DAQ-2024-004317

1

DAQC-1326-23
Site ID 10327 (B4)

MEMORANDUM

TO: STACK TEST FILE – INTERMOUNTAIN POWER SERVICE CORPORATION

THROUGH: Harold Burge, Major Source Compliance Section Manager

FROM: Robert Sirrine, Environmental Scientist

DATE: December 8, 2023

SUBJECT: Source: Boiler Units 1 and 2
Contact: Mike Utley, 435-864-6489
Location: 850 Brush Wellman Road, Delta, Millard County, UT
Test Contractor: In-house IPSC Personnel
FRS ID #: UT0000004902700010
Permit #: Title V operating permit #2700010006 dated November 21, 2023
Action Code: 3A
Subject: Review of Stack Test Report dated November 2, 2023

On November 7, 2023, Utah Division of Air Quality (DAQ) received a stack test report for the IPSC
Units 1 and 2. Testing was performed on September 13-14, 2023, to demonstrate compliance with the
emission limits found in 40 CFR 63 Subpart UUUUU and Title V operating permit Condition II.B.2.b.
The DAQ-calculated test results are:

Source Test Date RM/Pollutant DAQ Result Test Result Limit

Unit #1 9/13/2023 M5B/PM10 0.0036 lb/MMBtu 0.0036 lb/MMBtu 0.0184 lb/MMBtu

Unit #2 9/14/2023 M5B/PM10 0.0024 lb/MMBtu 0.0024 lb/MMBtu 0.0184 lb/MMBtu

DEVIATIONS: No deviations were noted.

CONCLUSION: The stack test report appears to be acceptable.

RECOMMENDATION: The IPSC Boiler Units 1 and 2 PM10 emissions appear to have been in
compliance with the permit limits at the time of testing.

HPV: No

ATTACHMENT: Test report dated November 2, 2023
DAQ generated excel spreadsheets

lntermou ntain Power Service Corporation
November 2,2023
Mr. Bryce Bird, Director
Utah Division of Air Quality
P.O. Box L4482O
Salt Lake City, Utah 847L4-4820
Attention: Compliance Section
Reference: Operating Permit #2700010005
Dear Director Bird:
UTAH DEPAHTMENT OF
ETWHOT.IMENTAL OUAIITY
NOv - 1 ?i)?i
DIVISION OF AIR OUALITY
Annual Compliance Particulate Testing of lntermountain Generating Station
lntermountain Power Service Corporation (IPSC) is submitting the results of the 2023 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 September 13 and 14, 2023 by IPSC personnel.
I certify that:
1. 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.
2. During testing, the source combusted fuels used raw materials and maintained process
conditions representative of normal operations.
3. 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,
fut q"rl-"'
Jon A. Finlinson
President and Chief Operations Officer
,rPf\
VL/HBl:he
Attachment
Gregory S. Huynh Mike Utley
Tamer Ellyahky
850 West Brush Wellman Road, Delta, Utah,84624 lTelephone: [phone] / FAX: [phone] / Fed, l.D. #87-0388573
UrAH DEPAr[MEI\rr OF I
ENVIRONMENTAL Ot,A,frY
NoI/ - 7 20n
DIVISION OF AIR QUAUW
TEST REPORT
Permit Requlred Fardotlate lt{atter Enlssions Tests
InEtmountdn Poluer Senile Corporadon
Boiler Unlts 1SGA and 2SGA
September L3 &14,2023
Testing and report by IPSC Environmental Personnel
ll
TEST REPORT
' Permit Required Farticulate Matter Emissions Tests
lntermountdn Power Service Corporation
Boiler Units lSGA and 2SGA
Executive Summary
The Intermountain Power Service Corporation [PSC) has performed stack testing to determine
particulate matter emissions (PMro) from the Intermountain Power Project (IPP) boiler Units
ISGA and 2SGA. The testing occurred on September 13 and 14,2023, and was required under
IPSC's Title V Operating Permit, #2700010005, Condition II.8.2.b.1(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 PMro per
million British Thermal Unit heat input (lb/mmbtu). The actual average PMro emissions during
testing were as follows:
UNIT Emission Rate
ISGA 0.00361b/mmbtu
2SGA 0.0024lb/mmbtu
TEST REPORT
Permit Required Paniculate Matter Emissions Tests
lntermountain Power Service Corporation
Boiler Units lSGA and 2SGA
Content Outline
1.0 Introduction
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
TEST REPORT
Permit Required Particulate Matter Emissions Tests
lntermountain Power Service Corporation
Boiler Units lSGA and 2SGA
1.0 Introduction
l.l Overview
IPSC operates under the authority of a Title V Operating Permit, #2700010005, issued
September 12,2018. PMro 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
I 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
l1l Hope St.
Los Angeles, CA 90012
TEST REPORT
Permit Required Particulate Matter Emissions Tests
lntermountain Power Service Corporation
Boiler Units 1SGA and 2SGA
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
435-864-4414
Jon A. Finlinson
Mike Utley
Vicki Lyman
Kirk Stevens
Vicki Lyman
Kirk Stevens
Vicki Lyman
Trevor Johnson
Rick Moody
Kirk Stevens
Utah Department of Environmental Quality
Utah Division of Air Quality
P.O. Box 144820
Salt Lake city, uT 84114-4820
TEST REPORT
Permit Required Particulate Matter Emissions Tests
lntermountain Power Service Corporation
Boiler Units 1SGA and 2SGA
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 al 2,97 5 psi and I ,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.
1.4 Test Description
The following sources were tested as per the operating permit:
- Intermountain Unit l SGA Boiler Stack
- Intermountain Unit 2SGA Boiler Stack
The testing was conducted on September l3 and 14, 2023. A pretest protocol
was submitted to the UDAQ on July 18,2023. 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.
TEST REPORT
Permit Required Particulate Matter Emissions Tests
lntermountain Power Service Corporation
Boiler Units lSGA and 2SGA
The following methods were used to evaluate compliance:
Method 1 - "Sample and Velocity Traverses for Stationary Sources"
Method 2 - "Determination of Stack Gas Velocity and Volumetric Flow Rate
(type "S" Pitot tube)"
Method 38 - "Gas Analysis for Carbon Dioxide, Oxygen, Excess Air and Dry
Molecular Weight"
Method 4 - "Determination of Moisture Content in Stack Gases"
Method 5E} - "Determination of Nonsulfuric Acid Particulate Matter
Emissions from Stationary Sources"
2.0 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 lSGA Boiler Stack
Test
Run No.
DSCF
Collected
Emissions Rates
lb/hr lb/mmBtu
I
2
3
75.376
77.116
75.293
38.3
18.4
34.4
0.0046
0.0022
0.0041
Averase:75.928 30.4 0.0036
TEST REPORT
Permit Required Particulate Matter Emissions Tests
lntermountain Power Service Corporation
Boiler Units lSGA and 2SGA
Unit 2 SGA Boiler Stack
3.0 Test Conditions
3.1 Source Operations
Unit l 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 bum bituminous, sub-
bituminous, and refined coal for steam-electric generation. Fuel analyses
representing the fuel bumed during testing are attached in Appendix C.
Test
RunNo.
DSCF
Collected
Emissions Rates
lb/hr lb/mmBtu
1
2
J
76.596
75.647
75.279
21.8
17.6
20.0
0.0026
0.0022
0.0024
Average:75.841 19.8 0.0024
TEST REPORT
Permit Required Particulate Matter
lntermountain Power Service
Boiler Units lSGA and
Emissions Tests
Corporation
2SGA
4.0 Sampling and Analysis Procedures
4.1 Emissions Testins
A.EPA Method l: Sample and velocity traverses for stationary sources.
Figures 1a and lb are diagrams of Unit lSGA 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 (12) separate
locations in the stack, six (6) per traverse. The locations ofthese 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 Dz with field and laboratory dataforms.
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.
TEST REPORT
Permit Required Paniculate Matter
lntermountain Power Seruice
Boiler Units 1SGA and
Emissions Tests
Corporation
2SGA
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 to calculate the Method 58 test
results. The data forms and the computer generated results are included by
Unit in Appendices Dr and Dz. The computer program used is:
IsoCALC Workbook (MS EXCEL) for IsoKinetic Sampling
(By Apex Instruments Version l.l4b (1998)
Figure 1 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 are99.999 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 at320o F + 25o F during
sampling.
A thermocouple was installed on the outlet of the filter to assure an outlet
temperature above the dew point ofthe stack gas. These readings are
recorded by Unit on the field sheets in Appendices Dr and Dz. 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:
TEST REPORT
Permit Required Particulate Matter
lntermountain Power Seruice
Boiler Units 1SGA and
Emissions Tests
Corporation
2SGA
Impinger
Number
I
2
3
4
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 1 criteria
as shown in Appendix F. The stacks are testable if the average flow rate
varies less than2} degrees from parallel to the vertical stack. The average
angles were found to satisff 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 zusure 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 Dz.
Quality Control / Quality Assurance
Compliance Testing
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
10
TEST REPORT
Permit Required Particulate Matter Emissions Tests
lntermountain Power Seruice Corporation
Boiler Units lSGA and 2SGA
5.3 Resulations
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 5B 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
APPENDIXA
Tables & Figures
Intermountain Power Service Corp.
850 W. Brushwellman Road
Delta, Utah 84624
Traverse Point Calculations
Plant: Intermountain Generating Station
Date: September 13rh through 74th,2023
Sampling Location: Unit #SGA-I 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 Inside Diameter: 336" = 615.75 sq ft
Point Calculation Basis:40 CFR Pt. 60, App.A, Method l, Table 1-2.
Traverse
Points
| &,7
2&8
3 &,9
4 &.10
5&11
68112
Percent of
Stack I.D.
04.4
14.6
29.6
70.4
85.4
95.6
Stack I.D.
inches
Product of
Columns 2&3
r4.784
49.056
99.456
236.544
286.944
321.216
Traverse point location
frorB gutti.d.qport. (inches)
23J84=23 314"
58.056 = 58"
108.456 = 108 2"
Traverse point
location fiom
outside port
23.784"
s8.0s6"
108.455"
245.544"
295.944"
330.216
Port
Length
336
336
336
336
336
336
9"
9"
9rt
9"
9"
9tt
Since each flue has 4 ports 90 degrees around the stack, sampling occurs from each port instead
of going all the way through the stack for the far points. Traverses were made at the following
points:
Traverse PointNumber
Port4 Port B Port C Port D147r0
5 I 11
691?
2
3
Table 2
METHOD 5. DETERMINATION OF PARTICULATE EMISSIONS - RESULTS
Plant Name NTERMOUNTATN GENERATING STATION Date 9t13t2023
Samolinq Location JNlr 1 STACK Proiect #PM Performance
f,perator y'icki Lvman Stack Tvoe 3ircular
Historical Data
lun Number ?Averaqe
Run Start Time 8:23 '10:58 13'.24 hh:mm
Run Stop Time 10:29 13:03 15:30 hh:mm
l/letar Calibratlon Factor ff)0.998 0.998 0.998
Pitot Tube Coefficient (c")0.840 0.840 0.840
[ctual Nozzle Diameter (D*)0.'193 0.1 93 0.193 tn
Stack Test Data
nitial Meter Volume u-),970.380 65.206 160.880 ft"
:inal Meter Volume (v,)r 1062.525 160.523 254.282 fl'
lotal Meter Volume (v.)92.145 95.317 93.402 93.621 flo
fotal Samolino Time (o)120.0 120.0 120.0 120.4 min
fuerane Meter Temoerature (t-)*80.0 86.0 88.0 84.7 "F
lverase Stack Temperature (t.)"*121.O 121.O 12',t.0 121.0 "F
3aromotrlc Pressure (Pu)24.97 24,97 24.97 24.97 in Hg
Stack Statlc Pressure (P"*i")-1.00 -1.00 1.00 -1.OO in H"O
Absolute Stack Pressure (P")24.90 24.90 24.90 24.90 in Hg
Averaoe Orifice Pressure Droo (dH),,"1.5s 1.66 1.67 1.55 in HrO
Absolute Meter Pressure (P.)25.09 25.09 25.09 25.09 in Hq
Avg Square Root Pitot Pressure (Apto),*1.21 1.21 1.21 1.21 (in HzO)
Moisture Content Data
lmpinqers l-3 Water Volume Gain u")Zojz.2 253.7 :z(j6.2 260.7 ml
lmoinoer 4 Silica Gel Weioht Gain (w,)20.3 20.4 19.8 20.2 s
Totat Water Volume Collected (V*)282.5 274.1 286.0 280.9 ml
Standard Water Vaoor Volume (V*)o,13.297 12.902 13,462 13.220 scf
Standard Meter Volume (V.).ra 75.376 77.116 75.293 75.928 dscf
Calculated Stack Molsture (B*.15.0 14.3 15.2 14.8 o/o
Saturated Stack Molsture (B*rr.,n)14.2 14.2 14.2 14.2 lo
Reported Stack Molsture Content G-.)14.2 14.2 14.2 14.2 o/o
Gas Analvsis Data
Carbon Dioxide Percentaoe (o/oCO:)13.3 13.5 13.5 13.4 c/a
Oxygen Percentage (7oOz)5.7 5.5 5.5 5,6 c,/a
Carbon Monoxide Percentaoe (%co)0.0 0.0 0.0 0,0 Yo
Nitrooen Percantaoe (%N,)81.0 81.0 61.U 81,O o/o
Drv Gas Molecular Weioht (Ma)30.36 30.38 30.38 30.37 lb/lb-mole
tlVet Stack Gas Molecular Weiqht (M.)28.51 28.61 28.50 28.54 lb4b-mole
Salculated Fuel Factor (F")1.143 1.141 1.141 1.142
Fuel F-Factor (Fr)9780 s780 9780 9780 dscf/mmBtu
Percent Excess Air (%EA)36.3 34.6 34.6 JC,Z Yo
Volumetric Flow Rate Data
Averaoe Stack Gas Velocitv (v.)78.61 74.47 78.62 ta_5t fUsec
Stack Cross-Sectional Araa (&)615.75 615.75 615.75 615.75 lt'
{ctual Stack Flow Rate (o,)2904246 2899074 2904616 2902645 actm
)ry Standard Stack Flow Rate (Q.a)1867016 1879039 1862860 1869638 dscfrn
Percent of lsokinetic Rate fl)102.4 103.7 102.1 102.6 %
Emlsslon Rate Data
Mass of Particulate on Filter (mr)-0.6000 0.1000 -0.3000 -0.3 mg
Mass of Particulate in Acetone (m")12.3000 5.6000 10.8000 9.6 mg
Mass due to Acetone Blank (w")0.0000 0.0000 0.0000 0.0000 mg
Total Mass of Particulates (mn)11.7 C./10.5 9.3 mg
stack Partlculate Concentratlon (c.)0.0002 0.0001 0.0001 0.o001 q/dscf
(cJ 0.0031 0.0015 0.0015 0.0020 gr/dscI
Particulate Emission Rate (E)22.40 11.27 1 1.18 14.95 kq/hr
{E)38.3 18.4 34.4 30.4 lbs/hr
(E)u.uu4t,0.0022 0.0041 0.0036 lbslmmBlu
Table 3
METHOD 5 - DETERMINATION OF P
Plant Name NTERMOUNTAIN GENERATING STATION Dete 9114t2023
Samollnq Location JNIT 2 STACK Proiect #PM Performence
0perator /icki Lyman Stack Tvoe lircular
Historieal Data
Run Number 1 2 3 Average
Run Start Time 7:4O 10:15 '12:51 Runs 1,2,
and 3
hh:mm
Run Stop Tlme 9:45 12:20 14:56 hh:mm
Ueter Calibration Factor tY)0.988 0.998 0.998
Pitot Tube Coefficient {c")0.840 0.840 0.840
{ctual Nozzle Diameter (D-)0.193 0.193 0,193 tn
Stack T.st Data
nitial Meter Volume (V')i 2s6.1 1 3 350.307 445.231 ft"
iinal Meter Volume (V.)t 349.739 443.463 538.454 ft"
lotal Meter Volume (v-)93.026 93.156 93.223 93.335 ft"
Iotal Sampllnq Tlme {o) 120.0 120.O 120.0 120.000 mtn
lveraoe Meter Temoerature (t.)"*80.0 84.0 87.0 83.667 "F
Average Stack Temperature (L).,o 117.0 1'18.0 120.0 118.333 "F
Barometric Pressure (Pb)24.97 24.97 24.97 24.970 in Ho
Stack Static Pressure (Por,")1.00 1.00 1.00 -1.000 in HrO
Absolute Stack Pressure (P.)24.90 24.90 24.90 24.900 in Ho
Average Orifice Pressure Drop (AH).,"r.69 1.67 1.64 1.667 in H"O
Absolute Meter Pressure (P")25.09 25.09 25.09 25.090 in Hq
Avq Square Root Pltot Prossure (Ap'o)o,o 1.22 1.21 1.24 1.210 (in H2O)
Moisture Contant Data
lmplngers 1-3 Water Volume Gain v")232.7 240.7 244.1 239.367 ml
lmpinEer 4 Sllica Gel Weiqht Gain w")21.1 224.2 19.6 88.300 o
Total Water Volume Collected (vh)253.8 465.3 264.3 327.800 ml
Standard Water Vapor Volume (V*).,a 11.946 21.902 12.441 15.430 scf
Standard Mcter Volume (V-)""76.596 75.647 75.279 75.U1 dscf
Calculated Stack Molsture (B*a.r"r)13.5 22.5 14.2 16.733 0A
Saturated Stack Molsture (B-.r*,)12.7 13.1 13.8 13.200 o/o
Reported St.ck Moisture Content (B*,)12.7 13.1 13.8 13.200 o/o
Gas Analysis Data
Carbon Dioxide PercentaEe (YoQOcl 13.1 13.5 13.5 13.56/c/o
Sxygen Percentage (ohOz)5.8 5.5 5.4 5.567 oA
3arbon Monoxide Percsntase {%co)0.0 0.0 0.0 0.000 oA
Nltrogen Percentage (%Nz)81.1 81.0 81.1 81.067 o/o
Drv Gas Molecular Weloht (M")30.33 30,38 30.38 30.363 lb/lb-rnole
,Yet Stack Gas Molecular Weioht (M.)28.67 27.59 28.62 28.293 lb/lb-mole
:alculated Fuel Factor (F")1.153 1.141 1.148 1.147
ruel F-Factor (F")s780 9780 9780 9780.000 dscf/mmBlu
Percent Excess Air (%EA)37.2 34.6 33.7 35.167 o
Volumetrlc Flow Rate Data
Average Stack Gas Velocity (v.)78.76 79.70 77.74 78.733 fUsec
Stack Cross€ectional Area (A.)615.75 615.75 615.75 615.750
Actual Stack Flow Rate (Q.)2909788 29445'.17 2872104 2908803 acfm
Dry Standard Stack Flow Rate (Q-)1 91 6785 1734840 1866944 1839523 dscfm
Percont of lsokinetic Rate fl)101.0 1 '1 0.1 101.9 104.333 oa
Emission Rate Data
Mass of Particulate on Filter (mr)-0.2000 {).2000 -0.1000 -0.167 mg
llllass of Partlculate in Acetone (m"')6.8000 6,0000 6.2000 6.333 mg
Mass due to Acetone Blank (W")0.0000 0.0000 U.UUUO U.UUU m0
Total Mass of Particulates (m")6.6 5.8 6.1 6.167 mg
Stack Partlculate Concentration (c.)0.0001 0.0001 0.0001 0.000 g/dscl
(cJ 0.0015 0.0015 0.0015 U.UUZ gr/dscf
Particulate Emission Rate (E)11-50 10.41 11.20 11.O4 kq/hr
(E)21.8 17.6 20.0 19.U lbs/hr
(E)U.UUZO o.oo22 O.1JUZ4 o.oo24 lbshmBtu
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APPENDIXB
Pre-Test Protocol
lntermountain Power Service Corporation
July 18, 2023
Mr. Bryce Bird, Director
Utah Division of Air QualiW
P.O. Box t44820
salt Lake City, Utah 84114-4820
Attention: COMPLIANCE SECTION
Reference: Ooeratine Permit f2700010005
Dear Director Bird:
Annual Particulate Testinr of Intermountain Generatine Station (lGS)
Unit 1 and 2 Boiler Stacks
Please find attached the pretest protocolfor the particulate testing of the lcs Unit 1 and Unit 2 boiler
stacks. Annual testing is required by our Title V Operating Permit, Section 11.8.2.b.1(bX1).
The testing is scheduled for September 13 and 14,2023, and will be performed by IPSC personnel.
Based on information and belief formed after reasonable inquiry, I certify that the statements and
information in the document are true, accurate, and complete.
lf you have any questions or comments, please contact Mike Utley, IPSC Environmental Engineer, at
[phone] or [e-mail].
Sincerely,
'n K Frt&)Hn,
Jon A. Finlinson
President and Chief Operations Officer and Responsible Official
VL/HBl:he Ae Y, mn
Attachment: Test Protocol
Gregory S. Huynh
Tamer Ellyahky
Mike Utley
850 West Brush Wellman Road, Delta, Utah, 84624 / Telephone: [phone] I FAX: (4351 86a.667O / Fed. l.D. s87-0388573
Pretest Protocol
EPA Gompliance Testing for Particulate Emissions at
lntermountain Power Generating Station
Proposed for IGS Unit t and Unit 2 Boiler Stacks
The tests will be conducted by lntermountain Power Service Corporation's
Environmental Group on September 13 and September 14,2023.
INTERMOUNTAIN POWER SERVICE CORPORATION
850 West Brush Wellman Road
Delta, Utah 84624€546
(435) 864-{414
Pretest lnformation Form and Attachments
SOURCE INFORMATION
Company Name: Intermountain Power Service Corporation (IPSC)
Facility Name: lntermountain Generatlng 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: (435) 86+4414
Plant Technical Contact: Mr. Mike Utley, Environmental Engineer [phone]
Proposed Test Date: September 13 and 14,2023
Testing to be done by: IPSC personnel
OPERATING PERMIT EMISSION LIM]TATIONS AND REASON FOR TESTING
On September 12,2018, the Utah Department of Environmental Quality (UDEO) Division of Air
Quality (UDAO) issued IPSC a Title V Operating Permit for a coa!fired, steam electric
generation station in Millard County, Permit Number 2700010005. A copy of that permit is
available at UDAQ's website.
(See http:l/168.178.3.241:808O/DAQ NOI/DogV-jgwer?!ntDoclD=69712&contqntType=application/pd0
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 (bX2), 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 Parameter Determined Units to Test
EPA Method 1 Location of Samples and Velocity Boiler Units 't & 2
Traverses from Stationary Sources
EPA Method 2 Determination of Stack Gas Velocity Boiler Units 1 & 2
and Volumetric Flow Rate
(Type S Pitot Tube)
EPA Method 38 Gas Analysis for the Determination Boiler Units 1 & 2
of Dry Molecular Weight
EPA Method 4 Determination of Moisture Content Boiler Units 1 & 2
in Stack Gases
EPA Method 58 Determination of Non-sulfuric Acid Boiler Units 1 & 2
Particulate Matter from Stationary
Sources
CALIBRATION DAT.A
The EPA and State agencies require various calibrations for specific 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 SOz control. Each Unit has a
dedicated fiberglass 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 from 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 'l 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 efficient on 0.3 micron particles and have no organic binders (\Matman 934-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 untilthe
final weight is constant. To facilitate a preliminary result while the testing is in progress, the probe
wash acetone willbe 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 collec{ed 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 will contain
the following impingers:
lmpingerNumber Contents
3 Empty
4 Silica Gel
1 Deionized Water 100 ml
Deionized Water 100 ml
Amount
200 s
Palameter
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 location 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 detail and
the sampling levelwith the port orientation.
Table 1
Traverse Point Calculations
Plant: lntermountain Generating Station
Date: September 13 and 14,2023
Sampling Location: Unit 1 and Unit 2 Main Boiler Stack
Port Size: 6"
Port Length (inside stack wall to outside flange): 9u
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 Percent e+^^r, Product of Traverse Point
Point of :'*" Column Location From
Number Sjack l.D. ,-':I:^ 2 and 3 Lenqth n-r Outside Portrncnes l-on
1 &7 04.4 336 14.784 9u 23.784"
2 A8 M.6 336 49.056 g', 58.056"
3 & I 29.6 336 99.456 g', 108.456"
4 &10 70.4 336 236.544 9" 245.544"
5 & 11 85.4 336 286.944 9" 295.944"
6 & 12 95.6 336 321.216 9" 330.216"
Since we have four ports 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 Location
Traverse Point Number From Outside Port (!nches)
1,4,7, &1O 23.784 = 23-314
2, 5, 8, & 11 58.056 = 58"
3, 6, 9, & 12 108.456 = 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.aSa(2Xi).
Nozzle diameter will be selected after the pretest velocity data is collected.
As required by 40 CFR Part 60.48(bx2xii), 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 will be 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 from 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 halfl will not be performed.
5.
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APPENDIX C
Test Period Production Data
13-Sep-23 08:24:00
13-Sep-23 08:30:00
13-Sep-23 08:36:00
13-Sep-23 08:42:OO
13-Sep-23 08:48:00
13-Sep-23 08:54:00
13-Sep-23 09:00:00
13-Sep-23 09:06:00
13-Sep-23 09:12:00
13-Sep-23 09:18:00
13-Sep-23 09:24:00
13-Sep-23 09:30:00
13-Sep-23 09:36:00
13-Sep-23 09:42:00
13-Sep-23 09:48:00
13-Sep-23 09:54:00
13-Sep-23 10:00:00
13-Sep-23 10:06:00
13-Sep-23 10:12:00
13-Sep-23 '10:1 8:00
13-Sep-23 10:24:00
13-Sep-23 10:30:00
950.6996395
950.3496796
948.3424948
950.9597479
950.0135544
950.1 0841 98
949.98891
948.6994357
950.6504546
951.2574607
949.750463
948.7346723
951.1887276
950.3682787
949.6513941
949.5920946
949.288053
9s0.6628071
950.4724321
950.3634074
949.0846211
950.3140545
391
386
s91
388
389
387
386
391
392
388
386
392
389
387
387
388
390
390
391
389
20,
392
IPP UNIT ONE Stack Particulate Test Pr.o-d.gction i lYlonitorinq Data
13-Sep-23 10:42:00
949.8697959
950.9267473
949,755700512310:48:00
I
13-Sep-23 10:54:
13-Sep-23 11:00:00
13-Sep-23 1'1:06:00
13-Sep-23 11 12:00
13-Sep-23 1'l:18:00
13-Sep-23 11:24:00
13-Sep-23 11:30:00
13-Sep-23 1 1 :36:00
13-Sep-23 11:42:OO
13-Sep-23 1 1:48:00
13-Sep-23 1'1:54:00
13-Sep-23 12:00:00
13-Sep-23 '12:06:00
13-Sep-23 12:12:00
13-Sep-23 12:18:00
13-Sep-23 12:24:00
13-Sep-23 12:30:00
13-Sep-23 12:36;00
13-Sep-23 12:42:00
13-Sep-23 12:48:00
13-Sep-23 12.5400
13-Sep-23 13:00:00
13-Sep-23 13:06:00
949.6779656
949.7089042
950.3739937
950.8503683
950,1826205
948.97101 13
950.9766'158
949.8223655
950.5063744
949.4232065
949.8447774
949.595277
950.092681 3
950.6806416
949.4000077
949.9749531
950.2824578
949.8492985
950.5515798
949.0023352
950.875542s
949.1278161
949.7769812
391
392
390
392
387
392
388
390
386
388
387
387
389
386
387
388
386
386
385
387
386
384
386
13-Sep-23 1 949.541202
IPP UNIT ONE Stack Partlculate Test Production / Monitorins Data
Period (6 min avq) Load (MWh-e) Asalusase (!gns/hD Avo Opacitv (%)
-2313:18:00
13-Sep-23 13:30:00
13-Sep-23 13:36:00
'13-Sep-23 13:42:00
13-Sep-23 13;48:00
13-Sep-23 '13:54:00
13-Sep-2314:00:00
13-Sep-23 14:06:00
13-Sep-23 14:12:00
13-Sep-23 14:18:00
13-Sep-23 14:24:00
13-Sep-23 14:30:00
13-Sep-23 14:36:00
13-Sep-23 14.42:00
'13-Sep-23 14:48:00
'13-Sep-23 14:54:00
13-Sep-23 15:00:00
13-Sep-23 15:06:00
13-Sep-23 15:12:00
13-Sep-23 15:18:00
13-Sep-23 15:24:00
13-Sep-23 15:30:00
949.9316149
950.9096366
949.990038
949.0701747
951.5425001
948.9986259
950.6057059
949.6512982
949.0217672
951.2148155
949.1115292
950.2322802
950.0239237
950.48467
950.5031156
949.6514855
949.7601218
950.0632s98
949.6089775
950.9873079
949.2387293
389
388
386
391
385
387
388
384
388
386
3,5
3.5
3.5
3.5
3.5
3.5
3.5
?C
3.6
388
385
389
384
387
IPP UNIT TWO Stack Particulate Test Pt'oduction / Monitorinq Data
14-Sep-23 09:48:00
14-Sep-23 09:54:00
14-Sep-23 10:00:00
14-Sep-23 12.24:OO
14-Sep-2312:30:00
3.4
3.4
3.4
3.4
388
387
387
387
951
951
949
949
950
3.5
3.5
14-Sep-23 07:42:00
'14-Sep-23 07:48:00
14-Sep-23 07:54:00
14-Sep-23 08:00:00
14-Sep-23 08:06:00
14-Sep-23 08:12:00
14-Sep-23 08:18:00
'14-Sep-23 08:24:00
14-Sep-23 08:30:00
14-Sep-23 08:36:00
14-Sep-23 08:42:00
14-Sep-23 08:48:00
14-Sep-23 08:54:00
14-Sep-23 09:00:00
14-Sep-23 09:06:00
14-Sep-23 09:12:00
14-Sep-23 09:18:00
'14-Sep-23 09:24:00
14-Sep-23 09:30:00
14-Sep-23 09:36:00
950
950
951
949
950
952
949
950
950
950
950
950
949
952
950
951
949
950
949
950
951
949
388
388
388
389
391
389
388
387
388
387
387
387
389
387
387
386
386
386
387
389
388
389
3.2
3.2
3.2
3.2
3.2
3.2
3.2
3.2
3.3
3,3
3,3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
3.3
aa14-Sep-23 09:42:00
14-Sep-23 10:12:
14-Sep-2310:'18:00
14-Sep-23 1O:24'.0O
14-Sep-23 10:30:00
14-Sep-23 10:36:00
14-Sep-23 10:42:00
14-Sep-23 10:48:00
14-Sep-23 10:54:00
14-Sep-23 1 1:00:00
14-Sep-23 1'1:06:00
14-Sep-23 11:12:00
14-Sep-23 1'l:18:00
14-Sep-23 11:24.00
14-Sep-2311:30:00
'14-Sep-2311:36:00
14-Sep-23 11:42:00
14-Sep-23 1 1:48:00
14-Sep-23 11:54:00
14-Sep-23 12:00:00
14-Sep-23 '12:06:00
14-Sep-23 12.12:00
951
949
951
9s0
951
950
949
950
950
950
950
951
949
952
950
947
949
951
950
950
951
389
391
390
391
389
391
391
392
390
393
390
388
390
391
384
391
392
391
390
392
38914-Sep-23 12:18:00
IPP UNIT TWO Stack Particulate Test Production / Monitorino Data
Period (6 min avo) Load (MWh-e) Coal Usaoe (tonslhr) Avq Opacitv (o/o)
14-Sep-23 12:36:00
14-Seo-23 12:42:OO
950
950
39'1
393
3.6
J.O
14-Sep-23 12:54:00
14-Sep-23 13:00;00
14-Sep-23 13:06:00
14-Sep-23 13:12:00
14-Sep-23 13:18:00
14-Sep-23 13:24:00
14-Sep-23 13:30:00
14-Sep-23 13:36:00
14-Sep-23 13:42:00
14-Sep-23 13:48:00
14-Sep-23 13:54:00
'14-Sep-23 14:00:00
14-Sep-23 14:06:00
14-Sep-23 14:12:OO
14-Sep-23 14:18:00
14-Sep-23 14:24:00
'14-Sep-23 14:30:00
14-Sep-23 14:36:00
14-Sep-23 14:42:00
14-Sep-23 14:48:00
14:54:00
95'1
949
951
950
948
951
949
951
951
950
950
950
951
947
950
950
951
951
948
951
950
949
3.6
3.6
3.6
3.6
3.6
3.6
3.6
3.6
3.6
3.5
3.5
3.5
3.5
3.5
3.4
3.4
389
392
390
388
392
389
393
392
391
39'l
391
390
388
390
392
391
391
389
391
389
389
392
FwFM0o02 As Fired Sample Final Report, t or 2
IPSC Fuel-s Lab
Date Sampled.: 09 /13 /2023 14 :00
Lab Sample Numberz 5852L
Analyst Initials: RGC/C,I
Date Analyzed: 09 /t4/2023
Short Proximate Analysis
As Received pry Basis
t Total Moisture 10.2L I xxxx
t Ash
t Sulfur
BTU/Lb
1L.53 t 12.84 *
0.85 t 0.96 t
70924 L2L66
MoisEure Ash Free BTU/Lb L3958
t Residual Moist,ure 2.99 t
Sample operated properly during sampling period.
Comment,s:
Prod 09:59:44 AIvI Intermounuain Power Service Corp L0/25/2023 80353
FWFMo001 2ot2
Date Sampled.: 09/13/2023 14:00
Lab Sample Number: 6852L
Analyst Initials: RGC/CJ
Date Analyzed: 09/L4/2023
* Air Drv Loss
Container Weight - 535.8
As Received Sample + Container WeighE - 1738.6
Dry Samp1e + Container Weight. - 1656.5
8 Air Dry Loss - 7.44 *
I Residual MoisEure in Duplicate
( 1) (2)
Crucible Weight - 15.4261 t5.0728
ToE,aI Wer Weighr - L6.4243 16.0777
ToEaL Dry WeighE - L6.3945 L6.0477
( 1) l2l (Ave)
* Residual Moisture - 2.99 * 2.99 * 2.99 B
Dry Const,anu - 0. 9701 0. 9701 0.9701
t ToEaI MoisEure - l-0.2L t L0.2L * 10,21 t
* Ash in .QqBlicate
( 1) (2)
Crucible Weight, - 20.2555 19.3252
ToEal Wet Weight - 21.2650 20.3255
Toral Dry Weight - 20.3902 !9.4495
( 1) (2) (Ave)
As Decermined Ash - 12.48 I L2.44 * L2.46 Z
t Dry Ash - L2.86 t 12.82 t 72.84 B
BTU in Duplicate
(1) 12) leve)
As DeEermined BTU/Lb - 11809 11795 LL802
( 1) (2) (Ave)
Dry BTU/Lb - L2L73 L2759 L2166
M. A. F. BrU/Lb - 13959 L3947 13958
Sulfur in Duolicate
( 1) l2l (Ave)
t As Determined Sulfur - 0.93 0.92 0.93 t
( 1) l2l (Ave)
t Dry Sulfur - 0.95 I 0.95 t 0.95 I
As Fired Sample Worksheet
IPSC Fuels Lab
80353 09:59:44 AI'1 Intermountain Power Service Corp L0/25/2023 Prod
t
I
FWFM0o02 As Fired. Sample Final ReporL L or 2
I
rPSC Fuels Lab I
Dat,e Sampled: 09 /L4/2023 14 :00
Lab Sample Number: 58523
Analyst tnitials:JWICJ
Date enalyzed: 09 /16/2023
Short Proximate Analysis
As Received Drv Basis
B Total Moisture 11 - 01 t XXXX
t Ash
t Sulfur
BTU/Lb
10. 98 t 12.34 *
0.78 t 0.88 t
10883 12229
Moisture Ash Free BTU/Lb 13950
t Residual Moisture 2.15 I
SamllLe operated properly during sampling period.
Comments:
Prod t0:00:05 AII IntermounEain Power Service Corp L0/25/2O23 80353
FWFMo001
Date Sanpled:
Lab Sample Number:
Analyst IniE,ials:
Date Analyzed:
CrucibLe WeighE -Total Wet, WeighE -
Tot,al Dry WeighE, -
* Ash in Dur:licate
Crucible Weight -Total Wet Welght -
Total Dry Weight, -
Sulfur in DupLicate
* As DeEermined Sulfur -
As Fired Sample WorksheeL
IPSC Fue1s Lab
09 /14/2023 l-4:00
68523
,fWlCJ
09/L6/2023
9.05 t
(1)
2.L5 *
0.978s
11.01 *
(1)
L2.09 *
12.35 I
(2) (Ave)
11953 11965
(1)
Dry BTU/r,b - t224L
M. A. F. BTU/Lb - 7396't
(1) (2) (Ave)
0.85 0.87 0.86 t
(1)
t Dry Sulfur - 0.87 t
2of2
* Air Dry Loss
Container Weight - 629.5
As Received Sanp1e + ConE.ainer Weight. - 1575.8
Dry Sample + Container WeighE, - 1491.1
t Air Dry Loss
t Re.siduaL Moisture j-n Duolicate
(1) t2)
L5.4263 LA.9207
L5.4269 L5.9206
15.4054 15.8990
Residual Moisture -
Dry ConstanE, -
t Total Moisture -
(1) (2)
2t.0648 20.s005
22.0576 21.5006
21.1850 20.62:-A
As DeEermioed Ash -t Dry Ash -
BTU in Duplicate
As Det,ermined BTU/Lb -
(1)
Lt97 8
t2)2.t6 *
0.9784
11.01 t
(Ave)
2.15 t
0. 9785
11.01 t
t2)
t2.04 4
12 .31 I
(Ave)
12.07 *
t2.34 *
(2) (Ave)
L22L7 L2229
13932 13950
(2't (Ave)
0. 89 t 0.88 t
80353 L0:00:05 A!1 Intermountain Porper Service Corp L0/25/2023 Prod
-r
I
APPENDIX D,
Field & LaboratoryData
UMT ISGA
Stationarv Source lnformation
Plant Name INTERMOUNTAIN GENERATING STATION
Fuel Tvpe GOAL. BITUMINOUS
Samolino Location UNIT 1 STACK
Operator y'ickiLvman
Date 9113t2023
Prolect #PM Performance
Base Run Number 1
ff of Ports Available
S of Ports Used 4
Port lnside Diameter o
Circular Stack?
Rectansular Stack?
Fuel F-Factor 9780 9780 9780
Test Eouioment lnformation
Meter Box Number 1 508035 Apex
Meter Calibration Factor {Y)0.9980
Orilice Meter Coefficient (AHo)1.790 in H2O
Pitot ldentification tPP 007
Pitot Tube Coefficient (c")0.840
Orsat ldentification 39-507
Nozzle Number 11
Nozzle Diameter (D^)0.1 93 ln
Probe Number 1
Probe Length 114.00 tn
Liner Material SS
Sample Case / Oven Number 522-14
lmoinoer Case Number 522-1C
Acetone Lot Number 248735
Testinq Companv lnformation
Comoanv Name lntermountain Power Service Coro
Address 850 W Brush Wellman Rd
Citv State Zio Countrv Delta, UT 84624
Phone Number 435-864-4414
Fax Number 435-864-6470
Plant Name INTERMOUNTAIN GENERAT]NG STATION Date 9l't3DO23
Sampllnq Locatlon UNIT 1 STACK Proiect #PM Performance
ODerator Vicki Lvman E of Ports Avallable 4
Stack Tvoe Circular F of Ports Used 4
Stack Slze Larqe lPort lnside Dlameter 6
lDlstance to Near watl of Srack I (L*) I g.OO I in I
t__<tfv/
,1.<-l +| -nv/
DDlstance from Port to Dlsturbtnces
Dlstance Upstream (B)3012.00 tn
Diameters lJostream (=B/D)(Bo)8.96 diameters
Distance Downstream (A)4274.00 tn
Dlameters Downstream (=4"/D)(Ao)12.72 diameters
Number of Traverse Points Required
Diameters to
Flow Dlsturbance
Minimum Number of
Traverse Points
Up
Stream
Down
Stream
Particulate
Polnts
Velocity
Polnts
2.00-4.99 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 ot 12'8 or 12'
.lpstream Spec 12 12
Downstream Spec 12 12
Traverse Pts Reouired 12 12
' Check Minimum Number of Points for lhe UpEtream
and Downstream conditions, lhen use lhe largest.
| 8 for Circular Stacks 12lo 24 inches
12 for Circular Stacks over 24 inches
Dorryn stre,SrnDistLrrb.:nce
lVeosurerner-rt
Site
Number of Traverce Points Used
4 Ports bv 3 Across
12 Pts Used 12 Requlred
17 lParticulate n Velocitv
lFmcrinr nf SrecL'Dia
Poirtr
R to
I
I
3
{
5
6
7
E
I
l0
ll
It
.r{6
.85{
.06?
.!50
.750
.933
,0{{
.IJ6
.296
.70.t
.85.1
.956
,OJ:
. r05
. 19{
Ira
-677
.806
.895
.968
.016
.08!
.1,16
.225
3{!
.65E
,771
.85{
.9It
.97t
.02t
.067
.t l8
.177
.150
.3S6
.6{{
.750
.E23
.882
.933
Traverse Point Locations
Traverse
Point
Number
Fraction
of
Stack
Diameter
Dlstance
from
lnside
Wall
Distance
lncluding
Nipple
Lenoth
IN in
1 0.044 14 6t8 23 6t8
2 0.146 49 58
3 0.296 99 4/8 108 4/8
4
5
5
7
I
9
l0
11
12
Plant Name I NTERMOUNTAIN GENERATING STATION Date 9t1312023
Sarnplinq Location UNIT 1 STACK Proiect #PM Performance
Operator Vicki Lvman B of Ports Used 4
Stack Tvpe Circular Pitot ldentificatlon IPP 007
Pitot Leak ChEck lll lPreTestl lJ lPostTest Pitot Coefficient (C.)1.8400
Stack Dimensions Velocitv Traverse Data
Diameter or Lenqth of Stack (D)336.00 tn Run Number 1-V1
/Vidth of Stack (w)tn Run Time 8:20
Area ofStack (A")615.75 t(Traverse
Point
Velocity
Head
(^p)
Stack
Temp
(t.)
Local
Velocity
(vJ'Pressures
Barometric Pressure (Ph)24.97 in Hg in HrO "F fUsec
Static Pressure (Pr,tl.)-1.00 in HrO A-1 1.35 118.00 75.0
Absolute Stack Pressure (P")24.90 in Ho A-2 1.55 12A.04 80.5
A-3 1.60 12A.OO 81.8
Stack Gas Composition B-1 1.30 120.00 73.7
Comoosition Data: I Actual Estimate l;l B-2 1.45 121.00 77.9
Carbon Dioxide Goncentration lo/oCOz)13.0 %B-3 1.55 121.00 80.6
Oxyoen Concentration (o/oO)6.0 o/o c-1 1.20 120.00 70.8
Carbon Monoxide Concentration (%co)0.0 o/o c-2 '1.35 121.00 75.2
Nitrogen Concentration (7oNz)81.0 o/o c-3 '1.s0 121.00 79.3
Stack Moisture Content (B*")0.130 o/o (0.lo<)D-1 1.20 120.00 70.8
Stack Dry Molecular Welght (Mr)30.32 lb/lb-mole D-2 1.45 120.00 77.9
Stack Wet Molecular Weiqht (M.)28.72 lbllb-mole D-3 1.55 121.00 80.6
Results
Avg Stack Gas Velocity (v")77.0 ft/sec
Avq Stack Drv Std Flow Rate (Q.a)129144639 dscf/hr
Avq Stack Drv Std Flow Rate (Q.u)2152411 dscf/min
Avg Stack Wet Flow Rate (Q*)2844765 acf/min 1.42
| - _ Stack Cross Section Schematic I
I
Average'1.19 120
Please reporl lhe average of lhe square roots of
Ap, or, (ap)'2"* = 1/"Xapr'21
Formulas Used
= DWK, for Rectangular Stacks T.(uus) = '/nEt" + 1,
= (nlDl2)2)lKufor Circular Stacks where T, = 273o(for metric units
where Ku = 1 for metric units where Tu = 460 oR for English units
where t( = 144 (in?fi() for English units vo = KpCp(ap)1/2",e (T.1""ey'(prM,))rz
P" = Prr, + P!rariJ13.6 where K, = 34.97 for metric units
o/oN, = 1gg -o/oCO2-o/oO2-o/oCO where K, = 85.49 for English units
Mo= .44\o/oCa) + .32(%02\ + .Z1(o/oNz+ o/oCO) Qr6 = 3600(1 - B*)v"A"(T"6/T,tuvs))(Pr/Pr,,1
M" = M6(1 - B*) + 188*. where T.16 = 293 oK, P.,6 = 760 mm Hg, for metric units
(ap)t'2n"o = t/n:(apt")where To6 = 528 oR, Pa,t= 29.92 in Hg, for English unils
Ptant Name INTERMOUNTAIN GEN ERATING STATION Date st13n023
Samolino Location UNIT 1 STACK Proiect #PM Performance
Operator Mike Utlev B of Ports Used
Fuel Tvoe COAL. BITUMINOUS tinimum Fuel Factor 1.083 lMaximum Fuel Factor 11,230
Orsat Leak Check lrl PreTest lvl I PostTest Orsat ldentificatlon 39.507
Gas Analysis Data
Run Number Run Start Time 6iZ3 Run StoD Time 10:29
Sample
Analysls
Tlme
Carbon
Dioxlde
Volume
(V.^r)
Oxygen
Volume
(Vor)
Carbon
Monoxide
Volume
(Vco)
Carbon
Dioxlde Oxygen
Concentra
(o/oO,\
Carbon
Monoxide Nitrogen
Concentra
(%Nz)
Dry
Molecular
Welght
(Ma)
Molecular
Weight
Deviatlon
(aMa)(%cor)(%co)
hh:mm ml ml ml percent per@nt percent percent lb/lb-mole lb/lFmole
16:11 13.3 19.1 13.3 5.8 0.0 80.9 30.36 0.00
16:26 13.3 19.0 13.3 5.7 0.0 81.0 30.36 0.00
16:37 13.4 19.0 13.4 5.6 0.0 81.0 30.37 0.01
Results Averaqes 13.3 5.7 0.0 81.0 30.36
Averaoe Calculated Fuel Factor {Fo)r*1.143 Ulolecular Wt Deviatlon < 0,3?lJl
Averaoe Excess Air (%EA).*36.3 percent Fuel Factor in Handbook Range?UJ
Gas Analvsis Data
Run Numb€r 2 Run Start Time 10:58 Run Stoo Time 13:03
Sample
Analysis
Tlme
Carbon
Dioxida
Volume
(V"^,)
Oxygen
Volume
(Vo:)
Carbon
Monoxide
Volume
(v.^)
Carbon
Daoxide Oxygen
Concentra
(o/oO"l
Carbon
Monoxide Nitrogen
Dry
Molecular
Weight
(Ma)
Molecular
Welght
Devlation
(aMa)(o/oCO"l (%Nd
hh:mm ml ml ml oorcent Dercent Dercenl Dercent lb/lb-mole lb/lb-mole
17:00 13.5 19.0 13.5 5.5 0.0 81.0 30.38 0.00
17,,25 '13.5 19.0 13.5 5.5 0.0 81.0 30.38 0.00
17i45 13.0 19.0 13.6 5.4 0.0 81,0 30.39 0.01
Results Averaqes 13.5 5.5 0.0 81.0 s0.38
Averaqe Calculated Fuel Factor (Fo)o,o 1.141 Uolecular Wt Deviation < 0,3?
Averaqe Excess Air (%EA).*34.6 percent --uel Factor in Handbook Ranoe?
Gas Analysis Data
Run Number Run Start Time 13:t4 Run Stop Time 15:30
Sample
Analysls
Time
Carbon
Dloxlde
Volume
(Vcou)
Oxygen
Volums
(Vor)
Carbon
Monoxlde
Volume
(Vco)
Carbon
Dioxide
Concentra
(%co,l
Oxygen
Concentra
(o/oOrl
Carbon
Monoxide Nitrogen
Dry
Molecular
Weight
(M,)
Molecular
Weight
Deviation
(AM,)(%co)(%N,)
hh:mm ml ml ml percent percent percent percent lb/lb-mole lb/lb-mole
18:3O 13.5 19.0 13.5 5.5 U.U 81.0 30.38 0.00
18:45 13.5 19.0 13.5 5.5 0.0 81.0 30.38 0.00
18:59 13.5 19.0 13.5 5.5 tJ.0 81.0 30.38 0.00
Results Averages 13.5 5.5 0.0 81.O 30.38
Averaoe Calculated Fue[ Factor (Fo)n,o 1.141 Ulolecular Wt Devlation < 0.3?E
Averaoe Excess Alr (o/oEA),,o 34.6 percent :uel Factor in Handbook RanEe?
Fuel Factor Fo
Fuel Type Minimum Maxlmum
Coal, Anthraclte 1.016 1.130
3oal, Lisnlte 1 .016 1.130
]oal. Bitumlnous 1.083 1.230
fil, Distillate 1.260 1.413
f,il, Residual 1.210 1.370
3as, Natural 1.600 1.u36
3as, Prooane 1.434 r.586
3as. Butana 1.405 't.553
flood 1.000 1120
/Uood Bark 1.003 1.130
= 100 - %COz -oloO2-YoCO
= .44(%COa)+ ,32(%O2l+,28(%N2 + %CO)
o = (20.9 - o/oO2- .5o/oCO)l(%CO2 + %CO)
Plant Name NTERMOUNTAIN GENERATING STATION Date 911312023
Samolino Location JNIT 1 STACK Proiect #PM Performance
Operator y'icki Lyman E of Ports lJsed
Stack Tvoe Sirerrlar Meter Box Number 1508035
Train Leak Check tl l PreTest l tJi l PostTest lJleter Cal Factor ff)).998
Moisture Content Data
Run Number Run Start Time 8:23 Run Stoo Time 10:29
fotal MeterVolume (v-)92.145 dcf Sarometric Preesure (Pb)24.97 in Hq
Avg Meter Ternp (t.).,o 80 OF Stack Static Pressure (Po.")-1.00 in H,O
Avg Stack Temp (t')"rc 121 'F Avq Orilice Pressure (aH)o,s 1.65 in H2O
lmoinoer 1 lmpinoer 2 lmpinqer 3 lmDinoer 4 [moinoer 5 lmoinoer 6 lmoinoer 7
ml ml ml 0 ml ml ml
Contents 100 Water 100 Water u.00 200 SiGel
Final Valuo (VJ,(wJ 918_'10 743.22 632.92 835.78
lnltial Value (VJ,(W)716.03 689.64 626.3s 815.50
Net Value (v"),(w")202.1 53.6 6.6 20.3
Results
Total Volume (Vt)262.34 ml lllater Vol Condensed (V*^tr')12.346 scf
Total Weisht (w)20.30 s lUater Vol Weiqhed (Vwrorsrar)0.957 scf
Std Meter Volume (V-r.tal)75.376 dscf Sat, Molsture Content (B*,*^,)142 o/o
Calc Moisture Content (B*,o 15.0 %Final Moisture Content (B*.)14.2
Moisture Contont Data
Run Number 2 Run Start Time 10:58 lun Stop Time 13:03
Total Meter Volume (v-)95.317 dcf Barometric Pressure (P")24.97 in Ho
Avo Meter Temo (t-),,.86 "F Stack Static Pressure (Pa,,io)-1.00 in H,O
Avg Stack Temp (tJ*o 121 -F {vg Orifice Pressure (AH)oro 1.66 in HzO
lmoinoer 1 lmplnqer 2 lmoinoer 3 lmoinoer 4 lmoinoer 5 lmoinoer 6 lmoinoer 7
ml ml ml s ml ml ml
Contents 100 Watel 100 Water 0.00 200 SiGel
Final Value (V),(W,)915.17 722.22 601.12 824.42
lnitial Value (V,),(W)706.76 682.1 0 595.94 803.98
Net Value (v").(w.)208.4 40.1 5.2 20.4
Results
fotal Volume (V,)zc,.tv ml lVater Vol Condensed (V*tr,ot)11.942 scf
Iotal YUeight (w)20.40 q lVater Vol Weiqhed (V*",",r')0.962 scf
Std Meter Volume (V-^,*)77.116 dscf Sat. Moisture Content (B*.14.2 o/o
Calc Moisture Content (B*.)14.3 o/o ilnal Moisture Content (B*.)14.2 %
Moisture Content Data
Run Number 3 lun Start Time 13:24 Run Stoo Time 't5:30
fotal Meter Volume (v-)93.402 dcf Barometric Pressure (Pn)24.97 in Ho
Avo Meter Temo (t-),""88 OF Stack Static Pressure (P -1.00 in H,O
dvg Stack Temp (lo)org 121 -F Avg Orifice Pressure (AH)",s 1.67 in HrO
lmpinEer 1 lmpinqer 2 lmpinser 3l lmpinqer 4 lmpinser 5 lmoinoer 6 lmoinoer 7
ml ml ml q ml ml ml
Contents 100 Water 100 Water 0.00 200 SiGel
Final Value (v,),(w,)939.1 3 734.45 632.51 839.17
lnitial Value (V,),(Wt)719,52 692.61 627.86 819.40
Net Value (V"),(W^)219.6 41.8 4.8 19.8
Results
Total Volume (V')266.20 ml Water Vol Gondensed (V*,.toJ 12.s30 scf
Total Weight (WJ 19.80 s Water Vol Weiqhed (V*o,n,o,)0,934 scf
Std Meter Volume (V-,n,o,)75.293 dscf Sat. Moisture Content (B*.,","t)14.2 o/o
Galc Moisture Content (B*r)15.2 %Final Moisture Content (B*)14.2 Yo
ls.mpllno Locrtlon luNlTl sTAcK lProlrctt IPM Plrformancc I
l*otPolnrr acrog lg ltotports Urcd l+
ldfll l{o2zle Dlrmot r end l3ol(lnetlc Frctor SoluD
Pltol Tubc Coltflct.nt (c-l 0.E40
Avo Strck Tomo 1L)120
Avo Grs MetarTimD {L',l 89 "F
tH @ 0.75 ScFll (^H@)1.79 in H,O
Avo PltotTubr Dlff, Prrsrurr (lD.*l 1.42 in tl,O
Strck Mol3turo Contont (B*)13.0 %(ur)
Btrck Drv l,lolrcsl.r Wcloht ffi,.)30.32 lbflb.molr
Erilmrtld Orllls. Flow Rri"(o-)0.730 .crm
lP lo H lroklncllc Frclor ,Kl 'l 12
Eru-r r
l,^"
SrmDllno EoulDmant
[at!r t 1508035
tlatcr Crllbr.tlon F.ctor m I 0.9980 I
{ozzlG t 11
\aturl Nozzlr Dhm.trr (o-)l 0.193 I in
d.rl Norzl. Ol.m.tcr (OJl0.18E I ln
treba ,, Landth 1 114.00 I in
.[ncr Mrt rl.l SS
irmola Ctrr, Ovan,522-14
mDlnoer CIa I 522-1C
AV- L.sk checks
Pn 0 It"rmln o 12 in l{o
Mtd ft'/min @ in Ho
Po3t 0 ftYmin @ 10 ln Ho
av- < o.o20 ff"/min ti ot?
Fhot OK?z ,rrrt OK?lrJ
Trrvctta
Polnt#
S.mpllng
Tlmo
tet
Clock
Tlme
ory Ga3
tl,llttt
Rcedln0
rut
V.loclty
Ho.d
lAo)
Dlrlred
Orltlsc
AH
{AHI
Actual
OrlflcE
AH
(AHl
St ck
Tcmp
,rl
Mctcr
lnl!t
Tomp
IL.I
Mrt r
Outl!t
Tomp
tL_l
Flltcl
Temp
lmplng.r
Erit
fomp
Pump
Vacuum
squara
Rool
AP
(ap'n)
Locrl
Strck
V.loclty
tv-1,
qumuttuvc
Motar
Volumo
ru_t-.,
sumutrlluc
Porcalrt
l.oKlnotlc
fl!
mtn hh:mm:ss tt"ia H,O in H,O ln H,O F .F .F 'F in Ho (in H,O)rn ,U$cc sct %
A-l 0.0 8:23:00 970_380 1.45 1.62 1.55 1?1 73 73 322 61 56 120 77 gt 6 157 08.5
a-2 'to o 8:33:OO 977 All 155 174 'r 74 121 7a 74 319 5't 6.'l 1.21 80,59 '12.620 99.3
A-3 20.o 8:43:00 gBs.622 1.60 1.79 1-80 21 76 76 322 53 5.5 1.26 81.88 19.203 99.6
8-1 30.0 8:55:00 993_605 1.30 1.46 1.46 21 78 78 322 53 55 1.14 73.80 25.1 19 99.7
8-2 40.0 g:05:00 1000,818 1.45 1.62 162 2'l 79 7g 3't8 56 60 120 77 e4 31 333 997
B-3 500 9:15:oO looa !o2 160 179 142 21 81 81 322 56 6.8 1.26 81_88 37.926 99-8
c-l 60-0 9:27:0O 1016.470 '1.2s 1.40 1.14 21 E1 81 320 56 5.8 1.12 72-37 43.958 100.4
c-2 70.0 9:37:00 1023.864 1.55 1.74 '1.74 22 82 82 323 58 55 12A 80.86 50.320 1 00.1
c-3 80.0 9:47:00 1031.658 1.60 '1,79 1.80 21 83 E3 321 61 70 1.26 81 88 56 865 100.1
D-1 so0 g:5erOO to39 708 't 30 'l 46 117 22 83 83 315 64 6.0 1.14 7?.A7 6?.422 't o0-2
D-2 't 00.0 '10:09:00 1{M7.038 1.r10 1.57 1.57 22 84 84 317 6l 6.5 1.18 76.65 88.912 1 00.1
D-3 't 10.0 10:'t 9:00 1054.542 1-60 1.79 1-79 21 84 8tl 323 61 7.0 126 81 88 75 3S9 100 0
Last Pt 120.0 10:29:00 1062.525
rln!l Vrlur 12(l.O 10:29:00 1062.Mrxlmum Vacuum l.o Flnrl Vrhcs 75.399 't00.0
\varaoa Valuas 1.47 1.65 121 00 00 320 58 121 78,45
EO
lrotpotntAcror 13 l#otportouscd ll I
ldo.l No22lo Dlrmotor and laoKinrtic Frctor Sotup
Pilol Tubo Cortficiant rc-l 0.840
lvo St.ck TlmD (Ll 121 "F
qvo Grs Motor TEmo n-t E6 -F
!H C? O.75 sCFilr (6H@)1.19 in H'O
vo Pitot TubE Diff. PrBBUro (AD*l 1.47 in H,O
illck ltorituro Content (8. )13.0 %
it.ck ory lrol.cul.r W.lshi (M/.)30.36 lbflSmol€
Srlim.tod Orllice Flow R.la (o-)0.768 actm
LP to AH lroklnotic Fictor il(}11
lBuometdsprcrurc I rp"l I el.sz I inHs I
lst.ck strtic Prouurc I (P**) I -t .Oo I a nrO I
AV- Lclk Checks
,fo 0 ff/min 6 95 in Ho
ntd fl-rmin @ in Ho
,o3t 0 fl'rmin 6 8,5 in Ho
rv-o.020 ll'rmin )k )k?
,ltot OK?Jl f,rsrt OK?tll
Trlvorao
Point *
Sampling
TiBc
t6)t
Clock
TlmG
Dry Grt
Mclor
Roadlng
Voloclty
Ho!d
lAol
ucttreo
Orifico
AH
IAI{ }
Actu.l
Orltica
AH
(aHt
Stlck
Tomp
lL)
Motor
lnlot
Tomp
Ir-l
lll€lor
Ou0at
Tomp
Ir--l
Fllt.l
Tamp
lmplngcr
Exlt
Tamp
Pump
Vacuum
Squ.ro
Root
AP
(apra)
Local
Slack
Voloclty
lv-1.
Cumulslive
Moior
Volume
lv,L-
Cumulativo
P6aconl
lsoXlnotlc
lll
mtn hh:mm:ss fl'rn HrO n HrO h H,o "F "F .F .F in Ho (in H,O)"'lusc scl .a
D-1 0.0 1o:58:00 65_206 1.40 1.55 50 122 ao ao 323 17 s5 118 76.51 6 029 qB3
o-2 10.0 1 1:O8:O0 72 SAO 150 1.67 71 122 81 81 47 6.0 1.22 79.30 12.332 98.8
D.3 20.0 1 'l:18:00 80.298 1.60 1.78 .83 121 83 83 319 49 6.5 1.26 81.83 18.938 99.5
30.0 11:30:00 88.412 1.20 1.33 .40 121 8/t a4 317 54 55 I 10 70 86 24 415 100 4
c-2 40.0 '11:4O:O0 95.658 1.1n 1.55 ,55 121 84 84 319 56 6.0 1.18 76.54 30.884 1 00.1
c-3 500 1r:5OrO0 I 03.1 34 1.50 1.67 .69 't21 E6 E6 320 59 6.5 1.22 79.23 37.242 1 0o_1
B-l 60.0 12:0'':00 't't0.991 1.40 55 121 85 85 318 67 6.0 t-'t8 76-5/t 43.3r 8 100.o
B-2 70.0 12:.11:OO 118_505 1.50 1.57 .70 121 e7 a7 323 68 65 122 79.23 49.637 99.9
B-3 800 12:21:OO 126 324 160 174 B)'t21 88 88 318 68 7.O 1.26 E1.E3 56.207 99.9
A-1 90.0 12:33:0(194.471 1-40 1.55 .59 121 88 88 313 66 7-O 1.18 76.54 63_263 101_4
A-2 100.0 12'.43:.O(143.220 1.65 1.83 _83 120 8g 89 323 66 ?124 83 02 70.683 102 4
A-3 1 10.0 12:53:0( 152.428 1.55 1_83 .73 12'l 90 s0 318 b/6.5 1,ZA 83.1 0 77.186 101.9
Last Pt 120 0 13:O3:O(160 323
rinrl Vrlur 120.0 13:03:0C 1 60.523 lrar trum Vacuum 7.5 Finrl Valuas /.1UO 101.9
Ucng6 Valuot 1.48 1.66 121 86 86 320 60 1_2''74.72
86
lderl Nozzlo Da.mat rrnd [toKlncllc FactorSetuD
,llot TubE Co.frlci.nt (c-)o.840
{vs St ck Tcmp (U 121
{Yq Ge3 llrcler T.mp (L)92 "F
!H @ 0.75 SCFM (AH@)l.7s in H.O
{vo PltotTubo Olff, Prcasurc (Ao*)1,48 h H,O
It ck Molrtur. Contsnt tB-)13_O oh
Itrch Drv Mol'culrr Waloht (M"J 30.38 lb/lEmok
:sthat.d Orlllca Flow Rrt.(Q-)0.794 eclm
lP to AH ltoklnrflc F.ctor {Kl 1.12
SamDllno EoulDmrnt
Meiar *r508035
M.br C.llbratlon F.ctor rn I 0.9980 I
Nozzlo #11
Actu!l Nozrlr DirmcLr (o--)10.'193 I in
ldcrl Nozzle Diamoter (D-,) I 0.192 I in
Proba *, Leneth 114.00 I in
LInrr Metcrirl 5-
Senph Cese / Ovrn # ;22-1A.
lmolnoer Cara *1C
AV- Lork Chocks
Pro 0 ft'rmin lo I in Ho
il[d fr'/min 6 ln Ho
Pott 0 ll'/rnin (&10 in Ho
av- < 0.020 n'/mh lk ck?
Pltat OK?)r3.t OK?IJ
Cumulrtivo
Plrcent
lroKlnelic
s8,8
99.2
s9.7
99.9
METHOD 5. SAMPLE REGOVERY AND INTEGRITY DATA SHEET
Plant Name INTERMOUNTAIN GENERATING STATION Date 9t13t2023
Samollno Location UNIT 1 STACK Proiect #PM Performance
Operator Vicki Lvman Acetone Lot Number 248735
Run History Data
Run Number 1 2 3
Run Start Time 8:23 10:58 13.24 (hh:mm)
Run Stop Time 10:29 13:03 15:30 (hh:mm)
Train Preoared Bv VL VL VL
Train Recovered Bv VL VL VL
Recovery Date 9t13t2023 911312023 9113t2023 (mm/ddlw)
Relinquished By nla nla nla
Received Bv
Relinsuished Date (mm/dd/w)
Relinouished Time fth:mm)
Equi pment ldentification Numbers
Filter 1 2 3
Acetone Wash cl c2 C3
Silica Gel DRP-12.108 DRP-12-1OB DRP-12.10E
lmpinqer Case 522-1C 522-1C 522-1C
Samole Box 522-14 522-14 522-14
Oven 1350G 1350G 13s0G
Formulas Used
% = Vr-V Wn = Ws-W1 Vr" = Vn + Wn/p* where p* =.9982 g/ml
MoisturE Content Data
lmoinoers 1. 2. and 3 - Water Volume
Final Volume (Vr)2294.2 2238.5 2306.2 s
nitial Volume (Vi)2032.0 1984.8 2040.o s
Net Volume (v")262.2 253.7 266.2 s
Comments
lmoinoer 4 - Silica Gel Weloht
FinalWeight (Wr)835.8 824.4 839.2 g
lnitialWeight (w)815.5 804.0 819.4 s
Net Weight (w.)20.3 20.4 19.8 s
Comments
Total Water Collected
Total Volume (VrJ 282.5 274.',|286.0 g
IPP_PM_U1-9_13_2023 - M5 - Recovery Page 1 Printed 1012612023
I METHOD 5 -SAMPLEANALYTICAL DATASHEET I
Plant Name NTERMOU NTAIN GENERAT]NG STATION Data th3no23
Samplinq Locatlon JNIT 1 STACK Proiect #PM Performance
0perator Vicki Lyman Acetone Lot Number 24s735
Analvtlcal Data
Placed In Deslccator Run Number 1
Number Date Time Run Start Time 3:23
sllter 1 0gt13n3 11:25 Leakaae Evident?!)no
lcetone Wash Beaker C,I o9t14t23 6:28 Estlmated Volume 170 ml
Filter Acetone Date Time Humidity Temp Cal Audlt
E E mm/dd/w hh:rnm %RH oF s
Measurement'l (m'r),(m'.)0.6129 130.6320 ogn8n3 4:24 32 73
Measurement 2 (m2il,(mz.)0.6129 130.6320 ogt18t23 12:21 30 72
Measuremant 3 (msr),(m*)
Measuremont 4 (m.),(m.")
Results Acetone Blank
Flnal Weloht (mr),(m"')0.6129 130.6320 0 Final Weisht (Ct')129.8991 g
tare Woisht (mr),(m'.')0.6135 130.6197 s Tare Weisht (Cr"')129.8992 s
Weloht Galn (m,),(m"')-0.6 12.3 mg Blank Concentration (c,)0.ooo0 mg/g
Blank Adiustment (W.)0.0000 mg
lotal Particulates (m.)11.7 mg
Analytical Data
Placed in Desiccator Run Number z
Number Date Time Run Start Time 10:58
Filter 2 09t13t23 14:17 Loakaq€ Evldent?vl no
Acetone Wash Beaker c2 09t14t23 6:28 Estimated Volume 100 ml
Fllter Acetone Date Time Humldity Temp Cal Audlt
o o mm/dd/w hh:mm o/rRH oF s
Measurcment 1 (mrr),(mrJ 0.6099 105.9974 09t18t23 4:24 32 73
MEasurement 2 (m-),(m,")0.6099 105.9975 o9118123 12:21 30 72
Msasuroment 3 (m"),(m.")
Moasuremont 4 (m.J,{m.J
Rssults Acetone Blank
Flnal Weasht (rnfl),(mh')0.6099 105.9975 g Final Weioht (ch)129.8991 q
fare Weight (mtr),(m"')0.6098 105.9919 s Tare Weioht (C''')129.8992 q
Weloht Gain (m),(m.)0.1 5.6 mg Blank Concontratlon (c,)0.0000 mq/E
Blank Adlustment (w.)0.0000 mg
Total Particulates (m,)5.7 mg
Analvtical Data
Placed in Dosiccator Run Number 3
Number Date Tlme Run Start Time 13:24
Fllter 3 ow13t23 15:O2 Lqakage Evident?lvl no
Acetono Wash Beaker c3 09/14n3 9:36 Estlmated Volume 130 ml
Filter Acetone Date Time Humldlty TomD Cal Audit
o q mm/dd/w hh:mm o/oRH oF q
Measurement I (mrd,(m,J 0.6044 130.6472 a9/18n3 4:24 32 73
Measurement 2 (mz),(mu")0.6047 130.6474 09n8n3 12:21 30 72
Measurement 3 (msr),(ms')
Mgasurement 4 (mrd,(mr,)
Results Acetone Blank
Final Weioht (mr).(mr.')0.6046 130.6473 s Final Weloht (Cr,)129.8991 0
fare Weight (m").(m,.')0.6049 130.6365 s Tare Welqht (c,,)129.8992 s
Weioht Gain (m).(m.')-0.3 10.8 mg Blank Concentration (c")0.000c mg/g
Blank Adlustment (vv.)0.0000 mg
fotal Particulates (mJ r0.5 mE
Formulas Used
= average of last two filte, measurements
,' = average of lasl lwo acelone measurements
u1_9_13_2023 -Printed 1On6nO23
Table 2
METHOD 5. DETERMINATION OF PARTICULATE EM]SSIONS. RESULTS
Plant Name NTERMOUNTAIN GENERATING STATION late 9t1312023
Samollno Locatlon JNIT 1 STACK ,roiect #PM Performance
0perator y'icki Lvman Itack Tvpe Oircular
Historical Data
Run Number 1 2 3 Average
Run Start Tlme 8:23 10;58 13:.24 hh:mm
Run Stop Time 10:29 13;03 15:30 hh:mm
Meter Calibration Factor ff){J.996 0.998 0.998
Pitot Tube Coefficient (Co)0,840 0.840 0.840
Actual Nozzle Diameter (D",)0.'193 0.1 93 0.193 tn
tack Test Dala
nitial Meter Volume (v-),970.380 6s.206 160.880 ft"
Flnal Meter Volume u-),1062.525 160.523 254.282 ft'
fotal Mster Volume (v.)92.145 95.317 93.402 93.621 flo
l"otal Samollno Time (o)120.0 120.0 '120.0 120.0 mtn
Average Meter Temperature (t.)o,o 80.0 86.0 88.0 84.7 "F
{veraoe Stack Temoorature (.)",.121.0 121.0 121.0 121.0 "F
Barometric Pressure (P")24.97 24.97 24.97 24.97 in Hq
Stack Static Pressure (P""n)-1.00 -1.00 -1.00 -'t.00 in H.O
{bsolute Stack Pressure (P.)24.90 24.90 24.90 24.90 in Hq
dveraoe Orifice Pressure Drop (^H)"-1.65 1.66 1.67 1-66 in H"O
lbsolute Meter Pressure (P,)25.09 25.09 25.09 25.09 in Ho
lvq Square Root Pltot Pressure (Apto).*1.21 1.21 1.21 1.21 (in HrO)
Moisture Content Data
mpingerg 1-3 Water Volume Gain u")262.2 253.7 266.2 z6(J.t ml
lmpinoer 4 Silica Gel Weioht Gain (w.)20.3 20.4 19.8 20.2 g
Total Water Volume Collected (Vb)282.5 274.1 286.0 280.9 ml
Standard Water VaBor Volume (V*)",13,297 2.902 13.462 13.220 scf
Standard Meter Volume (V.)"0 75.376 77.116 75.293 75.928 dscf
Calculated Stack Molsture (B-r-"t)15.0 14.3 15.2 14.4 o/o
Saturated Slack Molsture (Brrrr,ot)14.2 14.2 14.2 14.2 Vo
Reported Stack Moisture Content (B-.)14.2 14.2 14.2 14.2 o/o
Gas Analvsis Data
Carbon Dioxide Percantaqe (o/"CO2l 13.3 13.5 13.5 13.4 o
Oxygen Perceniage (%O,l 5.7 5.5 5.5 5.6 o/c
Garbon Monoxide Porcentaoe ffico)0.0 0.0 0.0 0.0 o
Nltroqen Percentaoe {%Nr)81.0 81.0 81.0 81.0 o/o
Dry Gas Molecular Weight (Md)30.36 30.38 30.38 30.37 lb/lb-mole
Wet Stack Gas Molecular Weioht ff.)28.51 28.61 28.50 28.54 lb/lb-mole
Calculated Fuel Factor (F")1.143 1.141 1.141 1.142
Fucl F-Factor {F,)9780 9780 9780 9780 dscf/mmBtu
Percent Excess Air (%EA)36.3 34.6 34.6 35.2 o/o
Volumetric Flow Rate Data
Average Stack Gas Velocig (vJ 78.61 78.47 78.62 78.57 fUsec
Stack Cross€ectional Area (A.)615.75 615.75 615.75 615.75 ft'
{ctual Stack Flow Rate (oJ 2944246 2899074 2904616 2902645 acfrn
Drv Stendard Stack Flow Rate (Q.")1867016 1879039 1862860 1869638 dscfin
lercent of lsokinetic Rate (l)142.O 103.7 102.1 102.6 o/o
Emission Rate Data
Ulass of Particulate on Fiiter (mJ -0.6000 0.1000 -0.3000 -0.3 mg
l/lass of Particulate ln Acetone (mn')12.3000 5.6000 10.8000 9.6 ME
Mass due to Acetone Blank (w.)0.0000 0.0000 0.0000 0.0000 mq
Total Mass of Particulates (mn)11.7 5.7 10.5 9.3 mg
Stack Particulate Concentration (c.)U.UUUZ 0.0001 0.0001 0.0001 g/dscf
(c")0.0031 0.0015 o.o015 0.0020 sr/dscf
Particulate Emission Rate G)22.40 11.27 1 1.18 14.95 koihr
(E)38.3 18.4 34.4 30.4 lbs/hr
(E)0,0046 0.0022 0.0041 0.0036 lbs/mmBlu
LOCATION OF TRAVERSE POINTS IN STAGKS
The following two tables give the location of traverse points across the stack as a fraclion 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 Circular Stacks
Traverce
Point
Number
(Fraclion of Stack Dimension from lnside Wall to Traverse Point)
Number of Traverse Points Across the Stack
2 4 6 I 10 12
1 .146
.854
067
2s0
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
.1 18
.177
.250
.356
.644
.750
.823
.882
.933
.979
2
3
4
5
6
7
8
I
10
11
12
Location of Traverse Points in RectanEular Stacks
Traverse
Point
Number
(Fraction of Stack Dimension from lnside Wall lo Traverse Point)
Number of Traverse Points Across the Stack
2 3 4 5 6 7 I 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
61'l
722
833
944
.050
.150
.250
.3s0
.450
.550
.650
.750
.850
.950
.045
.136
.227
.318
.409
.500
.s91
.682
.773
.864
.955
.04?
.1?5
.208
.292
,375
.458
.542
,625
.708
.792
.87s
.958
2
3
4
5
6
7
8
I
10
11
12
IPP_PM_U1_9_13_2023 - Fraction of Diameter Page 1 Printed 1013112023
isoCALC UNITS
Unlt8 Neme TablD
Unlti
Numbar
l,l.tiv.
Nrma
English
Nrm6
I Enolish Enolish
2 Melrlc Metric
3 Bfank Blank
)u?rent Unlt Numbcr 1
t nlt LookuD Tablc
Engll3h
t nltr
M.blc
LJniti
"F "c
tn mm
tn cm
ln m
fr m
t(m'
n'm'
dcf dcm
sct tcm
dsc{dccrn
ctrn cmm
ac{m acmm
ft'/min m'/min
dscfm dscmm
dscfrmin dscrvmin
dscflhr dssn/hr
ft,fsGc m/sec
in HrO mm HrO
in Ho mm Hq
in Ho kPa
(in H,O)(mm H:O)
lbnb.mole g/g.mole
o/d6cl o/dscm
or/d3c,qrldscrn
lb/hr ko/hr
I
Constants LookuD Table
Comt nt
Namo
conrtrnt
Sumhal
Currcnt
Vetue
Curasnt
tlnlts
Engllsh
Valu.
Englirh
ll^ltG
Uotrlc
Valuc
Mctric
Unlt3
Large Stack Dl.mcter (C"")24 tn 24 tn 0.61 IN
lnchor per fbot {C.i)12 in/ft 12 in/tt 't m/m
lnches DCI Foot mm oer tJlater (c 12 h/n 12 h/fr 1000 ,nm/m
Maxlmum Allow.ble Le.k Ratc (c*)0.02 ctm 0.02 6.tm 0.00057 mrlmin
Nozzlc Ditnrdrr Constanl (c")0.03575 ?0.03575 1 607.r ?
K F.ctor Conrtant (c.)849.8 ?M9.8 1 8.038E-05 ?
Pltot Tubo C;onttant K. 85.49 ,le)fin Hol,85.49 ,te)(in Holl u.g7
Metgr Mollturr Contenl (B--)0.00 olo 0.00 oh 0.00 c/o
Metcr Drv ilolccular Welaht (M.-)29.00 lMb.molc 29.00 lMb.mdc 29.00 o/o.mole
Pressure Droo ln Ga3 ilater (Pd,)0.25 in H,O o.25 in H,O 6.35 lllnl Ha9
Absolutc TcmDereture Olfsrt T!460 "R 460 273
Standrrd Ah!oll.rtG Prcssura o 29-92 in Ho 29.92 in Ho 760.00 mm Ho
Strndud Ahrol llto TomporaturE T 528 528 .R 293
9tendard Volume Corroctlon K, 17.64 "R/in Hg 17.64 "R/in Hg 0.3858 'Khm Hg
Jv.ter Volurna to Std Wrtar V.por Kz 0.04707 n"/ml 0.04707 ft'/ml 0.001333 m'/ml
loklnttlc V.ri.tion . Raw Data Kr 0.002659 Hg-ft'hl.'0.002669 Hg"fl"/ml"0.003454
soklnotlc Variatlon - lntermedl.te r(0.09450 ?0.09450 ?4.320 ?
{Uatcr ltlars to Std Water Vapor K*0.04715 fi'/g 0.04715 ft'/9 0.001335 fi"lg
oegrcc. F tr Degrecr C l$ultlpller }C 1.000 .FTF 1.000 "FTF 1.800 'Frc
Dogrle! F tc Oegrre. C Offset K7 0.000 0.000 r 32.00 r
Mllllmot.rs DGr lnch l(1,000 lnnn 1.000 in/in 25.40 mmfin
l)ound Kr 1.000 iMn 1.000 in/in 25.40 mm/in
of VYrtcr o-o.99E2 o/ml 0.9982 o/ml 0.9982 o/ml
IPP_PM_U 1_9_1 3_2023 - Units Page 1 Printed 10i31/2023
I tsoKtNETtc SAMPLTNG pATA _ [
lPtant Narne ltrur
lsamplinE Location IUNIT 1 STACK lProlect# I I
l# of Polnts Across 13 ll nt pnrte t tcaa la I
ldeal Nozzle Diameter and IsoKinetic Factor Setuo
Pltot Tube Coefficient (c")0.840
Avq Stack Temo (t,)r
{vs Gas Meter Temo 0^)F
rH @ 0,75 SCFM (AH@)in HrO
\vS Pltot Tube Dlff. Prese ure (AF."o)in H,O
Itack Molsture Content (B-.)% (p<.x)
itack Dry Molecular Welohi (MaJ lbllb-mole
Sstimated Orlftce Flow Rate (o-)acfm
AP to AH lsokinetlc Factor (K)
rsl
Sampllng Equlpment
M6EI#
Meter Calibration Factor (Y)
Nozzle *
Actual Nozzle Diameter (D-)tn
deal Nozzle Dlametor (D"r)tn
Probe # / Lenoth 1 114.00 I in
Llner Material SS
Samole Case I Oven #522-14
mplnqer Case # 522-1C
AV- Leak Ghecks
lre g fl'/min @ /.?in Hq
I'lid ft'/min @ in Hq
,ost &ft"/min @ /0 in Ho
av- < 0.020 fl"/min tr ok?
Pitot OK?V Orsat OK?w
Traverse
Polnt #
Sampling
Time
(o)
Clock
Time
Dry Gas
Meter
Reading
(v_t
Velocity
Head
(Ap)
Desired
Orlfice
AH
(^H)
Actual
Oriffce
AH
(^H)
Stack
Temp
{Lt
Meter
lnlet
Temp
(L,t
Meter
OuUet
Temp
(L-)
Fllter
Temp
lmpinger
Exlt
Temp
Pump
Vacuum
mtn hh:mm:ss ft'in H,O in H,O in H"O .F "F "F r "F in Hq
A-1 0.0 tz<?*7,*ao /r'/5 /,L J*{5 /2/a 322T,:E 6/'.) t (2
A-2 10.0 8:3-{FI.EII 1,.<g t.'.:fr
Vt
,ZI ,Tl 6rl
A-3 20.o 9,q_<q$<-t Iv t.an ).{t e ,J,E?7:7
B-1 30.0 mrr ffi9tht l,b /,4fo f ,f/;ZI 7zz .5:7 rC.f
B-2 40.0 fr'aF t.44 l.t-L LL7 l2t 7Y 3 5b 6,O
B-3 50.0 cl.tF MT.4 t.Lo ,47 hYZ t1 7I tz 6b /.t
c-1 60.0 q:?-v tb/L 472 /,2<n.il)l)I gt .VT)4Zo 5)
c-2 70.4 q:3?hlq.QAl /sd L7t t2:8L n_523 -62 , t,l
c-3 80.0 q."tff l,bD Irf Lru /zt B1
83
3 at T 3,O
D-1 90.0 4:Ka .rrtl.;TT t'l t t.Ll?t)z 't.{ZT m
D-2 100.0 D:Ol lDqAL '/,qD t.t*l.f?n-z-7q1 I ?IZ /-l -/F
D-3 1 10.0 o: t7 r>f4:r47 t.t.o t,77 -t,:t{tl lTrl FT-l vq 7't4,/-/ZO
Last Pt 120.0 b;tcl tOLl 6
rinal Valur 120.4 Maximum Vacuum
Averase Values
Plant Narne INTERMOUNT/\IN GENERATING STATION )ats "I-,17, aoz3
Samplinq Location UNIT 1 STACK )rolect #
0perator Rick Moodv Run #L
I of Points Aqross 3 I of Ports Used 4
ldeal Nozzle Dlameter and lsol(lnetlc Factor SetuD
Pitot Tube Coeflicient (c")0.840
Avo Stack Temo (L)"F
Avg Gas Meter Temp i.h)OF
lH @ 9.75 SL;FM (AH@)in HrO
Avo PltotTube Dlff. Pressure (A0",")in H"O
Stack Moisture Content (t3-.)% (:o<.x)
Stack Dry MotecularWcight (lvla.)lbllb-mole
Estimated Orifice Flow Rate ('1")acfm
tP to AH lsokinetic Factor ,lK)
Prgssures
Barometrlc Pressure I.Pr)in Hq
Stack Static Pressure (F'.r.rt)in H,O
Absolute Stack Pressure tP.)in Hq
Absolute Meter Pressurs (P.)in Ho
Dr)'Gas
Meter
Reading
(v
SamDllnE Equlpment
Meter #
Meter Callbration Factor (Y)
Nozzle #
Actual Nozzla Diameter (D-)tn
ldeal Nozzle Diamotsr (D.,)tn
Probe # I Lenoth 1 114.00 tn
Liner Material SS
Sample Cass / Oven #522-1A
lmoinqer Case #522-1C
AV- Leak checks
Pre /r fl"/min @ q,f in Ho
Mtd fl"lmin @ in Hq
Post -D-fi'/min @ a"r in Ho
av- < 0.020 flolmin tr ok?
Pitot OK?T-Orsat OK? l[-:,
t-
Plant Name INTERMOUNTAIN GENERATING STATION )ate 7.
'
3.2-02-3
lamplino Location UNIT,I STACK Proiect #
f,DErator Rick Moodv Run #.?
F of PolnG Across 3 # of Ports lJsed
ldeal Nozzle Dlameter and lsoXinetic Factor Setuo
Pitot Tube Coefficient (C,)0.840
AvE Stack Temp (t")"F
Avg Gae Meter Temp (t,)OF
rH @ 0.75 SCFM (AH@)in H"O
Avo Pltot Tube Diff, Pressure (Ap.,.)in H.O
Stack Moisture Content (B*")o/o (*..x\
Stack Drv Molscular Weioht (M,.)lblb-mole
Estimated Orifice Flow Rats (Q,)acf,m
IP to AH lsokinetic Factor (K)
Samplinq Equloment
Meter #
Meter Callbratlon Factor m
Nozzle #
Actual Nozzle Diameter (D"J tn
deal Nozzle Diameter (D*)tn
rrobe # / Lenqth 1 114.00 I in
Liner Material SS
Sample Case / Oven #i22-14
lmoinoer Case #522-1C
Pressures
Barometric Pressure (Pb)in Ho
Stack Static Pressure (P"rrrr")in H,O
Absolute Stack Pressure (PJ in Ho
Absolute Meter Pressure (P-)in Hg
AV- Leak Chesks
Pre .,t4-ft1min @ 4,n in Hq
nfid ft"lmin @ in Ho
Post g fto/min @ /D,/)in Hq
tv- < 0.020 fto/min E )k?
Pltot OK?V OrsatOK? lW
.4.
Traverse
Polnt #
Sampling
Time
(o)
Clock
Time
Ory Gas
Meter
Reading
ff-t
Veloclty
Head
(ap)
Desired
Orifice
AH
(AH)
Actual
Orifice
AH
(AH)
Stack
Temp
(r)
Meter
lnlet
Temp
(Lr)
Meter
Outlet
Temp
(L^)
Filter
Temp
lmpinger
Exit
Temp
Purnp
Vacuum
mtn hh:mm:ss ft"in HrO in H,O in HzO 'F OF F OF "F in Hq
A-1 0.0 1.7;71 rCI,X&
i,{tL4
6,14y
L4r lz7-gcl g'/7T w 5Ll 6,C)
A-2 10_o /3,:r l,bo l"v7 1,\?VLt qn 6F
2,#-
A-3 20.0 l3:U.l.9i .12 z4 a+313 48
B-1 30.0 tSi({a |F{.,t1 3*723 52
B-2 40.0 tIj%tql-R,ltt t7 w 3ry fa ET
B-3 50.0 'l{.tw.47 l,l,{/,74 LA
t,:,
tt T1 87 g,O
c-1 60.0 lqi.tr\4 Aq L3q t,tr'6t9 1^t 7d
c-2 70.0 i4;3 41.1,444 l,cg t.72,ta R *.7/{--6r ?l
80.0 {ry r,21.1.€41 /,?1 [+q /Z W qD 7/q /n4 -4-v-fr /-
D-1 90.0 l<'oa t30,&,L l,4L t,{.t?T ?th G4 Z;S_
D-2 't00.0 l\':l n t19 tflv t,<o t,/^9 a la qT i73 6 -f7
D-3 '110.0 ,5'10 ffta.il.
1,r4,ffi,
l./^o +Y tzt GT/3tE A7 7,5
Last Pt 120.0 T5;:{D
:inal Value 120.0 Maximum Vacuum
dveraoe Values
Gas Data
Fuel Factor Fo
:uel Type Minimum Maximum
coal, Anthracite 1.016 1.130
Coal, LiEnite 1.016 130
Coal, Bitumlnous 1.083 1.23U
Cit, Distillate 1.260 1.413
3il, Residual 1.210 1.370
Gas, Natural 1.600 1.836
ias, Propane 1.4U 1.586
Gas, Butane 1.405 1,553
JYood 1.000 1.120
Wood Bark 1.003 1.130
= Voa'Vco,
= Vco-Voz
%N2 = 1 96 - o/oCO2 - o/oO2 - YoCO
M6= .44(%CQ)+ .32(o/oO2)+.28(%N, + 7"69;
o = (20.9 - o/oO2- .5ohCO)/(o/oCOa + %CO)
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Plant Name INTERMOUNTAIN GENERATING STATION Date Q/tclzoz3
Samollnq Location Uurr t S'rr,c-r Prolect #MATS PM Performance
Operator Vicki Lvman F of Ports Used
Stack Type Circular Uleter Box Number
Train Leak Check 1Z PreTestl Z lPostTest itleter Cal Factor {Yt
Molsture Content Data
Run Number Run Start Tlme Run Stoo Time
fotal Meter Volume (v-)dcf Barometric Pressure (Po)in Ho
{vq Meter Temo (t-).*OF Stack Static Pressure (P"uri.)1.00 in H"O
Avg Stack Temp (t")",c -t-(vg Orifice Preseure (AH)*g in H2O
lmpinqer'l lmoinoer 2 lmpinqer 3 Imoinqer 4 lmpinger 5 lmDinoer 6 lmpinqer 7
ml ml ml q ml ml ml
Gontents 100 Water 100 Water 0.00 200 SiGel
Final Value M),(W)4lq rn 14e.?2 1a4292 5145.-7?
nitlal Value M),(W)1t la -h1 l^* tA Lct- zq *t6.6t)
Net Value (v"),(w")
Results
Total Volume (v,)ml ,Vater Vol Condensed (V*,rr,)scf
Total Weight (w)s {Uater Vol Weiohed (V*a"ur)scf
Std Meter Volume (V-,"*r)dscf lat, Moisture Content (B*r"-r)o/o
Calc Moisture Content (B*r"rro)o/o ;inal Moisture Content (B*)%
Moisture Content Data
Run Number Run Start tme Run Stoo Time
lotal MeterVolume (v-)dcf Barometrlc Pressure (Po)in Hq
Avq Meter Temo (r^ )"""OF Stack Statlc Pressure (P 1.00 in Hlo
Avg Stack Temp ( tn)r"s -F Avg Orifice Pressure (AH)",0 in H2O
lmpinqer I lmpinser 2 lmplnoer 3 lmpinqer 4 lmDanoer 5 lmninqer 6 lmoinqer 7
ml ml ml q ml ml ml
Contents 100 Water 100 Water 0.00 200 saGet
Final Value &),(w)qls -11 'T22.ZZ bl>t- 12 E2+.42
lnitial Value {v),w)1t\to-1lo t^Q?. lt)6qq?t4 Bl,)a-q8
Net Value (v.),(w")
Results
Total Volume {V,)ml rlVater Vol Condensed (V'*r"tol)scf
Total Weioht (w)q lVater Vol Weighed (V*",o,nJ scf
Std Meter Volume (V-o,*)dscf Sat. Moisture Content (B*"""r)%
Calc Moisture Content (B*)%Final Moisture Content (B*)%
Moisture Content Data
Run Number 3 Run StartTime Run Stop Time
Iotal Meter Volume (v-)dcf Barometric Pressure (PJ in Hg
Avq Meter Temo (t )n,o
.F Stack Static Pressure (P 1.00 in H,O
Avg Stack Temp (tr)*o -F Avg Orifice Pressure (AH)r"e in H2O
lmDinoer'l lmpinqer 2 lmolnoer 3 lmpinqer 4 lmpinqer 5 lmoinoer 6 lmpinger 7
ml ml ml q ml ml ml
ontents 100 Water 100 Water 0,00 200 SiGel
Final Value (V{),(W)q4c t4 124.44 lo4Z.[ol R49.
lnitial Value M),(Wr)1tq 52 bqz.bt bZ-l.&ln ,(rg.4D
Net Value (v"),(w")
Results
Totai Volume (V,)ml 4VaterVol Condensed (V**,",rJ scf
Total Weight (WJ g Alater Vol Weiohed (V*o,",oJ scf
Std Meter Volume (Vnrrorar)dscf iat. Moisture Content (B*,Yo
Calc Moisture Content (B*")%:inal Moisture Content (B*")to
Plant Name NTERMOUNTAIN GENERATING STATION Date 4lttlzz
SamplinE Locatlon UNIT # STACK Prolect#PM r lir rc'
Operator YICKILYMAN dcetone Lot Number z**tz
Analytlcal Data
Placed ln Deslccator Run Number 2
Number Date Tlme Run Start Timo
Fllter 2_6q IBI?3 ,4,-n LeakaOe Evident?lrl no
Acetono Wash Beaker c2 o{t,4lz't^. ,Q Estlmated Volume ldD ml
Fllter Acetone Dale Time Humldlty T6mp Cal Audit
q q mm/dd/yy hh:mm %RH OF o
ifeasurement 1 (m,r),(mn")D,bo.*r.6E.aEl-r/^allolcz t*',zl Z,-13
Measurrment 2 (mz),(mz")O-LhM tDJ-qq-rs a-ln'lzz tr-t2l 1t)'t?
lleasursment 3 (msr),(m3")
Moasuromont 4 (m<r),(m..)
Rosults Ace lone Blank
Final Weloht (mr),(mr.')s Final Weight (C"')s
Tare Weloht (mu),(m'"')s Iare Weight (c,.)s
Wolotrt Galn (mr),(m.')mg Slank Concentratlon (c.)mg/g
Blank Adlustment (w")mg
Iotal Particulates (mn)mg
Analytical Data
Placed in Desiccator Run Number
Number Date Time Run Start Time
Filtar 3 nclllal22 16:h)Leakaqe Evident?11 136 no
Acetons Wash Beaker e1 rtl,r-l 2a A':29 Estimated Volume rnl
Filter Acetdne Date Time Humiditv Temp Gal A,udit
q o mm/dd/yy hh:mm ToRH OF
s
Measurernent'l (mrr),(mr')o1fi#t1O.t 472 6attel2?:n4:24 32 11
Measurement 2 (m,),(m,")o.b.+-7 tzt.&1/|p[*lzl t2-'..21 1r\1'
Uleasurement 3 (m",),(m"")
m€asurement 4 (mrJ,(mr.)
Results Acetone Blank
Final Wdoht (mr),(m'"')I Final Weiqht (Crr')g
Tare Weiqht (m'r),(m.')I Tare Weioht (Cr"')IWeight Gain (m),(m.')mg Blank Goncontratlon (CJ mg/g
Blank Adiustment (W')mg
Total Particulates (mn)mg
Formulas Used
= average of lagt two filter measurements lTll=lTl1l-lTll W" = C"m*
mN = mbv + IIlr -
tTtn=tTt1 * mn'- Wo
' ; averaEe of last two acetone measurements l=m-l-
MATS Testing Blank Pages - M5 - Anatyticat Page 1 Printed 11t20t2017
APPENDIX D,
Field & Laboratory Data
UNIT 2SGA
Stationary Source Informatlon
Plant NamE INTERMOUNTAIN GENERATING STATION
Fuel Tvoe COAL, BITUMINOUS
Samplinq Location UNIT 2 STACK
Operator VbkiLyman
Date sn412023
Proiect #PM Performance
Base Run Number 1
# of Ports Avallable +
# of PorG Used
Port lnside Diemeter l
Circular Stack?
Rectanqular Stack?
Fuel F-Factor 9780 9780 9780
Test Equipment lnformation
Meter Box Number 1508035 Apex
lUeter Callbration Factor fi)0.9980
Orlflce Meter Coefficient (AHA)1.790 in HrO
Pitot ldentification IPP 007
Pitot Tube CoEfficlent (C,)0.840
frsat ldentification 39-507
Nozzle Number 11
Nozzle Diameter (D.)0.193 tn
Probe Number 1
Probe Lenolh 114.00 in
Liner Material SS
Sample Case I Oven Number 522-14
lmoinoer Case Number 522-1C
Acetone Lot Number 248735
Testim Companv lnformation
ComDany Name lntermountain Power Service Corp
Address 350 W Brush Wellman Rd
Citv State Zip Countrv Delta, UT 84624
Phone Number [phone]
Fax Number 435-864-6470
Plant Name INTERMOUNTAIN GENERATING STATION Date 9t1412023
Samolins Location UNIT 2 STACK Prolect #PM Performance
Ooerator Vicki Lvman F of Ports Available
Stack Tvoe Circular E of Ports Used
Stack Size Large Port lnside Diametsr l
-
Lril
Distance from Port to Disturbances
Distance Upstream (B)3012.00 tn
Diameters UpstrEam (=B/D)(Bo)8.96 diameters
Distance Downstream (A)4274.OO tn
Diameters Downstream (EA/D)(Ao)12,72 diameters
Number of Traverse Points Reoulred
Diameters to
Flow Disturbance
Minimum Number of'
Traverse Points
Up
Stream
Down
Stream
Particulate
Points
Velocity
Points
2.00-4.99 0.50-1.24 24 16
5.00-5.99 1.2s-1.45 20 16
6.00s.99 1.50-1.74 16 12
7.00-7.99 1.75-1.99 12 12
>= 8.00 >=2.00 8 or 12'8 or 12'
Upstream Spec 12 12
Downstream Soac 12 12
Traverse Pts Reouired 12 12
Check Minimum Number of Points for the Upstream
and Downstream conditions, then use lhe largest.
8 for Circular Stacks 12 to 24 inches
1 2 for Circular Stacks over 24 inches
--r-
I
,!.
I
Y
o\4/n stre,orn
fr isturrbonce
lV eo sLr r'ern er''r t
,>t r-e
A Iupetrecn-,I !--I lU,giLtr-OCnCe
'\+ |
I
I
i
E,
I
IYl
Numberof Traverse Points Used
4 Ports by 3 Across
12 Pts Used 12 Required
trt Particulate n Velocity
Tr /Fti.t;dr df Srn.l'Dirilar.r f6il lncidr N
Po int
j 6 s tn
I
1
3
t
6
7
8
I
t0
lt
It
.I{6
.85{
.067
.250
.750
.933
0{4
l{6
296
704
85.1
956
.03!
.r05.lr{
.323
.671
.806
.895
.968
,016
.08!
.r.16
,226
3{2
.65E
,771
.85{
.918
.971
.031
.067
.r r8
.177
.250
.356
.6{{
.750
.823
.E8!
.r33
Traveree Point Locations
Traverse
Point
Number
Fraction
of
Stack
Diameter
Dlstance
from
lnside
Wall
Dlstance
lncluding
Nipple
Lenolh
tn tn
1 0.o44 14 618 23 618
z 0.146 49 58
3 0.296 99 4/8 108 4/8
4
5
6
7
I
9
l0
11
12
Plant Name INTERMOUNTAIN GENERATING STATION Date w14n023
Sampllnq Location UNIT 2 STACK Proiect #PM Performance
Operator Vicki Lvman # of Ports Used 4
Stack Tvpe Circular Pitot ldentification tPP 007
Pltot Leak Gheck tj lPreTestl Lrl lPostTest Pitot Coeflicient (CJ 0.8400
Stack Dlmensions Velocitv Traverce Data
Diameter or Lenoth of Stack (D)336.00 tn Run Number 1-Vl
lltlidth of Stack (W)tn Run Tlme 6:20
Area of Stack (A.)615.75 ff Traverse
Point
Velocity
Head
(ap)
Stack
Temp
(t")
Local
Velocity
(vJrPressures
Barometric Pressure (Pr)24.97 in Hq in H,O "F ft/sec
Static Pressure (P.r"ri")-1.00 In HrO A-1 1.55 90.00 78.4
Absolute Stack Pressure (P.)24.90 in Ho A-2 1.75 92.00 83.4
A-3 1.80 92.00 84.6
Stack Gas Composition B-1 1.30 90.00 71.8
Composition Data: I Actual Estimate lrl B-2 1.65 92.00 81.0
3arbon Dioxide Concentration (YoCOr)13.4 o/o B-3 1.70 92.00 82.2
Sxysen Concentration (o/oO>l 5.6 o/o c-1 1.30 90.00 71.8
Carbon Monoxide Concentration (%co)0.0 o/o c-2 1.s0 e0.00 77.1
llitroqen Concentration (%Nr)81.0 o/o c-3 1.65 92.00 81.0
Stack Moisture Content (B*.)0.130 o/o (0.n)D-1 1.35 90.00 73.1
Stack Dw Molecular Weloht (Md)30.37 lb/lb-mole D-2 1.65 92.00 81.0
Stack Wet Molecular Weioht (M")28.76 lb/lb-mole D-3 1.70 92.00 82.2
Results
Avq Stack Gas Velocitv (v.)78.7 fUsec
Avq Stack Drv Std Flow Rate (Q.")138943036 dscflhr
Avq Stack Drv Std Flow Rate (Q.")2315717 dscf/min 1.58
AvE Stack Wet Flow Rate (oJ 2907572 acllmin
Stack Cross Section Schemadc
Average'1,25 91
Please reporl the average of the square roots of
ao. or. (ao)t'2.* = l/.s(aolz)
Formulas Used
= DWKu for Rectangular Stacks Tc(av0) = '/nEt, + 1,
= (n(Ol2)?)11<"for Circular Stacks where T, = 2TgoKfor melric units
where K, = 1 for metric units where Tu = 460 oR for English units
where I( = 144 (in2tft2) for English units v, = Kpcp(Ap)tn.,l (T<.,gy'(P,M,))t"
" = Pbr, + P.urJ13.6 where 1$ = 34.97 for metric units
= 100 - o/oCO2-o/oO2-o/oCO where lq = 85.49 for English units
= .44(o/oCO) + .32(o/oOz) + .28(7oNz + %CO) Q"o = 3600(1 - B*')v.A'(T",6/Tq"rg)XP'/P$d)
= Ma(l - B*.) + 188*, where T116 = 293 oK, Psra = 760 mm Hg. for metric units
)12oro = l/nr(api'2)where T"a = 528 oR, P"u = 29.92 in Hg, for English units
METHOD 3 . GAS ANALYSIS FOR THE DETERM]NATION OF DRY MOLECULAR WEIGHT
Plant Name INTERMOUNTAIN GENERATTNG STATION Date 9114t2023
Samolins Location UNIT 2 STACK Proiect #PM Performance
Operator Mike Utley E of Ports Used
Fuel Tvpe COAL, BITUMINOUS Vllnimum Fuel Faclor 1.083 lMaximum Fuel Factor 11.230
Orsat Leak Check lvl I PreTest lJl PostTest Orsat ldentification 39-507
Gas Analvsis Dala
Run Number Run Slart Time 7:40 lun Stop Time 9:45
Sample
Analysis
Tima
Carbon
Dioxlde
Volume
&^^")
Oxygen
Volume
(v^.'l
Carbon
Monoxide
Volume
(V. )
Carbon
Dioxide Oxygen
Carbon
Monoxide Nitrogen
Dry
llllolecular
Weight
(M.)
Molecular
Weight
Deviation
{AM,)(%cor)(oloOi (%co)(%Nz)
hh:mm ml ml ml percent percent percent Dercent lb/lb-mole lb/lb-mole
16:20 't3.1 't8.8 13.1 5.7 0.0 81.2 30.32 -0.01
16:31 13.1 18.9 13.1 5.8 0.0 81.1 30.33 0.00
16:50 13.1 18.9 13.1 5.8 0.0 8'1.1 30.33 0.00
ResulG Averaqes 13.1 5.8 0.0 61.1 30.33
Average Calculated Fuel Factor (Fo)o*1 .153 Molecular Wt Deviation < 0.3?
:00 (%il)o*3t.z percent ;uel Factor in Handbook Ranse?
10:10
Gas Analvsis Data
Run Number ?Run Start tme 10:15 Run Stop Time 12:20
Sample
Analysis
Time
Carbon
Dioxide
Volume
ru^^,)
Oxygen
Volume
ru-)
Carbon
Monoxide
Volume
ru^'l
Carbon
Dioxide Orygen
Concentra
(%or)
Carbon
Monoxide Nitrogen
Dry
Molecular
Weight
(M,'l
Molecular
Weight
Deviation
(AM")(%cor)(%co)(%N,)
hh:mm ml ml ml percent percent percenl percent lbflb-mole lb/lb-mole
17;01 't3.5 19.1 13.5 5.6 0.0 80.9 30.38 0.00
17:17 13.5 19.0 13.5 5.5 0.0 81.0 30.38 0.00
17:33 13.5 19.0 13.5 5.5 0.0 81.0 30,38 0.00
Results Averaqes rJ.b 5.5 0.0 81.0 30.38
Average Calculated Fuel Factor (Fo)n,o 1.141 Molecular Wt Devlation < 0.3?
Averaoe Excess Air (%EA)",o 34.6 pe.cent Fuel Factor in Handbook Ranoe?
Gas Analvsis Data
Run Number Run Start Tlme 12:51 Run Stoo Time 14:56
Sampla
Analysis
Time
Carbon
Dioxide
Volume
{v^^")
Oxygen
Volume
(V.r)
Carbon
Monoxide
Volume
(Veo)
Carbon
Dioxlde
Concentra
(o/oCO')
Oxygen
Carbon
Monoxide Nitrogen
llanaaala
Dry
Molecular
Weight
{M.)
Molecular
Weight
Deyiation
(AM,)(%oz)(o/oCO)(%N,)
hh:mm ml ml ml percent percent percent percent lb/lb-mole lbilb-mole
17:44 13.5 19.0 13.5 ET 0.0 81.0 30.38 0.00
17:58 13.5 18.9 13.5 5.4 0.0 81.1 30.38 0.00
18:18 13.5 18.9 13.5 5.4 0.0 61.'l 30.38 0.00
Results Averaoes 13.5 5.4 0.0 u1.'l 30.3E
{verage Calculated Fuel Factor (Fo)ouo 1148 Vlolecular Wt Deviation < 0.3?
qverage Excess Air (%EA)",o 33.7 parcent :uel Factorin Handbook Ranoe?rl
Fuel Factor Fo
Fuel Type Minimum Maximum
Coal. Anthracite 1.016 1.130
Coal, Lignite 1.016 1 .130
Coal, Bituminous 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 1.124
Wood Bark 1,003 1.130
o/oCOr=Y*,
7oO2=Vs2-Vq62
%CO=Vco-Voz
%N2 = 169 -o/oCO2-o/oQ2-o/oCO
= .44(7oCOz)+ .32(%O2l+.28(%Nz + %CO)
o = (20.9 - YoO2- .5o/oCOJl(%CO2 + %CO)
Plant Name NTERMOUNTAIN GENEMTING STATION Date 9t1412023
Samplinq Location UNIT 2 STACK Proiect #PM Performance
0perator Vicki Lvman f of Ports Used 4
Stack Tvoe Circular Meter Box Number 1 508035
Train Leak Check lvl I PreTest I l.rl I PostTest Meter Cal Factor ff)0.998
Moisture content oata
Run Number Run Start Tlme 7:4O Run Stoo Tlme 9:45
fotal Meter Volume ru-)93.626 dcf Barometric Pressure (P")24.97 in Ho
Avg Meter Temp (t.).,o 80 OF Stack Static Pressure (Prr")1.00 in H,O
Avg Stack Temp (t,)*o 117 .F 4vq Oriflce Pressure (AH)o,e 1.69 in HzO
lmoinosr I lmolnqer 2 lmolnqer 3 lmplnqer 4 lmplnqer 5 lmpinqer 6 lmoinoer 7
ml ml ml q ml ml ml
Contents '100 Water 100 Watet 0.00 200 SiGel
Final Value (V,),(W)896,92 721.65 602.04 824.88
lnitial Value (v,).(w)706.55 663.54 597.76 803.80
Net Value (v,),(w,)190.4 38.1 4,3 21.1
Results
Total Volume (v,)232.84 ml lllater Vol Condensed (V*rorar)10.958 scf
Total Weioht (w)21 10 s Illater Vol Weiohed (V*"r"trJ u.995 scf
Std Meter Volume (V^,.,n,)76.596 dscf sat. Molsture Gontent ( B*rrror) 12.7 Yo
Calc Moisture Content (B*r"rr.r)13.5 3lnal Moisture Content (8".)12.7 o/o
Moisture Content Data
Run Number Run Start Time 10 15 Run Stoo Tlrne 12:20
Total Meter Volume (v-)93.156 def 3arometric Pressure (Ph)24.97 in Ho
Avo Meter Temo (r-)","84 r Itack Static Pressure (P 1.00 in H"O
Avg Stack Temp (L)*n 118 -F {vq Orifice Pressure (AH).,0 1.67 in H2O
lmoinoer {lmoinoer 2 lmoinqer 3 lmoinqer 4 lmpinqer 5 lmpinqer 6 lmoinoer 7
ml ml ml q ml ml ml
Contents 100 Water 100 Water 0.00 200 SiGel
Final Value M),(W')917.66 730.22 632.1 I 838.56
lnitial Value M),(W,)720.14 691.'t4 628.1 6 614.40
Net Value (v"),w.)197.5 39.1 4.0 224.2
Results
fotal Volume (v,)240.60 ml WaterVol Condensed {V*r.raJ 11.325 scf
Total Weioht (WJ ZZ4,2U s Water Vol Welqhed (Voorum)10.571 scf
Std Meter Volume (V*'o,)75.647 dscf Sat. Moisture Content {8,13.1 to
Calc Moisture Contenl (B*)22.4 Yo Final Moisture Content (B*")13.1 %
Moisture Content Data
Run Number Run Start Time 12:51 Run StoD Time 14:56
Total Meter Volume (v-)93.223 dcf Barometric Pressure (Pb)24.97 in Ho
Avo Meter Temo (t-)",o 87 OF Stack Static Pressure (P 1.00 in H,O
Avg Stack Temp (L)u"s 120 -l-Avg Orifice Pressure (AH)o's 1.64 in HrO
lmoinoer I lmpinger 2 lmolnoer 3 lmoinqer 4 lmplnqer 6 [mpinqer €lmpinqer 7
ml ml ml a ml ml ml
Contents 100 Water 100 Water 0.00 200 SiGel
Final Value (VJ.(W,)905.03 725.93 601,42 823.32
lnitial Value (VJ,WJ 707.51 682.85 597,36 843.72
Net Value (V.),(W")197.5 43.1 4.1 19.6
Results
fotal Volume (V')244.70 ml lVater Vol Condensed (Vwcrrrar)11.518 scf
IotalWeight (WJ 19.60 s lVater Vol Weished (v 0.924 scf
Std Meter Volume (V*ot t)75.279 dscf Sat. Moisture Content (B*rr,or)13.8 o/o
Calc Moisture Content (B*)14.2 otto linal Moisture Contenl (B*)13.8 to
METHOD 5. SAMPLE ANALYTICAL DATA SHEET
Plant Name NTERMOUNTAIN GENERATING STATION Date 9114t2023
Samollno Location JNIT 2 STACK Prolect #PM Performance
Cperator ,/icki Lvman Acetone Lot Number 248735
Analytical Data
Placed ln Deslccator Run Number ,|
Number Date Time Run Start Time 7:4O
Fllter 4 09114t23 10:37 Leakase Evident?lll no
Acetone Wash Beaker c4 ow15n3 8:41 Estimated Volume 175 ml
Filter Acetone Date Tlme Humldlw 230 Cal Audit
o o mm/dd/w hh:mm %RH oF q
Meagurement 1 (mr),(m'.)0.6103 129.28ffi 09118t23 4:24 32 73
Measurement 2 (mr),(mr,)0.6103 129.2846 09118123 12:21 30 72
Measurement 3 (m:),(m:J
Measurement 4 (mor),(m.J
Results Acetone Blank
Flnal Weioht (m"),(m,,')0.6103 129.2846 q Final WdEht (Ca')129.899'l s
Iare Weight (mn),(m"')0.6105 129.2778 E fare Weioht (c,,)129.8992 s
/Veioht Gain {mr),(m"')-0.2 6.8 m0 Blank Concentration (c.)0.0000 mq/s
Blank Adiustment (w,)0.0000 mg
fotal Particu[ates (m")b.o mg
Analytlcal Data
Placed in Desiecator Run Number 2
Date Time Run Start Time 10:15
Filter 5 49114123 14'.45 Leakase Eviden0 I J,l no
Acetone Wash Beaker c5 09115t23 8:41 Estimated Volume 135 ml
Filter Acetone Date Time Humiditv Temo Cal Audit
o q mm/dd/w hh:mm %RH OF o
i,teasurement 1 (mt),(mr,)o.6121 136.9909 09t18t23 4'.24 32 73
Uleasurement 2 (mr,),(mrJ 0.6120 136.9908 09t18t23 12:21 30 72
Measurement 3 (m"),(m"J
Measurement 4 (m.),(m.o)
Results Acetone Blank
Final Weight (mn),(mr,')o.6121 136.9309 s =inal Weight (C',')129.8991 s
Iare Weight (mtr),{m.')0.6123 136.9849 s fare Weioht (c,"')129.8992 g
Welqht Galn (m),(m,')-0.2 6.0 mg 3lank Concentration (c")0.0000 mg/g
Blank Adjustment (w,)0.0000 mg
Total Particulates (m")5.8 mg
Analytical Data
Placed in Desiccator tun Number 3
Number Date Time ?un Start Time 12.51
Fllter 6 09t14t23 15i22 -eakaqe Evident?ltl no
Acetone Wash Beaker tJo o9115t23 8:41AM Estlmated Volume 140 ml
Filter Acetone Date Time Humidity Temp cal Audit
o q mnVdd/w hh:mm o/oRH "F a
Measurement I (m',),(m'")0.6091 127.4166 o9118t23 4:24 32 73
Measurement 2 (mr).(mr^)0.6092 127.4166 09118123 12:21 30 72
Measurement 3 (m"J,(m"J
Measuroment 4 (m.,).(m.")
Results Acetone Blank
Final Weight (mn),(mr"')0.6092 127.4166 s Final Weight (Gr,')129,8991 s
Tare Weisht (m,r),(m"')0.6093 127.4104 s Tare Weiqht (Co')129.8992 s
fVeiqht Gain (m),(m"')u.1 6.2 mg Blank Concentratlon (c,)0.000c mg/g
Blank Adjustment (w.)0.0000 mg
l'otal Particulates (mn)6.1 mg
= average of last twD tilter measuremenls
' = averaqe of last two acetone measuremenls
El1= lTll1 - lTl1l IlV, = Comn* lrln=m1 + Do' - Wo
m"'= mt'- IYlr"' lllle= [T15** lTl".- ITlrb
lsrmrllno Locdion lUNIfz STACK lProloctil | PM Pcrformanco I
t
l# of Pointr Acrorr lg ll of portr Uscd h I
ld.rl t{ozl. Dlimatcr rnd haKlnrtlc F.ctor S.luo
,ltoi Tubo Cocffkl!nl (c.)0.E40
\vq Slrck TrmD (Ll 91 -F
\Yo G!3 f,lctor TGmD lL)81 "F
IH @ 0.75 SCFil t8F.@'1.79 in HrO
\vo Pllot Tubo Ollf, Prmrur!(dD-*)1.58 in H,O
Itsck Mol5tur! Conlont (B..l 13.0 % (xx.x)
It ck DrY tlolrcuhrwolqht (M*l 30,37 hrlb-mol.
:allmrtod or[i4 Flffi R.tG (o-)0,730 rcfr
, to AH lioklnrllc Frclor 0(l 1. t5
lBrromoirrcprorsure | tp"l I z+.gz I inHs J
Slmollno Eoulomonl
lrGbr*1 508035
lrlbr Crllbrrilon Frclor Nl I 0.s9E0 I
Vorzlr #1
lcill Nozlc Dirmollr (D-l I 0.193 I in
do.l Nozlr Dhmot.t (D"r} 10.182 I in
,robo #, Lonqlh 114.00 I in
-lnal M.l.rlrl rs
iDol. C8c, Ovan ,i22-1A.
malnoer crto I i?2-1Q
AV- Lc.kch.c*r
tra 0 fi'/mh o 9 in Ho
nld ll'/min ID in Ho
toal 0 lt'rmin @ 10 in Ho
tv- < 0.020 ltlmin k1 ck?
,lloa OK?E )rqt ox? lA
Travotsc
Polnt #
Slmpllng
Tlmr
(el
Clock
Tlmo
Ory Cr3
lrotor
tcadlng
tv_l
VGI*lty
Ho.d
{Ap)
Dlslrod
Orilico
AH
IAH)
Actu.l
Odncc
alt
IAH)
SLck
TmP
(Ll
t olor
lnlot
T.mp
tL,)
ilct?t
Oudct
Tomp
Itl
Fllior
T.mp
lmplng0r
Exit
Tcmp
Psmp
Vacuum
Squrre
Rool
AP
(apta)
Local
Slrck
Volocaly
lv-1,
gumutlllYG
Motor
Volumo
av-t-.
gumutaflyo
Porconl
lsoXincllc
lll
mm hhmmrst h H,o in H,O in HrO .F "F 'F .F in Ho rh H,ol"'fusec sd rh
A-1 0.0 7:aO:OO 256 1,t3 tao 162 _62 tt4 73 73 300 82 6.1 1.18 76.07 6.376 to3 3
A-2 10.0 7:50:00 263.E07 1,65 1.91 e5 11t 75 75 32'.|55 6.5 1.28 82.58 13.018 10't.1
A-3 20.o 8:00:00 271.847 1.70 197 92 114 77 77 323 56 7.O .30 83.82 1g_847 '100.9
B-1 30.0 8:12:00 280.1 40 1.35 1.57 .54 1,l6 79 79 3'18 56 8.0 l6 74.83 26.062 101.3
g.)400 8:22:00 2A7 7rO 1.50 1.74 .58 1,t 8 80 80 315 59 5.5 ?)7E.0.l 32 378 oo-9
B-3 500 8:32:00 295.452 165 .t 91 85 'I't9 a2 82 320 58 7.0 .28 82.94 39.007 00.6
c-1 60.0 8:43:00 303.579 1.30 1.51 .45 119 a2 82 309 5g 6.8 14 73.62 44.984 o0.7
c-2 70.0 8:53:00 310 922 1.40 1_62 .55 1t9 83 83 310 58 6A t8 76.10 5t -05.1 00.5
c-3 80n 9:03:00 318.390 1 stt 174 56 rtg 83 83 321 62 7.0 .22 7e 08 57 7{)o0.3
D-1 90.0 9:15:00 326.120 1.40 1.62 .55 ',18 83 83 318 53 6.1 1.18 76.33 63.,142 o0.2
o-2 100.0 9:25:00 333_622 1-55 1.80 .74 1t9 84 8{319 60 70 1.24 80.39 69.e63 00.'l
D.3 110 0 9:35:oo 341.528 1.6S 1.9'l -87 1t8 84 84 318 61 7.2 ,28 82.47 76 537 00.1
Last Pt 120.0 9:,t5:00 349.739
:inal Vrlut 120.0 9:45:00 349.73S nu6 Vacuum 7.2 FIn.l VrlIca 76.537 '100.1
Vrlu6t .69 117 80 80 3.16 5S t,??
EO
l.Pr*
lfotpotnrsAcro$ 13 l*otponguroa lq I
ldGrl NozIG Olrmrtor ad lioKlndlc F.ctor SctuD
Pllot Tubc Coltllclonl tc"l 0.84q
AYo Strck TomD lLl 117 -F
W! G.! Illctor TomD (L)85
$l @ 0.75 scFl'l (AH@}1.79 in H"O
lvq Pllot Tuba Dlt . Prcrsura (aD-"l 1.50 an H,o
Shck Molrluro Conilnl (B*)13.0 %
Strck Dry tlol$uhr Wolght rM-t 30.33 lb/lb{ol.
Ertlm.trd Orltlco Flow Ralo to-)u- /a!tctm
tP to aH liokinltic Frctor aKt 1.12
lBsomatricProrrura I tprt la+.gz I ,rns I
ls
Srmnllffi EouiDmnt
llctca ,506035
Ictor Crllbrallon FrEtor m I 0.9980
{ozl. il 1
lctul Nozalo Dlrm.lGt (O-)10.193 I in
do.l Nozln DiDGtct (Dil) | 0.192 in
troho f , Lonoth 114-00 I in
-lnor Mrtorhl
iamolo Cto I Ovon #,22-14
molndsr Cise #i22-1C
AV- Loak Chlaki
,te o n'/min i @ 10 in Ho
lild ll"imin @ irr Ho
,o3l 0 Itr,lmin @ 10.5 in H0
Iv- < 0,020 ft'/min )k )k?
,lt6t OX?4 )rml Ox?IJ
Travorgc
Polnt f
Srmpling
Tim!
(o)
Cloch
Timo
ory G.s
Me lor
Rordln0
tv-_l
Voloclty
Hoad
(ap)
Ocrlmd
Orlrlco
AH
IAHI
Aclu.l
OrlllcG
AH
(aH)
Strck
Tomp
Irl
MGlor
lnlot
Tcmp
It .1
Mot.,
Outlol
Tomp
Ir -t
Flllor
TsIIP
lmplnger
Exit
Tomp
Pump
Vacuum
Squaro
Root
AP
(apra)
Locrl
Srrch
Volocity
Cumuhllvc
Motor
Volumo
Cumulrtva
Pcrcont
!]oNinotic
ln
min hhtmm:ss tt h HrO in H.O in H.O -F -F .F t -F in Ho (in H2O)(usac rcl .a
D-1 0.0 I 0:1 5:0( 350.307 1.40 1.57 1_49 '117 79 79 310 62 5.5 1.18 76.31 6.1 34 99.6
D-2 10.0 10r25:O(357_7S5 1-50 1_68 1.67 117 80 80 315 5t 5.8 1.22 78.99 '12.171 99.5
D-3 200 l0:35:0t 365.542 1.60 7.79 1-00 1t8 a2 a2 3,t 8 19 62 1.26 41.65 19.O08 9S.d
c-1 30.0 '10:47:0[373_558 1.20 1.U 1.38 117 83 83 313 53 5.5 1.10 70.65 24.841 too I
c-2 40.0 l0:57:0t sEO.737 1.35 1.51 1-44 '11 I 84 84 322 52 5.5 1.16 75.00 30.743 99,6
c-3 50.0 1:07:Ot 388.O1 I 1-50 1.68 1.70 118 85 85 322 53 6.1 1.22 79.06 37.046 9S.5
B-1 ao.0 1'18:Ot 395 785 130 1 .16 r50 18 85 85 320 56 67 114 73 60 43 284 100 3
a-2 70.0 11:2E:0[ 403.489 1.50 1.68 1.68 118 86 86 320 59 8.0 1.22 79.06 49.295 99.5
B-3 80.0 l1:38:0t 410_915 1.60 1.79 1.42 118 86 86 319 59 7.O 1.26 E1.65 55.849 99.5
A-r 90.0 l1:50:0t a.r s.ot0 1.45 1.62 r.65 t9 a7 a7 315 5g 62 120 77.aO G2.144 99.6
A-2 roo 0 l2:OO:0t i?6.ao5 {60 179 181 ,,t 0 87 87 317 5g 8.9 1.26 at 77 68.756 997
110.0 1 2: I 0:0[434.985 1.70 1.90 1.97 119 88 88 317 60 7.2 1.30 84.24 75_599 99,8
La3t Pt 120_O 12:2Otol 443.463
rinal Vrlur 't20.0 12]20"OO 443.463 Mrxlmum Vlcuum 7.2 Firnl Valuog 75.599 99.E
lvarado 1.47 118 64 34 317 56 121 -ra 31
84
)
I
,
ldaal Notzlc Di.mctrr.nd l3oKlnlllc Frcloi SetuD
ribi Tubr Coofficlcnt (c")0,640
No St cI T.mE (.)118
\vo Geg Motcr Temp (r-I 87 .F
rH 6' 0,75 ScFItt (ai1@)1.79 in HrO
Uo PltotTub3 Dlff. Pr€srun (AD-)1.44 h H"o
It ck Moi3turu ContBnt {B*)12.7 alo
It ck Drv Molecul.rW.loht (M"J lbrb.mol.
irumeied Orificc Flow R.t (o-)0.775 acfm
lP to AH l3oklnotlc Feclor {Kl 1.12
Srmollno Eoulominl
llct r#I 508035
![rt tC.libr.lion Frctor il) I 0.9980
tlozda #tl
lcturl Nozzle Dlamotcr (o".)t 0.193 I h
darl Nouzlo Dirmrtor (0"Jt0.192t h
,robc # / Lcnoth I 114.00 I h
-lncr Melrrirl >D
rmlle Crre I Ov.n *522-1A,
molnrar Cs3c *i22-1C
AV- Le:k Chscks
,fg 0 ttrrmh @ 9.5 hHo
ffd fi7mh @ in Ho
,o3t 0 tl'lmh @_I in Hq
w- < 0.020 It"imh )k ck?
,ltot OK?lErtOK?IJ
Cumulrtv.
P6rcsnt
lsoKlnctlc
100.0
1 00.1
METHOD 5. SAMPLE RECOVERY AND INTEGRITY DATA SHEET
Plant Name NTERMOU NTAIN GENERATING STATION lDate I 9t1412023
Samolino Location UNIT 2 STACK Proiect #PM Performance
Cperator y'icki Lvman Acetone Lot Number 248735
Run Historv Data
Run Number 1 z 3
Run Start Time 7:40 10:15 12:51 (hh:mm)
Run Stop Time 9:45 12:2O 14:56 (hh:mm)
Irain Prepared By VL VL VL
Irain Recovered Bv VL VL VL
Recoveru Date 9t1412023 9t14t2023 9t1412023 (mm/dd/vv)
Relinouished Bv nla nla nla
Received Bv
Relinquished Date (mm/dd/yy)
Relinouished Time (hh:mm)
Equipment ldentificatlon Numbers
Filter 4 5 6
Acetone Wash 121715 E 121715 E 121715 E
Silica Gel DRP.12.1OB DRP.12.1OB DRP.,12-1OB
lmDinoer Case 522-1C 522-1C 522-1C
Sample Box 522-1p' 522-1A 522-14
Oven 1 3s0G 1350G 1350G
Formulas used
V- = V.-=V-+where o* = .9982
Molsture Content Data
lmoinqers 1. 2. and 3 - Water Volume
Final Volume (Vr)2220.6 2280.1 2232.4 s
lnatial Volume (VI)1987.9 2039.4 1987.7 q
Net Volume (v")232.7 240.7 244.7 s
Comments
lmoinqer 4 - Silica Gel Weioht
Final Weight (WJ 824.9 838.6 823.3 s
Initial Weight (W,)803.8 814.4 803.7 q
Net Weisht (w")21.1 224.2 19.6 g
3omments
Total Water Collected
Total Volume (v.)253.8 465.3 264.3 s
IPP_PM_U2_9_14_2023 - M5 - Recovery Page 1 Printed 1012612023
Table 3
METHOD 5 - DETERMINATION OF PARTICULATE EMISSIONS. RESULTS
Plant Name NTERMOUNTAIN GENERATING STATION Date 9114D023
BamDlanq Location UNIT 2 STACK Prolect #PM Performance
Operator Mcki Lvman Stack Tvpe lircular
Hlstorica! Dala
Run Number 1 2 3 Averaqe
Run Start Tlme 7:4O 1O:'15 12:5'l KUnS 1,z,
and 3
hh:mm
Run Stop Time 9:45 12:20 14'.56 hh:mm
Ileter Callbration Factor rn 0.998 0.99E 0.998
Pitot Tube Coelficient (c,)0.840 0.840 0.840
lctual Nozzle Diameier (D-)0.193 0.193 0.193 ln
Stack Test Data
lnltlal MeterVolume (V-)r 256.113 350.307 445.231 ft"
Final Mster Volume (V.)t 349.739 443.463 538.454 fi"
Total Meter Volume u-)93.626 93.156 93.223 93.335 ft"
Total Samnlinq Time (o)120.0 120.O 120.O 120.000 mtn
Averaoe Meter TemDerature (r^).""80.0 84.0 87,0 83.667 OF
Avcraoe Stack Temoerature (t)n,o 117.O 118.0 120.0 118.333 r
Barometric Prcssure (Pr)24.97 24.9t 24.97 24.974 in Ho
Stack Static Pressurc (P*tJ -1.00 -1.00 -1.00 -1.000 in H"O
Absolute Stack Pressure (P.)24.90 24.gtJ 24.90 24.900 in Hq
Average Orifice Prassure DroD (AH)*1.6S 1.6t 1.44 1.667 in H"O
Absolute Meter Pressure (P,)25.09 25.09 25,09 25.090 in Hq
Avg Square Root Pitot Pressure (Apto)*1.22 1.21 1.20 1.210 (in HrO)
Moisture Content Data
.mDinoors 13 Water Volume Galn (v.)232.7 240.7 244.t 239.367 ml
mpinqer 4 Silica Gcl Weiqht Galn (wn)21.1 224.2 19.6 88.300 s
lotal Water Volume Collected (VJ 253.8 465.3 264.3 327.EOO ml
itandard Water Vapor Volume (V,)ro 11.946 21.902 12.441 15.430 sct
Standard Meter Volume (V-)ra 75.596 75.647 75.279 75.841 dscf
Salculated Stack Moisture (Bwrrotct)13.5 22,5 14,2 16.733 ol,
laturated Stack Moisture (B***r)12.7 13.1 13.8 13_200 0/6
leported Stack Moisture Content (B*.)12.7 13.1 13.8 13.200 o/n
Gas Analvsis Data
Carbon Dloxlde Percentaoe &co,)13.'1 13.5 't3.5 13.367 c/o
Oxygen Percentage l%az)5.8 5.5 5.4 5.557 c/c
Carbon Monoxlde Percent oe (%co)0,0 0.0 0.0 0.000 o/o
Nitrooen Percentase (%Nr)81.1 81.0 81.'t 81.067 o
Dry Gas Molecular Weiqht (Ma)30.33 30.38 30.38 30.363 lb/lb-mole
Wst Stack Gas Molecular Waloht (M.)28,67 27.59 28.62 28.293 lbflb-mole
Calculated FuGl Factor (F")1.153 1.141 1.148 1.147
Fuel F-Factor (Fo)9780 9780 s780 9780.000 dscfrmmBtu
Percent Excess Alr (q/oEA)37.2 34.6 33.7 35.167 oh
Volumetric Flow Rate Data
Average Stack Gas Velocitv (vJ 78.76 79.70 77.74 78.733 ff:/sec
Stack Cross-Sectlonal Area (&)615.75 615.75 615.75 615.750 ft'
{ctual Stack Flow Rate (Q.)2909788 2944517 2872104 2908803 acfm
lrv Standatd Stack Flow Rate (Q-)1 916785 1734840 1 866944 1839523 drcftn
Percent of lsokinetic Rate {t)101.0 1'10.1 101.9 t04.333 oh
Emlsslon Rate Data
Mass of Particulate on Falter (mJ -0.2000 {.2000 -0.1000 -0.167 mg
Mass of Particulate in Acetone (m.')6.8000 6.0000 6.2000 6.333 ME
Mass due to Acetone Blank w")0.0000 0.0000 0.0000 0.000 mg
Total Mass of Particulates (mJ 6.6 5.8 6.1 6.167 mq
Stack Particulato Concentratlon (cJ 0.0001 0.0001 0.0001 0.000 s/dscf
(c.)0.0015 0.0015 0.uu15 O,UUz gr/dscf
Partioulate Emission Rate (E)11.50 10.41 11.20 11.04 ko/hr
(E)21.8 17.6 20.0 19.8 lbs/hr
G)0.0026 o.oo22 u.ou24 o,oo24 lbYmmBtu
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 Traverse Points in Circular Stacks
Traverse
Point
Nurnber
(Fraction of Slack Dimension from lnside Wall to Traverse Point)
Number of Traverse Points Across the Stack
2 4 6 8 10 12
1 .146
.854
067
250
750
933
.044
.146
.296
.704
.854
.956
.032
.105
.194
.323
.677
.806
.895
.968
026
a82
146
226
342
658
774
854
918
974
.021
.067
.1'18
.177
,250
.356
.644
.754
.823
.882
.933
.979
2
3
4
E
6
7
I
I
{0
11
12
Location of Traverse Points in Rectanoular Stacks
Traverse
Point
Number
(Fraclion of Stack Dimension fiom Inside Wall to fraverse Polnt)
Number of Traverse Points Across the Stack
2 3 4 5 6 7 8 I 10 11 12
1 .250
.750
167
500
833
.125
.375
.625
.875
100
300
500
700
s00
.083
.250
.417
.583
.750
.917
.071
.214
.357
.500
.643
.786
.929
063
'188
313
438
563
688
813
938
.056
.167
.274
.389
.500
.611
.722
.833
.944
.050
.150
.250
.350
.450
.550
.650
.750
.850
.950
.045
.136
.227
,318
.409
.500
.591
.682
.773
.E64
.955
042
125
208
292
375
458
542
625
708
792
875
958
2
3
4
5
6
7
8
I
l0
11
12
IPP_PM_U2_9_14 2023 - Fraction of Diameter Page 1 Printed 1013112023
isoCALC UNITS
Unitr l{eme Teblc
Unltr
Number
l{.tlvG
llemr
Englbh
1 Enolish Enolish
2 Metric tc
3 Blank
;urrent Unlt Numb.,I
Unlt: Lookuo Tablc
Engllsh
I I nltr
Motrlc
llilk
rc
"K
in mm
in cm
tn m
tt m
lt'ln'
mo
dc,dqn
3cf 3cln
dscf dscm
cfm cmm
acftn acmm
It"/min m"/min
dsctrtr dscmm
dsc-f/mln dscrn/min
dscr/h( dscm/hr
'lusec mArec
in H"O mm HeO
in Ho mm Ho
ln Hq kPa
(ln H,O)(mm HrO)"'
lb/lb-mole o/o-mole
o/dscf o/dscrn
sr/dscf o/dscrfl
lb/hr ko/ht
Con3tants Lookuo T.ble
Conitant
Namo
Con3t nt
Svmh^l
Currcnl
Valuc
Current
I lhlt
Engllth
Vrhrr
English
l.lnltr
Mrtrlc
Valuc
M6trlc
UnltB
rroe stack Dlamater (C"")24 tn 24 tn 0.61 m
nchea oer Foot (C.r)12 inlft 12 in/fl 1 m/m
nches per Foot mm plr MGl6r (C^'12 irVft 12 in/fl 1000 mrn/m
Uaximum Allowable Lcrk Rst€(G*)0.42 rlm 0.02 cfm 0.00057 m'/min
{ozzle Ol.mrtor Conrtrnt (c")0.03575 ?0.0357s I 607.1 ?
( Factor Conrtrni (C.)849.8 ?849.8 ?8.038E.05 ?
tltot Tube Conslant K 85.49 rleXin Ho))r 85.49 :le)(n Hs))/34.97
t etor llrolsture contont G*)0.00 %0.00 oA 0.00 %
tloter Dry Molecuhr Welsht (M,-)29.00 lbflb-mole 29.00 lb/lbmola 29.00 gig-m016
,rcasurG Orop ln G!3 Mlter (P,-)o.25 in HrO 0.25 ln H"O 6.35 mm HzO
lbrolut Tsmplreture Offscl T..460 "R 460 273 -K
Itindard Absoluto Pre3sure Pra 29.92 in Ho 29.92 in Ho 760.00 mm Hg
3t.ndard Absoluta Tempcraturc T.,. 528 328 .R 293
ltandard Volumo Corroctlon Kr 17.64 "R/in Hg 17.64 "R/in Hs 0.3858 "l(mm Hg
lv.tor Volume to Std W.tor Vrpor Kr 0.04707 ft"/ml 0.04707 fi'/ml 0.001333 mJml
soklnetic Variatlon - Raw Drta Kr 0.002669 HoFfl'/ml-"0.002669 Hg-fi"/ml-'0.003454
3oklnetlc Varle0on - lntermedlete 1(.0.09450 ?0,09450 ?4.320 ?
,Valcr Ma.r to Std Wrter V.por Ks 0.0r'.715 tr"/g 0.il715 n"/9 0.001 335 m"/g
)eor6€s F to Dcoreas C MultlDller t&'1.000 -FTF 1.000 -FTF 1.800 "Ffc
Degrec3 F to Daqrec! C Offrot Kr 0.000 0.000 .F 32.00 "F
Millimotcrr p.r lnch Kr 1.000 in/in 1,000 ilvirl 25.40 mm/in
Sramr per Pound Kr 1.000 inlin 1.000 in/in 25.40 mmrin
Denrltv of Weler 0*0.9982 o/ml 0.9962 o/ml 0.99E2 g/ml
IPP_PM_U2_9_1 4_2023 - Units Page 1 Printed 10/31/2023
Plant Name INTERMOUNTAIN GENERATING STAION Date 9-r4ZO2 3
Samollno Location UNIT#STACK.Z-Proiect #r)x,i1L
Operator -/1,lol*"d-Run #1
# of Polnts Across # of Ports Used 4
ldeal Nozzle Diameter and lsoKinellc Faclor Setup
Pitot Tube Coefficient (c")0.840
Avq Stack Temp (r.)OF
[vo Gas MeterTemp (t,)F
\H @ 0.75 SCFM (aH@)in H2O
Avq Pitot Tube Diff. Pressure (40""^)in H"O
itack Moisture Content (B*")9'. (xx.x)
itack Dry llilolecular weicht (MrJ lb/lb-mole
istimated Orifice Flow Rate (Q,)acfm
!P to AH lsokinetlc Factor K)
Samolinq Equipment
Meter #
Meter Calibration Factor ry)
tlozzle #
Actual Nozzle Diameter (D.^)tn
ldeal Nozzle Diameter (D,r)tn
)robe * I Lenqth 1 144.00 I ft
Liner Material SS
Samolc Case / Oven #522-1B
moinoer Case #522-1C
Pressures
3aromotric Pressure (Pn)in Ho
3tack Static Pressure (P'o*)in HrO
Absolute Stack Pressure (P.)in Hg
Absolute Meter Pressure (P",)in Hg
AV- Leak Checks
Pre e tlo/min @ q in Ho
\rid fto/min @ in Hg
)ost -a-fto/min @ /D in Ho
tv- < 0.020 fto/min U ok?
ritot OK?W Orsat OK?w
Traverse
Point #
Sampling
Time
{e)
Clock
Time
Dry Gas
Meter
Reading
(v-)
Velocity
Head
(AP)
Desired
Orifice
AH
(AH)
Actual
Orlfice
AH
(AH)
Stack
Temp
(t.)
Meter
lnlet
Temp
{r-,}
Meter
Outlet
Temp
(r-J
Filter
Temp
lmpinEer
Exit
Temp
Pump
Vacuum
min hh:mm:ss ft"in H"O in H"O in H"O UF UF "F "F UF in Hq
D-1 0.0 t:40 1#-./13 ,,4t /.t
"hZ
//q oc)7 Z,
D-2 10.0 '.-,qo ,tt"l.Zrfr /./"d ,l l,X{tlh 7.1 ?<-wt tI q
D-3 20.0 9'/.al L7.l.Qcl:o t.9+?1 7 77 723 ,rt 4.,
c-1 30.0 3't7 ?Rb.lLlA t7A t,5 I lri //t +vt )47,6.O
c-2 40.0 9'72 187.7qA t,90 t,v4 lt 4 EO ilE L,5
c-3 50.0 ,l' 1,7 ffi4<1 /,ad /,q //.F</,/{
1l(g1 7L <2 A n
B-1 60.0 9'41 <fY r*/,4 ,,5 '/g 7 72 24.I /-, P
B-2 70.0 3;€3 10.917 /.4,l,laZ ,,6 lll 3 ,3 s/i)q7 ta
B-3 80.0 g,D3 ?t?-fi/)l,r<A l. tt :3 ra .37-l /, ?- /')
A-1 90.0 ,1,; 15 <%. tac./, qo /, /- 7-/,{5 9t
A-2 100.0 q.L{1.?1,L7)l,s5 LfrN ,,74 g*7 7D
A-3 1 10.0 1.'i5 E/t.f13 t.cd tgI t.*rl a)7;L
Last Pt 120.0 9'4
"4q,7iq
Flnal Value 120.0 Maximum Vacuum
Averaoe Values
I ISOKINETIC SAMPLING DATA I
Plant Name INTERMOUNTAIN GENERATING STATION Date ,lq,ZOZ3
Sampllnq Location UNIT 1 STACK Prolect #fi,t z
OpErator Rick Moodv Run #
# of Polnts Across 3 I of Ports Used
ldeal Nozzle Dlameter and lsoKlnetic Factor Setup
Pitot Tube Coefficient (C,)U.U4U
Avo Stack Temo (t")F
Avg Gas Meter Temp (h)-F
!H @ 0.7s scFM (^H@)in HzO
Avs Pitot Tube Diff. Pressure (Ap,*)in H"O
Btack Molsture Contont (B*")% Oo<.x)
3tack Drv Molecular Weioht (M&)lb/lb-mole
Estimated Orlfice Flow Rate (Q.)acfm
AP to AH lsokinotic Factor (K)
SamplinE Equipment
lleter #
lllster Calibration Factor (Y)
tlozzle *
Actual Nozzle Diameter (D-)tn
ldeal Nozzle Diameter (D")ln
Probe # / Lenoth 1 114.00 I in
Liner Material SS
Sample Case I Ovsn *,22-14
imDinoer Case #122-1c
Pressures
Barometric Pressule (Pr)in Ho
Stack Static Pressure (P""n)in H,O
Absolute Stack Pressure (P.)in Hq
Absolute Meter Pressute (P-)in Ho
AV^ Leak Checks
Pre -e-fro/min @ ,/n in Ho
Mid ff'/min @-in Hg
Post &ft"lmin @ /o,{in Ho
av- < 0.020 ft"/min n 0k?
Pitot OK?T Orsat OK?il4
Traverce
Point #
Sampling
Time
(o)
Clock
Time
Dry Gas
Meter
Reading
(v.)
Veloclty
Head
(Ap)
Desired
Orifice
AH
(AH)
Actual
Orilice
AH
(AH)
Stack
Temp
{L)
Moter
lnlet
Temp
{L,l
Meter
Outlet
Temp
{L-l
Filter
Temp
lmplnger
Exlt
Temp
Pump
Vacuum
mrn hh:mm:ss flo in H"O in H,O in H,O "F r .F ,F in Ho
A-1 0.0 l0!t{3SO,?al /,t/o t17 /4'il1 4q 71 i//)bL fi{
A-2 10.0 lD't q ?\?.zl i.eTi l,/.x t:i il7 7 xo ?td ,f/,{, y
A-3 20.0 |rt)' 7(il,g-qrl2 ,Ld t+q 1,9e2 AZ t el'{I,, Z
B-1 30.0 //1'47 q41.K#/.10 t,?q /,.77 )t f'tr.?3l<r?r.r
B-2 40.0 ln,#3*n.1?a l-?{l,S I l"l8 /tr 8.1 ???-5.L.,q-g
B-3 50.0 Il:a7 ?E*-Rr I t,co t"/R l,+D ltx '{ffd q22 53
c-1 60.0 il'H <x{18nthlrlfr /.?f)l,.l t"l,s'e lst ,{s{32D .5f.5,7
c-2 70.0 n'7_?l,Fr)l.bv I,LY t1 ,6 3L ?7D q9 1^, f)
c-3 80.0 1,,3P {ENF LAt)),7q t.?2 n lb f(3tq 6ti ?f)
D-1 90.0 t|{o {lr.Dr t,i{I,LZ-l.Lq il ar]tCr|d1 g7T .a'f-]
D-2 100.0 lau{,rlal.po\
'O
q It t)t.x,4t1,E b,q
D-3 110.0 tz it fJ t-'9ll l.1f)l6 t^q Jll T_?E .3t?6D .=..r.
Last Pt 120.O thi.4t
Final Value 120.0 Maximum Vacuum
Averaqe Values
I ISOKINETIC SAMPLING DATA I
' t ri
Plant Name INTERMOUNTAIN GENERATING STATION Date q . / 1,7,D7-3
SamDlinq Location UNIT 1 STACK Proiect #l)^,?L
Dperator Rick Moodv Run #?
I of PoinB Across 3 $ of Ports Used
ldeal Nozzle Dlameter and lsoKinetlc Factor Setup
Pitot Tube Coefficient (c")0.840
Avg Stack Temp (t.)"F
Avq Gas Meter Temp (t-)OF
[H @ 0,75 SCFM ( H@)in H2O
Avs Pltot Tube Diff. Pressure (Ap.*)in HzO
Stack Molsture Content (B-.)% 0o(x)
Stack Dry Molecular Weight (MoJ lb/lb-mole
=stimated Oritico Flow Rate (Q,)acfm
AP to AH lsokin.tic Factor (K)
Sampling Equipment
Ueter #
lileter Gallbration Factor (Y)
llozzle #
4ctual Nozzle Diameter (Do.)tn
deal Nozzle Diameter (D")tn
>robe # / Lensth 1 114.00 I in
-iner Materlal SS
lample Case / Oven #522-14
mpinqer CasG # 522-1C
Pressures
Barometric Pressure (Pb)in Ho
Stack Static Pressure (P*t.)in H"O
Absolute Stack Pressure (P,)in Ho
Absolute Metsr Pressure (P.)in Ho
AV. Leak Checks
,rg €fl'/min @ 9,9-in Ho
l,!id fl"/min @ in Ho
Post +fl"/min @ YrO in Ho
av- < 0,020 fl'/min n ok?
Pitot OK?W Orsat OK? ll!j/
Traverse
Point #
Sampling
Time
(o)
Clock
Time
Dry Gas' Meter
Readlng
(v-)
Velocity
Head
(Ap)
D€sired
Orifice
AH
(AH)
Actual
Orifice
AH
(AH)
Stack
Temp
(r)
Meter
lnlet
Temp
(Lr)
Meter
Outlet
Temp
(L^)
Fllter
Temp
lmplnger
Exit
Torirp
Pump
Vacuurn
mtn hh:mm:ss ft'in H.O in HrO in HrO .F r "F r -F "ln.Ho
A-1 0.0 Ut<l ryls.2it ItnO /.{7 /,<7 hfi 9.L 7D?b.L 5;d
A-2 10.0 l?:Dl 4!/,1
cf,l.Z
/,/K /. Bd't.90 )20 ,.E 1/,r4 {,,8
A-3 20.0 t3;1,t,%Lq0 AYC /k\tr-x{322 S8 fii.F)
B-1 30.0 /A'2A^*g.oEl /,Lo rt34 t,4i /rt>'/o 9L L,6,F
B-2 40.0 t ?:2.7 L)ld.5#l,'{5 1,62 l./^6 /tv N"31 i3lE b-7 /., D
B-3 50.0 t2'tJ 7 -d$-iid !.,(d:.n69-lr2 Vfi-ffi-tffi-',q?a a6q-,rt,f
c-1 60.0 t7,F t4 ft7*$qlm.m h?;ls L\t'l 1.1{-il ET ffi ?r?b/"t5l{-
c-2 70.0 tLt'hu l,4t)q1 ]-gv./KO ", a-.x'w?.h{'d, /*
c-3 80.0 tu: lu .,{'r?,AA t.?,1 )t r1 *7?7 h7
D-'1 90.0 tu'zfr hqz ''4D Lm.l,'/".h llt Jt.r {-:{/,,o
D-2 100.0 /,{,'3 t?5l2,Llh l,Ko l, lot {,+l lt'32t b2_a, Z-
D-3 110.0 tl;4 b b,2*Q t.trt ,+g t.qa /70 v?trt 3ZL 1^<5
Last Pt 120.0 t4 4/ i,/ ,
Final Valu(120.0 Maximum Vacuum
Averaoe Values
I [,lo
l6:: r
.L,,SO
Gas Analvsb Data
Run Number 2 Ron Shrt lm6 Run StoD TimsSample
Analysis
Time
Garbon
Dioxlde
Volume
O:<ygen
Volurne
Carbon
Monoxlde
Volumo
Garbon
Dloxide
Cnnaarla
Oxygen
Garbon
Monoxide Nltrogen
Dry
Molecular
Weiobt
Molecular
Welght
Devlation(V*)(VoJ (Vco)(%G02)(oAOr)(%co)(%N.',|(Md)(AMd)hh:mm ml ml ml Drrcenl percent DAlcent psrcent lb/lb-mole lb/lb-moleI I tlt I lZ, f 1.1- I
l', : l',l<,1q. ar7'.??t<.<l'lrA
FaeSulls Averages
Rvorags uatcuteted Fust Factor (F")*"urotEeutar wt Dev,afion < 0,3?I69E(%EA).s percent iuel Factor in Handbook Ranoe?r
its Analvsis Dala
Run Number ?lrn Slrr* Ti--Run Stoo TlmeSample
Analysis
Tima
Garbon
Dioxide
Volume
Oxygen
Volume
Carbon
Monoxide
Voluma
qarDon
Dioxlde Oxygen
Concsntra.
Carbon
Monoxide Nitrogen
Concentrle
Dry
Molecular
Weloht
Molscular
Welght
Deviation(Vco)(Va)(Vc-o)%cor)(%Or)(7oCO)(7oNz)(Mc)(Atvld)ml ml ml percent
l-7: rl t,percent percent percent lb/lb-mole lb/lb-molets. t lat Ol": f{1".<".qlat t4 t5,l R,q
Resulls AVeraqgs
qvorage Calculated Fuel Factor (Fo)o*Motecul'r Wf nrvi2ll^^ < n a2 J(%EA)*pBrcent uet Factor ln llandbook Ranse?_l
Fuel Factor Fo
;uel Type Minimum Maximum
Anthracite t.016 1.130
Llgnite 1.016 1.130
3oal, Bituminous 1.083 1.23A
Oil, Dlstillate 1,260 1.413
Oll, Residual 1.21D 137A
Gas, Naturat 1.600 1.836
Gas, Propane 1.434 1.586
iag, Butane 1.405 1.553
Wood 1.000 1.120
ffood Bark 1.O03 1.130
= 100 -%COa -YoO2-%CO
= .44lohCAz)+ .32(%Ozl+.28(%Na + %CO)
o = (20.9 - %O2- .5yo}O)t(o/oCe+ yggl
E!
oz
o
E
E
o
!J
o
5c
E
oI
E
o
F
o
oo
C
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tt
t
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4
o
B
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s
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rf
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ss
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€
uiI(
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tir
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Ft(\
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go
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t!]uaso
co
C)i*
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i.)*!
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Plant Name INTERMOUNTAIN GENERATING STATION Date I / A ltbz*
Sarnpllnq Locatlon llN ff 2 sfAok Proiect #MATS PM'Performance
Operator r'icki Lyman I of Ports Used 4
Stack Type ]ircular Meter Box Number
Traln Leak Check 14 lpreTestl Z lpostTest Meter Cal Factor (Yl
Moisture Gontent Data
Run Number Run Start ime tun Stop Time
fotal Meter Volume (v,)dcl Barometrlc Pressurc (Po)in Hq
dvs Meter Temp (tr)"*OF Stack Static Pressure (Pr.tiJ -1.00 in H"O
Avg Staek Temp (t").ro .F
Avg Orlffce Pressure (AH)*e in H2O
lmpinqer I lmolnoer 2 lmolnoer 3 lmoinqer4 lmoinqer 5 lmpinser 6 lmpinser ?
ml ml ml o ml ml rnl
Contents 100 Water 1ff)Waier 0.00 200 SiGel
Final Value (vr,(w)99.1a,q2--lr-r-L1 t-62-b4 rzc.tn
lnitial Value M),(W,)1Db.A6 baa.4.+4q'?-1b go8 qD
Net Value (v^),(w")
Results
Total Volume M)ml Water Vol Condensed (V*t"rar)scf
Total weiqht (w)s Water Vol Welohed M scf
Std Meter Volume (V-oo,)dscf Sat Moisture Content (B*r.*r)o/o
Calc Moisture Content (B*r*r"r)o/o Final Moisture Content (B*)o/o
Moisture Content Data
Run Number z Run Start Time Run Stop Time
fotal Meter Volume (v-)dcf Barometric Pressure (Pr)in Ho
Avo Meter Temo (L)"*OF Stack Static Pressure (P.",i.)1.00 in H"O
Avg Stack Temp (tJ*c -F Avg Orifice Pressure (AH)",0 in HrO
lmninqer 1 lmoinoer 2 lmoinoer 3 lmpinqer (lmpinoer 5 lmoinoer 6 lmoinoer 7
ml ml ml g ml ml ml
Gontents 100 Water 100 Water 0.00 200 SiGel
Final Value (v),(w)il1 .Lla la,,.rz bz2Jq *,38,-51^
lnitial Value (Vr),(W,)tzD.t4 tAt- 1&r-28.tt uul 4h
Net Value (v"),(w")
Results
Total Volume (v,)ml Water Vol Condensed (V*rrrt)scf
rotal Weiqht (w)s Water Vol Weiohed (V*or"tor)scf
Std Meter Volume (V-r"raJ dscf Sat. Moisture Content (B*r"-t)o/o
Calc Moisture Content (B*")%Final Moisture Contenl (B*)o/o
Molsture Content Data
Run Number Run Start me Run Stop fime
Total Meter Volume (v*)dcf Elarometric Pressurc (Po)in Hq
Avg Meter Temp (h)"*"F Stack Static Pressure (P^trn.)1.00 in H:O
Avg Stack Temp (t")",s -F {vg Orifice Pressure (aH)o"c in H2O
lmoinoer'l lmpinqer 2 lmplnqer 3 lmDinoer 4 lmplnqer 5 Impinqer 6 lmpinoer 7
ml ml ml q ml ml ml
Contents '100 Waler 100 Water 0.00 200 SiGel
Flnal Value M),Wr)bq.oc 126;.q4 (Dbl-42 azi3.z2
lnitial Value M),W)-t h1 ^t51 6t2.45 1q1 .?-t-9D1:lz
Net Value (v"),(w")
Results
Total Volume (v,)ml {l/ater Vol Condensed (V*,rto,)scf
Total Weioht (w)s Water Vol Weiohad (V*ot"tor)scf
Std Meter Volume (Vmrsar)dscf Sat Moisture Content (B*,*t)%
Calc Moisture Content (B*)Yo Final Moisture Content (B*)o/o
METHOD 5 -SAMPLE ANALYTICAL DATA SHEET
Plant Namo NTERMOUNTAIN GENEMTING STATION Date q lLtlL3
Sampllnq Location JNIT#STACK Prolect #PM tlrrtt ?
3pelEtor /ICKILYMAN dcetone Lot Number 24s17q
enaMical Data
Placed ln Desiccator Run Number 2
Number Date Time Run Start Tlme
Fllter q oelnllzZ t4:+1 LeakaEe Evident?,l no
Acetone Wash Beaker c6 tal lrl'.t.t na:41 Estlmated Volurne t3< ml
Filter Abetbne Date Tlme Humidtty Temp Cal Audlt
o 0 mm/dd/w hh:mm %RH "F q
lUoasurement 1 (ms),(mr.)O.l.l2l laLqDq oqlalzz ^4.1 2.1 e)'t3
Lleasurernent 2 (mzr),(mzn)0.t t zD taLnqD9 r;pl tdlcz t ,-! r,zn '12-
Ueasuremont 3 (mrr),(m*)
Vleasurement4 (m.r),(m.J
Results Acetone Blank
Final Weioht (md,(m,"')q Final Weight (t h I g
Tare Weioht (md,(m,"')q Iare Weight (Cr')s
Weiqht Gain (mr),(m,')rns Blank Concentration (c")mg/g
Blank Adiustment (w")mg
Total Partlculates (m^)mg
Analytlcal Data
Placed in Desiccator iun Number J
Number Date Time Run Start Tlme
Fllter 1-o4lwlzt I Fq22 Leakage Evident?IA no
Acetone Wash Beaker 4-lo te I tEli*Ao.Zt Estlmated Volume l4D ml
Fatter ,dbet6ne Date Time Humidity Temp Cal Audlt
q q mm/dd/yv hh:mm %RH OF s
lueasurement I (mtr),(mr")D-t^nQ I o,'t,4u,1,oqlnlq-e rl'qi ?)-l*
Measurement 2 (m2r),(mrJ n.Lrg,,2'13[tldl/rpl,c'lz2 , ar 2z,uf)-lr)
It|easurement 3 (msr),(m&)
Measurement 4 (mor),(m-)
Results Acetone Blank
rinal Weight (mn),(mr"')s =inal Weaght (Cr.')s
l"are Woisht (m,r),(mt"')s fare Weight (C'"')g
Welqht Gain (mr),(m"')mg 3lank Concentration (c.)mg/g
Blank Adiustment (W')mg
Total Pafticulates (mJ mg
Formulas Used
= average of lasttwo filter measurements
' = average of last two acetone measurements
IIll=IIlg-IIil Wo = Com*mn=mt + Dr'- Wo
'= m,-t -mtu=mbe+
MATS Testing Blank Pages - M5 - Analytical Page 1 Printed 1112012017
EhIDIX E
& TEST FORMI]LAE
Symbols and Units for Nomenclature used in Calculations
I
l
Meter Calibration Factor Y
Pitot Tube Coeflicient cp
Actural Nozzle Diameter Dnn tn
Initial Mefer Volume Vr(t)fd
Fiual Meter Volume Vrnrr)ft3
Total Meter Volume v,,ff
Total Sampling Time o mtn
Average Meter Temperature tnr(arg)0tr,
Average Stack Temp erature ts(rvg;,F
Barometric Pressurc Pb in Hg
Stack Static Pressure Pstatic in [I2O
Absolute Stack Pressure P,in Hg
Average Orifice Pressure Drop AH:rvg in HzO
Absolute Meter Pressure P*in Hg
Avg Square Root Pitot Pressure ap"'o",in H2OI2
AvgPitot Tube Diff. Pressure APurg in HzO
Impingers 1-3 Water Volume Gain vn ml
Impinger 4 Silica Gcl Weight Gain wn db
Total Water Volume Collected Vt.rnl
Standard Water Vapor Volume Vw(std)scf
Standard Meter Volume Vm(srd)dscf
Calculated Stack Moisture Bns(calc)oh
Saturated Stack Moisture Bnsls,p;%
Reported Stack Moisture Content 8,".%
AP to AH Isokinetic Factor K
Carbon Dioxide Percentage %co o/o
Oxygen Percentage o/rOz oA
Carbon Monoxide Percentage YICA %
Nitrogen Perceatage o/oNz %
Dry Gas Molecular Weight M6 Ib/Ib-mol
Wet Stack Gas Molecutar TVeight M,lb/lb-mole
Calculated Fuel Factor R
Fuel F-tr'actor Fd dscflmmBtu
Percent Excess Air %EA %
Average Stack Gas Velocity vo ftlsec
Stack Cross-Sectional Area As fe
Actual Stack f,'low Rate Qo acfm
Dry Standard Stack Flow Rate Qea dscfm
Percent of Isokinctic Rate I o/o
Mass of Particulate on f ilter Illg mg
Mass of Particulate in Acetone mo mg
Mass due to Acetone Blank wi mg
Total Mass of Particulates mn mg
Stack Particulate Concentration
cs g/dscf
cs grldscf
Particulatc Emission Rate
E kg/hr
E IbsArr
E lbs/mmBtu
Orifice Meter Coeflicient AH@ in H2O
Nozzle Diameter Dn tn
Distance to Far Wall of Stack Lr',IN
Distance to Nerr Wall of Stack Lot*m
Diameter of Stack D tn
Distance Upstream B in
Diameters Upstream BD diameters
Distance Dorvnstream A m
Diameters Dorvnstream AD diametsrs
Avg Stack WetFIow Rate Qo,,,acflmin
Carbon Dioxide Volume Ycoz ml
Orygen Volume voz ml
Carbon Monoxide Yolume Vco ml
Molecular Weight Deviation AMa Ib/lb-mole
Weight Final wr grams
Weight Initial wr grams
Weight Total wt grams
Weight Net w,grams
Volume tr'inal \rr ml
Volume Initial vi mI
Volume Total vt ml
Volume Net %ml
Water Vol Condensed Vrvt(std)scf
Water VoI Weight V*sggtd)scf
AvgOrifice Pressure Afln*c in H2O
Estirnated Orifice FIow Rate Qr ecfm
Yelociy Head Ap in II2O
Meter Inlet temp tmt ,F
Meter Outlet temp tro oF.
Blank Concentration c"melg
Blank Final Weight Cro grams
Blank Initial Weight C,,grams
Yelocity Stack Local %r ftlsec
Standard Barometric Pressure at SL = 760 Pstd Mm Hg
lrtl
1)
Exarrple Caleulation
Dry gas volume at slandard eonditions.
Qa-3 5 0 0( I - B*)vJE(TsE/Ts(a.,r))tp/p,,a)
Where leza=293oKrPr*=760tnmIlg, for metric ulits
i&relre Tau=528oR,Pr"u=29-92 in IIg, English r:'its
t+O CFR Pt.6O,App.A, Method. 2 Equatioa 2-LOj
Stack Velociti at sE,a.ck conditions
vr-I(rCr(ap)' o*s(I"r."a/(PMD r'
lftrere Kr=34 -97 for metric r-rnitsa
rstrere It=85.49 for Engl.ish r.rnits
l+O CER PE..6'0,APP-A, Method 2 Equatsion 2-91
Fraction of moiBture ia staek g:as
B.o=V*t",ay'V-raat+V-t",al
[+O CFR PE.-5O,App.A, Metrhod. 5 Equation 5-3]
Percent Isokinetsic
7oI=V.1061+T"*P 16* 1 0 0/60 * Tdd'*Vr* 0*4*prt (1 -BJ
[+o cFR Pt.60,App.A, Method 5 Eguation 5-8J
Volume of dry gas samp3-ed at btandard conditions
V.t,o=[Y,YTrd/TrrKPb+aIV13 .O/P,u]
[40 CFR Pt.50,App.A, Method 5 EEration 5-1]
2l
3)
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6) Mol.ecular weight of dry gas
Mf . 4 4 (%CO) +.3 2(%O z)+.2 s t%Nz+% Co)
Laa CI'R pt.60,App.A, Method 3 EEraEion 3_11
7l Vo1rrme of water vapor colLected iq standardcondition
V*:I( W1o
[4a. crR pt-60,App.A, Met]rod 4 Eguatlon 4_zl
A) Fuef- factor
F,<2O.O-%oOz-.SyoCO)/(y"CO2WoCA)
t+O CFR pe.GO,App.A, Method 38 Eguat.j.on 3B_fl
9) Molecular weiglet of wet gas
tuIr=IvI6(L-B.,)+18B*
lqa eFR pt-Gg,App_A, Method. 2 Equation 2_51
10) Stack Pressure
Pr=P*.tPodi"/13.6
t40 cFR pt-GO,App.A, Method 2 Eqrration 2_GJ
11) parEiculate Coneentration
C.=(lVf, AIa",6f (. 0 0 I ) =gidscfl4 f Flb/hr
[+O CFR pt,.G'0,App.A, lvlethod 5 Eguation 5_E]
13)
t2)Emiesioa r
B=C,Bdl20,AD0.
E+O CFR Pt.50
* E <c,eeg air
Metbod 19 Bquation L9-1J
.?.64/aNr(%Q-.57oC0)
[+o cER Pt.60,.4, Method 38 Eguatloa 38-31
L4l Actrual gtack volume at stack cond.ftf.on
Q.:Vr*4*3600:FtB
15)Bit'uminoug coa fueL F fact,or for various fuel,s
F6Factol=9780 06gal
t*a cFR Pt.50,.A, Metbod 19 Table 19-xJ
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Method 1 Absence of Cyclonics Verification
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Method 1 Absence of Cyclonlcs Verification
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APPENDIX G
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SEPTEMBER.a5,202,2
,F*MEASURED DIGITAL CALIPERSI'i
0.194-s"
ocToBER 25,2023
POST . TEST MEASUREMENT
"*MEASURED WITH DIGITAL CALiPERSN *
Tube End View
Tube I{o,A B C Average
1'l 0.1945'0.i950"0.1935"0.1943"
Pitgllqbe d Ptob-g Assemby (As Installed - re-fer to image on page 2.)
NOTES:
CERTIFICATION
I certifiT that pitot tube numbet T?F oo-T 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: tf - P q-P .?
INTERMOUNATI N POWER SERVICE CO RPORAT]ON
850 W Brush Wellman Rd
Delta, UT 84624
TEM PERATURE SEN SOR CATIBRATION
Temperature Element (TE) lD: Exit Probe
Temperature Element Type: Thermocouple, "K" Type
Date:
Calibrated by:
Barometric Pressure:
Ko Adj Conversion 460
10124/2023
Vicki Lyman
24.85 (in. Hg)
(AdJusted to Elevation)
Fixed Point Reference Reference (oCl TE value (oF) %Diff (K'I
lce Water 0 32 .0.0
Stack Gas 59 136 O.Z
Boiling Water 91 t94 0.2
NOTE: %Diff must be < +\- L.5% of Kelvin:(Ref"C + '/() - (TE "C +'K)
100 (Ref'C +'K)11.5o/o
TE Result:l PASS
INTERMOUNATIN POWER SERVICE CORPORATION
850 W Brush Wellman Rd
Delta, UT 84624
TE M PE RAT-V R E.s_E ly $O R CALI B RAfl ON
'emperature Element (TE) lD: TE 4323
Temperature Element Type:
Date:
Calibrated by:
Barometric Pressure:
Ko Adj Conversion 460
Thermocouple, "K" Type
L012412023
VickiLyman
24,8s (in. Hg)
(Adlusted to Elevation)
Fixed Point Reference Reference (oCl TE valqe (oFl %Dift $o I
lce Water 0 32 0.0
Stack Gas 59 137 0.1
Boiling Water 91 L94 0.2
NOTE: %Diff must be < +\- 1.-5% ot Kelvin:(Ref"C+'K)-(TE'C+"K)
100 ( 7.50/o(Ref'C +'K)
TE Result:l PASS
INTERMOUNATIN POWER SERVICE CORPORATION
850 W Brush Wellman Rd
Delta, UT 84624
TEM PERATURE SENSOR CALI BRATION
emperature Element (TE) lD: TE432O
Tem perature Element Type:
Date:
Calibrated by:
Barometric Pressure:
Ko Adj Conversion 460
VickiLyman
Fixed Point Reference Reference (oCl TE value fF) 7pDiff (K')
lce Water 0 32 0.0
Stack Gas 59 737 0.1
Boiling Water 91 194 0.2
NOTE: %Diff must be < +\- 1.5o/o of Kelvin:(Ref"C + "K) - (TE "C +'K)
(ReFC + "K)
INTERMOUNATIN POWER SERVICE CORPORATION
850 W Brush Wellman Rd
Delta, UT 84624
rEru PERATURE SENSOR CALTBRATTON
emperature Element (TE) lD: Stack Temperature Probe
emperature Element Type:Thermocouple, "K" Type
Barometric Pressure:
Ko Adj Conversion 450
lce Water 0 35 -0.5
Stack Gas 57 134 0.1
Boiling Water 88 188 O.2
NOTE: %Diff must be < +\- L.5% of Kelvin:(Ref'c + "K) - (TE'C +'K)
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Product Numben L*?t -tLO
Product Nome: Grode 934-AH circles, 110 mm, 100/pk
Lot Number/Seriol Number: gOZlZZg
Conformonce & Quolity systems stotement
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All products ore monufoctured vio o Quolity System certified to BS EN lSO900lZ00g 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
Reference Method 5 - PM10
Source Information
Company Name Intermountain Power Service Corporation - Unit SGA-1
Company Contact:Mike Utley
Contact Phone No.435-864-6489
Source Designation:Unit SGA-1
Test & Review Dates
Test Date: 9/13/2023
Review Date: 12/7/2023 Tabs Are Shown
Observer:Robert Sirrine
Reviewer:Robert Sirrine
Particulate Emission Limits
lbs/MMBtu lbs/hr gr/dscf
0.015
Emission Rates - "Front Half"
lbs/MMBtu lbs/hr gr/dscf
0.0036 30.5618 0.0019
Test Information
Stack_I.D._inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn
336.00 615.75 0.9980 1.79 0.84 24.97 -1.00
0.193
Contractor Information
Contracting Company: Intermountain Power Inhouse
Contact: Mike Utley
Phone No.: [phone]
Project No.:
9780
Round
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
Intermountain Power Service Corporation - Unit SGA-1
Testing Results Lab Data - grams collected
Test Date 9/13/2023 9/13/2023 9/13/2023 9/13/2023 Lab Data Probe Filter Back
Round Run 1 Run 2 Run 3 Run 4 Run 1 0.0123 -0.0006
As ft^2 615.75 615.75 615.75 615.75 Run 2 0.0056 0.0001
Pbar 24.97 24.97 24.97 24.97 Run 3 0.0108 -0.0003
Pq (static)-1.00 -1.00 -1.00 -1.00 Run 4
Ps 24.90 24.90 24.90 24.90
Avg. Ts F 121.00 121.08 121.08 Front Half Emissions Summary
CO2 - FCO2 13.30 13.50 13.50 0.00 Run 1 Run 2 Run 3 Run 4 Avg.
O2 5.70 5.50 5.50 0.00 gr./dscf 0.0024 0.0011 0.0022 0.0019
N2+C 81.00 81.00 81.00 100.00 lbs/hr 38.6521 18.3082 34.7252 30.5618
Md 30.36 30.38 30.38 28.00 lbs/MMBtu 4.600E-03 2.161E-03 4.083E-03 0.0036
Ms 28.59 28.61 28.61 28.00
Y 1.00 1.00 1.00 1.00
Cp 0.84 0.84 0.84 0.84 Total Emissions Summary w/back half condensable
Vm cf 92.15 95.32 93.40 0.00 Run 1 Run 2 Run 3 Run 4 Avg.
Vlc 282.50 274.15 285.97 gr./dscf 0.0024 0.0011 0.0022 0.0019
AVG. Tm F 79.83 85.50 88.33 lbs/hr 38.6521 18.3082 34.7252 30.5618
Vm std 75.40 77.19 75.25 lbs/MMBtu 4.600E-03 2.161E-03 4.083E-03 0.0036
Vw std 13.30 12.90 13.46 #VALUE!
Bws 0.15 0.14 0.15
S Bws 0.14 0.14 0.14
Avg. Sqrt
Dlp 1.21 1.21 1.21
Vs 78.61 78.28 78.57 F factor used
scfm wet 2.1961E+06 2.187E+06 2.195E+06 9780
acfm 2.904E+06 2.892E+06 2.903E+06
Qsd dscfh 1.130E+08 1.124E+08 1.129E+08
# Sample
Points 12.00 12.00 12.00 12.00
Dn 0.19 0.19 0.19 0.19
An 2.03E-04 2.03E-04 2.03E-04 2.03E-04
Total Test
time 120.00 120.00 120.00 120.00
Time @ point 10.00 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
%
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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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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
%
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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
Intermountain Power Service Corporation - Unit SGA-1Flow & Moisture Test Date 9/13/2023
As ft^2 Pbar Pq (static) Ps Avg. Ts F
CO2 - FCO2 O2 N2+C Md Ms
615.75 24.97 -1.00 24.90 121 13.30 5.70 81.00 30.36 28.59
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1427
0.9980 0.84 92.145 282.50 79.83 75.399 13.297 0.1499 0.1427 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time Time @ point Avg. Dlh
1.212 78.61 2,196,061 2,904,086 1.13E+08 12 0.193 120 10.00 1.650000
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out)Imp. Liquid Collected
1 970.380 1.450 1.55 121 73 73 Wt. (end) Wt. (start) lc
2 977.811 1.550 1.74 121 74 74 918.1 716.0 202.1
3 985.622 1.600 1.80 121 76 76 743.2 689.6 53.6
4 993.606 1.300 1.46 121 78 78 632.9 626.4 6.6
5 1000.818 1.450 1.62 121 79 79 835.8 815.5 20.3
6 1008.402 1.600 1.82 121 81 81 0.0
7 1016.470 1.250 1.44 121 81 81
8 1023.864 1.550 1.74 121 82 82 Isokinetics 102.1
9 1031.668 1.600 1.80 121 83 83 Test Date 9/13/2023
10 1039.708 1.300 1.47 121 83 83
11 1047.038 1.400 1.57 121 84 84
12 1054.542 1.600 1.79 121 84 84
13 1062.525
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
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46
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48
Page 1
Run 2
Intermountain Power Service Corporation - Unit SGA-1Flow & Moisture Test Date 9/13/2023
As ft^2 Pbar Pq (static) Ps Avg. Ts F
CO2 - FCO2 O2 N2+C Md Ms
615.75 24.97 -1.00 24.90 121 13.50 5.50 81.00 30.38 28.61
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1430
0.9980 0.84 95.317 274.15 86 77.186 12.904 0.1432 0.1430 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time Time @ point Avg. Dlh
1.207 78.28 2,186,609 2,892,001 1.12E+08 12 0.193 120 10.00 1.66
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out)Imp. Liquid Collected
1 65.206 1.40 1.50 122.0 80.0 80.0 Wt. (end) Wt. (start) lc
2 72.580 1.50 1.71 122.0 81.0 81.0 915.17 706.76 208.4
3 80.298 1.60 1.83 121.0 83.0 83.0 722.22 682.10 40.1
4 88.412 1.20 1.40 121.0 84.0 84.0 601.12 595.94 5.2
5 95.658 1.40 1.55 121.0 84.0 84.0 824.42 803.98 20.4
6 103.134 1.50 1.69 121.0 86.0 86.0 0.0
7 110.991 1.40 1.56 121.0 86.0 86.0
8 118.505 1.50 1.70 121.0 87.0 87.0 Isokinetics 104.1
9 126.328 1.50 1.82 121.0 88.0 88.0 Test Date 9/13/2023
10 134.471 1.40 1.59 121.0 88.0 88.0
11 143.220 1.55 1.83 120.0 89.0 89.0
12 152.428 1.55 1.73 121.0 90.0 90.0
13 160.523
14
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17
18
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20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
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Run 3
Intermountain Power Service Corporation - Unit SGA-1Flow & Moisture Test Date 9/13/2023
As ft^2 Pbar Pq (static) Ps Avg. Ts F
CO2 - FCO2 O2 N2+C Md Ms
615.75 24.97 -1.00 24.90 121 13.50 5.50 81.00 30.38 28.61
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1430
0.9980 0.84 93.402 285.97 88 75.248 13.461 0.1517 0.1430 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time Time @ point Avg. Dlh
1.211 78.57 2,194,872 2,902,930 1.13E+08 12 0.193 120 10.00 1.67
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out)Imp. Liquid Collected
1 160.880 1.40 1.55 122.0 84.0 84.0 Wt. (end) Wt. (start) lc
2 168.164 1.60 1.80 121.0 86.0 86.0 939.13 719.5 219.6
3 176.248 1.65 1.87 121.0 87.0 87.0 734.45 692.6 41.8
4 184.492 1.30 1.47 121.0 87.0 87.0 632.61 627.9 4.8
5 191.844 1.45 1.64 121.0 88.0 88.0 839.17 819.4 19.8
6 199.535 1.55 1.78 121.0 89.0 89.0 0.0
7 207.579 1.20 1.38 121.0 89.0 89.0
8 214.734 1.50 1.72 121.0 89.0 89.0 Isokinetics 102.1
9 222.548 1.60 1.74 121.0 90.0 90.0 Test Date 9/13/2023
10 230.566 1.30 1.52 121.0 90.0 90.0
11 238.098 1.50 1.74 121.0 90.0 90.0
12 246.020 1.60 1.88 121.0 91.0 91.0
13 254.282
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Source Information
Division of Air Quality
Compliance Demonstration
Reference Method 5 - PM10
Source Information
Company Name Intermountain Power Service Corporation - Unit SGA-2
Company Contact:Mike Utley
Contact Phone No.435-864-6489
Source Designation:Unit SGA-2
Test & Review Dates
Test Date: 9/14/2023
Review Date: 12/8/2023 Tabs Are Shown
Observer:Robert Sirrine
Reviewer:Robert Sirrine
Particulate Emission Limits
lbs/MMBtu lbs/hr gr/dscf
0.018
Emission Rates - "Front Half"
lbs/MMBtu lbs/hr gr/dscf
0.0024 20.5624 0.0013
Test Information
Stack_I.D._inches As ft^2 Y Dl H @ Cp Pbar Pq (static)Dn
336.00 615.75 0.9980 1.79 0.84 24.96 -1.00
0.193
Contractor Information
Contracting Company: Intermountain Power Inhouse
Contact: Mike Utley
Phone No.: [phone]
Project No.:
9780
Round
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
Intermountain Power Service Corporation - Unit SGA-2
Testing Results Lab Data - grams collected
Test Date 9/14/2023 9/14/2023 9/14/2023 9/14/2023 Lab Data Probe Filter Back
Round Run 1 Run 2 Run 3 Run 4 Run 1 0.0068 -0.0002
As ft^2 615.75 615.75 615.75 615.75 Run 2 0.006 -0.0002
Pbar 24.96 24.96 24.96 24.96 Run 3 0.0062 -0.0001
Pq (static)-1.00 -1.00 -1.00 -1.00 Run 4
Ps 24.89 24.89 24.89 24.89
Avg. Ts F 117.25 118.00 119.67 Front Half Emissions Summary
CO2 - FCO2 13.10 13.50 13.50 0.00 Run 1 Run 2 Run 3 Run 4 Avg.
O2 5.80 5.50 5.40 0.00 gr./dscf 0.0013 0.0012 0.0013 0.0013
N2+C 81.10 81.00 81.10 100.00 lbs/hr 22.0969 19.3844 20.2059 20.5624
Md 30.33 30.38 30.38 28.00 lbs/MMBtu 0.00257 0.00225 0.00236 0.0024
Ms 28.74 28.75 28.67 28.00
Y 1.00 1.00 1.00 1.00
Cp 0.84 0.84 0.84 0.84 Total Emissions Summary w/back half condensable
Vm cf 93.63 93.16 93.22 0.00 Run 1 Run 2 Run 3 Run 4 Avg.
Vlc 253.84 464.79 264.26 gr./dscf 0.0013 0.0012 0.0013 0.0013
AVG. Tm F 80.42 84.33 86.92 lbs/hr 22.0969 19.3844 20.2059 20.5624
Vm std 76.51 75.58 75.26 lbs/MMBtu 2.574E-03 2.246E-03 2.356E-03 0.0024
Vw std 11.95 21.88 12.44 #VALUE!
Bws 0.14 0.22 0.14
S Bws 0.13 0.13 0.14
Avg. Sqrt
Dlp 1.23 1.21 1.21
Vs 79.04 78.30 78.06 F factor used
scfm wet 2.2218E+06 2.198E+06 2.185E+06 9780
acfm 2.920E+06 2.893E+06 2.884E+06
Qsd dscfh 1.162E+08 1.146E+08 1.131E+08
# Sample
Points 12.00 12.00 12.00 12.00
Dn 0.19 0.19 0.19 0.19
An 2.03E-04 2.03E-04 2.03E-04 2.03E-04
Total Test
time 120.00 120.00 120.00 120.00
Time @ point 10.00 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
s
o
k
i
n
e
t
i
c
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
s
o
k
i
n
e
t
i
c
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
s
o
k
i
n
e
t
i
c
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
Intermountain Power Service Corporation - Unit SGA-2Flow & Moisture Test Date 9/14/2023
As ft^2 Pbar Pq (static) Ps Avg. Ts F
CO2 - FCO2 O2 N2+C Md Ms
615.75 24.96 -1.00 24.89 117 13.10 5.80 81.10 30.33 28.74
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1286
0.9980 0.84 93.626 253.84 80.42 76.506 11.948 0.1351 0.1286 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time Time @ point Avg. Dlh
1.225 79.04 2,221,792 2,920,321 1.16E+08 12 0.193 120 10.00 1.690000
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out)Imp. Liquid Collected
1 256.113 1.400 1.62 114 73 73 Wt. (end) Wt. (start) lc
2 263.807 1.650 1.85 114 75 75 896.9 706.6 190.4
3 271.847 1.700 1.92 114 77 77 721.7 683.5 38.1
4 280.140 1.350 1.54 116 79 79 602.0 597.8 4.3
5 287.730 1.500 1.68 118 80 80 824.9 803.8 21.1
6 295.452 1.650 1.85 119 82 82 0.0
7 303.579 1.300 1.45 119 82 82
8 310.922 1.400 1.55 119 83 83 Isokinetics 100.6
9 318.390 1.500 1.66 119 83 83 Test Date 9/14/2023
10 326.120 1.400 1.55 118 83 83
11 333.622 1.550 1.74 119 84 84
12 341.528 1.650 1.87 118 84 84
13 349.739
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Run 2
Intermountain Power Service Corporation - Unit SGA-2Flow & Moisture Test Date 9/14/2023
As ft^2 Pbar Pq (static) Ps Avg. Ts F
CO2 - FCO2 O2 N2+C Md Ms
615.75 24.96 -1.00 24.89 118 13.50 5.50 81.00 30.38 28.75
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1313
0.9980 0.84 93.156 464.79 84 75.579 21.878 0.2245 0.1313 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time Time @ point Avg. Dlh
1.213 78.30 2,197,875 2,892,638 1.15E+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
1 350.307 1.40 1.49 117.0 79.0 79.0 Wt. (end) Wt. (start) lc
2 357.795 1.50 1.67 117.0 80.0 80.0 917.66 720.14 197.5
3 365.542 1.60 1.80 118.0 82.0 82.0 730.22 691.14 39.1
4 373.558 1.20 1.38 117.0 83.0 83.0 632.19 628.16 4.0
5 380.737 1.35 1.80 118.0 84.0 84.0 838.56 614.40 224.2
6 388.011 1.50 1.70 118.0 85.0 85.0 0.0
7 395.785 1.30 1.50 118.0 85.0 85.0
8 403.489 1.50 1.68 118.0 86.0 86.0 Isokinetics 112.0
9 410.915 1.60 1.82 118.0 86.0 86.0 Test Date 9/14/2023
10 419.010 1.45 1.85 119.0 87.0 87.0
11 426.805 1.60 1.84 119.0 87.0 87.0
12 434.985 1.70 1.97 119.0 88.0 88.0
13 443.463
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Run 3
Intermountain Power Service Corporation - Unit SGA-2Flow & Moisture Test Date 9/14/2023
As ft^2 Pbar Pq (static) Ps Avg. Ts F
CO2 - FCO2 O2 N2+C Md Ms
615.75 24.96 -1.00 24.89 120 13.50 5.40 81.10 30.38 28.67
Y Cp Vm cf Vlc Avg. Tm F Vm std Vw std Bws S Bws 0.1376
0.9980 0.84 93.223 264.26 87 75.262 12.439 0.1418 0.1376 0.999
Avg. Sqrt
Dlp Vs scfm wet acfm Qsd dscfh
# Sample
Points Dn
Total Test
time Time @ point Avg. Dlh
1.206 78.06 2,184,892 2,883,843 1.13E+08 12 0.193 120 10.00 1.64
TRUE
Point No.Meter (cf) dl "p" dl "h" ts F tm F (in) tm F (out)Imp. Liquid Collected
1 445.231 1.40 1.57 120.0 82.0 82.0 Wt. (end) Wt. (start) lc
2 452.987 1.65 1.80 120.0 83.0 83.0 905.03 707.5 197.5
3 461.250 1.70 1.80 120.0 85.0 85.0 725.93 682.9 43.1
4 469.081 1.20 1.40 120.0 86.0 86.0 601.42 597.4 4.1
5 476.370 1.45 1.66 119.0 87.0 87.0 823.32 803.7 19.6
6 484.138 1.50 1.72 120.0 88.0 88.0 0.0
7 492.099 1.20 1.36 119.0 88.0 88.0
8 499.227 1.40 1.57 120.0 88.0 88.0 Isokinetics 101.4
9 506.758 1.50 1.71 119.0 89.0 89.0 Test Date 9/14/2023
10 514.692 1.40 1.60 120.0 89.0 89.0
11 522.400 1.50 1.71 119.0 89.0 89.0
12 530.288 1.60 1.82 120.0 89.0 89.0
13 538.454
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