AQ_F_1000067_20170516_CMPL_InspRpt

NORTH CAROLINA DIVISION OF Wilmington Regional Office
AIR QUALITY CPI USA North Carolina-Southport Plant
NC Facility ID 1000067
Inspection Report County/FIPS:Brunswick/019
Date: 05/16/2017
Facility Data Permit Data
CPI USA North Carolina-Southport Plant Permit 05884/T21
1281 Power House Dr SE Issued 9/9/2016
Southport,NC 28461 Expires 8/31/2021
Lat: 33d 56.6220m Long: 78d 0.7270m Classification Title V
SIC: 4911 /Electric Services Permit Status Active
NAICS: 221112/Fossil Fuel Electric Power Generation Current Permit Application(s)PSD
Contact Data Program Applicability
Facility Contact Authorized Contact Technical Contact SIP/Title V/PSD
Virginia(tinny)Grace David Groves Virginia(tinny)Grace MACT Part 63: Subpart BBBBB,SubpartBoiler-112j, Subpart ZZZZ
Senior Advisor, Plant Manager Senior Advisor, NSPS: Subpart Db
Environment [phone] Environment
[phone] [phone]
Compliance Data
Comments:
Inspection Date 05/10/2017
Inspector's Name Samir Parekh
Inspector's Signature: Operating Status Operating
Compliance Code Compliance-Inspection
Action Code PCE
Date of Signature: 5 I C 6 On-Site Inspection Result Annual RATA
Total Actual emissions in TONS/YEAR:
TSP S02 NOX VOC CO PM10 *HAP
2015 254.04 4774.00 875.21 9.34 1592.04 134.27 47700.00
2014 315.65 4090.00 880.01 11.39 1537.80 203.08 25000.00
2013 146.57 3565.00 834.02 9.97 1279.00 79.78 22000.00
*Highest HAP Emitted(in pounds)
Five Year Violation History:
Date Letter Type Rule Violated Violation Resolution Date
01/24/2017 NOV/NRE 2D.0530 Prevention of Significant Deterioration Pending
06/24/2016 NOV/NRE 2D .0501 Compliance with Emission Control Standards Pending
Performed Stack Tests since last FCE: None
Date Test Results Test Method(s) Source(s)Tested
I) DIRECTIONS: From Raleigh, take I-40 East (118 miles).

Take I-140 West/US-17S exit 416A toward Myrtle Beach and travel to the NC 87S(Ocean Hwy E)or 133S
Via US-17S. (exit is to your left—12 miles from Leland side of the Cape Fear River).
Follow Highway NC 87S or 133S toward Southport(14.8 miles).
Make a left onto Rob Gandy Blvd (before Prices Creek and Jubbertown Rd) and travel —0.8 mi to E.
Leonard St.
Turn left and travel—0.2 miles,making a left onto Powerhouse Dr,immediately before the Progress Energy
driveway.
Check in at the security check point at the scale house(if attended).
II) FACILITY DESCRIPTION:
CPI is a cogeneration facility that primarily combusts wood, coal, and Tire Derived Fuel(TDF) to
produce steam from two identical Electrical Generating Units (EGU's), each consisting of three
boilers (223 MMBtu/hr each) and a turbine generator. The TDF as received at this facility is
typically 1.5"pieces of shredded tires;unadulterated wood and railroad ties as chips; and coal— I"
and down. The steam is used to drive two identical 54.3 MW GE turbine generators (one per unit)
to provide electricity,which is sold to Duke Energy Progress. Steam is also sold to Archer Daniels
Midland for process use.
III) Inspection Summary:
On May 10,I observed the annual RATA for S02,NO,,and Flow on unit 1.The tests were conducted to meet Part 60
and 75 requirements.
On arriving at the plant,I met with Ginny Grace.We discussed the quarterly reporting requirements,specifically we
talked to modify the EERs to demonstrate the compliance with NO,,and S02 per boiler emission standard.
After this we went to observe the RATA.Michael Whitt was the lead tester for the Grace Consulting,Inc.The tester
was conducting the gas RATAs.While at the CEMS shelter,I reviewed the log book,verified CEMS serial nos. and
span settings. There were no observed deviations to the tests methods noted during the observation. The relative
accuracy value for the low and mid flow RATA was well below 20%specification.The CEM record review indicated
no major issues. I mentioned Ginny Grace to conduct the future RATAs at Southport and Roxboro in the units of
emissions standards(lbs/hr and lbs/mmBtu).
The observer checklist,calibration report, and other process data collected from the control room are attached.
The next annual RATA should be conducted by June 30,2018.

NC DAQ Source Test Observers Checklist - Reference Method CEM Testing
Facility Name/Location : C
Facility Contact/Phone q 10 - 3 43 -6 311(w).- `110 -4 9�
Testing Firm/Contact: `,Cn4,e-*-
Permit#/Source Tested: (,t,."A - f
Applicable Regulation/Pollutant: N 5 P.s I ([) 2-0 , d 573 v
Process Data/Production Rate(see reverse side): .2� k-L
601X1 A)ft VAX ,-rpF.
Sample Date/Time:Run 1 / - Run 2 / Run 3 /
Ask for an explanation to ao uesti.answeredon att aac comments to this rm.
Method 1 -Sample and Velocity Traverses for Stationary Sources YES NO
1.1)Method I calculated correctly(see reverse side)?
1.2)Cyclonic flow check completed? (Average of absolute value of all angles<20 degrees?) Z6 RATA
Method 2 -Determination of Stack Gas Velocity and Volumetric Flow Rate YES NO
2.1)Pitot tube leak check completed after each run?
2.2)Visual check of pitot tube heads-good condition?
2.3)Manometer level and zeroed correctly? >/
2.4)Static pressure measured during the test day?
2.5)Barometric pressure recorded and adjusted for elevation?(see reverse side)
2.6)Pitot tube heads oriented to axis of flue?/Pitot tube perpendicular to axis of stack?
2.7)Temperature recorded at each sampling point?
Method 3 -Gas Analysis for 0, CO , and Dry Molecular Weight YES NO
Skip this section if O,&CO:concentrations are determined via analyzers. - - -
3.1)Orsat or Fyrites used?(circle) '
3.2)Orsat performed in triplicate?Analysis consistent?
Method 4-Determination of Moisture Content in Stack Gases YES NO
4.1)Impingers used or some other type of condenser? Multi point sample?
4.2)H2O in first 2 impingers,3rd impinger empty,silica gel in 4th impinger?
4.3)Temperature at the exit of impingers/condenser<68F?(see reverse side)
4.4)Silica gel in good condition?-Blue-new,Pink-spent(unable to absorb more H2O)
CEM Methods: Method 3A-0 /CO , N16C-SO , WE-NO, M10-CO YES NO
5.1)System leak check perfonned during test day?(not required per method but good Q.A.) '
5.2) Sample point w/in centroid of stack(compliance test)?
5.3)Sample conditioner/dryer used?
5.4)Heated sample line used prior to sample conditioner?
5.5)Moisture visible in the sample line? (Do not explain a"No")
5.6)Filter used: "In stack"or"heated out of stack"
5.7)Sample system flow rates within 10%of calibration flowrates?
5.8)All concentration measurements below the span value for that pollutant?
5.9)Data Record e Digital Strip chart/Manual/other (circle one)
5.10)NO.monitoring:NO,-to NO convertor operating?Total NO,being analyzed?
5.11)Calibration Error Check performed for all analyzers and within specifications(2%of span)?
5.12)System Bias Check performed for each analyzer before the first run,between each run,and after the last run.
5.13 Test team monitoring analyzer zero drift and calibration drift between each run?
The following page(front/back)should be completed to the extent possible. The data may be transferred from print outs provided by
the tester. Preferably,the calibrations should be viewed at the time they are performed to assure monitor stability and correct
flowrates for each calibration gas.

Process Data: It is absolutely imperative for the facility to record the pertinent data durine the test so that the measured emissions can be
correlated to a production rate and compared to the permit limit. The test will be unacceptable without production data.
Method 1:If stack is between 4"- 12"then Method la must be employed. If duct is<4"then alternative methods must be used. (Contact
SSCB with any test questions)
Stack Diameter? Measured on site?
Port distance from upstream disturbance(A) Upstream Diameters(A)
Port distance from downstream disturbance(B) Downstream Diameters(B)
#of Sampling Points? (Draw a line vertically from the"Distance A"axis down to the step chart,and from the"Distance B"axis up
to the step chart. The maximum#of points marked on the chart yields the minimum#of points to be sampled.)
Dxf 0"ersLpstreamfranRwoDsttrbwW' (Dst arm A)
5 N1r.,h0� 1.5 20 25
agfa�a�icfs or Dds LFt.
t ia
A
16 aacc5aWer >Q61 (24in)
12
1 FFrr�ro DFni pp��,
ostir°�asioe"t(eaq' on. 6rtradim, etc. 9
aadc Daieta =0.3D i o0.61 m(12-24in)
Did Danalers OmitreamfromFowDsttrbarime (Dstmm B)
Figure 1-2.Minimum number of traverse points for velocity(nonparticulate)traverses.
Points correctly marked on the pitot tube? Port length agcounted for in calculations?
Remarks:
Barometric Pressure:Barometric pressure must be adjusted minus 0.1"per 100ft elevation increase or vice versa for elevation decrease.
(Elevation at which barometric pressure is measured compared to the elevation at the test platform.)
Exit Temperature: The temperature of the dry gas leaving the impingers/condenser must be below 68F. When the ambient temperature is
above 68F it may take approximately 5 minutes for the thermal effects of the ice bath to cool the exit thermometer below 68F.
CEM Methods:
There shall be no adjustments made to the analyzers after the start of the Calibration Error test. If an adjustment is made,reject all data since
the last completed system calibration. The Calibration Error test shall be re-performed and any subsequent system calibrations that are
necessary. The calibration and sample gas flow rates can and should be adjusted to within 10%of the flowrate during the calibration error test.
The mid range or high range gas can be used for the system bias test;however,it is preferred to use the upscale calibration gas closest to the
effluent concentration. It is also possible to use more than the required number of gases as long as the minimum gases were used. Single point
gas sampling is acceptable for compliance testing. The gas sample should be extracted from the center of the stack. The span of the analyzers
shall be selected such that the gas concentration equivalent to the emission standard is not less than 30%of the span. If at any time during a run
the measured gas concentration exceeds the span,the run shall be considered invalid.
Remarks:

-Jr� C,,,p - k fi
Client CPC Test Date ########
Southport Project# 17-602
Source Identification Unit 1 Operator M.Whitt
Calibration Data For Cylinder Expiration Cylinder Analyzer Absolute Difference
Sampling R (j2)
Number Date Value Response Difference %of Span
Gas Type: %or PPM %or PPM
Span: 1
Zero Gas 0 0.00 0.93 0.93 0.103
Low-Range Gas N/A 0 0
Mid-Range NC 489.8 490.3 0.5 0.055
High-RangE NC I 1 1 901.1 1 901.7 1 0.6 0.067
Run#: 1 Initial Values Final Values
Gas Type: SO2 Analyzer System System System System
Span: 901.1 Response Response Cal. Bias Response Cal. Bias Drift
%of Span % of Span %of Span
Zero Gas 0.93 1 0.01 0.93 0.00 -0.01
Upscale Gas 490.3 490.6 1 0.03 491.7-T 0.16 0.12
Run#: 2 Initial Values Final Values
Gas Type: SO2 Analyzer System System System System
Span: 901.1 Response Response Cal. Bias Response Cal. Bias Drift
%of Span % of Span %of Span
Zero Gas 0.93 0.93 0.00 1.15 0.02 0.02
Upscale Gas 490.3 491.7 0.16 492.5 0.24 0.09
Run #: 3 Initial Values Final Values
Gas Type: SO2 Analyzer System System System System
Span: 901.1 Response Response Cal. Bias Response Cal. Bias Drift
%of Span %of Span %of Span
Zero Gas 0.93 1.15 0.02 1.33 0.04 0.02
Upscale Gas 490.3 492.5 0.24 492.9 0.29 0.04
Run #: 4 Initial Values Final Values
Gas Type: SO2 Analyzer System System System System
Span: 901.1 Response Response Cal. Bias Response Cal. Bias Drift
%of Span %of Span % of Span
Zero Gas 0.93 1.33 E 0.04 1.45 0.06 0.01
Upscale Gas 490.3 492.9 1 0.29 492.5 0.24 -0.04

Client CPC Test Date ########
Southport Project# 17-602
Source Identification Unit 1 Operator M.Whitt
Calibration Data For Cylinder Expiration Cylinder Analyzer Absolute Difference
Sampling R 1- Number Date Value Response Difference %of Span
Gas Type: Nox % or PPM %or PPM
Span: 530.5
Zero Gas 0 0 0.65 0.65 0.123
No2 to No Converter C 0 42.58 40.90 -1.68 96.05% PASS
Mid-Range NC 230.3 230.1 -0.2 -0.038
High-Rang(NC 530.5 529.7 -0.8 -0.151
Run#: 1 Initial Values Final Values
Gas Type: Nox Analyzer System System System System
Span: 530.5 Response Response Cal. Bias Response Cal. Bias Drift
of Span %of Span %of Span
Zero Gas 0.65 0.88 0.04 0.45 -0.04 -0.08
Upscale Gas 230.1 230.8 0.13 231.5 0.26 0.13
Run#: 2 Initial Values Final Values
Gas Type: Nox Analyzer System System System System
Span: 530.5 Response Response Cal. Bias Response Cal. Bias Drift
of Span %of Span %of Span
Zero Gas 0.65 0.45 -0.04 0.41 -0.05 -0.01
Upscale Gas 230.1 231.5 0.26 232.8 0.51 0.25
Run #: 3 Initial Values Final Values
Gas Type: Nox Analyzer System System System System
Span: 530.5 Response Response Cal. Bias Response Cal. Bias Drift
of Span %of Span %of Span
Zero Gas 0.65 0.41 -0.05 0.75 0.02 0.06
Upscale Gas 230.1 232.87 0.51 231.4 0.25 -0.26
Run#: 4 Initial Values Final Values
Gas Type: Nox Analyzer System System System System
Span: 530.5 Response Response Cal. Bias Response Cal. Bias Drift
of Span %of Span %of Span
Zero Gas 1 0.65 0.75 0.02 0.3 -0.07 -0.08
Upscale Gas 1 230.1 1 231.4 0.25 230.4 0.06 -0.19

Client CPC Test Date ########
Southport Project# 17-602
Source Identification Unit 1 Operator M.Whitt
Calibration Data For Cylinder Expiration Cylinder Analyzer Absolute Difference
Sampling R 1- Number Date Value Response Difference %of Span
Gas Type: Co2 %or PPM %or PPM
Span: 17.7
Zero Gas 0 0.00 0.25 0.25 1.412
Low-Range Gas 0 0 0
Mid-Range NC 8.8 8.89 0.07 0.395
High-RangE NC I 1 1 17.7 1 17.45 1 -0.25 -1.412
Run #: 1 Initial Values Final Values
Gas Type: Co2 Analyzer System System System System
Span: 17.7 Response Response Cal. Bias Response Cal. Bias Drift
of Span %of Span % of Span
Zero Gas 0.25 0.25 0.00 0.29 0.23 0.23
Upscale Gas 8.89 9 1 0.62 9.01 0.68 0.06
Run#: 2 Initial Values Final Values
Gas Type: Co2 Analyzer System System System System
Span: 17.7 Response Response Cal. Bias Response Cal. Bias Drift
of Span %of Span %of Span
Zero Gas 0.25 0.29 0.23 0.33 0.45 0.23
Upscale Gas 8.89 9.01 0.68 9.11 1.24 0.56
Run #: 3 Initial Values Final Values
Gas Type: Co2 Analyzer System System System System
Span: 17.7 Response Response Cal. Bias Response Cal. Bias Drift
of Span %of Span %of Span
Zero Gas 0.25 0.33 0.45 0.34 0.51 0.06
Upscale Gas 8.89 9.11 1.24 9.28 2.20 0.96
Run#: 4 Initial Values Final Values
Gas Type: Co2 Analyzer System System System System
Span: 17.7 Response Response Cal. Bias Response Cal. Bias Drift
of Span %of Span %of Span
Zero Gas 0.25 0.34 0.51 0.27 0.11 -0.40
Upscale Gas 8.89 1 9.28 2.20 9.25 2.03 -0.17

Client CPC Test Date ########
Southport Project# 17-602
Source Identification Unit 1 Operator M.Whitt
Calibration Data For Cylinder Cylinder Analyzer Absolute Difference
Sampling R 1- Number Value Response Difference % of Span
Gas Type: 02 % or PPM % or PPM
Span: 21.95
Zero Gas 0 0.11 0.22 0.11 0.501
Low-Range Gas 0 0 0
Mid-Range NC 11.0 11.14 0.14 0.638
High-RangE NC 1 1 22.0 1 21.66 1 -0.29 1 -1.321
Run #: 1 Initial Values Final Values
Gas Type: 02 Analyzer System System System System
Span: 21.95 Response Response Cal. Bias Response Cal. Bias Drift
of Span %of Span %of Span
Zero Gas 0.22 0.19 -0.14 0.22 0.00 0.14
Upscale Gas 11.14 1 11.01 1 -0.59 11.05 1 -0.41 0.18
Run#: 2 Initial Values Final Values
Gas Type: 02 Analyzer System System System System
Span: 21.95 Response Response Cal. Bias Response Cal. Bias Drift
of Span % of Span %of Span
Zero Gas 0.22 0.22 0.00 0.15 -0.32 -0.32
Upscale Gas 11.14 11.05 -0.41 11.11 1 -0.14 0.27
Run#: 3 Initial Values Final Values
Gas Type: 02 Analyzer System System System System
Span: 21.95 Response Response Cal. Bias Response Cal. Bias Drift
of Span %of Span % of Span
Zero Gas 0.22 0.15 -0.32 0.1 -0.55 -0.23
Upscale Gas 11.14 11.11 -0.14 11.26 0.55 0.68
Run #: 4 Initial Values Final Values
Gas Type: 02 Analyzer System System System System
Span: 21.95 Response Response Cal. Bias Response Cal. Bias Drift
of Span %of Span %of Span
Zero Gas 0.22 0.1 -0.55 0.1 -0.55 0.00
Upscale Gas 11.14 11.26 0.55 11.22 0.36 -0.18

Client CPC Test Date ########
Southport Project# 17-602
Source Identification Unit 1 Operator M.Whitt
Calibration Data For Cylinder Cylinder Analyzer Absolute Difference
Sampling R 1- Number Value Response Difference % of Span
Gas Type: Co %or PPM %or PPM
Span: 996.8
Zero Gas 0 0.00 0.99 0.99 0.099
Low-Range Gas 225.4 225.1 -0.3 -0.0301
Mid-Range Gas 503.5 502.8 -0.7 -0.070
High-Range Gas 1 1 996.8 1 996.2 1 -0.6 1 -0.060
Run#: 1 Initial Values Final Values
Gas Type: Co Analyzer System System System System
Span: 996.8 Response Response Cal. Bias Response Cal. Bias Drift
%of Span %of Span %of Span
Zero Gas 1 0.99 0.93 -0.01 1.11 0.01 0.02
Upscale Gas 502.8 503.9 0.11 1 504.5 0.17 0.06
Run#: 2 Initial Values Final Values
Gas Type: Co Analyzer System System System System
Span: 996.8 Response Response Cal. Bias Response Cal. Bias Drift
of Span %of Span % of Span
Zero Gas 0.99 1.11 0.01 1.25 0.03 1 0.01
Upscale Gas 502.8 504.5 0.17 504.9 0.21 1 0.04
Run#: 3 Initial Values Final Values
Gas Type: Co Analyzer System System System System
Span: 996.8 Response Response Cal. Bias Response Cal. Bias Drift
%of Span %of Span %of Span
Zero Gas 0.99 1.25 1 0.03 0.99 0.00 -0.03
Upscale Gas 502.8 1 504.9 0.21 504.1 0.13 -0.08
Run #: 4 Initial Values Final Values
Gas Type: Co Analyzer System System System System
Span: 996.8 Response Response Cal. Bias Response Cal. Bias Drift
%of Span %of Span %of Span
Zero Gas 0.99 1 0.99 0.00 0.85 -0.01 -0.01
Upscale Gas 502.8 1 504.1 0.13 503 0.02 -0.11

ANALYZER DATA Run # 1
Client: CPC Project# 17-602 Test Date 05/10/17
Source Id: Southport Unit 1 Operator M.Whitt
Span: 21.95 17.70 530.50 901.10 996.80
Lower Lim 4.39 3.54 106.10 180.22 199.36
02 CO2 Nox S02 CO
Time % % ppm ppm ppm
8:30:00 7.58 12.41 108.7 313.47 307.45
8:31:00 7.52 12.52 108.51 315.44 286.72
8:32:00 7.31 12.61 108.28 313.26 374.41
8:33:00 7.31 12.71 106.95 307.11 373.36
8:34:00 7.37 12.62 105.95 303.78 331.65
8:35:00 7.31 12.71 106.06 304.28 370.04
8:36:00 7.2 12.76 105.08 307.21 393.04
8:37:00 7.43 12.68 105.24 303.12 313.61
8:38:00 7.23 12.64 105.46 312.6 440.91
8:39:00 6.95 12.91 104.75 322.75 649.6
8:40:00 6.98 12.9 103.47 318.91 675.64
8:41:00 7.35 12.67 102.99 303.77 315.97
8:42:00 7.65 12.45 104.68 305.35 214.09
8:43:00 7.69 12.33 107.25 306.86 203.01
8:44:00 7.48 12.49 109.49 311.13 246.06
8:45:00 7.27 12.65 109.35 317.96 342.88
8:46:00 7.27 12.74 107.34 319.33 412.61
8:47:00 7.44 12.6 106.22 310.35 363.2
8:48:00 7.48 12.53 106.33 307.19 364.91
8:49:00 7.39 12.65 106.5 310.53 465.7
8:50:00 7.39 12.53 106.86 310.29 422.86
Averages
For 21 7.36 12.62 106.45 310.70 374.65
Min. 6.95 12.33 102.99 303.12 203.01
Max. 7.69 12.91 109.49 322.75 675.64

ANALYZER DATA Run # 2
Client CPC Project# 17-602 Test Date 05/10/17
Source Id: Southport Unit 1 Operator M.Whitt
Span: 21.95 17.70 530.50 901.10 996.80
Lower Lim 4.39 3.54 106.10 180.22 199.36
02 CO2 Nox SO2 CO
Time % % ppm ppm ppm
9:00:00 7.23 12.66 109.85 318.05 443.09
9:01:00 6.99 12.88 108.17 325.3 597.26
9:02:00 7.08 12.89 106.31 318.97 414.48
9:03:00 7.35 12.66 105.98 308.72 317.99
9:04:00 7.69 12.34 107.2 300.42 240.04
9:05:00 7.57 12.37 106.97 302.75 236.57
9:06:00 7.27 12.63 108.52 311.58 279.1
9:07:00 7.42 12.57 108.68 304.08 373.39
9:08:00 7.27 12.66 107.65 313.61 320.47
9:09:00 7.25 12.6 108.28 319.51 293.96
9:10:00 7.22 12.71 108.92 324.74 325.34
9:11:00 7.59 12.49 108.94 305.95 239.01
9:12:00 7.64 12.34 110.04 300.79 230.66
9:13:00 7.4 12.5 111.1 303.36 305.8
9:14:00 7.23 12.67 109.46 309.22 427.08
9:15:00 7.17 12.72 108.36 311.08 629.36
9:16:00 7.05 12.81 105.21 312.99 735.4
9:17:00 6.92 12.9 104.35 317.15 629.45
9:18:00 7.24 12.71 104.37 300.61 413.5
9:19:00 7.13 12.75 105.28 290.82 462.77
9:20:00 7.36 12.62 105.06 281.36 368.53
Averages
For 21 7.29 12.64 107.56 308.62 394.44
Min. 6.92 12.34 104.35 281.36 230.66
Max. 7.69 12.90 111.10 325.30 735.40

ANALYZER DATA Run # 3
Client CPC Project# 17-602 Test Date 05/10/17
Source Id: Southport Unit 1 Operator M.Whitt
Span: 21.95 17.70 530.50 901.10 996.80
Lower Lim 4.39 3.54 106.10 180.22 199.36
02 CO2 Nox SO2 CO
Time % % ppm ppm ppm
9:30:00 7.57 12.43 103.85 275.47 342.85
9:31:00 7.63 12.35 104.68 280.52 378.23
9:32:00 7.44 12.55 105.13 284.29 395.87
9:33:00 7.39 12.61 105.18 279.56 366.98
9:34:00 7.37 12.69 104.72 277.26 322.74
9:35:00 7.48 12.51 104.68 278.26 268.54
9:36:00 7.54 12.47 106.04 279.56 286.98
9:37:00 7.49 12.51 106.47 276 314.35
9:38:00 7.53 12.47 106.59 281.46 387.95
9:39:00 7.6 12.42 105.44 283.68 424.48
9:40:00 7.4 12.56 104.83 290.38 589.73
9:41:00 7.17 12.73 102.83 299.43 570.81
9:42:00 7.22 12.65 102.28 300.2 610.52
9:43:00 7.18 12.73 102.67 313.68 997.51
9:44:00 7.17 12.73 101.37 311.93 627.28
9:45:00 7.33 12.68 101.21 301.73 433.82
9:46:00 7.17 12.67 102.44 305.98 471.41
9:47:00 7.35 12.61 103.03 299.51 365.67
9:48:00 7.41 12.52 102.97 292.97 322.55
9:49:00 7.38 12.53 104.43 296.99 372.06
9:50:00 7.39 12.52 103.84 298.55 375.24
Averages
For 21 7.39 12.57 104.03 290.83 439.31
Min. 7.17 12.35 101.21 275.47 268.54
Max. 7.63 12.73 106.59 313.68 997.51

Calibration Report Page 1 of 3
Facility Name: Capital Power Southport LE-rv-)
Location: Southport, NC
Date Time Analyzer Type Target Analyzer Analyzer Perf Span P60 5-day P75 Process Cylinder Cylinder
Value Value Drift Spec Status Count Status Status Number Exp
05/10/2017 06:02 COM Unit 1 Opacity Zero 0.00 -0.02 0.02 2.00 27.60 Pass 0 ON
05/10/2017 06:04 COM Unit 1 Opacity Upscale 27.60 27.64 -0.04 2.00 27.60 Pass 0 ON
05/10/2017 06:06 Stack Unit 1 CO Zero 0.00 0.20 -0.01 5.00 3,500.00 Pass 0 ON CC2782 12/19/24
27
05/10/2017 06:17 Stack Unit 1 CO Upscale 1923.00 1923.50 -0.01 5.00 3,500.00 Pass 0 ON CC5074 12/06/24
4
05/10/2017 06:06 Stack Unit 1 CO2 Upscale 10.90 10.90 0.00 0.50 20.00 Pass 0 ON CC2782 12/19/24
P60 27
05/10/2017 06:11 Stack Unit 1 CO2 Zero 0.00 0.10 -0.10 0.50 20.00 Pass 0 ON CC4437 12/27/24
P60 0
05/10/2017 06:06 Stack Unit 1 CO2 Upscale 10.9 10.9 0.00 0.50 20.00 0 Pass ON CC2782 12/19/24
P75 27
05/10/2017 06:11 Stack Unit 1 CO2 Zero 0.0 0.1 -0.10 0.50 20.00 0 Pass ON CC4437 12/27/24
P75 0
05/10/2017 05:22 Stack Unit 1 Flow Zero 1.00 Pass ON
DP Int
05/10/2017 05:38 Stack Unit 1 Flow Zero 1.00 Pass ON
DP Int
05/10/2017 05:46 Stack Unit 1 Flow Zero 1.00 Pass ON
DP Int
05/10/2017 05:18 Stack Unit 1 Flow Zero 0.00 0.01 -0.80 3.00 1.25 Pass 0 ON
DP P60
05/10/2017 05:20 Stack Unit 1 Flow Upscale 0.70 0.66 3.20 3.00 ' .25 Pass 0 ON
DP P60
05/10/2017 05:33 Stack Unit 1 Flow Zero 0.00 0.01 -0.80 3.00 1.25 Pass 0 ON
DP P60
Report generated on: 05/10/2017 10:50 Data is expressed in Standard Time Version 1.0

Calibration Report Page 2 of 3
Facility Name: Capital Power Southport
Location: Southport, NC
Date Time Analyzer Type Target Analyzer Analyzer Perf Span P60 5-day P75 Process Cylinder Cylinder
Value Value Drift Spec Status Count Status Status Number Exp
05/10/2017 05:35 Stack Unit 1 Flow Upscale 0.70 0.67 2.40 3.00 1.25 Pass 0 ON
DP P60
05/10/2017 05:41 Stack Unit 1 Flow Zero 0.00 0.01 -0.80 3.00 1.25 Pass 0 ON
DP P60
05/10/2017 05:43 Stack Unit 1 Flow Upscale 0.70 0.67 2.40 3.00 1.25 Pass 0 ON
DP P60
05/10/2017 05:18 Stack Unit 1 Flow Zero 0.0 0.0 0.00 3.00 1.25 0 Pass ON
DP P75
05/10/2017 05:20 Stack Unit 1 Flow Upscale 0.7 0.7 0.00 3.00 1.25 0 Pass ON
DP P75
05/10/2017 05:33 Stack Unit 1 Flow Zero 0.0 0.0 0.00 3.00 1.25 0 Pass ON
DP P75
05/10/2017 05:35 Stack Unit 1 Flow Upscale 0.7 0.7 0.00 3.00 1.25 0 Pass ON
DP P75
05/10/2017 05:41 Stack Unit 1 Flow Zero 0.0 0.0 0.00 3.00 1.25 0 Pass ON
DP P75
05/10/2017 05:43 Stack Unit 1 Flow Upscale 0.7 0.7 0.00 3.00 1.25 0 Pass ON
DP P75
05/10/2017 06:06 Stack Unit 1 NOx Zero 0.00 -0.10 0.03 2.50 400.00 Pass 0 ON CC2782 12/19/24
P60 27
05/10/2017 06:11 Stack Unit 1 NOx Upscale 349.80 350.10 -0.08 2.50 400.00 Pass 0 ON CC4437 12/27/24
P60 0
05/10/2017 06:06 Stack Unit 1 NOx Zero 0.0 -0.1 0.00 2.50 400.00 0 Pass ON CC2782 12/19/24
P75 27
05/10/2017 06:11 Stack Unit 1 NOx Upscale 349.8 350.1 -0.10 2.50 400.00 0 Pass ON CC4437 12/27/24
P75 0
05/10/2017 06:06 Stack Unit 1 SO2 Zero 0.00 2.70 -0.19 2.50 1,400.00 Pass 0 ON CC2782 12/19/24
High P60
27
Report generated on: 05/10/2017 10:50 Data is expressed in Standard Time Version 1.0

Calibration Report Page 3 of 3
Facility Name: Capital Power Southport
Location: Southport, NC
Date Time Analyzer Type Target Analyzer Analyzer Perf Span P60 5-day P75 Process Cylinder Cylinder
Value Value Drift Spec Status Count Status Status Number Exp
05/10/2017 06:17 Stack Unit 1 S02 Upscale 1280.00 1282.40 -0.17 2.50 1,400.00 Pass 0 ON CC5074 12/06/24
High P60 4
05/10/2017 06:06 Stack Unit 1 S02 Zero 0.0 2.7 -0.20 2.50 1,400.00 0 Pass ON CC2782 12/19/24
High P75 27
05/10/2017 06:17 Stack Unit 1 S02 Upscale 1280.0 1282.4 -0.20 2.50 1,400.00 0 Pass ON CC5074 12/06/24
High P75 4
05/10/2017 06:06 Stack Unit 1 S02 Zero 0.00 0.90 -0.20 2.50 450.00 Pass 0 ON CC2782 12/19/24
Low P60 27
05/10/2017 06:11 Stack Unit 1 S02 Upscale 413.00 413.20 -0.04 2.50 450.00 Pass 0 ON CC4437 12/27/24
Low P60 0
05/10/2017 06:06 Stack Unit 1 S02 Zero 0.0 0.9 -0.20 2.50 450.00 0 Pass ON CC2782 12/19/24
Low P75 27
05/10/2017 06:11 Stack Unit 1 S02 Upscale 413.0 413.2 0.00 2.50 450.00 0 Pass ON CC4437 12/27/24
Low P75 0
Report generated on: 05/10/2017 10:50 Data is expressed in Standard Time Version 1.0

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Unit 1 Gas Rata Data X�'t
Facility Name: Capital Power Southport Location: Southport, NC Source: Stack
Stack CO2 Stack STEAM Stack CO Stack CO Stack NOx Stack NOx Rt Stack SO2 Stack SO2 Rt _
P75 Total Corr P75 P60 P75 P60
PCT KLBHR PPM PPMD PPM LBMMBTU PPM LBMMBTU
05/10/2017 08:30 10.7 394 309.1 380.5 89.5 0.183 262.5 0.745
05/10/2017 08:31 10.6 394 258.8 321.6 89.9 0.185 262.6 0.753
05/10/2017 08:32 10.6 392 227.8 283.1 90.5 0.187 264.4 0.758
05/1 01201 7 08:33 10.5 392 230.1 288.7 91.0 0.189 275.8 0.798
05/10/2017 08:34 10.5 391 247.8 310.9 91.3 0.190 271.5 0.785
05/10/2017 08:35 10.5 390 283.8 356.0 91.3 0.190 268.1 0.776
05/10/2017 08:36 10.6 392 302.6 376.0 91.4 0.188 265.3 0.760
05/10/2017 08:37 10.7 393 312.6 384.8 91.0 0.186 264.7 0.752
05/10/2017 08:38 10.7 394 315.0 387.8 90.6 0.185 264.2 0.750
05/10/2017 08:39 10.8 396 325.3 396.7 90.0 0.182 264.2 0.743
05/10/2017 08:40 10.7 398 321.2 395.4 89.7 0.183 264.2 0.750
05/10/2017 08:41 10.8 399 350.4 427.4 89.4 0.181 268.1 0.754
05/10/2017 08:42 10.9 399 456.4 551.5 88.7 0.178 280.8 0.783
05/10/2017 08:43 10.9 398 537.5 649.5 88.4 0.177 268.4 0.748
05/10/2017 08:44 10.8 394 461.4 562.7 88.6 0.179 265.4 0.747
05/10/2017 08:45 10.6 394 297.9 370.2 89.3 0.184 266.3 0.763
05/10/2017 08:46 10.5 391 202.6 254.2 90.0 0.187 266.8 0.772
05/10/2017 08:47 10.5 391 205.4 257.7 90.2 0.188 267.8 0.775
05/10/2017 08:48 10.6 389 259.7 322.7 90.8 0.187 269.9 0.773
05/10/2017 08:49 10.6 388 322.9 401.2 91.3 0.188 271.8 0.779
05/1 01201 7 08:50 10.6 388 350.6 435.7 91.6 0.189 271.9 0.779
Average 10.7 393 313.3 386.4 90.2 0.185 267.8 0.764
Maximum 10.9 399 537.5 649.5 91.6 0.190 280.8 0.798
Minimum 10.5 388 202.6 254.2 88.4 0.177 262.5 0.743
Report generated on: 05/10/2017 09:43 Data is expressed in Standard Time Page 1

Unit 1 Gas Rata Data
Facility Name: Capital Power Southport Location: Southport, NC Source: Stack
Stack CO2 Stack STEAM Stack CO Stack CO Stack NOx Stack NOx Rt Stack SO2 Stack SO2 Rt
P75 Total Corr P75 P60 P75 P60
PCT KLBHR PPM PPMD PPM LBMMBTU PPM LBMMBTU
05/10/2017 09:00 10.4 382 293.2 371.3 94A 0.198 258.3 0.754
05/10/2017 09:01 10.4 384 237.9 301.3 94.5 0.199 259.2 0.757
05/10/2017 09:02 10.5 388 229.4 287.8 94.3 0.196 261.2 0.756
05/10/2017 09:03 10.6 391 311.1 386.6 93.6 0.193 265.7 0.761
05/1 01201 7 09:04 10.8 390 427.6 521.5 93.0 0.188 276.3 0.777
05/10/2017 09:05 10.8 387 448.9 547.5 92.5 0.187 268.1 0.754
05/10/2017 09:06 10.7 385 365.8 450.3 92.2 0.188 259.8 0.738
05/10/2017 09:07 10.5 384 268.1 336.3 91.9 0.191 256.8 0.743
05/10/2017 09:08 10.5 383 233.9 293.4 91.6 0.191 257.9 0.746
05/10/2017 09:09 10.5 383 243.1 305.0 91.7 0.191 259.4 0.750
05/10/2017 09:10 10.6 384 288.3 358.2 92.0 0.190 260.7 0.747
05/10/2017 09:11 10.6 385 309.7 384.8 92.3 0.190 263.4 0.755
05/10/2017 09:12 10.6 381 309.0 384.0 92.6 0.191 278.5 0.798
05/1 01201 7 09:13 10.6 379 288.5 358.5 92.8 0.191 269.3 0.772
05/10/2017 09:14 10.5 379 263.7 330.8 93.1 0.194 262.2 0.759
05/10/2017 09:15 10.4 382 242.6 307.3 93.0 0.195 262.0 0.765
05/10/2017 09:16 10.5 385 257.2 322.6 93.3 0.194 263.1 0.761
05/10/2017 09:17 10.6 387 342.1 425.1 92.8 0.191 265.0 0.759
05/10/2017 09:18 10.7 390 459.0 565.0 92.2 0.188 267.1 0.758
05/10/2017 09:19 10.7 389 584.4 719.4 91.5 0.187 270.2 0.767
05/10/2017 09:20 10.8 389 581.9 709.7 90.7 0.184 272.3 0.766
Average 10.6 385 332.6 412.7 92.7 0.191 264.6 0.759
Maximum 10.8 391 584.4 719.4 94.5 0.199 278.5 0.798
Minimum 10.4 379 229.4 287.8 90.7 0.184 256.8 0.738
Report generated on: 05/10/2017 09:44 Data is expressed in Standard Time Page 1

Unit 1 Gas Rata Data
Facility Name: Capital Power Southport Location: Southport, NC Source: Stack
Stack CO2 Stack STEAM Stack CO Stack CO Stack NOx Stack NOx Rt Stack SO2 Stack SO2 Rt
P75 Total Corr P75 P60 P75 P60
PCT KLBHR PPM PPMD PPM LBMMBTU PPM LBMMBTU
05/10/2017 09:30 10.7 376 347.2 427.4 90.0 0.184 245.2 0.696
05/10/2017 09:31 10.6 376 362.1 450.0 89.9 0.185 244.1 0.700
05/10/2017 09:32 10.6 374 345.8 429.7 89.8 0.185 243.4 0.698
05/10/2017 09:33 10.5 374 312.3 391.8 90.0 0.187 243.0 0.703
05/10/2017 09:34 10.5 374 308.7 387.3 90.1 0.187 243.5 0.704
05/10/2017 09:35 10.5 376 317.7 398.5 90.1 0.187 243.8 0.705
05/10/2017 09:36 10.5 375 314.6 394.7 90.4 0.188 244.4 0.707
05/10/2017 09:37 10.5 377 288.0 361.3 90.6 0.189 244.2 0.707
05/10/2017 09:38 10.5 377 254.4 319.1 91.0 0.189 244.3 0.707
05/10/2017 09:39 10.5 378 235.0 294.8 91.2 0.190 243.3 0.704
05/10/2017 09:40 10.5 377 254.9 319.8 91.3 0.190 244.4 0.707
05/10/2017 09:41 10.5 380 292.0 366.3 91.5 0.190 245.4 0.710
05/10/2017 09:42 10.5 383 355.8 446.3 91.3 0.190 246.6 0.713
05/10/2017 09:43 10.6 386 428.1 532.0 91.0 0.188 251.9 0.722
05/10/2017 09:44 10.7 388 488.0 600.7 90.5 0.185 258.0 0.732
05/10/2017 09:45 10.8 388 549.4 670.1 90.0 0.182 267.1 0.751
05/10/2017 09:46 10.8 389 638.9 779.2 89.2 0.180 269.8 0.759
05/10/2017 09:47 10.8 388 637.9 778.0 88.6 0.179 266.8 0.750
05/10/2017 09:48 10.8 389 529.0 645.2 88.2 0.178 260.2 0.732
05/10/2017 09:49 10.8 386 417.4 509.1 88.2 0.178 262.5 0.738
05/10/2017 09:50 10.7 382 362.1 445.8 88.6 0.181 256.4 0.728
Average 10.6 381 382.8 473.7 90.1 0.185 250.9 0.718
Maximum 10.8 389 638.9 779.2 91.5 0.190 269.8 0.759
Minimum 10.5 374 235.0 294.8 88.2 0.178 243.0 0.696
Report generated on: 05/10/2017 09:52 Data is expressed in Standard Time Page 1

Unit 1 Gas Rata Data
Facility Name: Capital Power Southport Location: Southport, NC Source: Stack
Stack CO2 Stack STEAM Stack CO Stack CO Stack NOx Stack NOx Rt Stack SO2 Stack SO2 Rt
P75 Total Corr P75 P60 P75 P60
PCT KLBHR PPM PPMD PPM LBMMBTU PPM LBMMBTU
05/10/201710:00 10.6 381 368.7 458.2 90.9 0.187 252.1 0.722
05110/201710:01 10.5 380 280.2 351.5 91.4 0.190 253.0 0.732
05/10/201710:02 10.5 379 249.5 313.0 92.2 0.192 253.9 0.735
05/10/201710:03 10.5 380 230.9 289.7 93.0 0.194 254.5 0.736
05/10/201710:04 10.4 381 227.1 287.6 93.4 0.196 254.6 0.744
0511 01201 7 1 0:05 10.5 381 245.9 308.5 94.1 0.196 255.2 0.738
05/10/201710:06 10.5 379 254.0 318.6 94.3 0.196 254.9 0.737
05/10/201710:07 10.4 372 224.9 284.8 94.3 0.198 254.6 0.744
05/101201710:08 10.3 368 184.8 236.3 94.8 0.201 253.9 0.749
05/10/201710:09 10.1 365 160.8 209.7 95.1 0.206 252.7 0.760
05110/201710:10 10.1 364 150.6 196.4 95.3 0.206 252.0 0.758
05/10/201710:11 10.1 365 158.5 206.7 95.7 0.207 251.2 0.756
05/10/201710:12 10.2 370 178.4 230.4 95.6 0.205 253.3 0.754
05110/201710:13 10.2 373 210.0 271.2 95.4 0.204 272.3 0.811
05/10/201710:14 10.4 378 253.8 321.4 95.1 0.200 273.7 0.799
05110/201710:15 10.4 381 297.4 376.7 94.5 0.199 273.4 0.799
05110/201710:16 10.5 384 302.3 379.2 93.9 0.195 274.9 0.795
05/10/201710:17 10.5 387 288.7 362.2 93.4 0.194 274.9 0.795
05/101201710:18 10.6 390 309.4 384.5 93.0 0.192 275.5 0.790
05/10/201710:19 10.7 394 388.8 478.6 92.3 0.188 277.0 0.786
05110/201710:20 10.7 397 492.5 606.3 91.6 0.187 279.2 0.793
Average 10.4 379 259.9 327.2 93.8 0.197 261.8 0.763
Maximum 10.7 397 492.5 606.3 95.7 0.207 279.2 0.811
Minimum 10.1 364 150.6 196.4 90.9 0.187 251.2 0.722
Report generated on: 05/10/2017 10:32 Data is expressed in Standard Time Page 1

Data Summary Report
Facility Name: Capital Power Southport Location: Southport, NC Source: Stack
Stack CO Stack CO Stack CO2 Stack NOx Stack NOx Rt Stack S02 Stack S02 Rt Stack STEAM
Corr P75 P75 P60 Low P75 P60 Total
PPM PPMD PCT PPM LBMMBTU PPM LBMMBTU KLBHR
05110/201710:30 859.5 1029.2 11.0 86.8 0.172 253.8 0.701 389
05/10/201710:31 326.8 394.9 10.9 90.5 0.181 232.8 0.649 385
05/10/201710:32 201.1 247.6 10.7 93.0 0.190 228.0 0.647 383
05/101201710:33 208.0 258.5 10.6 92.8 0.191 232.0 0.665 380
05/101201710:34 217.7 270.5 10.6 92.9 0.191 233.6 0.670 374
05/10/201710:35 215.0 267.2 10.6 93.0 0.192 233.3 0.669 372
05/101201710:36 196.6 244.3 10.6 93.4 0.193 231.6 0.663 370
05/10/201710:37 182.6 229.1 10.5 93.6 0.195 230.2 0.666 371
05/10/201710:38 191.1 239.7 10.5 93.9 0.195 228.7 0.662 373
05/10/201710:39 214.2 266.2 10.6 94.0 0.194 227.6 0.652 375
05/10/201710:40 231.8 288.0 10.6 94.2 0.194 229.0 0.657 376
05/10/201710:41 234.6 291.5 10.6 94.5 0.195 231.8 0.664 378
05/10/201710:42 235.3 292.4 10.6 94.5 0.195 233.5 0.669 377
05/10/201710:43 250.0 310.7 10.6 94.4 0.195 235.2 0.674 373
05/1 01201 7 1 0:44 246.1 308.7 10.5 94.5 0.197 234.8 0.679 369
05/10/201710:45 223.8 280.7 10.5 94.9 0.197 224.9 0.651 369
05110/201710:46 207.0 262.2 10.4 95.4 0.200 230.4 0.673 368
05/10/201710:47 205.2 259.9 10.4 95.7 0.201 232.7 0.680 367
051101201710:48 196.8 249.3 10.4 96.2 0.202 236.9 0.692 365
05/10/201710:49 177.8 227.4 10.3 96.7 0.205 236.6 0.698 366
05/10/201710:50 172.9 223.3 10.2 97.4 0.209 236.4 0.704 367
Average 247.3 306.7 10.6 93.9 0.194 233.0 0.671 374
Maximum 859.5 1029.2 11.0 97.4 0.209 253.8 0.704 389
Minimum 172.9 223.3 10.2 86.8 0.172 224.9 0.647 365
Report generated on: 05/10/2017 12:14 Data is expressed in Standard Time Page 1

Data Summary Report
Facility Name: Capital Power Southport Location: Southport, NC Source: Stack
Stack CO Stack CO Stack CO2 Stack NOx Stack NOx Rt Stack SO2 Stack SO2 Rt Stack STEAM
Corr P75 P75 P60 Low P75 P60 Total
PPM PPMD PCT PPM LBMMBTU PPM LBMMBTU KLBHR
05/10/201711:00 224.0 278.3 10.6 96.5 0.199 256.3 0.735 383
05/10/201711:01 232.8 286.6 10.7 96.2 0.196 256.2 0.727 383
05/10/201711:02 227.9 280.5 10.7 96.2 0.196 255.1 0.724 383
05/10/201711:03 204.2 253.7 10.6 96.2 0.198 254.6 0.729 383
05/10/201711:04 197.7 245.7 10.6 96.4 0.199 253.6 0.726 381
05/10/201711:05 199.9 248.4 10.6 96.2 0.198 251.5 0.721 378
05/10/201711:06 191.2 239.9 10.5 96.8 0.201 250.0 0.723 374
05/10/201711:07 166.7 211.1 10.4 97.2 0.204 248.5 0.726 373
05/101201711:08 147.2 186.4 10.4 97.4 0.205 247.1 0.722 374
05110/201711:09 173.8 220.1 10.4 97.2 0.204 246.1 0.719 374
05110/201711:10 234.5 297.0 10.4 96.8 0.203 245.5 0.717 375
05/10/201711:11 281.0 352.5 10.5 96.5 0.201 245.6 0.711 377
05/10/201711:12 287.4 360.5 10.5 96.5 0.201 250.4 0.724 378
05/10/201711:13 267.9 336.1 10.5 96.4 0.201 263.7 0.763 375
05/10/201711:14 240.3 301.4 10.5 96.2 0.200 259.1 0.750 375
05/10/201711:15 218.6 276.9 10.4 96.5 0.203 257.1 0.751 377
05/10/201711:16 211.1 267.4 10.4 96.6 0.203 258.6 0.755 376
05/10/201711:17 223.4 282.9 10.4 96.6 0.203 259.9 0.759 376
05/10/201711:18 256.2 321.4 10.5 96.3 0.200 260.5 0.754 376
05/10/201711:19 331.4 411.8 10.6 88.2 0.182 261.5 0.749 375
05/10/201711:20 453.8 558.6 10.7 86.0 0.176 263.1 0.747 376
Average 236.7 296.1 10.5 95.7 0.199 254.5 0.735 377
Maximum 453.8 558.6 10.7 97.4 0.205 263.7 0.763 383
Minimum 147.2 186.4 10.4 86.0 0.176 245.5 0.711 373
Report generated on: 05/10/2017 12:15 Data is expressed in Standard Time Page 1

Data Summary Report
Facility Name: Capital Power Southport Location: Southport, NC Source: Stack
Stack CO Stack CO Stack CO2 Stack NOx Stack NOx Rt Stack SO2 Stack SO2 Rt Stack STEAM
Corr P75 P75 P60 Low P75 1360 Total
PPM PPMD PCT PPM LBMMBTU PPM LBMMBTU KLBHR
05/10/201711:30 367.5 448.2 10.8 85.3 0.173 201.0 0.565 373
05/10/201711:31 284.6 353.7 10.6 86.1 0.177 199.8 0.573 370
05/10/201711:32 220.8 277.0 10.5 86.9 0.181 198.6 0.575 373
05/101201711:33 212.9 267.1 10.5 87.8 0.183 215.3 0.623 374
05/10/201711:34 276.8 344.0 10.6 88.3 0.182 232.9 0.667 375
05/10/201711:35 335.2 408.8 10.8 89.1 0.180 230.1 0.648 374
05/10/201711:36 322.8 397.4 10.7 89.8 0.183 226.1 0.642 371
05110/201711:37 261.8 325.3 10.6 90.4 0.186 225.6 0.647 370
05/10/201711:38 219.5 275.4 10.5 91.1 0.190 225.5 0.653 370
05110/201711:39 210.0 263.4 10.5 91.9 0.191 226.6 0.656 370
05/10/201711:40 197.2 249.8 10.4 93.2 0.196 238.7 0.698 367
05/10/201711:41 172.5 220.6 10.3 94.9 0.201 246.6 0.727 363
05/10/201711:42 151.6 195.8 10.2 96.6 0.207 250.6 0.747 359
05/10/201711:43 144.6 188.6 10.1 98.0 0.212 245.5 0.739 354
05/10/201711:44 151.8 199.9 10.0 99.1 0.217 246.7 0.750 353
05/101201711:45 156.8 208.6 9.9 100.2 0.221 248.0 0.761 353
05/10/201711:46 155.5 206.9 9.9 101.5 0.224 259.6 0.797 356
05/10/201711:47 146.2 194.5 9.9 101.7 0.224 275.4 0.845 359
05/10/201711:48 142.2 187.3 10.0 101.9 0.223 278.0 0.845 363
05/10/201711:49 147.2 192.0 10.1 101.5 0.220 270.8 0.814 365
05110/201711:50 152.9 197.4 10.2 101.2 0.217 269.8 0.804 365
Average 211.0 266.7 10.3 94.1 0.199 238.6 0.704 366
Maximum 367.5 448.2 10.8 101.9 0.224 278.0 0.845 375
Minimum 142.2 187.3 9.9 85.3 0.173 198.6 0.565 353
Report generated on: 05/10/2017 12:15 Data is expressed in Standard Time Page 1

1
Unit 1 Boiler C: Overview — ' 13:15:03
Selected Level Attemperauort e^; .al:e 10May17
126.9 -E-= �; - - Security:
$
Air Fivw SP i_ L
FO+ROFA i Crur+� RAr� I
Flow PS' It F-` Main V 1
Sagho.use Inlet i• I W
Fuel SP 79.69 Temp SuperheaterTC
810,w- oWn primary Seei.ndar}
8agnouse OF
ID Fal� ::- s3s.7 - System
am fa L F �
• r Baghouse C
70
To Stack
M1Alr O$ l -- "D L Ornp-PG9
MU%In dg -7 - 5ootalowers
7 9 C=_r
f --- 2 7rl1n{?nld•ArF Rdil0 ..
Fr,FAN - -:
�i L j ! Air eater r
S. 7xygen Setpaint
"1IaIAS Bias !_!1 Alarm
Fntr Is r
$Q $ ;.I-�'�-: _ 3 1 G 18.7 4.1 Summary
�Drrip-FL35 -- Furnace Pressure
I'Mr 08 ROFAAir Flo,.-,, Sezpoint Si l e ri ce
alas a.o
Ack All
SP �Eductors yy
S FJ_O ti i Gra3e I+ress,ire Ac k Top
-
F❑F1Yr 12 lir Tntar L GFA FAN
- - woo, 18AG_@_1NTEMP
OF a"hv 12Hr TOSaI �:J iVllx Fuel Dand� � ` f `- - ! _ _
SL1.,1 a
CC= f
= - omp-Pos .l �_- UnderGrate ' �i 4 = 1E3AG $ INTP
`I LO SP Untlerc�rase = - _ _
Air Press ` Wood Fuel Grnd l--BSTT130B
sun Flw Caiiy Total 0•0 I _ _ v _.. �. �� iF'STC280_PIL
1BLRBTCS
iPSTT?70
- — 1BLRBTCP B F
. _
_ BGFC200 - _
QV , 1MHTSH5104
,lMHTSHH5104
. - i <_, r , , • _ ... - _ � Sal ��
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Unit 1 Boiler B: Overview ' 13:14-52
Attemmperanan f vent valve �+ 10Ma 17
FD f ROFA 32 w�_75. C --��- -_-= L
I
Air Flow SP ! �r 1� 3 _ Security: r3
lanual Tri - Boiler 8 �r.,_= jeCc•_.
rrr Cru ,Press 1 •- 3 � - �
FD+RAFA 1 Drum E =1 ' ..-. nAain ' I1
Baghouse Inlet
Fuel SP $5A1 T ma SuperheaterTC
341.6 _'_ Primary Seconaary
Eaghcuse OP Biowdewn �
10 FAN
System
_* - Baghouse 6 f .. .. -= - 994.8 1EtsTr_1?A
TO Sack r
"tris 1130.E _ = i00 C., -1$ L - ^3�.� _ ., .
,Itf 17 E onomiaer F Dmp•Pas _
FSootBlowers
-_ 02 Trim Dma-A F Ratio
FD FAhI
3 9.9 �'= o 00 rir r
Air Heater -
1- .,,,,_,_-r I Retraored ©xygen 5etpaint
+r alas a,as r U1 Alarm
F— -- 3,137 0-3 Summary
Mtf [8 3-: _', �•-`=- Om Pes - Furnace Pressure
-----� P RCP.AAir Flvr: Setparnt Silence
I ; -
Mir Ce
Q.25
r,•�l .. ,� Coal Ack All
Bias 0-0 —�
Eauctors -
�.
pFAAir Press SP �. C,sai� f'�essict '•-
wfs.lAS 6. 7 Ai s .. i�ri _ I �. . +c Ack Top
OFA FAN - 16AG B INTE149P
1 Evood
FD Flw 12 Kr Total L
r-- - - Mix Fuel Ointl `
OF Flw 12Hr Total Imo' Under,arate Rear r^--Frroo-- 1CSLT2C
Omp•Pos .. UntlerGr3te Air Press;Temp �= _ = CEI;r G 0"1
9t I`a18 1 L 1BAG B_iF it= r+:
- L4 SP r 719 =.r_r � 2.3 _ Woad Fiisi prrttl185T 1130E
E
`- �----- 1RSTG2$0 Pik`
Srr!t Flw Daily Total 0.3 653 '_ � ? 3 l ` '' �" IOLRBTCS
1 P S TT270
=+LRBTCP B A.
r 1, _ til
NA , _ MHTSH51Q4
V ,. r. : , Eck 1 MHTSHH5104
- - Sei P;
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Unit 'I Boiler A: Overview — 13:13:38
SID•-• e:Iel Attemperatfan :er:'da:ve 10Mav17
PD:T RCFA i F9Q.67 B C - - L rr
Air Flow SP I - L _�..w - —
Manual Trip Boiler A } � Security: 3
FO+ROFA urn Press- I _ ! 1 1' — -
PI4-ROTA -. - - — Main U 1
Baghouse Intel �~
Fuel 5P 82.39'-: Temp Superheater M
J hvuse OP
8lownflwn _ primary Secondary
Sag
ID FAN �- �. o. ... System
L
Baghouse A _
To Stack r" - r- -- !� -
MtrIB0.8
iritrDH - r 1[7(} Cmp-Fos _ �7 r J -
' � '__ Feed,4ater �•
sootB€owers
rftrwndy :C1 -=:F c.g 5 L==F
3 1) i,_. _ . Print
k 2 02 Trim Dmd-A•F Ratio
8�4. '-' _ snap
L -
�. Airlestlsr
Retracted oxygen Setpolnt
F❑FAN
' %wBIAS
. * Bias U1 Alarm
'' 3 15 •0.7 SummaryMtr sB 3 _:.F 42 r L I ;.
'.::DmP-Po.s ., a a.
r Furnaet Pressure
Mtr 02 ROFA Air Flowsetpaint Silence
r _
-0.25 - -
zx lrr coal ACk Al l
Bias 0.0
OFAAIr press SA Enucters ' r
w'131As 6,01 i' , rae,z s'resssue 45 5 •"r• L Ack Top
I �-
OFAFAtd F `� 1BAG B INTEMP
Ft1 Five 12 Hr Total yr L � _ 4VgRR _ _
F
- * I 'CWTE20H_AIP 1 F
� i,r•. * 1 PSFT270 AIP
OF FIw 12Hr Tata; 1 " r.7lx Fue€ortic€
c, � prrp-Pas 1lndarGrate Undergrate Rear - Front _- 1 C 5LT20
O Fir Press:TemD O r; rI,,; 1 BAG 8 INTEMP2
wood Fuel Dmd i 113STT7308
Sim FFIYINr Cafly Total --
•� _-_- 5 18LRSTCS C
1 PSTT270
f1BLR6TCP B A!P
1 BGFC200 - 1 HBLY65 - -
NAVStartu _ -- - _ _ __--
Y�.:� 'Condensate 's' a- -1: G "�.�_ F 1MHTSH5104
�c• 1 MHTSHH5104
r I_r Sel Pt
g 1 a b l' j: A min" VW 1FI7(A6111A ALM