14 LeakaEe Evldont?N^
Acotone Wash Beaker c-a t-dt04 t!6*Estimated Volume ln, nrl-
Fllter Acetono Date Timo Humidlty Temo Cat Audlt
q o mm/dd/w hh:mm %RH q
Moasursment I (mrr),(mr.)b-t 24 ,7.bAAly'n*bl .9, at I 7.6 -t?
Measurement 2 (mx),(mrJ 0.b28?lea qctrl atdl a*,lA1 ,LF 22
MeasurGment:(msr),(mr)l4-na ralaaltA nEr tA ?r 'lq
Measurement 4 (mrr),(mr.)
Rerults Acetone We.h
Flnal Weishl (mi),(mh')g Bottle Wt with Wash (mu,)g
Tare Welohl (mr),(m-')s Addltlonal RinteW (m-)q
Weight Galr (mJ.(m.')mo Bottle Tare Welqhl (m'r)s
Blank Adiustmenl (w,)mg NetWrsh Weiohl (m*)s
Total Particulates (mn)mg Blank Goncentratlon (c^)ms/9
Analytical Data
Placed ln Dericcator Run Number
Numbor Date Tlme Run Start Tlms
FIlter 4 *-z*-r4 ,2r.qA Leakage Evident?No
Acotone Warh Beaket ot+a-qa-il d*rR*Estamated Volume , AO trytL
Fllter Acetone Date Tlme Humidlty Temo Cal Audlt
CI q mm/dd/w hh:mm %RH oc o
Msasurement't (mrr)'(mr.)D-b2124 t 4at.2*1,a*ldzd 2E 11L
Measurement i (mrr),(mr.)o.tr224 trQ,A.t*"1|-t8 ao.tll 2*'l)
Measuremont 3 (msr),(m3J ,.A.r*rq allokl"d nl:n ER 12
Measuroment 4 (mrr),(mr.)
ResultE Acetone Wash
Final VUelqhl (mr),(mr.')s Bottle Wt wlth Wash (mu,)s
Tare Welqhl (mr),(mh')s Addltional Rlnso W (m-)g
WelghfGalfl (m)-Jm:'f mo -B-ottle-Tare Welqhl _*ffi,]--'q
Blank Adiurtmont (W.)m9 NetWa.h hlclghl (m*)g
Total Pailiculates (m^)mo Blank Concentrotion (c.)mq/q
Anrlytical Data
Placed ln Derlccator Run Number
Number Dato Tlme Run Start Ttrne
Filter 9.-22-2/l uL, a.)Leakaqe Evident?Il Nr"l
Acatono Wash Beaket trL *-zt -qll ra'Af Ertlmated Volume l?h rnL
Filter Acetone Date Time Humldltv Tomo Cal Audit
rt o mm/dd/w hh:mm %RH ec a
Measurement I (mr),(mr.)d. t-) l^ ,tr1 1t4n trlatl*ACI 'A I t<'72
Measurement 2 (mr),(mr.)h-t-, LO t az-4111,ihilqt ^12,4t
aQ..l?
Measuremont 3 (md,(mr.),ot-4t1A ^iit*ltt nx:tq qQ 't6
Mcasurement {(md,(mrJ
Rcaults Acetone Wash
Flnal Weishl (m,,),(mh')q Bottle Wtwith Waeh (mn )s
Tare Welshl (m*),(mr')s Additional Rinse W (m-)s
Welght Galn (m),(m,')mg Bottle Tare Welghl (mr)s
Blank Adiugtmenl (W')mq NetWash Welohl (m*)s
Total Particulates (mJ mg Blank Concentratior (c.)mg/g
Formulas Used
nrn ="r";n"oflasttwotiltermeasuremenls rn1 =trl;-1116 Wr=C.m* mn=mr+m.'-W.
' = averaoe of last two acEtone measurements ID,' = D'lrr' - lllrr' Illm = mbr + mrr -
A PEX sou?c. tEs*\,G rorrp .rEMT[ T..|rTrlit' tMtl1\TFtrl(\
APPENDIX E
EMISSIONS & TEST FORMULAE
Symbols and Units for Nomenclature used in Calculations
Meter Calibration Factor Y
Pitot Tube Coefficient cp
Actural Nozzle Diameter Dn,m
Initial Meter Volume Vm(i)ft3
Final Meter Volume V,o(o ft3
Total Meter Volume v,ft3
Total Sampling Time e mln
Average Meter Temperature tm(rvg;otr'
Average Stack Temperature ts(evg1 otr,
Barometric Pressure Pb in Hg
Stack Static Pressure Pstatic in II2O
Absolute Stack Pressure P,in Hg
Average Orifice Pressure Drop AHnve in H2O
Absolute Meter Pressure P,in Hg
Avg Square Root Pitot Pressure Lp"^u,in H2Olz
Avg Pitot Tube Diff. Pressure APore in H2O
Impingers 1-3 Water Volume Gain vn ml
Impinger 4 Silica Gel Weight Gain wn (tb
Total Water Volume Collected Vt.ml
Standard Water Vapor Volume Vrvlstd)scf
Standard Meter Volume Vm(std)dscf
Calculated Stack Moisture Bws(c:lc)o/"
Saturated Stack Moisture Brvslsvp;%
Reported Stack Moisture Content Br",%
AP to AH Isokinetic Factor K
Carbon Dioxide Percentage o/rCO o//o
Oxygen Percentage o/oOz oh
Carbon Monoxide Percentage oco o/o
Nitrogen Percentage ToNz oh
Dry Gas Molecular Weight Md lbflb-mol
Wet Stack Gas Molecular Weight Ms lb/lb-mole
Calculated Fuel Factor Fo
Fuel F-Factor Fd dscflmmBtu
Percent Excess Air o/rEA Y"
Average Stack Gas Velocity v"fUsec
Stack Cross-Sectional Area A.ft
Actual Stack Flow Rate Q"acfm
Dry Standard Stack Flow Rate Q.a dscfm
Percent of Isokinetic Rate I o//o
Mass of Particulate on Filter Illg mg
Mass of Particulate in Acetone mt mg
Mass due to Acetone Blank we mg
Total Mass of Particulates mn mg
Stach Particulate Concentration
cs g/dscf
cs grldscf
Particulate Emission Rate
E kg/hr
E lbs/hr
E Ibs/mmBtu
Orifice Meter Coefficient AHo in II2O
Nozzle Diameter Dn ln
Distance to Far Wall of Stack Lr,,tn
Distance to Near WaIl of Stack Lrr ID
Diameter of Stack D in
Distance Upstream B m
Diameters Upstream BD diameters
Distance Downstream A m
Diameters Downstream AD diameters
Avg Stack Wet F''low Rate Q.',acflmin
Carbon Dioxide Volume Vcoz ml
Orygen Volume voz ml
Carbon Monoxide Volume Vco ml
Molecular Weight Deviation AMa lbilb-mole
Weight Final wf grams
Weight Initial wl grams
Weight Total wt grams
Weight Net wn grams
Volume Final vr ml
Volume Initial vi ml
Volume Total vr ml
Volume Net vn ml
Water Vol Condensed Vwc(srd)scf
Water Vol Weight Vwsg(std)scf
Avg Orifice Pressure AHare in H2O
Estimated Orifice Flow Rate Q,acfm
Velociy Head Ap in E2O
Meter Inlet temp tmi of,.
Meter Outlet temp t.o oF
Blank Concentration c8 mglg
Blank Final Weight cr,grams
Blank Initial Weight C,,grams
Velocity Stack Local Vst ftlsec
Standard Barometric Pressure at SL = 760 Pstd Mm Hg
1)
Example Calculation
Dry Gas Volume at Standard Conditions
Q'o=3 6 00 ( 1 - B**)V'A'(T',a/T'('ug1)(P'/P't6)
Where Trra=2930K, Ps16:760mmHg, for metric units
Where Trta:528oR,Psa=29.92 in Hg, for English units
[40 CFR Pt. 60, App. A, Method 2 Equation 2-10]
Stack Velocity at Stack Conditions
vr:KoCo(Ap) I /2uue(Trr",g/(PrM.)) I /2
Wlrere Ko=34.97 for metric units
Where Kp=85.49 for English units
[40 CFR Pt. 60, App.A, Method 2 Equation 2-9]
Fraction of Moisture in Stack Gas
B ws:Vru(stdy'Vm(sto)*V w(std)
[40 CFR Pt. 60, App.A, Method 5 Equation 5-3]
Percent Isokinetic
04I=Vr1g6)* Tr* Prta* 1 00/60 * Ts16 * V, * O t An*Pr* ( I -B,us)
[40 CFR Pt. 60, App.A, Method 5 Equation 5-8]
Volume of Dry Gas Sarnpled at Standard Conditions
Vmtstot= [V,,YT,alT,] [(Pb+AL 1 3 . 6 )/P'td]
[40 CFR Pt. 60, App. A, Method 5 Equation 5-l ]
2)
3)
4)
s)
6)
7)
8)
e)
Molecular Weight of Dry Gas
Mo:0.44 (% C Oz)+0 .32(%O z)+0.2 8 (%Nz +%co)
[40 CFR Pt. 60, App.A, Method 3 Equation 3-1]
Volume of Water Vapor Collected at Standard Condition
V*:KWr"
[40 CFR Pt. 60, APp. A, Method 4 Equation 4-2]
Fuel Factor
Fo=(2 0.0- %O2-0 .s%CO)l (%CO2+%CO)
[40 CFR Pt. 60, App. A, Method 3B Equation 38-l ]
Molecular Weight of Wet Gas
Mr:Mo( 1-8,,r):1SB*s
[40 CFR Pt. 60, App.A, Method 2 Equation 2-5]
Stack Pressurc
P5:P6ur=Pstatic/ 1 3 .6
[40 CFR Pt. 60, App. A, Method 2 Equation 2-6]
Particulate Concentration
Cr:(MnA/mrstalX 0. 00 1 ):g/dscfl 45 4:lb lhr
[40 CFR Pt. 60, APp. A, Method 5 Equation 5-6]
10)
11)
t2)
l3)
14)
Emission Rate
E:C'Fa [2 0 .0 I 20 .0 -%Oza]
[40 CFR Pt. 60, App. A, Method l9 Equation 19-l]
% Excess Air
yoE A: t0 0 (% o z _ 0 . s%co) I (0 .2 6 4o/N z- (% o _ 0 . 5 %c o ) )
[40 CFR Pt. 60, App. A, Method 38 Equation 3B-3]
Actual Stack Gas Volume at Stack Condition
Qu=Vs*As*3600:Ft3lhr
15) Biturninous Coal Fuel F Factor for Various Fuels
Fa Factor:9780 dscfl I 06Btu
[40 CFR Pt. 60, App. A, Method I 9 Equation l9-l ]
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Field Flow Data
Method 1 Absence of Cyclonics Verlfication
Method 2 Flow Rate
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of absence of cyclonic flow. Negative numbers indicates clockwise
rotation of
Method 1 Absence of Cyclonics Verificafion
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rotation of
APPENDIX G
Calibration and Standards Data
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MAY 18,2024
PRE - TEST MEASUREMENT
**MEASURED WITH DIC]TAL CALIPERS**
Tube End View
Tube No.A B C Average
't'l 0.1930"0.1940"0. r 93s"0.i 935"
SEPTEMBER23,2024
POST . TEST MEASUREMENT
XXN4g4${JftED WITH DIGITAL CALIPERS * *
Tube End View
Tube No.A B C Average
t'l 0.1 93s', 0.1935"0.1 930"0.1 933"
TypE s ptToT TUBE TNSPECT|ON & CERT|FIGAT|ON
Pitot Tube & Probe Assembv (As installed - refer to image on page 2.)
NOTES:
CERTlFICATION
I certify that pitot tube number TP? DO1 meets all specifications,
criteria, and applicable design features as required under 40 CFR Part 60 Appendix A,
EPA Reference Method 2, Section 10.1 and 10.1.1.
The pitot tube certification factor of 0.84 is hereby assigned.
Assembly lnspected & Measured by:
Pitot lnspected & Measured by:
Certified by:
Date: 7-23- 7q
INTERMOUNATIN POWER SERVICE CORPORATION
850 W Brush Wellman Rd
Delta, UT 84524
TEM PERATURE SENSOR CALIBRATION
Temperature Element (TE) lD:4323
emperature Element Type:
Date:
Calibrated by:
Barometric Pressure:
K'Adl Conversion 460
Vicki Lyman and Kirk Stevens
?4.53 (in. Hg)
reEhvitionl
lce Water
Stack Gas
Boiling Water
Reference (oCl
0
50
95
TE value (oFl
31
119
204
%Diff (K'l
0.1
0.3
0.1
NOTE: %Diff must be < +\- 1..5% of Kelvin:100
(Ref"C +'K) - (TE "C +'K)( 1.50/o
(RefoC + oK)
TE Result:
9lL6l2O24
INTERMOUNATIN POWER SERVICE CORPORATION
850 W Brush Wellman Rd
Delta, UT 84624
TEM PERATURE SENSOR CALIBRATION
ernperature Element (TE) lD:4334
Temperature Element TYPe:
Date:
Calibrated by:
Barometric Pressure:24.53 (in. Hg)
!(Adjusted to Elevation)
Ko Adj conversion
Fixed Point Reference
lce Water
Stack Gas
Boiling Water
NOTE: %Diff must be < +\-
460
Reference (ocl
0
50
96
1.5o/o of Kelvin:
TE Value (oFl %Diff (K" )
31 0.1
L27 0.1
203 0.2
100
(Rel"C + "K) - (TE "C +'K)
(Ref'C + oK)11.5o/o
TE Result:l PASS
e/1612024
n and Kirk Stevens
INTERMOUNATIN POWER SERVICE CORPORATION
850 W Brush Wellman Rd
Delta, UT 84524
TEM PERATURE SENSOR CALI BRATION
Temperature Element (TE) lD:
Tem perature Elernent Type:
Date:
Calibrated by:
Barometric Pressure:
Ko Adj Conversion 460
Stack
Thermocouple, "K" Type
9lt6l2O24
Vicki Lyman and Kirk Stevens
24.53 (in. He)
(Adjusted to Elevation)
I Reference (oc) TE value (oFl %Diff (K" I
0 31 0.1
50 120 0.2
96 204 0.1
lce Water
Stack Gas
Boiling Water
NOTE: %Diff must be < +\- !.5o/o of Kelvin:(Ref"C + '/() - (TE "C + "/()100 1L.50/o(RefoC + oK)
TE Result:I PASS
INTERMOUNATIN POWER SERVICE CORPORATION
850 W Brush Wellman Rd
Delta, uT 84624
TE M PE RATU RE SENS9 R CALI BRATIO-N
Temperature Element (TE) lD:
Temperature Element Type:
Date:
Exit
Thermocouple, "K" TyPe
e/t612024
ibrated by:Vicki Lyman and Kirk Stevens
Barometric Pressure:(in. Hg)
Ko Adj Conversion
Fixed Point Reference
lce Water
Stack Gas
Boiling Water
NOTE: %Diff must be <
460
Reference (oC)
0
50
96
+\- 1.5% of Kelvin:
tE Value (oF)
31
120
203
%Diff (K" I
0.1
o.2
o.2
(Ref"C + 'K) - (TE "C + "K)1L.50/o100(Ref'C + "K)
TE Result:l PAss
24.53
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Product lnformotion
Product Number: L827 -LLO
Product Nome: Grode 934-AH circles, 110 mm, 100/pk
Lot Number/Seriol Number: 9627729
Conformonce & Quolity systems stotement
This is to certify thot this product conforms to GE Heolthcore Life Sciences
specificotions.
AII products ore monufoctured vio o Quolity System certified to BS EN !509001:2008 ond
tested in occordonce with documented quolity procedures ond opproved os o result of
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Source Information
Division of Air Quality
Compliance Demonstration
Source Information
Company Name IPP - Unit 1
Company Contact:Mike Utley
Contact Phone No.[phone]
Source Designation:Unit 1
Test & Review Dates
Test Date: 8/27/2024
Review Date: 10/25/2024 Tabs Are Shown
Observer:
Reviewer:Paul Morris
Particulate Emission Limits
lbs/MMBtu lbs/hr gr/dscf
0.018
Emission Rates - "Front Half"
lbs/MMBtu lbs/hr gr/dscf
0.0027 23.0706 0.0014
Test Information
Stack_I.D._inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn
336.00 615.75 1.0010 1.6 0.84 24.95 -1 0.193
Contractor Information
Contracting Company:
Contact:
Phone No.:
Project No.:
9780
Circular
10100
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
F factor usedF factors for Coal, Oil, and Gas
Anthrocite 2
Lignite
Natural
Propane
Butane
COAL
OIL
GAS
Bituminous 2
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
O2
CO2
lbs/MMBtu
Page 1
Summary
Division of Air Quality
Reference Methods 5 - TSP
Compliance Demonstration of
IPP - Unit 1
Testing Results Lab Data - grams collected
Test Date 8/27/2024 8/27/2024 8/27/2024 8/27/2024 Lab Data Probe Filter Back
Circular Run 1 Run 2 Run 3 Run 4 Run 1 0.0067 0
As ft^2 615.75 615.75 615.75 Run 2 0.0067 0
Pbar 24.95 24.95 24.95 Run 3 0.0074 0
Pq (static)-1.00 -1.00 -1.00 Run 4
Ps 24.88 24.88 24.88
Avg. Ts F 117.50 118.92 119.33 Front Half Emissions Summary
CO2 - FCO2 13.60 13.60 13.60 Run 1 Run 2 Run 3 Run 4 Avg.
O2 5.40 5.30 5.40 gr./dscf 0.0014 0.0014 0.0015 0.0014
N2+C 81.00 81.10 81.00 lbs/hr 22.4029 22.2262 24.5826 23.0706
Md 30.39 30.39 30.39 lbs/MMBtu 2.675E-03 2.625E-03 2.941E-03 0.0027
Ms 28.79 28.72 28.70
Y 1.00 1.00 1.00
Cp 0.84 0.84 0.84 Total Emissions Summary w/back half condensable
Vm cf 90.09 92.11 92.00 Run 1 Run 2 Run 3 Run 4 Avg.
Vlc 245.56 266.08 268.86 gr./dscf 0.0014 0.0014 0.0015 0.0014
AVG. Tm F 83.08 88.50 92.25 lbs/hr 22.4029 22.2262 24.5826 23.0706
Vm std 73.42 74.33 73.74 lbs/MMBtu 2.675E-03 2.625E-03 2.941E-03 0.0027
Vw std 11.56 12.52 12.66
Bws 0.14 0.14 0.15
S Bws 0.13 0.13 0.14
Avg. Sqrt Dlp 1.18 1.19 1.18
Vs 75.91 76.89 76.58 F factor used
scfm wet 2131835.00 2154102.15 2143903.85 9860
acfm 2804422.65 2840666.42 2829252.52
Qsd dscfh 111339996.68 111827441.61 111095890.43
# Sample
Points 12.00 12.00 12.00
Dn 0.193 0.193 0.193
An 2.03E-04 2.03E-04 2.03E-04
Start Time 0:00 0:00 0:00
End Time 0:00 0:00 0:00Total Test
time 120.00 120.00 120.00
Time @ point 10.00 10.00 10.00
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
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Points
Run 1 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
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Sample Points
Run 2 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
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Sample Points
Run 3 PxP Isokinetic
O2
CO2
lbs/MMBtu
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
Sample Points
Run 4 PxP Isokinetic
Page 1
Run 1
IPP - Unit 1 Flow & Moisture Test Date 8/27/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
615.75 24.95 -1.00 24.88 118 13.60 5.40 81.00 30.39 28.79
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1295
1.0010 0.84 90.094 245.56 83.08 73.423 11.559 0.1360 0.1295 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
1.177 75.91 2,131,835 2,804,423 1.11E+08 12 0.193 120 10.00 1.564167
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 261.571 1.30 1.51 119 74 74 Wt. (Final) Wt. (Initial) lc
2 268.954 1.40 1.55 118 76 76 890.25 716.96 173.3
3 276.378 1.55 1.70 118 78 78 728.82 685.14 43.7
4 284.115 1.30 1.48 119 80 80 633.18 626.24 6.9
5 291.372 1.40 1.60 119 82 82 828.63 806.98 21.7
6 298.931 1.50 1.70 119 84 84 0.0
7 306.811 1.20 1.35 119 85 85
8 313.828 1.35 1.52 119 86 86 Isokinetics 100.7
9 321.265 1.45 1.62 114 87 87 Test Date 8/27/2024
10 328.970 1.25 1.40 115 88 88 Start Time enter
11 336.188 1.45 1.64 115 88 88 End Time
12 343.922 1.50 1.70 116 89 89 Run 1
13 351.665
14
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Page 1
Run 2
IPP - Unit 1 Flow & Moisture Test Date 8/27/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
615.75 24.95 -1.00 24.88 119 13.60 5.30 81.10 30.39 28.72
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1348
1.0010 0.84 92.108 266.08 89 74.330 12.524 0.1442 0.1348 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
1.189 76.89 2,154,102 2,840,666 1.12E+08 12 0.193 120 10.00 1.60
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 352.501 1.30 1.45 118.0 84.0 84.0 Wt. (Final) Wt. (Initial) lc
2 360.151 1.45 1.60 119.0 84.0 84.0 905.16 705.14 200.0
3 367.754 1.50 1.70 118.0 85.0 85.0 717.12 678.94 38.2
4 375.598 1.25 1.40 119.0 87.0 87.0 601.34 595.36 6.0
5 382.802 1.40 1.55 119.0 87.0 87.0 828.61 806.71 21.9
6 390.248 1.50 1.70 119.0 89.0 89.0 0.0
7 398.096 1.30 1.50 119.0 90.0 90.0
8 405.554 1.40 1.59 119.0 90.0 90.0 Isokinetics 101.9
9 413.183 1.50 1.70 120.0 91.0 91.0 Test Date 8/27/2024
10 421.051 1.30 1.47 119.0 91.0 91.0 Start Time
11 428.474 1.50 1.73 119.0 92.0 92.0 End Time
12 436.432 1.60 1.80 119.0 92.0 92.0 Run 2
13 444.609
14
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Page 1
Run 3
IPP - Unit 1 Flow & Moisture Test Date 8/27/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
615.75 24.95 -1.00 24.88 119 13.60 5.40 81.00 30.39 28.70
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1363
1.0010 0.84 91.995 268.86 92 73.741 12.655 0.1465 0.1363 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
1.184 76.58 2,143,904 2,829,253 1.11E+08 12 0.193 120 10.00 1.63
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 446.601 1.25 1.36 120.0 89.0 89.0 Wt. (Final) Wt. (Initial) lc
2 452.868 1.50 1.85 120.0 89.0 89.0 920.9 719.5 201.4
3 461.002 1.60 1.95 120.0 90.0 90.0 729.3 687.9 41.3
4 469.448 1.25 1.50 119.0 91.0 91.0 633.2 627.9 5.3
5 477.005 1.40 1.64 119.0 92.0 92.0 830.8 810.0 20.8
6 484.758 1.50 1.73 119.0 93.0 93.0 0.0
7 492.762 1.25 1.42 120.0 93.0 93.0
8 500.105 1.45 1.63 119.0 93.0 93.0 Isokinetics 101.8
9 507.810 1.50 1.70 119.0 94.0 94.0 Test Date 8/27/2024
10 515.755 1.25 1.40 119.0 94.0 94.0 Start Time
11 523.025 1.40 1.60 119.0 94.0 94.0 End Time
12 530.633 1.50 1.76 119.0 95.0 95.0 Run 3
13 538.596
14
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Page 1
Source Information
Division of Air Quality
Compliance Demonstration
Source Information
Company Name IPP - Unit 2
Company Contact:Mike Utley
Contact Phone No.[phone]
Source Designation:Unit 2
Test & Review Dates
Test Date: 8/28/2024
Review Date: 10/28/2024 Tabs Are Shown
Observer:
Reviewer:Paul Morris
Particulate Emission Limits
lbs/MMBtu lbs/hr gr/dscf
0.018
Emission Rates - "Front Half"
lbs/MMBtu lbs/hr gr/dscf
0.0026 23.2297 0.0014
Test Information
Stack_I.D._inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn
336.00 615.75 1.0006 1.85 0.84 24.8 -1 0.193
Contractor Information
Contracting Company:
Contact:
Phone No.:
Project No.:
9780
Circular
10100
9780
9860
9190
8710
8710
8710
10540
10640
11950
320
10610
10200
10390
1970
1800
1910
1420
1040
1190
1250
F factor usedF factors for Coal, Oil, and Gas
Anthrocite 2
Lignite
Natural
Propane
Butane
COAL
OIL
GAS
Bituminous 2
Fd Fw Fc
scf/MMBtu scf/MMBtu scf/MMBtu
O2
CO2
lbs/MMBtu
Page 1
Summary
Division of Air Quality
Reference Methods 5 - TSP
Compliance Demonstration of
IPP - Unit 2
Testing Results Lab Data - grams collected
Test Date 8/28/2024 8/28/2024 8/28/2024 8/28/2024 Lab Data Probe Filter Back
Circular Run 1 Run 2 Run 3 Run 4 Run 1 0.0081 0
As ft^2 615.75 615.75 615.75 Run 2 0.0063 0
Pbar 24.80 24.80 24.80 Run 3 0.0063 0
Pq (static)-1.00 -1.00 -1.00 Run 4
Ps 24.73 24.73 24.73
Avg. Ts F 116.75 108.92 118.67 Front Half Emissions Summary
CO2 - FCO2 13.60 13.50 13.50 Run 1 Run 2 Run 3 Run 4 Avg.
O2 5.40 5.40 5.40 gr./dscf 0.0017 0.0013 0.0013 0.0014
N2+C 81.00 81.10 81.10 lbs/hr 27.0865 21.7514 20.8513 23.2297
Md 30.39 30.38 30.38 lbs/MMBtu 3.147E-03 2.417E-03 2.367E-03 0.0026
Ms 28.81 29.11 28.71
Y 1.00 1.00 1.00
Cp 0.84 0.84 0.84 Total Emissions Summary w/back half condensable
Vm cf 93.14 95.19 97.66 Run 1 Run 2 Run 3 Run 4 Avg.
Vlc 244.48 461.67 274.29 gr./dscf 0.0017 0.0013 0.0013 0.0014
AVG. Tm F 87.58 92.58 95.42 lbs/hr 27.0865 21.7514 20.8513 23.2297
Vm std 74.82 75.79 77.38 lbs/MMBtu 3.147E-03 2.417E-03 2.367E-03 0.0026
Vw std 11.51 21.73 12.91
Bws 0.13 0.22 0.14
S Bws 0.13 0.10 0.13
Avg. Sqrt Dlp 1.20 1.22 1.24
Vs 77.56 77.73 80.29 F factor used
scfm wet 2167845.64 2202624.04 2236900.51 9780
acfm 2865368.49 2871795.79 2966467.94
Qsd dscfh 113471282.79 118668393.72 116142370.66
# Sample
Points 12.00 12.00 12.00
Dn 0.193 0.193 0.193
An 2.03E-04 2.03E-04 2.03E-04
Start Time 0:00 0:00 0:00
End Time 0:00 0:00 0:00Total Test
time 120.00 120.00 120.00
Time @ point 10.00 10.00 10.00
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
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Points
Run 1 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
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Sample Points
Run 2 PxP Isokinetic
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
% I
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Sample Points
Run 3 PxP Isokinetic
O2
CO2
lbs/MMBtu
80.00
90.00
100.00
110.00
120.00
1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 31 33 35 37 39 41 43 45 47
Sample Points
Run 4 PxP Isokinetic
Page 1
Run 1
IPP - Unit 2 Flow & Moisture Test Date 8/28/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
615.75 24.80 -1.00 24.73 117 13.60 5.40 81.00 30.39 28.81
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1276
1.0006 0.84 93.141 244.48 87.58 74.822 11.508 0.1333 0.1276 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
1.200 77.56 2,167,846 2,865,368 1.13E+08 12 0.193 120 10.00 1.655000
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 539.012 1.35 1.50 116 80 80 Wt. (Final) Wt. (Initial) lc
2 546.475 1.55 1.77 116 81 81 862.52 680.08 182.4
3 554.354 1.65 1.93 116 83 83 738.90 702.24 36.7
4 562.675 1.25 1.44 117 85 85 607.26 601.13 6.1
5 570.035 1.45 1.62 117 87 87 824.50 805.25 19.3
6 577.683 1.75 1.97 117 89 89 0.0
7 586.055 1.20 1.38 117 90 90
8 593.242 1.35 1.54 117 90 90 Isokinetics 100.6
9 600.672 1.50 1.73 117 91 91 Test Date 8/28/2024
10 608.668 1.20 1.38 117 91 91 Start Time enter
11 615.842 1.50 1.74 117 92 92 End Time
12 623.808 1.60 1.86 117 92 92 Run 1
13 632.153
14
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Page 1
Run 2
IPP - Unit 2 Flow & Moisture Test Date 8/28/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
615.75 24.80 -1.00 24.73 109 13.50 5.40 81.10 30.38 29.11
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1021
1.0006 0.84 95.189 461.67 93 75.787 21.731 0.2228 0.1021 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
1.218 77.73 2,202,624 2,871,796 1.19E+08 12 0.193 120 10.00 1.71
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 632.675 1.30 1.45 118.0 89.0 89.0 Wt. (Final) Wt. (Initial) lc
2 640.196 1.50 1.74 118.0 89.0 89.0 914.30 721.08 193.2
3 648.135 1.60 1.86 118.0 90.0 90.0 729.48 688.46 41.0
4 656.381 1.30 1.50 117.0 90.0 90.0 634.41 628.85 5.6
5 663.924 1.50 1.70 118.0 92.0 92.0 832.44 610.57 221.9
6 671.738 1.55 1.78 11.0 93.0 93.0 0.0
7 679.781 1.30 1.50 118.0 93.0 93.0
8 687.303 1.45 1.65 117.0 94.0 94.0 Isokinetics 111.9
9 695.042 1.64 1.89 118.0 95.0 95.0 Test Date 8/28/2024
10 703.335 1.35 1.57 118.0 95.0 95.0 Start Time
11 710.958 1.64 1.90 118.0 95.0 95.0 End Time
12 719.296 1.70 1.99 118.0 96.0 96.0 Run 2
13 727.864
14
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Run 3
IPP - Unit 2 Flow & Moisture Test Date 8/28/2024
As ft^2 Pbar Pq (static) Ps Avg. Ts F CO2 - FCO2 O2 N2+C Md Ms
615.75 24.80 -1.00 24.73 119 13.50 5.40 81.10 30.38 28.71
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1346
1.0006 0.84 97.656 274.29 95 77.376 12.911 0.1430 0.1346 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time (minutes)
Time @ point
(minutes)Avg. Dlh
1.238 80.29 2,236,901 2,966,468 1.16E+08 12 0.193 120 10.00 1.80
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out) Imp. Liquid Collected
1 728.202 1.50 1.75 118.0 93.0 93.0 Wt. (Final) Wt. (Initial) lc
2 736.360 1.70 1.95 119.0 93.0 93.0 903.1 703.8 199.3
3 744.768 1.75 2.06 119.0 94.0 94.0 730.3 681.6 48.7
4 753.420 1.30 1.54 118.0 94.0 94.0 603.1 597.3 5.8
5 761.125 1.50 1.75 119.0 95.0 95.0 824.7 804.2 20.4
6 769.102 1.80 2.10 118.0 96.0 96.0 0.0
7 777.729 1.40 1.65 118.0 96.0 96.0
8 785.528 1.50 1.79 119.0 96.0 96.0 Isokinetics 102.0
9 793.558 1.60 1.90 119.0 97.0 97.0 Test Date 8/28/2024
10 801.926 1.30 1.54 119.0 97.0 97.0 Start Time
11 809.515 1.55 1.82 119.0 97.0 97.0 End Time
12 817.668 1.55 1.80 119.0 97.0 97.0 Run 3
13 825.858
14
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