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License Amendment Request for Extended Power Uprate, Attachment 08; Cameron/Caldon Ultrasonics Engineering Reports
	ML103560184
Person / Time
Site:	Turkey Point
Issue date:	12/14/2010
From:	Stacy P; Alden Research Lab
To:	; Office of Nuclear Reactor Regulation
References
	L-2010-113, L-2010-299, LAR 205
	Download: ML103560184 (79)
	v • d • e

Turkey Point Units 3 and 4 L-2010-113 Docket Nos. 50-250 and 50-251 Turkey Point Units 3 and 4 LICENSE AMENDMENT REQUEST FOR EXTENDED POWER UPRATE ATTACHMENT 8 Cameron/Caldon Ultrasonics Engineering Reports:

ER-748, Revision 1, Meter Factor Calculation and Accuracy Assessment for Turkey Point 3 Nuclear Power Plant, dated June 2010 ER-752, Revision 1, Meter Factor Calculation and Accuracy Assessment for Turkey Point Nuclear Power Plant Unit 4, dated June 2010 ER-783, Revision 2, Bounding Uncertainty Analysis for Thermal Power for Turkey Point Units 3 & 4 Using LEFM CheckPlus' System, dated June 2010

[Proprietary Reports Withheld Under 10 CFR 2.390]

Alden Research Laboratories Test Reports:

No. 2009-100-C1229, Calibration of Three 14" LEFM CheckPlus Meters, dated May 2009 No. 2009-101-C1229, Calibration of Three 14" LEFM CheckPlus Flow Meters, Rev 1, dated June 25, 2010 This coversheet plus 78 pages

CALIBRATION OF THREE 14" LEFM CHECKPLUS METERS CAMERON MEASUREMENT SYSTEMS PURCHASE ORDER NUMBER 4501956005 MAY 2009 - REPORT NO. 2009-100-C1229 CERTIFIED BY Philip S. Stacy ALDEN RESEARCH LABORATORY, INC.

30 SHREWSBURY STREET HOLDEN, MASSACHUSETTS 01520

All Client supplied information and calibration results are considered proprietary and confidential to the Client. If a third party is a witness during calibrations or if the Client requests transmittal of data to a third party, Alden considers that the Client has waived confidentiality for the Witness.

In the event the Client distributes any report issued by Alden outside its own organization, such report shall be used in its entirety, unless Alden approves a summary or abridgment for distribution.

No advertising or pUblicity containing any reference to Alden or any employee, either directly or by implication, shall be made use of by Client without Alden's written approval.

INTRODUCTION Three 14" LEFMCheckPlus Meters, Serial Numbered 29013, 29016, and 29018, were tested and calibrated at Alden Research Laboratory, Inc. for Cameron Measurement Systems under their Purchase Order Number 4501956005 using Alden's standard test procedures, QMSM-01 Rev. 3. Flow meter performance is presented in both tabular and graphical format for configurations simulating field piping and included parametric testing. Results are shown as meter factor versus flow in gpm.

FLOW ELEMENT INSTALLA nON The meters were installed in Test Lines 1 and 2 in the Allen High Reynolds Number Facility shown in plan view on Figure 1. Water was provided by a pair of 300 HP electrically driven centrifugal pumps providing a maximum head of 135 ft and a maximum flow of20,000 gpm.

The detailed piping arrangements, immediately upstream and downstream of the flow meter, are shown in Figures 2 through 5 and include all significant fittings and pipe lengths with meter location identified. Careful attention was given to aligning the flow element with the test line piping and to assure no gaskets between flanged sections protruded into the flow. Vents were provided at critical locations of the test line to purge the system of air.

TEST PROCEDURE After checking the installation, water was introduced into the system to equalize line and primary element temperature to water temperature. The downstream control valve was then closed and vent valves in the test line were opened to remove air from the system. With the line flow shut off, the flow meter output was checked for zero flow indication. Prior to the test run, the control valve was set to the desired flow. For the gravimetric measurement method, the flow was diverted away from the weigh tank.

After steady state conditions in the test line and instrument readings had been reached, the weigh tank discharge valve was closed and the weigh tank scale indicator and the electric timer were both zeroed.

The flow was then diverted into the weigh tank, which automatically started the timer.

As the weigh tank run was initiated, Cameron personnel noted the time on the flow meters and logged the meter output continuously. At the end of each test run, flow was diverted away from the weigh tank and the timer and the totalizer was stopped to terminate the test run. The weight of water in the tank, elapsed time, and water temperature were recorded on a data sheet. At the end of the weigh tank Report No. 2009-100-C1229 Page 1 of38

run Cameron personnel noted the time again so that the meter output could be averaged over the collection time. Cameron personnel provided Alden the average meter reading at the end of each test series. The control valve was then adjusted to the next flow and the procedure repeated. During the time allowed to stabilize the new flow, the data were entered into the computer to determine the flow and the results were plotted so that each test run was evaluated before the next run began.

FLOW MEASUREMENT METHOD Flow was measured by the gravimetric method using a tank mounted on calibrated scales having a capacity of 100,000 pounds (resolution 1 lb). Water passing through the flow element was diverted into the tank with a hydraulically operated knife edge passing through a rectangular jet produced by a diverter head box. A Hewlett-Packard 10 MHz Frequency Counter with a resolution 0.001 sec was started upon flow diversion into the tank by an optical switch, which is positioned at the center of the jet. The timer was stopped upon flow diversion back to waste and the elapsed diversion time was recorded. A thermistor thermometer measured water temperature to allow calculation of water density.

Volumetric flow was calculated by Equation (1).

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. d Ibm aIr enslty, ft3 The buoyancy correction includes air density calculated by perfect gas laws with the standard barometric pressure, a relative humidity of 75%, and measured air temperature. The weigh tank is periodically calibrated to full scale by the step method using 10,000 Ibm of cast iron weights, whose calibration is traceable to NIST. Flow calculations are computerized to assure consistency. Weigh tank calibration data and water density as a function of temperature, are stored on disk file. Data were recorded manually and on disk file for later review and reporting.

Report No. 2009-100-C1229 Page 2 of38

TEST RESULTS Test results are shown both in tabular form and plotted versus flow. The raw data required to calculate flow by the gravimetric method, the meter flow total, and the meter factor are listed in the tables.

Meter factor is plotted versus flow for each configuration. A typical test series included equally spaced test flows ranging from the maximum system flow to a minimum flow of about 1,900 gpm with multiple runs at each flow. Tests were conducted with the piping simulating the field installation, parametric tests, including a flow disturbance.

An uncertainty analysis was conducted of the flow measurements in accordance with the methods of NIST Technical Note 1297 Guidelines for Evaluating and Expressing the Uncertainty of NIST Measurement Results and NISTIR 6919 Recommended Guide of Determining and Reporting Uncertainties for Balances and Scales by evaluating each elementary error source for flow measurement. Type A uncertainties were estimated from the precision indices of the test data and Type B uncertainties were estimated from experience. The collection weight was about 95,000 lb for most flow measurements. An example calculation for one test run is shown in the Appendix as a table listing the elementary error sources for each measured component (weight, time, density, and diverter) and combine the error sources by the root sum square (RSS) method. Combining the components results in an expanded uncertainty estimate of about 0.09% at the 95% confidence level. Analyses were conducted for each test flow and the results are plotted versus flow.

Calibrations of the test instrumentation (temperature, time, weight, and length measurements) are traceable to the National Institute of Standards and Technology (formerly the National Bureau of Standards).

Alden's Quality Assurance Program is designed to meet ANSIINCSL Z540-1-1994 "Calibration Laboratories and Test Equipment-General Requirements" (supercedes MIL-STD-45662A).

Report No. 2009-100-C1229 Page 3 of38

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00 11 98 94725 344.841 1990.24 1995.67 0.9973 12 98 94877 345.461 1989.86 1996.39 0.9967 13 98 94771 345.156 1989.39 1996.63 0.9964 14 98 94825 345.275 1989.80 1996.44 0.9967 15 98 94739 344.991 1989.63 1996.69 0.9965 16 98 95386 92.840 7443.73 7467.03 0.9969 17 98 95286 92.785 7440.38 7457.93 0.9976 18 98 95437 92.952 7438.93 7456.85 0.9976 19 98 95316 92.735 7446.86 7465.80 0.9975 20 98 95331 92.910 7434.03 7457.73 0.9968 21 98 96200 53.791 12958.15 12997.48 0.9970 22 98 96244 53.910 12935.40 12982.94 0.9963 23 98 96196 53.904 12930.62 12979.92 0.9962 24 98 96051 53.685 12963.95 13010.31 0.9964 25 98 96167 53.899 12928.36 12975.65 0.9964 The data reported on herein was obtained by measuring equipment the calibration of which is traceable to NIST, following the installation and test procedures referenced in this report, resulting in a flow meaSurement uncertainty of +/- 0.25% or less.

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THIS PAGE INTENTIONALL Y LEFT BLANK Report No. 2009-100-CI229 Page 28 of38

Figure 5 Allen Facility Lines 1 & 2 CAM44J - CAM44K

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ITEM #1 24" 36"x24" CAM44J 112 MOON INSTALLED (SEE SECTION AA)

CAM44K 112 MOON INSTALLED (SEE SECTION BB)

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GPM GPM 63.268 10983.32 11010.82 63.292 10980.12 10997.68 63.238 10978.60 10999.39 63.345 10970.91 10993.04 63.293 10980.70 11005.68 184.850 3726.56 3736.44 184.935 3725.34 3736.38 184.768 3724.46 3733.89 184.829 3723.93 3734.18 184.927 3723.69 3732.92 92.252 7490.22 7509.18 92.225 7491.12 7505.13 92.246 7487.65 7501.23 92.241 7485.77 7500.08 92.281 7488.51 7504.38 56.786 12258.66 12284.60 56.782 12251.46 12277.18 56.708 12260.55 12286.85 56.863 12252.47 12275.80 56.752 12260.77 12279.95 The data reported on herein was obtained by measuring equipment the calibration of which is traceable to NIST, following the installation and test procedures referenced in this report, resulting in a flow measurement uncertainty of +/- 0.25% or less.

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GPM GPM 56.625 12305.82 12335.60 56.567 12307.11 12328.51 56.515 12301.75 12318.51 56.651 12301.40 12326.03 56.628 12300.76 12320.35 184.324 3735.80 3745.89 184.102 3736.24 3747.18 184.562 3736.47 3748.41 184.258 3737.92 3749.55 184.335 3737.22 3747.94 63.531 10952.64 10974.87 63.468 10951.44 10969.11 63.382 10949.75 10967.75 63.512 10945.73 10968.18 63.465 10945.03 10962.75 92.332 7494.32 7504.81 92.216 7494.66 7502.02 92.061 7492.98 7522.60 92.056 7513.42 7520.71 92.071 7496.98 7520.13 The data reported on herein was obtained by measuring equipment the calibration of which is traceable to NIST, following the installation and test procedures referenced in this report, resulting in a flow measurement uncertainty of +/- 0.25% or less.

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WATER DENSITY Temperature Density Temperature Density Temperature Density Fahrenheit lb m/ft 3 Fahrenheit Fahrenheit lb m/ft 3 32 62.4179 62 62.3549 92 62.0903 33 62.4201 63 62.3489 93' 62.0788 34 62.4220 64 62.3427 94 62.0671 35 62.4235 65 62.3363 95 62.0552 36 62.4246 66 62.3296 96 62.0432 37 62.4255 67 62.3228 97 62.0311 38 62.4260 68 62.3157 98 62.0188 39 62.4262 69 62.3084 99 62.0063 40 62.4261 70 62.3010 100 61.9937 41 62.4257 71 62.2933 101 61.9810 42 62.4250 72 62.2855 102 61.9681 43 62.4240 73 62.2774 103 61.9551 44 62.4227 74 62.2692 104 61.9419 45 62.4211 75 62.2608 105 61.9286 46 62.4193 76 62.2522 106 61.9151 47 62.4171 77 62.2434 107 61.9015 48 62.4147 78 62.2344 108 61.8878 49 62.4121 79 62.2252 109 61.8739 50 62.4092 80 62.2159 110 61.8599 51 62.4060 81 62.2063 111 61.8458 52 62.4025 82 62.1966 112 61.8315 53 62.3988 83 62.1868 113 61.8172 54 62.3949 84 62.1767 114 61.8027 55 62.3907 85 62.1665 115 61.7880 56 62.3863 86 62.1561 116 61.7733 57 62.3816 87 62.1456 117 61.7584 58 62.3768 88 62.1348 118 61.7434 59 62.3716 89 62.1239 119 61.7284 60 62.3663 90 62.1129 120 61.7132 61 62.3607 91 62.1017 121 61.6978 Report No, 2009-100-C1229 Page 34 of38

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Mass 96993 Time Uncertainty Analysis Allen 100,000 Lb Scale Cameron Purchase Order No: 4501956005 14" LEFM Check Plus: sin 29013 Calibration Buoyancy Reproducibility Loss Resolution Repeatability Standard Uncertainty Percent 0.03635 0.00520 0.01600 0.00208 0.00060 0.00119 47.0 seconds Standard Deadband 0.00030 0.00102 Resolution 0.00123 Repeatability 0.00246 Density Temperature 96 Standard Impurities 0.00279 0.01000 Reproducibility 0.01117 Resolution 0.00112 Diverter Inclusive 0.01000 Flow Standard Uncertainty Percent 0.044 Expanded Uncertainty Percent 0.088 Report No. 2009-1 OO-C 1229 Page 37 of38

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CALIBRATION OF THREE 14" LEFM CHECKPLUS FLOW METERS CAMERON MEASUREMENT SYSTEMS PURCHASE ORDER NUMBER 4501956006 JUNE 2009 - REPORT NO. 2009-101-C1229 REVISION 1 - 6/25/1 0 CERTIFIED BY Philip S. Stacy ALDEN RESEARCH LABORATORY, INC.

30 SHREWSBURY STREET HOLDEN, MASSACHUSETTS 01520

All Client supplied information and calibration results are considered proprietary and confidential to the Client. If a third party is a witness during calibrations or if the Client requests transmittal of data to a third party, Alden considers that the Client has waived confidentiality for the Witness.

In the event the Client distributes any report issued by Alden outside its own organization, such report shall be used in its entirety, unless Alden approves a summary or abridgment for distribution.

No advertising or publicity containing any reference to Alden or any employee, either directly or by implication, shall be made use of by Client without Alden's written approval.

INTRODUCTION Three 14" LEFM CheckPlus Flow Meters were tested and calibrated at Alden Research Laboratory, Inc. for Cameron Measurement Systems under their Purchase Order Number 4501956006 using Alden's standard test procedures, QMSM-01 Rev. 3. Flow meter performance is presented in both tabular and graphical format for configurations simulating field piping and included parametric testing.

Results are shown as meter factor versus flow in gpm. Revision 1 issued to correct a typographic error showing a pipe dimension of 7' 1/2" on page 25. The length of the pipe used during testing was confirmed to be 8'-10-1/2" and the Figure was corrected.

FLOW ELEMENT INSTALLATION The meters were installed in the Allen High Reynolds Number Facility shown in plan view on Figure

1. Water was provided by a pair of 300 HP electrically driven centrifugal pumps providing a maximum head 135 ft and a maximum flow of20,000 gpm.

The detailed piping arrangements, immediately upstream and downstream of the flow meter, are shown in Figures preceding the test data and include all significant fittings and pipe lengths with meter location identified. Careful attention was given to aligning the flow element with the test line piping and to assure no gaskets between flanged sections protruded into the flow. Vents were provided at critical locations of the test line to purge the system of air.

TEST PROCEDURE After checking the installation, water was introduced into the system to equalize line and primary element temperature to water temperature. The downstream control valve was then closed and vent valves in the test line were opened to remove air from the system. With the line flow shut off, the flow meter output was checked for zero flow indication. Prior to the test run, the control valve was set to the desired flow. For the gravimetric measurement method, the flow was diverted away from the weigh tank.

After steady state conditions in the test line and instrument readings had been reached, the weigh tank discharge valve was closed and the weigh tank scale indicator and the electric timer were both zeroed.

The flow was then diverted into the weigh tank, which automatically started the timer.

As the weigh tank run was initiated, Cameron personnel noted the time on the flow meters and logged the meter output continuously. At the end of each test run, flow was diverted away from the weigh Report No. 2009-101-C1229 Page 1 of36

tank and the timer and the totalizer was stopped to terminate the test run. The weight of water in the tank, elapsed time, and water temperature were recorded on a data sheet. At the end of the weigh tank run Cameron personnel noted the time again so that the meter output could be averaged over the collection time. Cameron personnel provided Alden the average meter reading at the end of each test series. The control valve was then adjusted to the next flow and the procedure repeated. During the time allowed to stabilize the new flow, the data were entered into the computer to determine the flow and the results were plotted so that each test run was evaluated before the next run began.

FLOW MEASUREMENT METHOD Flow was measured by the gravimetric method using a tank mounted on calibrated scales having a capacity 100,000 pounds (resolution lIb). Water passing through the flow element was diverted into the tank with a hydraulically operated knife edge passing through a rectangular jet produced by a diverter head box. A Hewlett-Packard 10 MHz Frequency Counter with a resolution 0.001 sec was started upon flow diversion into the tank by an optical switch, which is positioned at the center of the jet. The timer was stopped upon flow diversion back to waste and the elapsed diversion time was recorded. A thermistor thermometer measured water temperature to allow calculation of water density.

Volumetric flow was calculated by Equation (1).

w (1) qa = Tp B w c where ft3 qa actual flow, -see W

mass of water collected, Ibm T

time, sec Pw d

Ibm water enslty, ft3 Be buoyancy correction, 1 - 2 Pw Pa

. d Ibm aIr enslty, ft3 The buoyancy correction includes air density calculated by perfect gas laws with the standard barometric pressure, a relative humidity of 75%, and measured air temperature. The weigh tank is periodically calibrated to full scale by the step method using 10,000 Ibm of cast iron weights, whose calibration is traceable to NIST. Flow calculations are computerized to assure consistency. Weigh Report No. 2009-101-C1229 Page 2 of36

tank calibration data and water density as a function of temperature, are stored on disk file. Data were recorded manually and on disk file for later review and reporting.

TEST RESULTS Test results are shown both in tabular form and plotted versus flow. The raw data required to calculate flow by the gravimetric method, the meter flow total, and the meter factor, are listed in the tables.

Meter factor is plotted versus flow for each configuration. A typical test series included equally spaced test flows ranging from the maximum system flow to a minimum flow of about 1,900 gpm with multiple runs at each flow. Tests were conducted with the piping simulating the field installation, parametric tests, including a flow disturbance.

An uncertainty analysis was conducted of the flow measurements in accordance with the methods of NIST Technical Note 1297 Guidelines for Evaluating and Expressing the Uncertainty of NIST Measurement Results and NISTIR 6919 Recommended Guide of Determining and Reporting Uncertainties for Balances and Scales by evaluating each elementary error source for flow measurement. Type A uncertainties were estimated from the precision indices of the test data and Type B uncertainties were estimated from experience. The collection weight was about 95,000 lb for most flow measurements. An example calculation for one test run is shown in the Appendix as a table listing the elementary error sources for each measured component (weight, time, density, and diverter) and combines the error sources by the root sum square (RSS) method. Combining the components results in an expanded uncertainty estimate of about 0.09% at the 95% confidence level. Analyses were conducted for each test flow and the results are plotted versus flow.

Calibrations of the test instrumentation (temperature, time, weight, and length measurements) are traceable to the National Institute of Standards and Technology (formerly the National Bureau of Standards).

Alden's Quality Assurance Program is designed to meet ANSI/NCSL Z540-1-1994 "Calibration Laboratories and Test Equipment-General Requirements" (supercedes MIL-STD-45662A).

Report No. 2009-101-C1229 Page 3 of36

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GPM GPM 63.559 10949.55 10956.02 63.590 10942.07 10962.66 63.412 10972.89 10978.16 63.460 10954.19 10946.01 63.416 10964.85 10970.45 98.980 6989.46 6998.23 98.955 6985.46 6993.38 98.777 6987.93 6999.90 98.596 6992.42 6998.79 98.858 6988.85 6993.90 73.248 9471.29 9474.22 73.139 9482.03 9482.72 73.202 9471.95 9479.03 73.102 9490.41 9501.65 73.045 9485.94 9493.78 125.748 5491.28 5499.09 126.234 5473.65 5480.57 126.159 5466.53 5474.36 126.226 5460.96 5469.59 126.302 5459.71 5466.25 The data reported on herein was obtained by measuring equipment the calibration of which is traceable to NIST, following the installation and test procedures referenced in this report, resulting in a flow measurement uncertainty of +/- 0.25% or less.

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GPM GPM 63.244 10998.35 11030.98 63.232 10991.08 11016.64 63.187 10994.43 11038.71 63.117 11001.08 11027.05 63.122 10989.15 11030.48 99.195 6965.18 6989.34 99.131 6967.87 6992.29 99.175 6966.45 6990.28 99.249 6957.96 6975.82 99.269 6965.38 6987.03 73.137 9489.06 9515.82 73.049 9487.95 9507.05 73.118 9485.49 9507.67 73.028 9489.51 9514.05 73.089 9474.33 9498.17 125.843 5481.39 5497.26 126.079 5468.04 5482.64 126.420 5456.41 5472.22 126.451 5452.41 5466.25 126.636 5451.17 5465.79 The data reported on herein was obtained by measuring equipment the calibration of which is traceable to NIST, following the installation and test procedures referenced in this report, resulting in a flow measurement uncertainty of +/- 0.25% or less.

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Meter Factor 0.9970 0.9977 0.9960 0.9976 0.9963 0.9965 0.9965 0.9966 0.9974 0.9969 0.9972 0.9980 0.9977 0.9974 0.9975 0.9971 0.9973 0.9971 0.9975 0.9973

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GPM GPM 63.897 10886.03 10890.07 63.910 10877.91 10895.71 63.994 10878.81 10905.14 63.908 10862.82 10875.71 63.945 10878.17 10884.21 98.786 6985.57 6996.16 98.904 6981.47 6995.83 98.884 6984.09 6992.64 98.920 6977.36 6991.02 98.943 6976.95 6989.31 73.157 9487.54 9497.00 73.035 9488.11 9510.21 73.082 9479.34 9491.19 73.134 9484.42 9496.87 73.072 9489.44 9502.48 125.492 5489.85 5501.36 125.790 5486.18 5497.49 125.820 5488.69 5499.53 125.745 5485.72 5497.45 125.734 5487.21 5500.37 The data reported on herein was obtained by measuring equipment the calibration of which is traceable to NIST, following the installation and test procedures referenced in this report, resulting in a flow measurement uncertainty of +/- 0.25% or less.

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CERTIFIED BY: ~~

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CERTIFIED BY: ~~

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WATER DENSITY Temperature Density Temperature Density Temperature Density Fahrenheit lb m/ft 3 Fahrenheit Fahrenheit 32 62.4179 62 62.3549 92 62.0903 33 62.4201 63 62.3489 93 62.0788 34 62.4220 64 62.3427 94 62.0671 35 62.4235 65 62.3363 95 62.0552 36 62.4246 66 62.3296 96 62.0432 37 62.4255 67 62.3228 97 62.0311 38 62.4260 68 62.3157 98 62.0188 39 62.4262 69 62.3084 99 62.0063 40 62.4261 70 62.3010 100 61.9937 41 62.4257 71 62.2933 101 61.9810 42 62.4250 72 62.2855 102 61.9681 43 62.4240 73 62.2774 103 61.9551 44 62.4227 74 62.2692 104 61.9419 45 62.4211 75 62.2608 105 61.9286 46 62.4193 76 62.2522 106 61.9151 47 62.4171 77 62.2434 107 61.9015 48 62.4147 78 62.2344 108 61.8878 49 62.4121 79 62.2252 109 61.8739 50 62.4092 80 62.2159 110 61.8599 51 62.4060 81 62.2063 111 61.8458 52 62.4025 82 62.1966 112 61.8315 53 62.3988 83 62.1868 113 61.8172 54 62.3949 84 62.1767 114 61.8027 55 62.3907 85 62.1665 115 61.7880 56 62.3863 86 62.1561 116 61.7733 57 62.3816 87 62.1456 117 61.7584 58 62.3768 88 62.1348 118 61.7434 59 62.3716 89 62.1239 119 61.7284 60 62.3663 90 62.1129 120 61.7132 61 62.3607 91 62.1017 121 61.6978 Report No. 2009-101-C1229 Page 32 of36

Mass 96985 Time Uncertainty Analysis Allen 100,000 Lb Scale Cameron Purchase Order No: 4501956006 14" LEFM: sin 29017 Calibration Buoyancy Reproducibility Loss Resolution Repeatability Standard Uncertainty Percent 0.03635 0.00520 0.01600 0.00208 0.00060 0.00119 46.9 seconds Standard Deadband 0.00030 0.00103 Resolution 0.00123 Repeatability 0.00246 Density Temperature 93 Standard Impurities 0.00268 0.01000 Reproducibility 0.01073 Resolution 0.00107 Diverter Inclusive 0.01000 Flow Standard Uncertainty Percent 0.044 Expanded Uncertainty Percent 0.088 Report No. 2009-101-C1229 Page 33 of36

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0508180439 PRIMARY STANDARD 00444 STAINLESS STEEL NIST TEST NO. 822/263871-8/23/2005 8/21/2015 S-1 WEIGHT 1969 BLDG 1&2 MASS(20LBm & 10LBm) 00 GE Infrastructure SET TRANSFER STANDARD

0508180444 PRIMARY STANDARD 00471 AMBIENT THERMOMETER AMBIENT TEMPERATURE 1/6/2009 7/7/2009 DP-26RTD 34401 BLDG 1 WI AMBIENT PROBE 0471-A ALLEN FACILITY Page 1 of2

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LAST NEXT CAL CAL DATE DUE 1/6/2009 7/7/2009 2/9/2009 8/10/2009 5/26/2009 5/23/1995 MODEL SERIAL Location NUMBER DP41-RTD 5410983 BLDG 1 53131A MY47000389 BLDG 1 2382 800635 BLDG 1 26DL 9041602 BLDG 1&2 NIA BLDG 1&2 DT2805/571 0118473 BLDG 1 VERIFIED BY HAND CALCS.

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ML103560184

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