Text

Reactor Containment Bldg Integrated Leak Rate Test
	ML20042G590
Person / Time
Site:	Brunswick
Issue date:	02/28/1990
From:	Loflin L; CAROLINA POWER & LIGHT CO.
To:	; NRC OFFICE OF INFORMATION RESOURCES MANAGEMENT (IRM)
References
	NLS-90-105, NUDOCS 9005150119
	Download: ML20042G590 (126)
	v • d • e

L Cp&L Carolina Poner & Light Company NAY 8 1990 SERIAL: NLS 90 105 10 CFR 50, Appendix J United States Nuclear Regulatory Commission

' ATTENTION: Document Control Desk

~

i Washington, DC 205b5 BRUNSWICK STEAM ELECTRIC PIANT, UNIT NO. 2 DOCKET NO. 50 324/ LICENSE NO. DPR 62 INTEGRATED LEAK RATE TEST RESULTS I

Centlemen:

l In accordance with the requirements of 10 CFR 50, Appendix J Paragraphs V.S.1 and V.B.3, Carolina Power & Light Company hereby submits the results of the Brunswick Steau. Electric Plant, Unit 2 Integrated Leak Rate Test performed February 16 17, 1990. Representatives of NRC Region II witnessed the test.

Their findings are discussed in Inspection Report No. 50 325/324/90 09 dated March 29, 1990, t

s Please refer any questions regarding this submittal to Mr. W. R. Murray at (919) 546 4661.

Yours very truly, Leona I.

flin Manag/r Nuc1 car Licending Section WRM/wrm

(\\cor\\b2ilrt)

Enclosure cc:

Mr. S. D. Ebneter (w/cncl.)

Mr. N. B. Le (w/est.)

Mr. W. M, Ruland (w/ encl.)

900515013p 900228

{DR ADOCK 05000324 PDC 411 FayettevHle Street

P. O. Don 1551

Raleigh. N C 27602

}

TENEM I//

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BRUNSWICK STEAM ELECTRIC PIANT

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UNIT NO. 2 REACTOR CONTAINMENT BUILDING INTEGRATED LEAK RATE TEST i

s FEBRUARY 1990 CAROLINA POWER & LIGHT COMPANY l

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i TABLE OF CONTENTS Sect.

Item Title Page 1.0 SYNOPSIS 1

2.O INTRODUSTlQH 3

3.0 GENERAL, TECHNICAL. AND TEST DATA 4

l 3. *.

GENERAL DATA 4

3.2 TECHNICAL DATA 4

3.3 TEST DATA 5

4.0 ACCEPTANCE CRITERIA 6

5.0 TEST INSTRUMENTATION 7

5.1

SUMMARY

OF INSTRUMENTS 7

5.2 SCHEMATIC ARRANGEMENT 8

5.3 CALIBRATION CHECKS 8

5.4 INSTRUMENTATION PERFORMANCE 9

5.5 VOLUME WEIGHTING FACTORS 9

5.6 SYSTEMATIC ERROR ANALYSIS 10 5.7 SUPPLEMENTAL VERIFICATION 13 6.0 TEST PROCEDURE 15 6.1 PREREQUISITES 15 6.2 GENERAL DISCUSSION 15 6.3 TEST PERFORMANCE 17 7.0 METHODS OF ANALYSIS 20 7.1 ABSOLUTE METHOD 20 7.2 STATISTICAL EVALUATION 23 8.0 DISCUSSION OF RESULTS 25 8.1 RESULTS AT Pa 25 8.2 SUPPLEMENTAL TEST RESULTS 28 8.3 AS FOUND ANALYSIS 29 8.4 LOCAL LEAKAGE RATE TEST RESULTS 30

9.0 REFERENCES

31 4

fs APPENDICES SCHEMATIC ARRANGEMENT OF TEST INSTRUMENTATION A

REDUCED TEST DATA B

LEAKAGE RATE TEST GRAPHS C

COMPUTER RESULTS D

E

SUMMARY

OF MEASURED DATA F

TYPE B & C TESTING

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1.0 SYNOPSIS The Brunswick Steam Electric Plant Unit No. 2 reactor containment building was subjected to a periodic

)

integrated leak rate test during the period of February 18 to February 19, 1990.

The purpose of this test was to demonstrate the acceptability of the building leakage rate at an internal pressure of 49.0 psig It/a ) '

Testing was performed in accordance with the requicements of 10CFR50 Appendix J,. ANSI N45.4-1972, Bechtel Tvpical i

Report BN-TOP-1 and Brunswick Steam Electric Plant Unit No. 2 Technical Specifications.

t The Mass Point method of analysis resulted in a measured leakage rate of 0.278%'by weight per day.

The leakage i

rate at the upper bound of the 95% confidence interval was 0.281% by weight per day.

A correction factor of 0.036% by weight per day for ll~ penetrations which were not vented during the test and 4 penetrations that were isolated prior to the test must.be added to the test results.

Therefore, the leakage rate at the upper bound of the 95% confidence interval is 0.317% by weight per

?

day which is below the allowable leakage rate of 0.375%

by weight per day.

Utilizing the Total Time method of analysis, the calculated leakage rate was found to be 0.273% by veight per day and 0.308% by weight per day at the upper bound of the 95% confidence interval.

The mean of the measured leak rates based on total time calculations for the last i

five hours of the test was 0.273% by. weight per day.

With the addition of the Type C penalty, the leakage rate at the upper bound of the 95% confidence interval is 0.344% by weight per day.. All total time analyses are below the allowable leakage rate of 0.375% by weight per day and meet the criteria set ~forth-in Bechtel Topical Report BN-TOP-1 for conduct of a reduced duration integrated leakage rate test.

Using the minimum pathway leakage analysis to determine the "as found" reactor containment integrated leakage rate, indicates that the acceptance criteria would have been exceeded.

1

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I The supplemental instrumentation verification test at Pa demonstrated an agreement between measured reactor containment building integrated leakage rates of 4.6%

using the Mass Point method and 3.6% using the Total Time method which are within the 25% requirement of 10CFR50, j

Appendix J,Section III A.3.b.

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2.0 INTRODUCTION

The objective of the integrated leak rate test was the establishment of the degree of overall leak tightness of the reactor containment building at the calculated design basis accident pressure of 49.0 psig.

The allowable leakage is defined by the design basis accident applied in Nie safety analysis in accordance with site exposure gul aelines specified by 10CTR100.

For the Brunswick Stsam Electric Plant Unit No.

2, the maximum allowable integrated leak rate at the design basis accident pressure of 49.0 psig (P ) la 0.5% by weight per day a

(L ) -

a Testing was performed in accordance with the procedural requirements us stated in Brunswick Steam Electric plant Integrated Primary Containment Leak Rate Test Procedure PT-20.5.

This procedure received two independent technical safety. reviews and was approved by the Manager, Technical Support prior to the commencement of the test.

Leakage rate testing was accomplished at the pressure level of 49.5 psig for a period of eight hours.

The eight hour period was followed by_a four hour supplemental test for verification of test instrumentation.

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3.0 GENERAL, TECHNICAL AND TEST DATA 3.1 GENERAL DATA Owner:

Carolina Power and Light Docket No.

50-324 Location:

Southport, North Ca,rolina Type:

Mark 1, BWR-4 Containment Steel lined, reinforced concrete,

==

Description:==

' light bulb' shaped drywell with torus shaped suppression chamber i

connected by a vent system.

Vacuum breakers are provided between the suppression chamber and both the drywell and reactor building, j

Date Test Completed:

February 19, 1990 3.2 TECHNICAL-DATA Containment Net Free Volume:

294,981 cubic feet Design Pressure:

62 psig Design 0

Temperature:

300 F (drywell), 220 F (suppression chamber)

Calculated Accident Peak Pressure:

49.0 psig Calculated Accident Peak 0

Temperature:

297 F 4

3.3 TEST DATA l

Test Method:

Absolute Data Analysis:

Mass Point.and Total Time Test Pressure:

64.2 psia Max Allowable Leakage Rate (L ):

0.500 wt % per day a

Measured Leakage Rates i

Mass Point 0.278 wt % per day Total Time 0.273 wt % per day Measured Leakage Rate at UCL Mass-Point 0.281 wt % per day Total Time 0.308 wt 4 per day Supplemental Test Flow Rate:

0.495 wt % per day supplemental Toot Measured Leak Rate:

Mass Point 0.750 wt % per day Total Time 0.749 wt % per day Supplemental Test and L Agreement:am Mass Point

4. 6%.

. Total Time 3.6%

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4.0 ACCEPTANCE CRITERIA Acceptance criteria established prior to the test and as specified by 10cFR50, Appendix J, ANSI N45.4-1972 and the Brunswick Steam Electric Plant Unit No. 2 Technical specifications are as follows:

The measured Ic.kage rate (L at the calculated design accident pressure of $$).0 psig (P )

1.

shall be a

less than 75% of the maximum allowable leakage rate (L ), specified as 0.5% by weight of the building a

atmosphere per day.

The acceptanco criteria is determined as follows:

L

= 0.5%/ day a

0.75 L

= 0.375%/ day a

2.

The test instrumentation shall be verified by means of a supplemental test.

Agreement between the containment leakage measured during the Type A test, and the containment leakage measured during the

+

supplemental test shall be within 25% of L.

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5.0 TEST INSTRUMENTATION 5.1

SUMMARY

OF INSTRUNENTS Test instruments employed are described, by system, in the following subsections.

5.1.1 Itmp rature Indicatina System Coraponents:

1.

Resistance Temperature Detectors Quantity 24 Manufacturer Rosemount Type 78-S 100 ohm platinum Range, OF 0 to 400

Accuracy, F

0.1 Sensitivity, OF i 0.01 2.

Digital Tamparature Scanner / Printer:

l Quantity 1

Manufacturer Fluke Type Model 2285B

Accuracy, F

i 0.2 Repeatability, OF i 0.1 5.1.2 DeWooint Indicatina System 1.

Dewcell Elements:

Quantity 10 Manufacturer Foxboro Type Model 2781 O

Range, F

0 - 150 dewpoint

Accuracy, F

i2 Sensitivity, F

i 0.5 2.

Digital Temperature Scanner / Printer:

Quantity 1

Manufacturer Fluke Type Model 2285B

Accuracy, F

i 0.2 Repeatability, OF i 0.1

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1 5.1.3 Pressure Monitorina System i

Precision Pressure Gauges

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Quantity 2

Manufacturer Heise Type Series 10 (with angular readout)

Range, psia 0 - 75 Accuracy, psia 0.0005% f.s.+0.0065% of reading sensor sensitivity, i

psia 0.001% of full scale Repeatability, psia 0.0005% of full scale j

5.1.4 Sucolemental Test Flow Monitorina System

' Flowmeter Quantity 1

Manufacturer Brooks Type Model 1110 Range, scfm 1.0 - 10.0 Accuracy i 1% of full scale 5.2 SCHEMATIC ARRANGEMENT The arrangement of the four measuring systems summarized in Section 5.1 is depicted in Appendix A.

Drybulb temperature sensors were placed throughout the reactor containment vessel volume to permit monitoring of internal temperature variations at 24-locations.

Dewcells were placed at ten locations to permit 1

monitoring of the reactor containment partial pressure of water vapor.

5.3 CALIBRATION CHECKS Temperature, dowpoint, and were checked for calibratio, pressure measuring systems n before the test, as recommended by ANSI N45.4-1972, Sections 6.2 and 6.3.

The results of the calibration checks are on file at 3runswick Steam Electric Plant.

A containment temperature survey was conducted which verified that there were no unmonitored regional temperature variations.

The supplemental test confirmed the instrumentation acceptability.

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r 5.4 INSTRUMENTATION PERFORMANCE The ten dewealls, 24 RTD's, two precision pressure gauges, and flow meter performed satisfactorily throughout the performance of the integrated leak rate test and provided more than adequate coverage of the containment.

5.5 VOLUME WEIGHTING FACTORS Weighting factors were assigned to each drybulb temperature sensor and dowpoint tem'ferature sensor based on the calculated volume of the reactor containment building each sensing device monitored.

Drybulb and dewpoint temperature sensors elevation and weighting factors for the test were as follows:

Elevation /

Temperature Weighting Azimuth Element Factor 0

93/0 TE'1

.0264 0

93/180 TE 2

.0264 0

78/270 TE 3

.0187 0

78/90 TE 4

.0187 0

66/0 TE 5

.0115 0

66/180 TE 6

.0115 0

54/270 TE 7

.0136 0

54/90 TE 8

.0136 46/300 TE 9

.0194 0

46/0 TE 10

.0194 0

46/180 TE 11

.0194 0

33/0 TE 12

.0500 0

33/120 TE 13

.0500 0

33/240 TE 14

.0500 0

16/0 TE 15

.0577 0

16/270 TE 16

.0577 0

16/180 TE 17

.0577 0

16/90 TE 18

.0577 0

Torus 0 TE 19

.0701 0

Torus /60 TE 20

.0701 0

Torus /120 TE 21

.0701 0

Torus /180 TE 22

.0701 0

Torus /240 TE 23

.0701 0

Torus /300 TE 24

.0701 0

93/270 DPE 1

.0527 0

78/90 DPE 2

.0489 i

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Elevation /

Temperature Weighting Azimuth Element Factor 0

54/0 DPE 3

.0386 0

46/180 DPE 4

.0583 0

33/270 DPE'S

.1502 0

16/90 DPE 6

.2309 i

0 Torus /0 A

DPE 7

.1051 0

Torus /90 -

DPE 8

.1051 0

Torus /180 DPE 9

.1051 0

i Torus /270 DPE 10

.1051 5.6 SYSTEMATIC ERROR ANALYSIS Systematic error, in this test, is induced by the operation of the temperature indicating system, dewpoint indicating system, and the pressure indicating system.

Justification of instrumentation selection was accomplished, using manufacturer's sensitivity and repeatability tolerances stated in Section 5.1, by computing the instrumentation selection guide (ISG)'

formula.

containment leakage determined by the Absolute Method requires accurate measurement of small changes in containment pressure with suitable corrections for temperature and water vapor.

Since the Absolute Method utilizes the change in a reading (i.e., pressure and temperature) to calculate leak rate, the repeatability, sensitivity, and readability of the instrument system is of more concern'than the accuracy.

To perform the ISG calculation, the sensitivity error of the sensor and the repeatability of the measurement system must be used.

Sensitivity is defined as "the capability of a sensor to respond to change".. Sensitivity is usually a function of i

the system measuring the sensor output.

When the sensor energy state is raised or lowered an amount equal to the smallest value which the entire system will process, a change of indication will occur.

To determine sensitivity for ILRT' sensors, it is necessary to analyze the smallest value of the analog sensor output which will cause a one digit change in the digital display.

Repeatability is defined as "the capability of the measurement system to reproduce a given reading from a constant source".

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Utilizing the nethods, techniques, and assumptions in Appendix G to ANS 56.8-1987, the ISG formula was computed for the Absolute Method as follows:

1.

Conditions:

L 0.5 wt. %/ day

=

a 64.2 psia P

=

0 T

538.8 R drybulb

=

0 dp 72.9 F dewpoint T

=

eight hours t

=

2.

Total Absolute Pressures ep I

No. of sensors = 2 Range = 0 - 75 psia Sensor sensitivity error (E ) = 10.001%

p of full scale Measurement system error (c o) = i 0.005% of full scale p = i ((E )2 + (cp)2)l/2/(no, of sensors)1/2 e

p p = i ((0.0075)2 + (0.000375)2)1/2/ (2)1/2 e

p = 1 0.0006 psia e

3.

Water Vapor Pressure: epy No. of sensors = 10 0

Sensor sensitivity error (Epy) = 1 0.5 F Measurement system error (Epy) excluding sensor

=11F 1

1 11 L

0 At a dewpoint temperature of 72.9 F, the equivalent water vapor pressure change (as determined frota steam tables) is 0.0133 psia / F' 0

0 Epy = 1 0.5 (0.0133 psia / F)

Epy = i 0.00665 psia 0

0 cy=i 0.1 F (0.0133 Psia / F) p cpy =

0.00133 psia

{

py = i (Epy) 2 + (cpy) 2)1/2/(no. of sensors)1/2 e

py = i ((0.00665)2 + (0.00133)2)1/2/(10)1/2 e

py = 1 0.00214 psia e

4.

Temperature: eT I

No. of sensors = 24 0

0 Sensor sensitivity error (E,y) = 1 0.1 F = 1 0.1 R Measurement system error (cer) 0 0

excluding sensor

= i 0.1 F = i 0.1 R e,p = i ((E )

+ (CT) ]1/2 / [no. of sensors) 1/2 T

eT = i ((0.1)2 + (0.1)2)1/2 / (24) 1/2 0

eT " i 0.0289 R S.

Instrument Selection Guide (ISG):

[ 2(h)2. 2(epy) 2. 2 (g) 2 ) 1/2 2400 ISG =

t P

P T

ISG = 1 2400 [ 2(0.0006)2 + 2(0.00214)2 + 2(0.0289)2) 1/2 8

64.2 64.2 538.8 ISG = 1300(1,.745 x 10-10 + 2.222 x 10-9 + 5.754 x 10-9)1/2 ISG = 1 0.027 wt. %/ day 12

l The ISG value does not exceed 0.25 L (0.125% wt/ day) and a

it is, therefore, concluded that the instrumentation selected was acceptable for use in determining the reactor containment integrated leakage rate.

t 5.7 SUPPLEMENTAL VERIFICATION In addition to the calibration checkn described in Section 5.3, test instrumentation o,,eration was verified by a supplemental. test subsequent to the completion of the eight' hour leakage rate test.

This test consisted of imposing a known calibrated leakage rate on the reactor containment building.

After the flow rate was established, it was not altered for the duration of the test.

During the supplemental test, the measured leakage rate was:

o=L'+Lo L

y Where:

Measured composite leakaga rate.

L

=

c consisting of the reactor containment building leakage rate plus the imposed leakage rate Imposed leaka'ge rate L

=

o Leakage rate of the reactor containment L'

=

y building during the supplemental test phase Rearranging the above equation, Q'

=L

~L c

o 1

The reactor containment building leakage during the Supplemental test can be calculated by subtracting the known superimposed ieakage rate from the measured composite leakage rate.

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L 1

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The reactor containment building leakage rate during the supplemental test (L ') was then compared to the measured y

reactor containment building leakage rate during the preceding eight hour test (L,) to determine instrumentation acceptability.

Instrumentation is considered acceptable if the difference between the two building leakage rates is within 25% of the maximum allowable leakage raie (L )*

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I 6.0 TEST PROCEDURE 6.1 PREREQUISITES e

1 Prior to commencement of reactor containment building pressurization, the following prerequisites were satisfied:

1.

Proper operation of all test instrumentation was verified.

i 2.

All reactor containment building isolation valves were closed using the normal mode of operation.

All associated system valves were placed in post-accident positions.

3.

Portions of fluid systems, which under post-accident 4

conditions become extensions of the containment boundary, were drained and vented to the extent possible or the Type C penalty taken as appropriate.

4.

Type B and C testing was completed with a leakage value less than 0.6 L.

a 5.

Containment pressurization system was operational.

6.

Potential pressure sources were removed or isolated from the containmert.

7.

An inspection of the accessible interior and exterior surfaces of the containment was completed, t

6.2 GENERAL DISCUSSION Following the satisfaction of the prerequisites stated in Section 6.1, the reactor containment building pressurization was initiated at a rate of approximately 7.2 psi per hour.

After the containment was stabilized, leak rate testing was initiated at the 50.3-psig pressure level.

For the duration of the eight hour leak test and the four hour supplemental test, average internal containment temperature slowly decreased due to the low 0

(85-87 F) Residual Heat Removal (Shutdown Cooling) System temperature.

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During the test the following occurred at 15 minute intervals (see Appendix B - Reduced Leakage Data):

1.

Readings indicated by the two precision pressure gauges were recorded and entered into the computer.

2.

Readings indicated by the 24 RTDs were recorded and entered into the computer.

The computer program calculated the weighted average containment building drybulb temperature by use of a weighting factor that was assigned to each RTD.

This value was subsequently converted to degrees Rankine for use in the ideal gas law equation to calculate containment building weight of air.

3.

Readings indicated by the ten dewpoint temperature.

sensors were recorded and entered into the computer.

The computer program converted the readings to dewpoint temperatures and then calculated the average containment dowpoint temperature by use of a weighting factor assigned to each sensor.

This weighted average dowpoint temperature was then converted to a partial pressure of water vapor.

The use of water vapor pressure (Pyy), temperature (T),

and the total pressure (P ) is described in more detail t

in Section 7.1 Data was entered into a compaq Portable Computer located at the leak rate instrumentation room.

The ILRT computer program utilized for tha test *had been previously checked with sample data of known results and certified prior to the test.

The computer program then calculated the following at 15 minute intervals:

1.

Total weight of containment air.

2.

Mass point least squares fit leakage rate.

3.

Mass point 95% upper confidence level leakage rate.

1 4.

Observed total time leakage rate.

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5.

Total time mean leakage rate.

6.

Total time least squares fit leakage rate.

7.

Total time 95% upper confidence level leakage rate.

A plot of weighted average containmert temperature, containment total pressure, containnent average dewpoint temperature, and weight of air was performed for each 15 minute data set (see Appendix C).

Immediately following the eight hour leak test, a superimposed leakage rate was established for a four hour test period.

During this time, t.omperature, pressure, and vapor pressure were monitored as described above.

6.3 TEST PERFORMANCE 6.3.1 Pressurization'and Stabilization 2hkgg Pressurization of the reactor containment building.was-started at approximately 1130 on February 16, 1990.. The

. pressurization rate was approximately 7.2 psi per hour; When containment' internal pressure reached 50.3 psig at 2000 on February 16, 1990, pressurization was secured.

By 0019, on February 17, temperature stabilization

(

. criteria had been met.

6.3.2 Intecrated Leak Rate Testina Phase-At 0034 on February 17, 1990, 15 minute frequency test data collection was initiated.

Initial indications showed a fairly constant leakage rate of'approximately 0.55% by weight per day.

Leak detection and identification teams were dispatched but no maje source of containment leakage was identified.

Only one substantial packing leak was identified on the.RHR containment spray valve E11-F021A.

At this time no repairs were made.

By 1619, the containment leakage rate was 0.49% by weight per day and still decreasing slowly.

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At 1630 on February 17, 1990, a decision was made to terminate the integrated leakage rate test.

The.drywell-sumps were pumped out and the reactor vessel was refilled to approximately 240 inches.

In addition, an air seal of 48 psig was established on the inerting header for the drywell and the torus-(penetrations X-25 and X-205),.and on_the torus purge exhaust (penetration X-220).

Test data analysis was restarted at~1734 on February 17,.

3 1990.

By 2334 a fairly constant leakage. rate of 0.38%

per day was established.

At this time the packing' leak on E11-F021A was refaired, an air seal of 48 psig was

'i established on the drywell purge exhaust (penetration X-26), drywell sumps were pumped and reactor vessel level was raised to 240 inches.

i The integrated. leakage rate test was. restarted at 0849 on February 18, 1990.

The leakage rate gradually increased and stabilized at a value of~approximately 0.34% per day.

Again-leak detection and identification was initiated and at approximately 1300,.a significant leak was found on the Torus to Reactor. Building vacuum. breaker inboard isolation value CAC-V16.

CAC-V16 was then opened and containment pressure of 49.5.psig was applied-against vacuum breaker X-20A.

After this evolution ncr leakage was detected from the vacuum breaker.

At approximately 1500 the drywell sumps were again pumped out and the reactor vessel refilled to'242 inches.

4 The integrated leakage rate test was officially restarted atL1619 on February 18, 1990 and an acceptable total time leakage rate of 0.273% weight per day was obtained at 0019 on February 19,.1990.

The leakage rate at the upper 95% confidence level was 0.308% by' weight per day.

6.3.3 Supplemental Leakace Rate Test Phase Following completion of the eight hour integrated leak i

rate test, a leakage rate of 4.31 scfm was imposed on the containment building-through a calibrated flow meter at 0019 on February 19.

After a one hour stabilization period, leakage rate data was again collected at 15 minute intervals for a period of four hours.

With an imposed leak rate of 0.495% per day, a measured composite leakage rate of 0.749% per day was obtained using the Total Time method.

This results in a containment building leakage rate agreement of 3.6% of L with the 3

results of the eight hour test.

This value is within the acceptance limit of 25% of L

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. 6.3.4 Deoressurization Phase After all. required data was obtained and evaluated, containment building depressurization to 0~psig was started.

-A post test inspection of the containment ~

revealed no unusual findings.

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7.0 METHODS OF ANALYSIS l

7.1 ABSOLUTE METHOD l

7.1.1 General The-Ab'selute Method of leakage rate determination was employed during testing at the 49.0 psig pressure level.

The Gilbert / Commonwealth, Inc., ILRT. computer code calculates the percent per day leakage rate using both the mass point and total time methods.

7.1.2 Mass Point Analysis The Mess Point method of computing leakage rates uses the following ideal gas law equation to calculate the weight of' air inside containment for each 15 minute interval:

y,144 PV = KE 1

RT T

Where:

W = Mass of air inside containment, lbm 5 lbm OR - in.2 K = 144 V/R = 7.96199 x 10 lbf P = Partial pressure of air, psia T = Average internal containment temperature, OR I

V = 294,981 ft

- l 3

lbf - ft R = 53.35 i

O lbm R The partial pressure of air, P,

is calculated as follows:

P=PT-Pyy Where:

T Total containment pressure P

=

Partial pressure of water vapor determined P

=

wy by averaging the ten dewpoint temperatures and converting to partial pressure of water vapor, t

psia.

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The average internal containment temperature, T, is calculated as follows:

1 1

T=

fi E i Ti 1

1 The weight of air-is plotted versus time for the eight-i hour' test and for the four hour supplemental test.

_The ILRT computer code fits the locus of these points to a straight line using a linear least rquares fit.

The equation of the linear least squares fit line is-of the form W = At + B, where A is'the slope in Ibm per hour and B is the initial weight at time zero.

The least squares parameters are calculated as follows:

W). (Et ) (EW )

A=N (Ett i

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S xx i

B = gEt 2) (EW )

(Et ) (Ett W) i i

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Syg i

Where:

2) - ( Et ) 2

.Sxx = N (Eti i

The weight percent leakage per day can then be determined from the following equation:

-2400 A L

=

B j

where the negative sign is used since A'is a negative-slope to express the leakage rate as a positive quantity.

7.1.2 Total' Time Analvgis

.The total time method utilizes the following equation to determine the leakage rate of the reactor containment building:

l 2400 -1_T1 2

P~

L=

t TP

' i 2 1-l' 21 o

'1 1

1 s

Where:

I

= Measured leak rate'in weight percent per day I

t

= Time interval, in hours, between measurements T,T2 = Average internal containment temperature, 1

R, at the bejinning and the end of the test. interval._respectively.

Pi,P2 = Average containment pressure (corrected for water va or pressure) at the begjnning j

and end of the test interval respectively.

The mean total time leakage rate is derived from the above individual total time calculations.

The equation for the mean' leakage rate is in the form:

L=Ei Li n

1 Where:

' L1 = Individual total time leakage rates 1

n: = Number o.f total time leakage rates The ir.dividual leakage rates are then plotted against 1

time for the duration of the eight hour test.

The ILRT computer code fits the locus of these points to a straight line using a linear least squares fit.

The equation is of the form L = L is th'e o + L t where.Li 1

slope in percent per hour and L is-the initial leakaga o

L rate at time zero.

The least squares parameters are calculated as follows:

It 2 ELi - Eti Et Lii i

_ t Sxx N Et t ELi - Ett ELi n

Sxx Where:

Sxx = N ('Eti) - ( Et )2 2

i I

L 22 h

~

L L

l

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- 7.2 STATISTICAL EVALUATION 7.2.1-General 1

After performing the least squares fit, the ILRT computer code calculates the following statistical parameters:.

1.

Limits of the 95% confidence interval for the mass point leakage rate'(C ).

g 2.

Limits of the 95% confidence interval for the total time'lenkaga rat.e (C ).

L These statistical parameters are then used to determine that the measured-leakage rate plus the 95 dCL meet the acceptance criteria.

7.2.2 Mass Point Confidenqa The upper 95% confidence limit for the mass point leakage rate is calculated.as follows:

Cg = 2400 t95 (8 /B)

A Where:

M

= Upper 95% confidence limit C

J t

= Student's t distribution with N-2 degrees of 95 freedom S

= Standard deviation of the slope of the 3

least squares fit line B

= Intercept of the least squares fit line The standard deviation of the slope of the least squares fit line (Sg) is calculated as follows:

S (N) 1/2 _ __

Sg =E N (Et ')

( Et ) '] */ '

i i

Where:

Common standard deviation of the weigheed S

=

from the least squares fit line t'

Number of data points N

=

23 1

(.'

i I

1 t1=

Time interval of the ith data point The common standard deviation (S) is defined by:

S =(

(Wi W) ] 1/2 N-2 l'!

Wherc:

Wi = Observed mass of air 1

W

= Least squares calculated mass of air The ILRT computer code calculates an upper 95% confidence leakage rate as follows:

UCL = Lam + 2400 t95 (S /B) l A

This UCL value is then used to determine that the measured leakage rate at the upper 95% confidence limit meets the acceptance criteria.

7.2.3 Total Time confidence J

The 95%-confidence limit for the total time leakage rate is calculated as-follows:

CL=

t Se [1 + 1 +

(t - tf

}

1/2 95 n

E(ti - t) i e

l Where:

Total time interval.

t

=

-i t =.Ett n

ti=

Time interval for each data point i

n

= Number of individual total time leakage rates 24 i

-i 4

i 1

5;

[

8.0-DISCUSSION OF RESULTS 8.1 RESULTS AT PA B

8.1.1 Mass Point Method of Analysis Data obtained during the leak rate test at P indicated the following changes-(highast to fowest) during the eight hour test:

Variabla Maximum Chanae P

0.085 pr,ia T

P 0.0018 psia l

wy 0

T 0.21 F

The method used in calculating the Mass Point leakage rate is described in Section 7.1.1.

The results of this pelculation is a, mass point leakage rate of 0.278%/ day (see Appendix D).

The 95% confidence limit associated with this leakage rate is.0.003% per day.

Thus, the leakage rate at the upper bound of the 95% confidence level becomec:

.q

'UCL = 0.0278 + 0.003

.UCL = 0.281%/ day Additional leakage rates must be applied to the measured leakage rate at the upper 95% confidence level to account for penetration paths not-exposed'to the test pressure, penetrations isolated prior to the test and for changes in the net free volume of the containment due to water level changes.

Penetation paths and the corresponding.

-leakage rates based on analysis of minimum pathway local leakage rate testing are as follows.

25

Y i

Minimum' Pathway

^

i' Containment Local System Isolation Valves Leakace Rate (SCFH)

Drywell Drains 2-G16-F003/F004 0

Drywell Drains 2-G16-F019/F020 0

Feedwater (RCIC 2-821-F032B, 0

- Injection Line B)- 0-E51-V88, 2-321-F010B, j

Feedwater-(HPCI 2-B21-F032A, O

l Injection Line A) 2-E41-F006, j

2-B21-F010 A -

Reactor Building 2-RCC-V28/V52 2.5

)

Cooling Water RXS-SV1222B/C 0

9 CRD Purge to 2-B32-V24/V22, 2.347 Reactor V30 Recirc Pumps 2-B32-V32/V22, 0

V30 Recire Sample B32-F019/F020 0.41

.l

,i RHR Suction 2-E11F008/F009 3.2 2_E11-F008/F009

' Reactor Water 2-G31-F001/F004 0

Cleanup Inerting Header 2-CAC-V4/V5/V6/V15 5.705 Drywell Purge 2-CAC-V9/V10 2.743 Exhaust Torus Purge 2-CAC-V7/V8 2.145 Exhaust The total applicable local leakage rate is 19.05 scfh which is equivalent to a leakage rate of 0.036%/ day.

Water level changes in the containment during the eight hour integrated leakage rate test are summarized below:

26

(

. - - ~ -

n:

s

[

1 Reactor Vessel Water Level:

1600 2/18/90 241.0 inches 0019 2/19/90 231.2 inches t

y Torus Water Level:

f 1600 2/18/90

-28.0 inches j

0010 2/19/90

-28.0 inches During the test, no makeup water was introduced into the reactor vessel.

Therefore, the volume change associated with the change in reactor vessel water level shows an increase in the net free volume which would correspond to-a reduction in the measured containment leakage rate.

However, it is conservatively assumed that the water

. level decrease in'the reactor vessel.was not lost out of containment and therefore no change in net free volume

occurred, n.

na-v-n,..

The total containment" leakage rate at the upper 95%

,t confidence level (UCL) is calculated as follows:

UCL = Lam + 95% confidence limit + Type C leakage +

. changes in net free volume UCL = 0.278%/ day +0.003% wt/ day + 0.036%/ day + 0.000%/ day UCL = 0.317%/ day.

This value is well below the acceptance criteria leakage rate of 0.375%/ day (.75L )*

a 8.1.2 Total Time Method of Analysis The method used in calculating the total time leakage rates is defined in Section 7.1.2 The results of these calculations are as follows:

1.-

The measured total time leakage rate for the eight hour test was 0.273% by weight per day.

27

4 2.

The 95% confidence limit associated with this leakage. rate is 0.035% per day.

.Thus, the leakage rate at the upper bound of the 95% confidence level becomes:

H UCL = 0.273 + 0.035 UCL = 0.308%/ day 3.

The mean of the measured leakage rates based on the last five hours of the test was 0.273% by weight per day.

The corrected reactor containment leakage rate at the upper 95% confidence level (UCL)'for Type C

-penalties and changes in net free volume is calculated as follows:

UCL = Lam + 95% confidence limit + Type C' leakage +

~

changes in net free volume.

UCL = 0.273%/ day + 0.035%/ day + 0.036%/ day +0.0004/ day UCL = 0.334%/ day The total time measured leakage rate, the measured leakage rate at.the upper bound of the'95% confidence-e level and-the mean of the measured' leakage rates based on the last five hours of tecting are below the i

acceptance criteria of 0.375%/ day.

Therefore, the reactor. containment building leakage rate, based on both, mass point method and total time method of analysis, at the calculated design basis accident pressure -(P ) of 49.0 psig is acceptable.

a 8.2 SUPPLEMENTAL TEST RESULTS After conclusion of the eight hour test at 49.0 psig(P ), the flowmeter was placed in service and a a

flow rate of 4.31 scfm was established.

This flow rate is. equivalent to a leakage rate of 0.495% per day.

After the flow rate was established it was not altered for the duration of the supplemental test.

The measured leakage rate (L ) during the supplemental-test was c

calculated to be 0.750% per day using the Mass Point method of analysis and 0.749% per day using the Total Time method.

I 28

r k

i 1

a

.The building leakage rate during the supplemental test' is then determined as follows:

Mass Point Total Time L'=L

-L L'=L

'L y

o o

y o

o i

L ' = 0.750 - 0.495' L ' 6 0.749 - 0.495 l

y y

i L ' = 0.255%/ day L ' = 0.254%/ day y

y Comparing this leakage rate with the building' leakage.

rate measured during the eight hour test yields the y

following:

255l'

+-

Mass Point = lL

~ h #l

.278 -

= 0.046 am v

=

L 0.5 a

Total Time = lL

~ L 'l

.273 -

254

= 0.036-am v

=

L 0.5

[

1 The building leakage rates agree within 4.6% of L using a

the Mass Point method and 3.6% using Total Time which are

'below the acceptance criteria of 25%.

Using the formulation of ANS 56.8-1987, i

(Lo+ Lam - 0.25L ) I bc 5 (Lo+ Lam.+ 0.25L )

a a

(0.495 + 0.273 - 0.125) $ L (0.495 + 0.273 + 0.125) c 0.643 $ Ln S 0.893

.Since L was measured to be.749%/ day, this value-falls 1

c within the acceptable range of 0.643% to 0.893% per day.

Therefore,.the acceptability of the test instrumentation is considered to have been verified..

8.3 AS FOUND ANALYSIS

-To determine the as-found containment leakage rate, an analysis was performed to evaluate any leakage savings from repairs or maintenance to containment isolation barriers.

Leakage savings are realized when containment isolation barrier repairs or maintenance result in a lower minimum pathway leakage than that which existed prior to tl.e repair or maintenance.

29 i

s me m

5

' l

'j

\\

-The results of Type B & C testing are. presented in Appendix F.

The total leakage savings due to performing these tests prior to the Type A test indicate a leakage savings of 0.153% which would have exceeded the acceptance criteria of L

a 8.4 LOCAL LEAKAGE' RATE TEST RESULTS The local (Type B&C) leakage rate test results since the last integrated leakage rate test are included :h1 Appendiy F.

t 1

I.

l-u h.

l l

30 l

s

'i I

i

9.0 REFERENCES

1.

PT-20.5, Integrated Primary Containment Leak Rate Test.

2.

Brunswick Steam Electric Plant Final Safety Analysis Report.

t b-3.

Code of Federal Regulations, Title 10, Part 50, App 9nd3x.T.

m 4.-

ANSI N45.4-1972, " Leakage Rate Testing of Containment Structures for Nuclear Reactors, t

American Nuclear Society (March 16, 1972).

5.

ANS-56.8-1987, " Containment System Leakage Testing Requirements," American Nuclear Society.

i

'6.

ILRT Computer Code, Gilbert / Commonwealth, Inc.

7.

Steam Tables, American Society of Mechanical Engineers, 1967.

8.

BN-TOP-1, Testing Criteria for Integrated Leakage Rate Testing of Primary Containment Structures for Nuclear Power-Plants, Revicion 1, November 1,.1972..t 1

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h4TE TIME PAVG PWV TAVG MASS WEIGHT J02-18-90 1619 64.312 0.4018 79.305 94407.30 1634 64.309 0.4018 79.297 94404.77 1649 64.306 0.4022 79.289-94400,70 4

1704 64.303 0.4016 79.285 94398;30-1719 64.301 0.4017

'79.274 94396.31' 4

1734 64.298 0.4014 79.265 94394.52 1749 64.295 0.4015 79.261 94391.32.

1804 64.292 0.4013 79.249 94388.59 1819 64.289 0.4011 79.236 94387.22-1834 64.287 0.4011-79.228 94384.79 1849 64.284 0.4004 79.219

-94303.61-1904 64.281 0.4012 79.211 94379.51 1919 64.278 0.4016 79.2011 94376.63 1934 64.275 0.4015 79.196 94373.33 1949 64.273 0.4016 79.191 94369.60 2004 64.270 0.4011 79.184 94367.74 e

2019 64.268 0.4017 79.175 94365.13 2034 64.264 0.4014 79.171 94361.20 2049 64.262 0.4007 79.164 94359.62 2104 -

64.259 0.4010 79.159 94356.30' 2119 64.256 0.4014 79.156 94352 28 2134 64.254 0.4010 79.147 94350.60

~2149 64.251 0.4006 79.142 94348.29 2204 64.249 0.4009 79.138 94344.69 2219 64.246 0.4013 79.130 94341.58 2234 64.243 0.4012 79.123 94339.22 Li 2249 64.242 0.400Q-79.119 94337.72 2304 64.239 0.4004 79.117' 94334.15 2319 64.236 0.4006 79.108 94332.16' 1

2334 64.234 0.4006 79.100 94328.26 2049 64.231 0.4009 79.098 94326.23 02-19-90 4

64.229 0.4007 79.097 94323.47 19 64.227 0.4012 79.092 94319.70 VERIFICATION TEST DATA d

I E02-19-90 134 64.199 0.4005 79.062 94284.46-149 64.193 0.4001-79.058 94276.92 204 64.187 0.4004 79.052 94268.03 219 64.181 0.4006 79.057 94259.99 234 64.176 0.4007 79.048 94253.02 249 64.170 0.4009 79.044 94245.23 304 64.165 0.4008 79.037 94238.90 t

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VERIFICATION TEST DATH 9

5 DATE TIME PAVG PWV TAVG MASS WEIGHT 02-19-90 319 64.159 0.39.98 79.034

-94232.04 334 64.153 0.4010' 79.026 94223.3S' 349 64.148 0.4002

.79.022' 94217.40 404 64.143 0.4007 79.016 94209.99 s

419 64.137 0.4007 79.014 94201.64 434 64.132 0.4009 79.008 9419S.13 449 64.126 0.4010 79.000 94187~14 504 64.121 0.4003 70.997 94180.93 S19 64.115 0.4008 78.992 94172.81 534 64.109 0.4002

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PSIA AYG PRESU E vs: TIME

~

LPLOTTDn" ~

~

ggggg79g.

118:25:43:

a IBI 64'40 STARfD::

1 92/18/99 16:19:58 64.35 l

MAJOR INCRDENT 64,30

\\

NufES 64,25 1 iI i l I 1 Ii i II iI I i 1 1 ii l ii li I l I 'l 11 1 I

'1619-19 4

flME I

e

...u

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T 4

''M" A -%aW*'

W

MG F AYG RD vs IIE PL0ffD:

02/26/90 79,5-19:25:43 IBI 79'4 STARfD:

02/18/90 16:19:58 i

79.3 'N 9

N 79.2 MIllifB 79.1 1 II I II I II I II I ;I II I II I II II l II I II I I 1619 19 i

IIE i

4 7

i

~... - -.

y DEGF AUG DDI POINT fBGMTURE vs flE

- PL0ffD::

~

82/26/99 18:25:43 i

fBf 73.10 4

STARfD:

i 92/18/93 16:19:58 73,85 MJ0R 73,90 g

g.

I N

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72,95 I

. u m,,,,,,

,,,,,,,,,,,,,,,, /,,,,,,

1619-19 IIE 1

f 1

-.m m

m m

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m-.

m.

m

- m a

.d PSIA liATER YAMR PESSHE vs fIE PL0ffD:-

92/26/99 9.492 19:25:43 TEST O'402 STARfD:

82/18/90 t

V 16:19:58 4

l s

9,491 h

/NAJon 9.491 INCRDENT 15 NI!tlIES

/

9.499 1619 19 -

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4 HOUR VERIFICATION 4

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7,/MY TOTAL II E LB M E O fE vs fl E FL0ffD:

LDSTHAN24N0DRS R/19/90 05:33:38

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82/19/90 N.

01:34:58 9.85

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9.89 4

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N MIEfB

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i 9.75 4

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234 534 fIE j

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...... _ - -. ~ -... -.

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Ihou LM O SS EIGT vs II E luffD:

02/19/90 i

F

~05:33:38 a

IBI 94.35 STARfD:

82/19/90

^

81:34:58' 94.30

+_

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N MAJ0R 94.25 IERNM 15 MlltifB

~

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1 1

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PSIA AUG PBS$URE vs IIllE PL0ffD:-

E/19/98 64'28

\\.

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'N TEST 64,18 L

N SIARfD:

N 82/19/99 64.16 j

MJ0R 64,14 IllCRDEE 15 llI1117B

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64,12 i

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134 534

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PIAffD:

HG F AH MDvsflE 79.98 N/19/90 M:33:38 79'" ~N fBf N,A SIAND:

i

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82/19/90 i

01:34:58 l

79.04 R

NJ0R INCRDEE i

79.92

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MINTE 79.99 i

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i 134 534 i

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DEGF AVG DDI MIE IDEWIBRE~vs flE PL0ffD:

s N/19/90 -

85:33:38 73'95 IEff STARfD:

82/19/96 i

01:34:58 73,89 l-IIAJOR 72,95 r

IllCRDEll!

15

,/

IIINTES s

\\

72'90

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134 534 i

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J

-l APPENDIX D COMPUTER RESULTS a

(

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1

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=

b I

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m

- - ~ -

Fr Y,~:'

t

{.

i 1

h-

/

i 8 HOUR TEST t

t i

INTEGRATED LEAK RATE TEST RESULTS by81LIERT.'COMMONNEALTHINC.

i MASS POINT ANALYSIS l

lill ILRT lill L

FROM TEli POINT NUMBER 1 10 33 FROM 1619(02/10/90) 10 19 (02/19/90) l

-I!ME-088.WE!8HT '095. MIN. CALC.

INTERVAL (L8)

(L8) p l:

0 94407.31

.7526965

.25 94404.77~

.5581228

'l

.5 94400.7

-1.897M7

.75 94398.31

-1. % 5501 t

t 94396.31

.8291904 1.25 94394.52

.106M31 l.5 94391.32

.M3034 1.75 94388.59

.3652959 2

94387.22

.9970881 2.25 94384.79 1.293684 4

2.5 94383.61 2.845826-

'2.75 94379.52 1.47863

.3-94376.63 1.32474 3,2$

94373.34

.7H1212 315' 94369.59 a.2496983 3.78 94M7.73

.6191995 4

94M5.13

.7376496 4.25' 94Mt.2

.458%65 e

4.5 94359.62

.6897928 i

4.75 943 %.31

.1029077 5

94352.28

-1.187374 5.25 94350.6

.143B757

- 5.5 94348.29

.2773967 5.75 94344.7

.5910993 6 :-

94341.59

.9712213 6.25 94339.22

.6097981

' 6.5 94337.72

.6217215 6.75 94334.16-

.2142601 7

94332.16

.5171326 7.25 94328.26

.6544582 7.5 94326.23:

4.596545E-02 7.75 94323.48 2.341882E-02

[

8-94319.7,

-1.026274 N0 e 94400.0555441033 L8

W1 e -10.91667969192292 L8/HR LEAKAGE RATE =

.277519~1PER0AY l THE 951 UPPER CONFIDENCE INCREMENT =

3.111808E-03 1 FER DAY

. UPPER LIMil Of THE 951 CONFIDENCE LEVEL a

.2006308 1 FERDAY l I ' RATE IS ( 751 0F LA (.375 )

i

p TIME ANALYSIS

-TOTAL till ILRT list FROM TEST POINT NUMBER 1 TO 33 -

r FROM'!619(02/18/90) TO 19 (02/19/90)

I CBS. LEAKAGE RATE

.25

.2577356 i

.5

.3357203

.75

.3050718 1

.2794659 1.25

.2600461 s

1.5

.2709173 1.75

.2718936 2

.2552799 2.25

.2544001 2.5

.2409289

'2.75

.2568942 3

.2599172 3.25

.2657192' c

3.5

.2738671 3.75

.268221 4

.2680494 4.25

.2757619. '

I 4,5

.2693722 4.75

.2729421 5

.2797313 5.25

.2745732 5.5

.27276 5.75

.2768068 6

.2784471 6.25

.27694 6.5

.2721458

-6.75 J754934 7

.2729096 7.25

.2771768 7.5 ~

.2748141 7.75

.2749754

-l 8

.2783906 L0 =.2727071090628367 1 PERDAY L1. 5.61465203763160-M 1 PER DAY PER HR IHE 5 HOUR MEAN LEAIA6E RATE =

.2732964 1 PER DAY-CALCULATED LEAKAGE RATE =

.272752 1 PER DAV t

( 24 HR$ 951 UPPER CONFIDENCE INCREMENT =

.03487/l 1 PER DAY

( 24 HR$ UPPER LIMIT OF THE 951 CONFIDENCE LEVEL

.3076291 1PERDAY I

=

) 24 HRS 951 UPPER CONFIDEWCE ]NCREMENT.

9.463B97[ 03 1 PER DAY

) 24 HRS OFFER limit 0F THE 951 CONFIDENCE LEVEL i

.2022159 1 PER DAY t

RATE !$ ( 7510F LA (.375 )-

"-5=-

.y

fW

_f

'N ev s,.

4 f

-nv

. f p.

4 4

r

(-.

h s.

3-3 4 HOUR VERIFICATION j

1 t

e.k I

t

't t

P I

5 tt t

F T

i t

h k

f fi 8

6 t

r E

.. f 4

v r

t t

1,5 4%puvus % ~a a m _ a _ _ _,,_,

.n.

_c.

e

.y

. ~

I INTESRATED LEAK RATE. TEST RESULTS by$1LMRT/CDSONNEALININC.

1 MASS POINT ANALYSIS 1888 Superlapose4 till

)

FRM TEli PolNT NM MR 1 10 17 FROM 134 (02/19/901 10 534 (02/19/90)

TIME OPS.NElBH1 096. min. CRC.

]

INi[RVAL (ll)

(LB) 0 94294.45 1.184328

. 25 94276.92 1.019628 94260.83

.2976603 i

.75 94259.99 1.166179 l

1 1

-94253.02

.7706163 1.25 94245.23-

-1.117896 1.5-94238.9

.148559 1.75 94232.04

.3614345 2

94223.34

.9629385 l

2.25 94217.41

.461937 2.5 94209.99

.4207685 2.75 94201.64

.5503104 3

94195.13

.3036561

^3.25 94107.13

.3263637 3.l' 94100.93

.8394333 L25 94172.81 0.687118E-02 4.

94165.49

.143153

,Oe 94233.26903327356 LB j

W1

27.47924520140632 Ll/HR I'

LEAKA6ERATE*

.7504003 1 FERDAY THE951UPPERCONFIDENCEINCREMENT*

6.696672E 03 I PER DAY

- i UPPER LIMil 0F.iHE 951 CONFlMNCE LEVEL *.757097.1 PERDAY t

s

.j

u.

s

,t

)

i 9

l-TOTAL'- TIME ANALYSIS litt Superiapped till j

J FROM TEST POINT NL,9KR 1 10 17 f-fROM 134 (02/19/90) TO 534 102/19/90)

I 086. LEAtAGE RATE

.25-

.7673642

.5

.7956327

.75

.8302346 1

.0002046 i

1.25

.7987393

-1.5

.7730430 E

1.75

"'1994 2

.Iu14%

2.25

.7595061 h

2.5

.75E1958 2.75

.7665398 3

.7578003 3.25

.7622386 3.5

.7529137 3.75

.7578539 i

4

.7570293 L6 o.00009476922M732 1 PER M Y i

L1 o -1.2074550816H9120 C2 1 PER MY PER IF.

TWE MEAN LEAEASE RATE =

.7735363 2 PERDAY CALCULATED LEALAGE RATE =

.7493966 1 PER M Y

( 24 HR$ 951 UPPER CONFIDENCE INCREMENT ' =

3.773256E-02 1 PER MY

'( 24 CS UPPER Linli 0F THE 951 CONFIDENCE LEVEL =

.7871291 1 FER DAY t

) 24 CS 951 UPPER CONFIDENCE INCREMENT =

1.335642E 02 1 FER DAY

) 24 HRS UFPER LIMli 0F THE 951 CONFIDENCE LEVEL =

.762753 1 FER DAY e

< i l'

? '

.?

I-l c

4

,1 r

_a n,9 w--wv.--a w-e esM-'"-

Ar-""~

-M"-'F-

^rM*T'Ww-HAM-WJM**""^^M**F""* " " '

A

&&&AOU***M^*H*-64%*$MMM**

^

^" * '

M

^*

-*4sw

^M-O ASLA-

om'A-b-1% % '

i I

l A

I l

1 1

1 I'

n APPENDIX E

SUMMARY

OF MEASURED DATA I

i 0

1 l

l I

i 1

I h

i l

l I

i r

5 0

I s

i 4

1 l

1 1

- t

-,n.--,-~.

.....-,--,n.-,_,-

.-,n.-,,,--,-,

n.,,,,,e.--n

-w-.,,,

,.an-,-,w,-,,.--,.

,--r 1

e b

},

3.

/

)

i 4

y ;,

f 8 HOUR TEST k

4 1

1-1 i

f t '.

' I

i'

- - SENSOR READINGS AND AVERAGES ***

1888 -

ILRT lill TEli P0lui W OER 1 I

CLCi ~ Cuelina Powr 6 Light ilME OF REMING:

PLANT llit Brunseitt Hits 02/10/90 Cli 2

!!NE:16:19

,l IR4ltlMill10N:46 L

RfD MNPo!NT PRESSURE i

K~3-AlREM CAllM. SENI AS READ CALIM. SEN4 Al READ CAllBR.

a-001 87.400 17.000 001 !$6.M0 75.657 N1 64970.000 64.316 H2 M.730 M.730 002 157.900 76.410 002 8 M97 M 0 64.300 l'

(

C3 ;99.'t0 99.920 003 157.570 76.135

' ;. M4 09.280 99.200 004 160.92 78.407 El6HTEDAV6. 64.312 C5 08.0 %

08.0 % 005 12.200 76.5M 0%

90.120 90.120 04 157.820 76.303

+

007 88.460 88.460 007 145.690 68.007 000 B7.9H 87.9H 000 146.800 60.095-1 009 - 88.410 98.410 009 144.M0 67.346 010 17.H0 17.500 010 146.120 68.379 011~

87.630- 87.630 012 90.M0 90.H0 NE10NTESAYS. 73.012 ell ' 87.9M 87.9M 014.II.290 II.290 o

til M.2H - M.2W 016 82.530 12.530 017 B4.510 94.510 Olt ' 05.930 85.930 019 ' 69.040 ~69.040

-020 69.700 69.7H 021

'69.940' 60.940-022' 69.290- 69.290

-023 69.400 69.400 024. 69.350~ 69.350 NE16HIEDAV6. 79.305F 538.995R H

l L

l q

l l

' NATER VAPOR PARilAL PRESSURE:

0.401B23 PSIA i

NAllNElGHT: 94407.3020 LIM

.. - I

L "sss SENSOR READINGS AND AVERAGEB ***

lill ILRT lill -

e TEli Polui uuMBER 2

)'

CLIENT

CarolinaPower6Litht 11NE OF READING:

PL4NT$1TE:Brunsoitt-DATE:02!!B/90 l -- ' Cli i2 ilME:16:34 1RANSMIS$10N 47 RfD DEuPolNT PRESSURE i

"SE3 AS READ CALIBR. SEW 8 AS READ Call 8R. SENt AS READ CAllBR.

001 - 17.830 87.830. 001 !$7.640 76.182 00194966.000 64.313 002 B6.670 86.670 002 157.530 76.108 00285994.000 64.305 003 '89.910 09.910 -003 157.830 76.309 004 99.230- 89.230 '004 160.700 78.293 WE16HIEDAV6.

64.309

' C5 80.020-B8.B20 005 1 H 130-76.511 006 90.040- 90.040 006 157.790 -76.282 l

007 98.460 88.460 007 145.770 68,141 000 87.930 87.930 008 144.820 68.954 r

009 98.390 '88.390 009 144.600 67.400 010 - 87.400 B7.400 010 146.020 68.311 r

011 87.610-17.610 012 90.040 90.M0 NE10 HIED AYS. 73.013 til - 97.940 87.940 014 80.200 II.200 -

015 ~ 04.2M - H.250 016' 82.520 82.520 017 84.500 ' 04.W0 018 85.920. 85.920 019

~69.040-69.040 020 69.700 69.700

-021, 68.940 68.940-022 : 69.290 69.290 023 69.490- 69.490 024 69.360 69.360 NEl6HlIDAV6. 79.297F 538.987 R l

WATER VAPOR FAR11AL PRES $URE:

0.401640 PSIA MASS W(16His 94404.76B3LBM

4 !!

i 888-SENODR RECDINGS CND AVEROGES ***

lill ILRT lill itsi PolNT NUH8ER 3

CLIENT.

Carolina Poetr 6 Light fint 0F REAllWS

'PLCl$1TE:Brunsultt DATE:02/18/90 Clt

2 ilnt:16:49 ie TRAntallSION:48

+

RfD D(NPOINT PRESSURE St~3 AS READ Call 8R. StW8 AS READ Call 8R. BEW8 AS R[A0 Call 8R.

,001 87.790 87.790 001 157.470 76.067 001 84962.M0 64.310 M2.86.650 86.6 % M2 157.530 76.108 M285889.000 64.302 i

003 89.890 89.890 003 157.890 76.3M M4 89.210 89.210 004 161.020 78.454 WElBHTEDAV6. 64.306

~M5 88.8 %

88.8 % M5 158.2 %

76.592 M6-89.950- 89.950 006 157.790 76.282

.' 007. 88.440 88.440 007 145.8 %

68.195 008 87.940 87.940 M8 146.920 68.922 OM 88.380 88.380 009 144.610 67.353 010 I?.400 87.480 010 146.000 68.352 011 87.600 87.600 0!!

90.030 90.030 U(18Hi[8AV8. 73.043 013 87.9% - 87.9M 014 88.288 88.288 015 M.240 M.240

-016 82.510 82.510

-017 84.490 84.490 018 : 85.900.85.900 019.69.030 69.030 020 69.700 69.7%

021 68.940 68.940 022 69.290 69.290 023 69.480-69.480 024 69.3%

69.350 Ntl6HIEDAV6. 79.209F 538.979 R t

t i

NAl[R VAPOR FARilAL PRESSURt 0.402235 PSIA MASSNE16HT: 94400.6998 L8H

lssa" SENSOR READINGS AND AVERAGES ***

J till ILRT litt I

TEli POINT NUMM R 4 l

CLIENT :: Carolina Power 6 Light ilnt 0F READING:

i PLANT $1ft: Brunsultk Hit:02/10/90 UNIT

2 i!ME:17:04 5

1RANSMIB$10N 49 RfD DEWPolNT PRES $URE i

lE'] Al READ Call M. BEk8 AS READ CALI M. BEM AS READ CAllM.

{

'M1 87.740 87.740 001 157.030 75.771 001 84958.0 M 64.307

~002 86.590 86.590 002 157.6M 76.155 00285866.M0 64.299 W3 09.880 89.880 003 157.66' 76.195 M4 89.180 89.180 004 160.840 78.333 WE16HTEDAV6. 64.303 005 89.730 88.730 fM 150.250 76.592 i

006 90.200 90.200 006 157.000 76.209

.i 007 88.420 88.420 007 145.730 68.!!4 l

000 87.930 87.930 008 146.000 68.995 M9 98.370 98.370 009 144.570 67.325 l

010 07.480 87.480 010 146.020 68.311 0!!

07.6M 17.H0 012 M.040 90.H0 NEIONTEDAY6. 72.999 013 87.900 ~ 57.980 014 31.290 08.290 t

-015 B4.230 H.230 016 82.5M 32.5M '

017 84.470 84,470 018 85.910 85.910 019 69.040 69.040 020, 69.700 69.700 021 68.930 68.930 022 69.270 69.270

?

023 69.480 69.400 I024 69.350 69.350 WE16HTED AV6. 79.285F

't

'538.975R

-i i

e i

t i

6 WATERVAPORPARilALPRES$URE:

0.401648PS!A I

MASS WEIGHT: 94398.3025 LBM

888 SENSOR READINGS AND AVERAGES **

1888

!LRT litt TEST POINI NUNMR 5 CLIENT

CarolinaPowr6 Light ilNE OF REAtlN6:

r PLANT $ lit Brun6 mitt DATE:02/10/90 Clf 2

11NE:17:19 TRAN6 MIS $10N 50

[

RfD MNP0thi PRESSURE Mh4 AS REAt CALIBR. SEN4 AS READ CA!,lDR. BE M AS READ CAllBR.

M1 87./00 87.700 001 156.970 75.731 00184954.M0 64.304 002

86. % 0

86. % 0 002 !$7.710 76.229 00215083.000 64.297 003-99.9'.0 89.640 003 157.990 76.417 M4 99.150 89.150 004 160.620 78.185 WE16HIEDAV6, 64.301 06 08.730 88.730 005 150.000 76.477 0%

90.M0 90.050 006 157.840 76.316 007 88.410 68.410. M7 145.000 69.161 000 87.990 87.890 008 146.990 68.970 009 08.3M 88.350 009 144. % 0 67.319 010 87.460 B7.460 010 146.%0 68.338 011-B7.590 17.590 012 '. 90.030 90.030 WE10NTED AYS. 73.005 013 ' B7.970 07.970 014 II.200 08.200 018 M.220 94.220 016 82.490 02.490 017 84.460 84.460 018 95.990 85.B90 1

019 69.030 69.030 020 -69.690 69.690 021 68.930 68.930 022 69.200 69.280 9

023 69.490 69.480 024 69.350 69.350 WE16HIEDAV6. 19.274F 538.964 R r -

l Il 1

WATERVAPORFARilALFRESSURE:

0.401722 PSIA i

MASS NE16Hii. 94396.3097LIR s

i I

$$$ SENSOR READINGS AND AVEkAGES ***

lill ILRT litt itsi POINT NURSER 6 l

CLitNT CarolinaPowr6 Light 11ME OF READIN6:

.t l

PLCf $111: Brunsuitt MIE:02/18/90 UNif -

t2 TIME:17:34 I

TRANSMlBl!DN il 1

1 RfD DENPOINT PRESSURE SE D Al READ CAllM. BIN 8 AS READ CAllM. BEN 8 AS READ CAtlBR.

001 87.640 87.640 001 156.930 75.704 001949M.000 34.301 002 86.520 86.520 002-157.600 76.209 002 B5800.000 64.295 l

003 01.830 89.630 003 157.490 76.081 4

M4 09.110 99.110 004 160.8%

78.306 NEl6Hi[D AV6. 64.298 005 98.7M 88.700 M5 iM.290 76.619

- M6. 90.020 90.020 006 157.750 76.2 %

007 88.410 88.410 007 145.620 61.039 008 87.820 87.820 MO 146.770 68.820 l'

009 68.3M 88.3 % 009 144.640 67.373 010 87.440 87.440 010 146.020 68.311 0!!

B7.500

17. 2 0 012 90.020 90.020 NE16HillAV6. 72.970 013 - 87970 87.970 014 II.200 II.200 Oil 84.210 B4.210 016 B2.460 02.460 017 84.4M 64.4 %

010 - 65.980 B5.000

(

019 69.040 69.040 020 69.690 69.690 021 68.930 68.930 1

022 69.200 69.200

. 023 69.480 69.480 024 69.350 69.350 NE!GHilDAV6. 79.265F

.538.955R a

u l'

l l ~

i L

NATER VAPOR FART!AL PRESSURE:

0.401360ISlA MASS NE!6His 94394.5163 LBM.

sss SENSOR READINGS AND AVERACEO 888 l

1988 ILRT litt itST POINT lluSER 7 CLIEpi"

Carolina Powr 4 L19ht ilnt 0F READING:

PLANT Slit Brunseitt DAlt 02/18/90

' I lf-2 IIME:17:49-tRAN$nlBSION: M AfD DENPOINT PRESSURE C:' A8 READ CAllDR. SEN4 AS READ - CALIBR. SEN6 Al READ CAllBR.

Gl 17.6M 17.600 001 1 %.980 75.738 00104947.0M 64.299 C2 B6.470 86.470 002 157.850 76.323 00295876.0H 64.292 003 99.810 89.010 003 !$t600 76.'/o9 M4 89.000 89.060. 004 160.540

'/8.131 NE16HIEDAV6.

64.295 C5 98.740 98.740 OH 158.260 76.598 OM 90.040 90.040 0% 157.740 76.249

'007 88.390 98.390 007 145.590 68.019 000 07.B60 17.860 000 146.930- 60.929 009 98.330 88.330 M9 144.720 67.427 010 87.440 B7.440 010 145.950 68.263 011 87.570 87.M0

.012 90.010 90.010 WE16HiQ AVS. 72.996 013 17.990 87.990 L 014 08.200 II.200

+

ell 08.210 - 84.210 016 B2.440 12.440 017 ' 84.440- 94.440 018 85.870 85.870 l

019 69.040 69.040 020. 69.690 69.690

' 021 68.930 68.930 022 69.280- 69.290

. 023 - 69.480 69.480 024-69.350 69.350

'WEl6HTEDAV6. 79.261F

$38.951R e

t NATER VAPOR FARilAL FRISSURE:

0.401462 PSIA MASSNEl6His 94391.3175LM i

?+.-

t' q

1

.888 SENSOR READINGS AND AVERAGES ***

l titt ILRT litt

)

TEST PolNT lluMMR I j

I

'l CLIENT CarolinaPower& Light ilk 0F RfAllb6:

PLC.1 Slft: Brunssick Daft:02/18/90 l

Cli.

12 ilM ll:H j

TRANSMIS$10W: 53

)

l RfD DEWPolNT PRESSURE

- SEM AS RfAD CAllBR. BEM Al htAD CAllBR. SEM AS REA8 CAlltt.

001

87. 3 0 87.6 % 001 157.320 75.9M 001 84943.000 64.296

,002 B6.490 B6.490 002 157.630 76.175 H2 B5871.0M 64.298 003 69.800 89.800 003

!$7.92'.

76.370-

' M4 '99.060 89.M0 004 161.M0 78.441 NE10HifDAV6. 64.292 605

08. 4 0 B0.40 00$ IM.M0' 76.464 M6 90.030 90.030 0% 157.740 76.249 M7 69.380 08.380 M7 145.640 68.0$3

' 600 17.010 B7.810 OM 146.7H 68.807

'609 08.330 89.330 M9 144.4H 67.264

'010 ' 07.430 B7.430 010 146.M0 68.297 0!! ' 07.M0' 47.H0 J 011 - ' 90.010 90.010. UF10KittAV6. 72.972 013- 07.9M 37.9N 014 II.270 98.270 i

. til 'M.190 -M.190 016i 82.440 12.440 017 94.420 94.420 y

' 018 85.860

" 860

019, = 69.030. 69.030 0201 69.690 69.690

. 0?!

68.930- 68.930 022: 69:280-69.280 023 i69.470 69.470 024 -69.350 69.350 Wil6HIEDAV6. 79.249F 538.939 R i

L 1i lc W41[RVAPORPAR11ALPRESSURE:

0.401273FSIA.

1 MAS $W[l6NT: 94388 $661 LBM

f n:

s ss*-SENSOR READINGS AND' AVERAGES ***

4488--

ILRT till TEST POINT NUMBER 9 CLIENT - Carolina Pown & Licht TIME OF READIN6:-

PLCT Slit Brunswick DATE:02/18/90 UNil -

t2 TIME:18:19 TRAltSMIS$10N: 54 RTO DENP0lNT PRESSURE SE"3 AS READ

-Call 8R. SEN8 AS REA8. Call 8R. SEN8 AS READ CALIBR.

t 001 87.!# 87.500 001 157.250 75.919 001 84939.000 64.293 002 h6.440 ; 86.440 002 -158.100 76.504 002 85868.000 64.286 003-89.77t 89.770 003 157.520 76.101

.004-89.020.

89.020 004-160.490 78.098 NEl6HTEDAV6. 64.289 005 88.680. 88.600 005 !$8.160- 76.531 006' 90.010- 90.010- 006 ' 157.690 - 76.215 007 88.300 - 88.3001.007-145.650 68.059 008 87.750' 87.750 000 146.770 68.820

'009 88.300 88.300 009 144.530- 67.298

' 010 87.420: '87.420 010 145.980 68.284 L011' 87.530 : 87.530 012 89.900 '89.900' NE18MTE8AYS. 72.961 013' 87.888 87.III 014 ' II.260 -!88.260'

+

'Oll. 84.190 84.190

- 016 82.420: 82.420

017 84.400L 84.400 018: 85.850 85.850 019 69.030 69.030 l

c020..69.690-69.690 1 021 ;68.930; 68.930

. 022-l 69.200; 69.280 1023 - 69.480 69.400 024.69.340 6?,340 lNE16HIEDAVD.= 79.236F'

538.926 R 4

i l"

l~

[

f i;-

t

- WAIER VAPOR PARTIAL FiiESSURE:

0.401136 PSIA MASS NE16His 94387.2193LBM

ylN

!***T ENSOR READING 3 ANDiAVERADEOS***

titt ILRT.

till -

' TEST POINT NUMBER ^10.

4 CLIENT

' Cucliu Power 6 Licht' TIME *0FREADING:

iPLAWTSliElBruusitt--

DATE: 02/18/90 s]QN17 32

~ TIME:18:34.

r RTD DEWPOINT PF. ESSURE f

4 SEH. AS READ CAlliiR. SEN8 AS READ Call 8R. SENt AS READ CALIBR.

601 67.4604 87.460 '001 -157.520- 76.101 001 84935.000 64.290

'002 '86.360.

86.360 -002 157.900 76.356 002 85865.000 64.284 003 89.760- 89.760' 003 157.190- 75.879

'004 88.990. 88.990 004 160.550 78.138 WElGHTEDAYB.

64.287 i

' 005 68.740 88.740 005 158.130 '76.511

096'~90.010 90.010 006 157.600 76.209.

007 88.350 88.350 L007 145.720 68.107 006 87.740- 97.740~ 000 146.770 68.820 009L 88.300 88.300 '009 144.570 67.325 0101 -87.400 87.400 010 145.960 68.270 Olle ;87.520 *87.520 3

012a 89.900.89.900 'WEIBHTED AVG. 72.959 013l 87.870 87.870 014--

86.240. 88.240

-l'(

015,. 84.180' '84.180 -

016..

82.400 '82.400L 017-.-84.390.84.390 018-85.850 85.950 1019, '69.030 69.030

<020' 69.690 69.690 7

' 021 68.930 '60.930 3

0221.69.200. - 69.280 023'.

69.430 69.490

~u

[

c024 - 69.340 69.340 Wil6 HIED AV6. 79.228F 538.918R t

.(

q:- s L.,

l ls l

WATER VAPOR PAR 11 AL PRESSURE:

0.40!!09 PSIA

-1 MASSWEIGHT: 94304.7867 LEM l

]

3

g e

o t

sse BENSOR READINGB'AND AVERABES ass-till

llRT-

'till T($1POINTNUMBER 11.

CLIENT:

CarolinaPoer&~ Light-TINE OF READING:

' PLANT $11Et Brunsult!

DATE:02/10/90

.UN!I.

I2 TIME:18:49 TRANSMlBSION: 56 Rio DEUPOINT PRESSURE BCi AS READ CAllBR. 'SEN4 AS REA0; CAL 18R. SEN4 AS READ Call 8R.

001 <- 97.410 - 87.4101- 001' 156.740' 75.577 001 84932.000 64.287 86.380.

86.380 : 002.-157.400 76.074 002 85861.000 64.281 002

-003 - 89.740 89.740- 003 D157.760- 76.262 004. - 88.970 88.970 '004 160.410' 78.044 NE16HlEDAV6. 64.264

" 005L 04.680 88.600 005 '158.040 76.451' 006> 89.930 89.930: 006 157.610' 76.161-

. 007 88.350 -.88.350 007 - 145.500 68.012

000 87.740.

87.740 : 008 146.770 68.820 009 - 90.270 ' -80.270 009 144.720 67.427 010 17.390-87.390 010 145.900- 68.284

. 011 ' 07.510 ' 87.516 M ; N9.970. - 99.970. WE10HTEDAY6. 72.909

,1

. 0a

.>.s.

.7.

0 R

.014',II.240 ' 10.240

- Oil - M.100 84,100 016 82.390 82.390'

( 017 ; 84.300.84.380 x

018 85.830 85.930'-

d 019^ 69.030 -69.030

,N

)5

'020 69.690" 69.690 021 ' 68.930~ 68.930 022-69.270 69.270..

')

1 023. 69.470-69.470' 1

024 69.340

,69.340.

U

' j.

NE16HIEDAVG. 79.219 F

]

' Mj

$38.909R-s q

I

.)

i a

i T

NA1ER YAPOR PARilAL PRESSURE:: 0.400435 PSIA MASSWEl6 Hit' 94383.6097LBM YI

'-1 9

^.'

$$$ L SENSOR READINGS AND AVERAGES ***

T 1648 -

LlLRT lill ~

TEST POINT NUMBER '12-

' CLIENT:

CarolinaPoser& Light TIME OF READIN8:

PL'!T SifE: Brunsalck DATE:02/1B/90 UNii -

l2 illEs 19:04 TRANSMISil0N 57 -

t RID DENPOINT PRESSURE ti SE:3: AS READ' CAllOR.-.SEN4:ASREAD: CAllOR. SENI AS READ - CAllBR.

t 001-87.370- 87.370- 001 l'56.960 75.724 001 84928.000- 64.284

_j 002 86.300 86.300 002: 157.700, 76.222 002 85857.000 64.278

!003 89.720 89.720- 003: 157.610.

76.161' 004 88.930-- 88.930 004 160.550: 78.138 ' NEl6HTEDAV8. 64.281

. 005 : 88.650 88.650 005 ' 158.230' 76.570' 5

L006- '89.980. 89.980 '006. 157.720 - 76.235'

- 007: 88.330 : 88.330 007 145.630 68.046-008-87.700 87.700 - 006 '.146.800 68.841 -

009 88.170 88.270 - 009. 144.640 67.373 010 87.380 'B7.380. 010 146.010 68.304 011 '87.510 - 87.510.

i

' 012 ' 89.970 - 89.970 1 NE10HTED AV8. 72.964

.f.

-013

07.060 ' 07.060

014: II.2201 80.220 1015 - 84.170 L 84.170.~

i

,016 82.380 82.380'

- 017 :- 84.370- 84.370

'018" L85.830 85.830-019l -69.020 69.020-020 69.690 : 69.690 021' -68.920 68.920 l

. 022' 69.270 69.270 g

l 023 69.470 69.470-024.

69.340 69.340 g

WEIGHTED AVG.- 79.211F f

p

'30.401 R l

l:

ll l

I);

[,'

l' u

l' l

WATElt.VAP0R PARTIAL PRESSURE:

0.401177 PSIA I'

-['

MASSWElGHT: 94379.5133LBM

~

{%,

3 i

- - SENSOR. READINGS;AND AVERAGES ***

l 2

till

-. ILRT :

till ~

j TESTPolNTNUMBER-13=

, CLIENT.

' Carolina Pou r 6 Light ilME OF READIN6:

, PLCT Slits Brunwick DATE: 02/10/90-

+

UNIT '

2 TIME: 19:19 TRANSMIS$10N 2 j

t

?

p RfD

-DENPOINT.

PRESSURE SE N 'AS REA*- ' CAllDR. i SEN8 AS READ CALIBR. SEN8 AS READ CALIBR.

3 001-87.310.. - 87.310-- # 1 !$7.600 76.209 001 04924.000 64.281

! M2.-

86.24 0 -84.240 002-157.B40 76.316 002 E5854.000 64.271 M3, 69.700 89.7M : 003 157.650

-76.188-t

, M4 c08.930 B8.930 004' 160.650 78.205-NE!6HTED AV6.- 64.278 M5 ' 80.630 - 88.630 00$ ; 158.100 76.491 o

IL

' 0M s 89.970 89.970.' 0% 157.720 76.235

-1 E

- M7 88.320 - '87.710' 000 146.830 68.861 88.320L 007 145.690 68.087-

~

L 000 : 87.710 I

009i 88.2 %, St.2% ' M9. 144.650 - 67.380 l--

h 010 87.380 L 87.380 010 146.070- 68.345-011.~

87. M0 87.500' 012" M.960 89.960 NE18 HIE 8 AYG. c72.998 L

~ 013 97.H0 ' 57.M0 '

I 014: II.200 80.200.

015 84.160 84.160 016: 82.370: B2.370 017 - 84.360 - 84.360

-018 ' B5,BM -. 85.800 >

l l'

019-69.030 69.030-020: 69.690 69.690 t

s l '-

-021-68.920'. J68.920 l

022 l69.270 6 *.270..

l L023 69.470 69.470

~ ~ 024 ' 69.340' 69.340

-. c

. NE!6 HIED AV6.-

19.201F l:

538.891R 1'

d h

1 I

,j r

,~'

I-y

?

d I

ll 4;

NATER VAPOR PARilAL PRESSURE:

0.401626 PSIA i

'MASSNE16His 94376.6302LBM i

%;( ?jn,

'i

m

'_:{

'888:! SENSOR.' READINGS'AND AVERAGES t**

till ILRT 8888

'l T[liPolNTNUMBER.14

.~ CLIENT j

..o -

.~ 'sCarclinaPower6 Light 11ME OF READIN8:i PCT Slit Brunsulc0 SATE: 02/18/90-UNIT

2~

TIME:19:34 1

TRANSMISSION: 59 l

RfD DENPOINI PRESSURE

. SE D AS READ' Call 8R.. SEN8 AS REA8' Call 8R. SEN4 AS READ CALiliR.

001-87.280 87.280 001' ~157.540 76.!!4 001 84921.000 64.279

'.002L 86.210 86.210 002 157.700. 76.222 00285849.000 64.272

-003

'89.600 89.600 003.157.840 76.316

- 004 88.880 88.880 004 160.590 78.165 NE16HTED AV6.

64.275-

'005 88.630 88.'630 005 158.130 76.511 006 89.800 89.800 ' 006-157.770 76.269-(

.007e 88.310 88.310 007 '145.630 68.046 008 s 87.740- 87.740 000 146.820 '68.854

. 009 : 88.240_ 88.240 009 144.550 67.312 010- :87.370 87.370 010.146.070- 68.345 T 011-87.490 '87.490

'012 - 89.950- 89.950' E18HTEDAY8. 72.990 013 87.830 87.030

' 014 - 80.220 80.220 815 - 84.160 ' 84.160.

016-82.360 82.360-2017-84.350' 84.350 j

018-65.000: 85.000 019 ' 69.030 69.030

.t 020- 69.690 69.690 021-68.930L 68.930

-l 022 69.270 69.270 5

0231 L69.470 69.470

.1

'024. 69.340. 69.340 NE16HIEDAV6. s79.196 F'

+

538.886 R-

'I

-)

NATER VAPOR PARilAL PRESSURE

0.401516 PSIA MASS NE16HT: 94373.3325LBM c

i 1

4

+

p'

**.BENSOR. READINGS AND AVERAGES * * * -

l 1888

=ILRT lill l

'TE$iPOINTNURSER'15 b

I CLIENil. : Car'elina Power & Light TIME OF READIN6:

, PLC~i Slit Brunswict DATE: 02/10/90 UN!i

.: 2 ilME:19:49 IRANSMIS$10N: 60 s

RT8 DENPOINT PRESSURE 8CL AS REAB. Call 8R.'SEN4 AS REA8 CALIBR. SEN6 AS READ Call 8R.

p

. M 1 : 87.240 87.240- 001-157.650 -76.188 M1 84917.000. 64.276

' M2. 86.200. 86;200'. 002: 157.710 76.229- ~002 85845.000 64.269-H3 89.680 :. 89.600 M3 157.720-76.235

. ElBHTED AVG. 64.273

'004' 88.860 '88.860 004 160.700 78.239 W

005 88.700 88.700+ 005 158.260 76.598 L 0%. 89.860 ' 89.860 ; 006 157.750 : 76.256 M7 '88.300 88.300 007 145.660

~68.066 1

008 87.720=

87.720-'008 146.790 68.834 009' 88.240 88.240 009 144.510 67.285

~010 87.370 87.370 010 145.990 68.290 0!!- 87.480 87.480 p

'012L '89.950 89.9 #

NE18HTES AY8. 72.996 t

L 013 ' 07.830 87.830 014 ' 88.190 80.190 015. 84.150- -84.150-E

-. 016 ' 82.350. 82.350c 4

'!017 84.350 84.350 018 = 85.790 85.790

~019 '69.020 69.020:

'020L 69.690 69.690' L

021, 6B.930, 68.930 1.-

J022

-69.270' 69.270 h

023. 69.470 -69.470 1N

_024i 69.340 69.340' i WE!6 HIED AV6.. - 79.191 F '

-l 538.881 R

'1 c

L H

H l

L

'()

l WATER YAFOR PARilAL PRESSURE:

0.401609 PSIA

, 1.

MASSWE!6HT: 94369.5975LBM a-

i

- - ESENSOR. READINGS ~AND AVERAGES ***-

litt :

JILRT :-

- till -

TEST POINT NUMER 16 i

CLIENT- :CarolinaPoser6 Light TIME OF READIN8:

'I

. PLANT SITE: Bruualck:

DATE:02/10/90 MIT

2 ilNE:20:04 TRANSMISSION'61' q

i RfD MWPOINT PRESSURE SEN4!.ASREAD cal!8R. SEN4 AS READ _CAllBR. SEN8 AS READ CAllBR.

1

-001 87.180 '87.180 M 1,157.390. 76.014 001 84913.000 64.273 l

002 96.200 96.2 % 002 = 157.440 76.047 00285842.M0 64.267-003 '89.660 89.660. 003 157.500 76.088 004' 88.840- 88.840- 004 160.610 78.179 WE!6HTED AV6. 64.270 i005 88.610 88.610 MS 158.200 76.558

.?

5006 89.950 89.950,006-157.710 76.229 j

M7: 88.290 88.290 ' 007145.680 68.M0 4

L M8 87.710 - 87.710 ; M8 146.8 % - 68.841

' M9 t 88.230l 88.230 009 -144.580 67.332 010 1 87.340 87.340 010 145.960 68.270 011 87.470- 87.470 012-89.940 89.940 : ' UEIONTE8 AV6. 72.962 j

013, 87.830 87.830 014-88.190' 88.190 015 =84.150 '84.150 016 92.330

=82.330~

017> 84.330 84.330 j.

018-85.780' B5.700 019 69.020 69.020

- 020 69.680- 69.600 1 021 68.930 68.930

.t E022' 69.270: 69.270

+-

023 69.470 '69.470 024 ' 69.340, ~69.340 t

NEl8HTED.AV6. 79.184F 538.874 R I

'i e

i

-i

'l i

LWATER VAP0R PARTIAL PRESSL'RE:

0.401141 PSIA

53WE!6HT: 14367.7372L55

h

- - 1 SENSOR READINGS AND AVERAGES ***

litt.

.lLRT-till' l

^

TEST POINT WR8ER 17 CLIENT:. : CarolinaPower& Light

.flMEOFREADIM8:

PLCf SliE Brunsulck DATE:02/10/90 UNii

2

. TIME:20:19

-IRANSMIS$10N: 62

.RfD DEMPOINT PRESSURE-SENG' AS READ Call 8R.. SEN4 'AS READ Call 8R. SEN4 AS READ - Call 8R.-

001 87.110 87.140 001 158.290. 76.619 001 84910.000 64.271

002 86.000 86.000 002:-157.820- 76.343 00285839.000 64.265

_ 003 - 89.610' 89.610. 003 - 157.610 76.161 004; 88.820 88.820 004 '160.520. 78.118 -NEl6HIEDAY8. 64.268-003' 88.710 88.710 005.158.210 76.565

'006:.89.810 89.810. 006 157.640 76.182

~t

~

007 88.290 88.290 007 145.720- 68.107

'000-87.740 87.740 008 146.770 68.820

009 88.220 86.220 009 - 144.560' 67.319~

010 87.340 -87.340 010 144.030. 68.318 -

4 011 87.470 87.470 012 ' 89.930 89.930 WE18HTE8AV8. 73.000

'813-87.820 87.820 014-- 88.180 88.180 015' 84,140 84.140

'-016 82.330 82.330 017 84.330'~

84.330

'l" 018 85.780- 185.700 IL

' 019 69.020- 69.020

.020 69.680' 69.680 021 68.920 68.920' 1022 '69.270' 69.270 a,

'023 69.470 69.470 L

024 69.340 69.340 i

[

' WEl6 HIED AV6. 79.175F l

'538.865 R j

l p

t l

l

((

V WATER VAPOR PARI!AL PRESSURE: 0.401656 PSIA u

,-m MASS WE!6HT: 94365.1265LBM

'A_,

3

'M.'N

t

, ).'

J g i, p

%2888" SENSOR ~READINGB'AND. AVERAGES ***

J

]~,m lista ILRT '-

litt-K,x TEST POINT NUMKR 18

CLIENT-CarolinaPouer6 Light-

-ilME OF READIN6:

' PL O SITE: Brunswick.-

MTE:02/18/90

'UNii

2-TIME: 20:34 TRANSMISSION:63

i =

. AfD

-DENPOINT PRESSURE g

U

. SEM AS READ - Call 8R. SEN4 AS REA8. CALIBR. SEM - AS READ CALIBR.

001' 87.!10 ' B7.110 ; Ml: 157.790 76.282 001 849%.000 64.268 "002: ^86.090 :86.090 002 157.5M 76.088 00285234.M0 64.261

-r

- 003 89.630 ~ 89.630. 003. 157.620 76.168-

'M4

-88.800

-88.800' 004 160,820 78.320 NEl6HTEDAYS. 64.264 4

MS' 88.630 88.630 005 158.180 76.545 OM : : 89.820 89.820 0% 157.720. 76.235

!007c 188.280, 88.200 '007 145. 4 0 - 68.M6 s

e M8 87.730- 87.730. 000:' 146.820 68.854 M9-88.220.: 88.220 '. 009~ 144.480 67.264

-010'>:07.340; 87.340 010 144.000 68.297

011 > - 87.40 87.460-L012: . 89.930' 89.930, NEl8HTEDAV8. 72.985 l

813 f 87.820L 87.820 -

1014i i N.170 N.170 -'

015.' :84;130 H.130

.016 - 82.310

~82.310~

l01784.320- -84.320 t 018 - 85.760l - 85.760

- 019. '69.030,. 69.030.:

r020 : :69.680- - 69.600

.,~

7 m 021 f68.920'.68.920 0235 -69,270 ; 69.270 U

033 - 69.480 69.480 b;

024 69.340/ :69.340 i

NE16HTEDAV6.. 79.171 F' 538.861 R i:

L l-l' J.:

i.

j n NATER YAPOR PARilAL PRESSURE 0.401448 PSIA

,~

l:

MASSNEl6His 94361.20!! LOM J

gis c'

~ !

I

- - SENSOR READINGS 1AND: AVERAGES ***

litt ILRT.

till i

TEST PolNT NUMBER 19 CLIENT.

Cu olina Power & Light TIME OF READINB:

PLOTS 11EsBrunswick DATES 02/18/90 UNii 2-TIME: 20:49 TRANSRISSION: 64

-(

.RfD~

DENPOINT

' PRESSURE

'I SEN8 AS READ CAllBR.' SEN4 AS READ Call 8R.D SEN8 AS READ Call 8R.

001 N.050 '87.050 001 157.220 75.899 001 84903.000 64.266 l002l 86.060 86.060 002 ' 157.810 76.296 00285830.000 64.258 003--

89.590 89.590 003 157.710 76.229

'004 88.760 88.760 004' 160.600 78.172 NE16HTEDAV6. 64.262 005 88.750- 88.750' 005-157.990 76.417 ON. 89.880 89.980 006 157.680 76.209

7-88.270' 88.270.007 145.550 67.991 000 ' 87.670 87.670 008 146.720 68.786 009: 88.210' 88.210 _ 009 144.570 67.325' 010 -17.330 87.330 010 145.970 68.277:

}

0!!

87.450- 87.450-j 012' i 19.920 19.920- WE!8HTED AYS. 72.932 813 87.820 27.820 l014 88.170 88.170 015

.84.130-84.130

016. 82.300 B2.300' 017 84.310 84.310 013 85.760 85.760 019

'69.020 69.020-020 69.680 69.680 021.68.920 68.920 022; 69.2701 l69.270

.023' 69.470 69.470-t 024' 69.330 69.330 NEIGHTEDAV6. 79.164F 538.854 R q

f f

l 1

WATER VAPOR PARTIAL PRESSURE:

0.400741 FSIA RMSS NE!6HT:~ 94359.6203 L8M i

. #i).[3 l

2 x

is**ESENSOR READINGS AND AVERAGESi***.

8888

.lLRi-1888'

[

TEST POINT NUGER 20 i

lCLIEWi-CarolitiaPower& Light.

11ME OF READIN6:

PLAN 7 $!TE: Brunsultt DATE:02/18/90-

' i UNii -

s' 2 TIME:21:04 TRANSMIS$10N 65 -

,p 4

RfD :

DEWPCINT PRESSURE l

SEN8: AS READ Call 8R. SEN8 AS READ OAll8R. SEH AS READ Call 8R.

..t 001:

87.020 87.020 001 157.180 75.872 001 84899.000 64.263

.M2 85.990 85.990 H 2 ~ 157.580-76.141- 002 85827.000 64.256 W W3: 89.590 89.590 - H3 157.560 76.128 i

M4 - 88.740 ' 88.740 M4 160.490 78.098 NE16KTEDAV8. 64.259 005 L 88.680,88.600 005 158.240 76.585 006' 89.780 ' ' 89.780 - 006 ~ 157.650 76.188 007! 88.270 -88.270 M 7 145.700. 68.093

'000. 87.740 87.740 - 008 146.710. 68.780 009: 88.200 : 88.200' 009_ 144.640 67.373-p J010 87.320' 87.320 010 - 145.960! 68.270 011-87.450: 87.450,

'012 t 89.920 89.920'.NE18HTEDAV8. 72.950

'013 - 87.818 '07.818

. r I

<014. 88.170 <88.170 015-' ?84.130 : '84.130

016 L 82.3M 82.3 %

- 017' '84.290: 84.290 e 018.. 85.760.85.760

' 019 : ' 69.030 69.030 020 t69.680- 69.680-

.r.021 68.920. 168.920

+ 022 69.270 ~69.270

> 023. 69.470 69.470

.024 69.330; 69.330 Fuel 6HTEDAV6. 79.159F 538.849R-

' t g-L.

4:

L

- i o

l' WATER VAPOR PARilAL FRESSURE:

0.400979 PSIA MASSWEl6His 94356.3042LBM t

3 7

gt

(

. ? f' 1

88sfSENSOR READINGD?AND'AVERACEO ***

4 8844 ILRI.

8888:

[

' fE61 PolNT NURSER 21 -

I CLIENTJ Carolina Power 6 L19 t

- i!NE OF READING h

PLOT Slit Brunsultt:

DATE:02/10/90 UNIT-

2 '-

TINE:21:19 l

TRANSN]SS!0N 66 8

.1.

' RTD DENPOINT PRESSURE s>

I

'SEN4 46 READ ' Call 8R. SEN4 AS REA8 CALIBR..SEN4 AS READ Call 8R.-

001('86'.97/

86.970- 001 157.930 76.377 001 84896.000 64.260 002 85.9/0 05.970 002 157.730 '76.242 H285823.M0 64.253 1

003-89.570 89.570 003 157.220 75.899

004 ;88.720.88.720 004 160.620 78.185-NEl6HTEDAY6. 64.256 005'-

88.680- ~88.680 M 5' 158.250 76.592 l

'006'~89.830-89.830,0%

157.640 76.182 M7 ' 88.260. 88.260.007 145.640 68.053-i

M8 : 87.720- 87.720 000 146.8 %

68.841

009 - 88.200' 88.2M- 009 144.620 67.359 010 / 87.320. 87.320 010 146.000 68.297

. 0111 '87.450 87.450:

'012 -89.910 89.910 NE18HILSAY6. 72.981 4

013 87.810 ~ 87.810-014 88.100 88.180 015i.84.120 84,120:

"e 016 82.300: 82.3M -

.017 84.280 ' 84.280 -

018' 85.750 85.750 1(

,019:

69.030. 69.030

B

,0201 :69.690 69.690:

A L021: ;68.930< 68.930.~

s 022 "69.270- 69.270

!023i 69.470; 69.470 024i 69.330 "69.330

}

p

.q.

l INE!6HTED'AV6. 79.156 F 538.646R

}

[

i o.

1 a

~

l I:'

l l

- NATER VAFOR FARilAL PRESSURE:0.401395 PSIA L'

i l

MASSbE16HT:

94352.2848 LIM l

.a ar

' M/t

338 SENSOR READINGS AND AVERAGES-***.

till ILRT litt TEST POINT NUMBER 22.

.I 1 CLIENT

Carolina Power 6 Li8 t-TIME OF REA0lN8 h

PL Ci EliE: Brunswick DATE:02/10/90 UNIT-2 TIME: 21:34 TRANSXISSION: 67

,1 9

o1 Rf D -

DENPOINT PRESSURE.

SE",) AS READ CAL 18R. SEN8 AS READ' Call 8R. SENG AS READ CAllBR.

001 - 86.930 86.930 001. ~156;950 75.718 001 84893.0 N 64.258 002' 85.950 85.950' 002' 157.710 76.229 00285819.M0 64.250 6

i 003 : 89.560 89.560. 003 157.500

-76.088 -

-004 88.7M 88.700 004 160.630 78.192' NE16HlEDAV8.. 64.254 005.88.610 88.610 - 005 158.090 76.484.

006

89.770. 89.770 - 006 157.690 76.215 l,

'007.

88.260- 88.260- 007 5.45.730 68.114

-0081 87.700- 87.700 D4 446.820- '68.854 0091 88.200 - 88.200 009 144.630 '67.366

'O.to

-87.310 87.310 010 145.990 68.290 011.'87.4301 87.430 0121 ' 09.900' 09.900- NE!OHTEDAY6. 72.952 013 87.000 87.000 1 014 88.158 88.150

-015-84,110 H.110 l

0161 82.290 82.290

017l. 84.200 84.280 i

. 018. 85.740- -85.740 l,

'019 69.030' 69.030 t

4

,020-69.600- 69.600 I

021 - 68.920 68.920 s

022

69.270 =69.270 i '

023 ; 69.470 - 69.470 :

l 024' 69.340 69.340 f

L.

79.147F UE16HTEDAV6.

538.837 R l

i i

o i

L NATERVAPORPAR11ALPRESSURE: - 0.401014 PSIA MASS NEl6HT: 94350.5991LSM i

[

p 4

r i <

g',w:

w 3

- - LSENSOR' READINGS AND AVERAGES'***

.4818 ILRT till TEST POINI NUMBER 23-

]

fj iln _'

iCLIENic 'sCarolinaPower&Li8ht

-TIME OF REA81118 -

PLAlli Slit Brunssid -

W TE: 02/18/90

[

's2 ilME: 21:49-l J uilli TiANSMISSION: 68-

-- i

,;4

~..g RID DENPOINT PRESSURE-g j

SENS:A6 READ Call 8R.- SENt AS REA8.04L18R. SEN4 AS READ-Call 8R.

P

- M i{ '86.800 86.880 ~001 ~157.310 75.960 - 001 84889.000 64.255 5003c 85.880.-85.880.-002 157.510.76.094 002 85816.M0 64.247 M3 - 89.540 89.540 003 157.330- 75.973 U J M4 - 88.680 - 82.680 M4 160.640- 78.199' NE.BHTED AY6. 64.251

.005' 88.760 88.760 005 '158.120 76.504 i#6:,89.810' 09.810- 006 157.630: 76;175 007 88.250- 88.250 007 145.630- 68.046 l

' 006 < 87.720:. 87.720 -- 008.146.740 - 68.800 1

009 88.180 BR.100. 009 144.380' -67.196

'010 '87.310 81.310 010 ~ 146.000 - : 68.297

^

i

'0!!1 87.430. 87.430-j. 012 ' 89.914 89.918 NEl8HTE8AV8.- 72.918 e 1013 87.000. 87.000 014 - 88.160 - '80.160 1 015 - 84.1M - 84.100 L

'016.82.290' 82.290 c017-94.280 - 84.280 p

1 018 __ 85.730 85.730

}t [019) 69.040--

69.040 y

L E020. 69.670. 69.670' 021--

68.910 69.910.

c022 69.260. '69.260-b:

~033 69.460 69.460 i

l 034 :69.330' 69.330

l

,i

.WEIGHTEDAVG. 79.142F l

538.832 R j

i s

[.

l,'il 4

lh

!l i

l

'NATER'YAPOR FAR11AL FREESURE:

0.400553 PSIA y,,

MASSWilGHT: 94348.2912 LBM :

j

3

w

ag g

\\.Oj

" n; oH AND' AVERAGES ***

Y)Ez*$$sSENSOR. READINGS till ILRT litt TEST POINT NUMBER 24 2

U CLIENT =

Carolina Power 4 Light ilMEOFBEADIN6:

PLCTSlitstrunswick.-

DATE:02/10/90 UNIT-2-

TIME: 22:04 t

IRANSRISSION:69 i

"i; t

'i 1-t l,

_RfD DENPolNT PRESSURE C

SENG AS READ. CAllBR.' SENO AS READ CAllBR..SEN4 AS READ CAllBR.

'.001 86.840 ' 84.840- 001 '157.030 75.771. 001 84886.000

-64.253.

001 ; 05.880 85.880' '002 '157.880~ ' 76.343. 002 85012.000 64.244

'5!

i 003' 09.520 P9.520'- 003 157.600 76.155 i

4

004 88.670 88.670 004 160.470 ' 78.064 NE16HTED AY8. ' 64.249-005, 88.600 88.680 0051 158.000 76.477--

006 89.800 - 09.800. 006 157.720'.

76.235'-

'007 88.240 88;240 007 - 145.620.68.039 008 '87.680 87.680 : 608 146.800 468.841

.t 009 -- 88.180 88.180 009.144.550 '67.312 t

010 ' 87.300 : 87.300 -010 - 145.990-68.290 p

011-87.430.. -87.430

.l L

012 - 89.900 89.900 NE18HTESAYS, 72.946 1

013 -87.000 87.888 l

014 ~88.150 80.1 2 015,84.110 ' B4.110 i?

.016-82.270 -82.270 k

1017 84.260 '84.260

!l 018 -85.730 85.730' L

~019/.69.020- 69.020 i

020 68.600 69.600 s

021-68.920. 68.920

)

[

+ 022.69.270t 69.270 p

023 ' 69.470 69.470 ll 024 69.330 69.330 l

NE!6 HIED AV6. 79.1381 i

'538.828R I

l-

~.

iNATERVAPORPARilALFRESSURE:

0.400925 PSIA MASS NE16His 94344.6935 LBM

4

?

Fr t>

s' l4 8

SENSORTREADINGS AND AVERAGES.-***.

1,

Ills '

!LRT lill -

B cTEST POINT NUMBER 25

, - CLIENT;--:CarolinaPoser& Light.

TIME OF READINB:

[

'PLCi 611Es Brunsujet DATE:02/10/90 UNii:

-2 ilME:22:19

[

TRANSMISSIDN 70 p.,

i

~ AfD DEuPolNT PRESSURE z;;

~ CALIM.- SEN8 AS READ Call 8R. SEN4 AS READ Call 8R.=

J

'! SE3 l AS READ -

^

001-86.810 86.810 1 001-157.440 -76.047 001 84883.000- 64.251 002-85.820 z 85.820= 002 157.900 76.356 '002 85800.000 64.241

.003: 99.510 89.510 003: 157.330 75.973 s

e

. 004l -88.650 - 88.650-'004 - 160.700 78.239: WE!6HTED AY6. 64.246

005-88.680 88.680: 005 158.150- 76.525' W

006: 89.730- 89.730. 006-157.680 76.209 j!

" 007 ' 88.230 - 88.230 007 145.650.68.059

.008; -87.700-87.700-. 008--146.750 68.807 009 88.180 88.180 009.144.636.

67.366 4

- 010 -87.280: 87.200 010.146.030 - 68.318

-011.87.410 87.410:

'012,,;89.890 ' 89.890. - tlE16HTED AYS.'

72.971 013 c 87.800 87.800 ;

014 : 88.150 88.150 I

l015. 84.110 ' 84.110L

'016-82.260 82.260.

017-. 84.250-.

84.250 018-85.720; 85.720

.019

--69.020-69.020 020

'69.670-69.670::

i 1

, 021 -68.920 68.920 LO22'. 69.270 69.270 t

'023.

69.470 69.470 t

'024 69.330- 69.330

- WE!6HTED AVG. 79.130 F.

538.B20 R t

s WATER VAPOR PAR 11AL PRESSURE:

0.401265 PSIA

~'

MASS kEl6HT:- 94341.5842LBM

.4

' - - ~

~ - - -

,,. g >" g

?

g!; J

)

~.J q

1

' fle

?

y L***cBENSOR;READINGB'AND AVERAGES ***

-till

.lLR1

'sitt-

TEST PolN1 NUMBER 26 n

CLIENT, 1 Carolina Poner 6 Light-ilMI 0F READIN6 cPLANiySITE:Brunsuit!

DATE: 02/18/90

'(

- l 21 ilME: 22:34 UN!i:

TRANSMISSION:71 y

-i

'i

-t

.y

- RfD

'DENPo!NT PRESSURE 1

y SEN4;fAS READ' CAL 18A.. SENG AS READ. Call 8R. SENG-AS READ Call 8R. -

d Y ' 001!,86.7801 86.'780 - 001 157.800.76.343 -001 84879.000 '64.247 003 103.790 '85.790 M2 157.670 76.202 002 85805.000 64.239 003; 89.490 89.490 003 157.310 75.960

. -M4T, 88.610 -- 88.610: M4 160.720' 78.252 NEl6HTEDAV8. 64.243 7

M5 88.630 1 -88.630- 005: 158.130' 76.511 006 > 89.680 - 89.680 M6.157.660 76.195

' M7 '88.230: 88.230. M7-145.6301 68.046 006 ' 87.630 87.630 L 008 146.810 - 68.848 009 t J 88.160 < : 88.160 ? 009 144.490 67.271

' " 010 J ? B7.280 ' 87.280' 010' 146.000 68.297 011 - '87.410L 87.410' a

A

. ? 012 1 89.890 ' '89.890: 'NEIONTEDAY8. 72.965 4

' 013 ? -. 87.080 : : 87.808 -

g

' l 014

'88.130 ;88.130

Oil 5 84.'100 t 84,100-016',82.250; 82.250

'017 84.250-. ' 84.250

' l

-018.

85.720 85.720-

.f 019: !69.020' 69.020 J

030 69.680 69.680

' 631J 68.920 - 68.920 d

023 69.260

'69.260' t0234 69.460 69.460 3

f024

-.69.330 69.330:

J NEIGHTED AVG. 79.123 F

}

$38.813R j

i

'I i

,i

.i NATERVAPORPAR11ALPRESSUREt 0.401182 PSIA MASSNEIGHT: 94339.2165LBM

.g

~ ;

p i-

_'st*' SENSOR READINGB'AND AVERAGES'***=

1 titt

ILRT

~8888 i

TEST POINT NUMBER' 27'

,1 Carol'na Power 6 Light TIME OF READIN6:

CLIENil :

i l' ' PLCT $1TE: Brunswict DATE:02/18190 UNIT-2 --

TIME: 22:49 TRANSMIS$1DN: 72 i

RfD DENPOINT

' PRESSURE 1

SE$ASREAD CAL 18R. - SEN4 [ AS READ.- Call 8R. SEN4' AS READCall 8R.

1 o

Ah. 001 - 86.740- -86.740 001 IM.760 > 75.590 001 84876.000 64.245 002-85.750f ' 85.750 002' '157.710 76.229 002 85803.000 64.238 003 89.470' 89.470 - 003.157.670 76.202 4

M4-88.600 88.600 004 '160.470 78.084 WE!611TED AYB. 64.242 H5 88.500' 08.H0 005 158.220' 76.572 006 89.760 89.760 006' 157.550 76.121 007 - 88.210 89.210' 007 145.740- 68.121 1

000 87.680- 87.600 MS 146.770. 68.820

009 88.180 88.180 009 '144.670 67.393 10101 '87.270 - 97.270. 010 145.960 68.270 j

011 87.390 87.390'-

012 M.090 ' 89.890 NE!8HTE8AY8. 72.933-013 ' 87.780 <87.780 3

.014 88.150 - 80.1M.

[

ell! 84.090 M.090 016 82.240 02.240' j

017 '84.240i 84.240-

r; 010 ; 85.710 85.710-

-- 019.

69.020 69.020

-020: 69.670 : 69.670'

, 021 68.920- 68.920' 022 69.270 69.270

'023 69.470' '69.470 t024' 69.330 69.330-NEl6HTEDAV6. 79.119F

'538.809 R

-i Y

l a

r o

p

q 2

WATER VAPOR PARilAL PRESSURE:

0.400753 PSIA h

.MASSNE16HT: ' 94337.7188LBM

y

+

i f-s t**; SENSOR,READINGSEAND AVERAGES <**3

~

6 till ILRT lill TEST POINI NUMBER' 28-

- CLIENT- :CarolinaPoweriL18ht TIME OF READIN6:

j 5 PLC1 SliE Brunswick

-DATE:02/18/90-l

.UNii 12 TIME:23:04' 3,"

TRAN8 MIS $10N 73 RfD DEWPOINT PRESSURE a

SEW 8LASREAD Call 8R. SEN8. AS READ C'll8R. SEN8 AS READ - Call 8R.~

001 86.690 86.690 - 001 ~156.670 75.529. 001 84872,000 64.242 002 85.710 85.710 002 157.570.76.135 002 85799.000 64.235 003 - 99.460 69.460- 003 157.270 75.933 3

004' 88.500 88.580 004-160.460 7d.078 WE!6HTEDAYS. 64.239 x. 005 - 88.700 88.700 005 !$8,120 76.504 006 -89.750 -89.750 ' 006 157.640 76.182 M7: -88.210 80.210 007 145.650 68.059

-M8 87.660 87.660 008 !a6.770 68.820-009 86.160 88.160 009, 144.610 ' 67.353 010 '87.280 87.280 010 145.970 68.277 0!! ' 97.4M 87.400 012 ;89.870 89.870 ; UElGHTED'AV8. 72.908 013 ' - 87.780 - 87.7M 014-88.140 88.140

-0!$.

84.090 84.090' 016 82.250 82.250 L

017 84.240 ;84.240 b

.018-85.710 85.710'

,i 019 69.020' 49.020 l

~020-69.60')

69.600

.031:

68.920- '60.920 s

'022 69.270 :69.270 023 69.470; 69.470 034 : '69.330-69.330 b

W:16 HIED AVB. 79.117 F 538.607 R I

t t

> f,1 b

!I*

t

?

lr

-kATER VAF0R PARilAL PRESSURE:

0.400420 PSIA MASS WE16HT: 94334.1537 LBM

~

FT

+.. u.

t t

's8s SENSOR READINGS'AND AVERACEO-***

j i

~ 1888 llRT -

litt-TEST POINT NUMBER.29

- CLIEN11 :CarolinaPower6 Light ilRE OF READIN6:

, ' PLCi SITE: Bruualck -

DAlis02/18/90 Cli.

.I 2 TIME:23:19 1RANSHIS$10N 74 RTD :

' MWPOINT.

PRESSURE'

]

BEN 8 AS READ Call 8R. SEM AS READ ~ Call H. SEN4 AS READ Call 8R.-

001 86.650,86.650 '001 156.940 75.711 001'B4869.000 '64.240

,L 002.85.700 <85.700 002 157.790' 76.282 00285796.000 64.233 1

,003, 89.440' 89.440 003 157.220 ~75.099 r

004 88.570 38.570 004~ 160.460. 70.078 - WElGHTED AV6. 64.236

'005- ~ 88.660~ 88.660.005 158.100 76.491

' M6~ : 99.750 89.750- 006 157.660- 76195 007 88.210 =88.210 007.145.750' 68.127 j

t

008: 87.700 87.700 008. 146.770 68.820

' 009 - - 80.150. 88.150 009 ' 144.460 67.251 010,- 07.200 - 97.280 010 145.960 68.270 i'

0!!

B7.390 ' B7.390 012 :99.870 89.870- WEllHTEDAV6. 72.921 013: '07.760 '87.760

' 414. 4 98.120 ' II.126

.015'.84.070 H.070

-016-82.240 82.240 t

. 017 84.230-' 84.230 018 - 85.690 85.690 -

-019' 69.020 69.020

't 070. 69.670 :69.670 021- ~68.920 68.920 022L 69.260 -69.260

-023:.69.470 69.470 1 024 -69.330.69.330 WEIGHTEDAV6. 79.108 F -

8 i

'538.798 R -

I r

WATER VAPOR PAR 11AL PRESSURE:

0.400586 PSIA MASS WE!6His 94332.1559LBM

N mm' a

3 1

y ii

!**$tSENSOR READINGS AND AVERAGES.***-

m.

1814 ILRT litt TEST PolNT letBER 30 -

CLIENT =

lCarolinaPower6L18ht-TIMEOFREADINB:

' PLMT $11E Brunssid -

DATE: W/18/90 UNIT -:

12.

ilME:'23:34 1RANSMIS$10N 75 RID DEWPOINT" PRESSURE f

SEn: AS READ CALIBR.' SEN4 AS READ CAllBR. SEN4: AS READ CAllBR.

i

'001 - 86.630 86.630 ' 001 157.350 75.987 00184865.0M 64.237'

} M2. 85.700 85.700 M2 157.650,76.188 00285793.000 64.230 003 ; 89.430.

89.430- 003 157.470 76.067 M4 88.540- :88.540- 004-160.300 77.970- NE16HTEDAV6.

64.234 005J 88.660 88.660 005 -158.190 '.76.551 l

0%

89.760- 89.760 0% 157.580 76.141 M7 - 88.210 88.210 M7 145.660 : 68.M6

. M8 87.730~ 87.730 MB 146.790 68.834-M9 - 88.160 ': 88.160 M9 144.450 67.244

,[

010 L - 87.270'~ 87.270- 010 145.910 68.236 0!!

87.390. 87.390 1012' 89.870 89.870 NE!8HTED AV8. 72.918 4

~ 013 - 87.770 87.770 I

' 014 88.1M ; ;88.140 r

015 '~ 84.070 = 84.070.

i

'016' ' 82.230 82.230 4

017..

84.220 84.220 i018 -85.680 85.680.

.[

019: = 67.020: 69.020' 020. 69.670 !69.670 021" - 68.920' 68.920

~i i.-

-022- -69.270 69.270 023-69.470 '.69.470

024 1 69.340 69.340

]j

'NElGHTEDAV6.=.79.108F 538.798 R r.

~

p

(

i s

'i l.

i l'

l l

1

,1 y

NATER VAPOR PAR 11AL PRESSURE:

0.400552 PSIA

~i L

MASSNEl6HT: 94328.2552 LPM p

j o

f

?

1nh';

Y 1

-3$$ SENSOR READINGS AND AVERAGES ***

l till ILRT lill r

TEST P0lhi NUMBER 31 i

i

. CLIENT it' Carolina Power & Li8 t -

ilME OF READIN6:

h

- PLANT Slit Brunswick OATF 82/19/90 UNIT' 2-i!ME:23:49 1RANSMISS10N 76 1

Rip OENPOINT PRESSURE i

b

.SCJ'ASREAD Call 8R.' SENG AS READ CALIBR. SEN8 AS READ cal!8R.

I 1

. 66.610 86.610 001' !$7.540 ~76.!!4 001 84863.000 64.235 001 -

4 Ff 002 ~ 85.620- 85.620 002-157.560 76.128 002 85789.000 64.227

i 003 -89.420 89.420 ' 003 ~157.810 76.296 004-88.510 88.510. 004 160.420. 78.051 WEl6HTEDAV6. 64.231 005 88.510 88.510 005 158.130' 76.511 i

006 2 89.730 89.730 006 157.650 76.188:

t 007 88.180 88.180 007 145.600 68.080 i

008 87.610 87.610 '008 146.770 68.820

[

009 88.!60 88.160 009 -144.450- 67.244 l

.010 87.250 87.250 010 145.980 68.284 0!!

87.370- 87.370 012.89.870 89.870 NEIGHTED AY8. 72.945 013 - 87.770: 87.770 ele 88.130 - - 88.130 -

015 H.070~ 84.070.

- 016 82.210i 82.210'

j

.017 84.220 ~84.220:

. 018. 85.6001 '85.600

.019' '69.020, 69.020

- 020: '69.660.69.600

- I L

021 I 68.920 68.920-

~ 22' 69.260 - 69.260 0

023

._69.470 69.470

' 024-,69.330 69.330 -

-j

.WE16HTEDAVS.' 79.098 F i

$38.788 R dj i

WATER VAFOR PARIIAL PRESSURE:

0.400918 PSIA MASSWE16His 94326.2264 LBM

k b

-888: SENSOR' READINGS AND AVERAGES ***

8888 ILRi~

litt.

TEST POINT NUNMR 32

! CLIENT! : Carolina Power n L18ht' ilE OF READIN6:

PLANT SITE: Brunsnick

~

DATE: 02/19/90 UNii :

2-ilNF M 04 IRANSRIS$10N 77 4

^

RfD MNPOINT PRESSURE BEN 8 AS READ CAL 18R. SEN8 AS READ C.18R. SEN8 AS READ-Call 8R.

C

-001: 86.500 86.580. 001 157.390 76.014 00184859.M0 64.232 002: 85.6M 85.600 ~002 157.530 76.108 002 85787.000 64.226

!-, l 003 89.400 89.400 003 157.420 16.034 004-88.500.'

88.500 004 160.730 7P.259 NE16HTEDAYB. 64.229

-005 88.780 88.780 M 5 -158.130 76.511 006 89.560-' 09.660 006 157.650 76.188.

M7 88.100_ '_88.180.007 145.640 68.053

008 87.690 87.690 008 146.660 68.746 009-88.1b0 :88.150 009 144.'.90 -67.271 010-87.250 87.250 010 145.920 68.243 011' 87.380 87.380 012' 89.850 89.850~ -WE18 HIED AV8. 72.929 013 87.7W '. 87.7W -

'014 J 98.148 : 88.140 015-94.070 84.070 016 82.210 82.210-01784.210 84.210 018 - 85.670

.85.670-

, 019; 69.020 - 69.020 020'.69.6B(

69.680'

'021' 68.920 68.920 022 69.260 69.260 023 s9.460-69.460 024 69.330 69.330 WE16 HIED AV6. -79.097 F

=

538.787 R

' WATER VAPOR PAR 11AL PRESSURE:

0.400696 PSIA

, MASS WE16His 94323.4747LBM

q%

1

.*** SENSOR READINGS AND AVERAGES ***

1848.

ILRI

' list i

b TEST POINT NUMM R 33 i

l,JCLIENT:

CarolinaPower6 Light.

TIME OF READIN8:

" PLANT. SifE: Brunwid DATE: 02/19/90 1

'N T li,

.I2 ilME: 00:19.

TRANSMISSION:78 i

' RTD DENPOINT-PRESSURE

" J SEN8: AS READ

ALIBR. SENG AS REA8 CAL 18R. SEN4'ASREAD ' Call 8R.

l

? :00lc 96.530.86.530 001 157.630. 76.175 00184856.000 64.230.

6 002: 85.590~ 85.590.'002 157.910 76.363 002 85703.000 64.223

,003.

89.400 89.400 003 157.540 76.114 004 88.480 E8.400 004 - 160.640 78.199-NEl6HIEDAV6. 64.227-

.005 88.700' 88.700 005 158.220 76.572

006 ' 89.610 89.610. 006 157.630 l 76.175

~ 007 88.180 88.180 007-145.580 68.012

. 006 87.750 87.750 008 146.770 68.820

- 009 88.150 88.150 009 144.560 67.319 010 :87.240 '87.240 010 145.930 68.250 011-87.370 87.370

.012

89. H4 09.840 - NE!8HTEDAV8. 72.965

' ~ 013 L B7.760 87.760 -

014 'II.130 80.130 '

015 - -14.050 84.050 -

016 82.200 82.200=

a

.017' '84.200

-84.200-i 018

.-85.670-83.670

' L019: '69.020 69.020 020 :69.680 69.680.

j

-021 : 68.920 68.920 022 69.260: 69.260 023'.69.470-69.470 024- '69.330 69.330 o.

c NE16HIEDAV6, 79.092F s

538.762R si L.

1 e

i

-t WATER VAPOR PARilAL FRESOURE:

0.401180 PSIA MASS NEIGHT: 94319.6958LOM t

1N,.

(I

[

4 e..

i 1

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s

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[g,g SENSOR' READINGS ~AND: AVERAGES I

O till.'Superleposed

.I184<

TEST POINT NUMBER 1 CLIENT..: Carolina Power 6 Light =

TIME OF READING:

< - PL O SITE: Brunsulti DATE: 02/19/90 UN!il i2 TIME: C1:34

-TRANSM18510Ni4 1

RfD-DENPOINT

' PRESSURE SEN4AS READ : Call 8R. SENI AS READ-Call 8R.: SEN4 AS READ. Call 8R.

0011 86.390: 86.390 001 157.010 75.758 001.84818.000 64.202

002 : 85.430. 85.430 :002l-157.980.76.410 002 65746.000. '64.195

' M3. 89.320 '89.320 M 3 157.'610 76.161 i M4 : '80.410 :88.410' 004 ~ 160.380 78.024 NEl6HTED AV6. 64,199 I

-0051 88.560 88.560 ' 005 158.040 76;451 M6. 89.710 89.710 006 157.580: l76.141 4

. 007 88.lW - 88.1 % 007 145.700 68.093 3

006 ' 87.630 87.630 008-146.730' 68.793 L 009.-.88.120 88.120. 009 144.580 67.332 010. 87.2M

-87.2 M 010 145.930 68.250 0111 87.340. 87.340_

,012 '. 89.820 5 M.820 ' - NEl8HiEl AV8. 72'.918 l

' 013 ' 87.7M B7.7M E 14; 88.130 88.130.'

0 Olli 94.040! 84.040

-016-82.160 -82.160-l 1017.

84.170' -84.170' l?

018

'85.640 85.640

~(19 ~ '69.0001 69.000 020 69.660-69.660 L

021-68 900 68.900-022'. - 69.250 ' : 69.250 l1 l'

033 - 69.450 69.450.

024. 69.330 69.330

~

- NEl6 HIED AV6. 79.062F-L

'538.752R o

1

'l NATER VAPOR PARilAL PRESSURE:

0.400548 PSIA-MASSNEl6HT: 94284.4554LBM

,r,

'f -

~

W,

- 'I!Q iss*tSENSOR READINGS-AND AVERAGES ***

litt -Superisposed litt -

m y

c:

i TEST POINI NURER 2

' CLIENT ' s Carolina Power & Light TIME OF READIN8:

>PLCiS11EsBrunsulck' DATE:02/19/90

, UNii -

2.

i!ME:01:49 1RANSMISSIONr 5 y

RfD DEWPolNi PRESSURE O tSEN4 :A8 K AD>. Call 8R. SENO AS READ-c d.1DR. SENG AS READ CAllBR.

b2 001.86.360 66.360 001 '156.930- ' 75.704 001 64810.000 64.196 J002; '85.440 B5.440 002 157.470

'6.067 00285738.000 64,190

003.- -89.310' ' 99.310 003 157.350 - 75187 004 9 88.390 B8.390 M4 160.280' 77.957 WE16HTED AYB. 64.193 1

00$f'88.470 88.470- 005' 158.120 76.504 0% >89.7901 89.790- 0 %. 157.550 76.121 q

$007, 88.130: 88.130. 007 145.740 68.121 M8 87.570' 87.570 : M8 146.720 68.786

.j 009. 88.100 88.100 009 -144.460 67.251 7

010l- - 97.lM 97.lP0 010- 145.970' 68.277

)

/ 011J i 87.340 :87.380 4

< i 012 l 89.820 ' 89.820 WE18HTE8 AV8.. -72.887 -

1 4-f 013.-

87.730f 87.734

014 L ' 88.100 - 88.100 015' 84.030- 84.030

]j J0165 82.170' '82.170

017 -84.170; 84.170-Jl l01B-E5.640 1 85.640-

'019- '69.000-.69.000' 020 s 69.660,.69.660' L031^ 68.910 68.910

.i

'032l !&9.260 69.100 033 1 69.460 69.460 02 h. 69.320 - 69.320 j

m 1.WElGHTED AVG. 79.05B F 538.748 R i

.o l

I h

Y, o

'x

[

lWATERVAP0RPAR11ALPRESSURE:

0.400138PS!A l ) i MASS W PT: 94276.9168LBM-

f $$$ SENSOR R4ADINGS AND AVERAGES $$$ lill leprisposed litt 1[$1 PO!WI NURb[R 3 CLitui

CarolleaPoseriLfght i!ME OF RCA0!N6:

o PLANT $1T[ Bruhtelti Daft:02/19/90 Mli 2 11ME: 02:04 1RANSM16510N 6 RfD MWP0lki PR65URE ti d Al RtA0 .All M. $th0 Al READ CAllDR. StWI AS READ CAllM. 001 86.320 86.320 001 1%.970 75.731 00204003.000 64.190 002 85.300 Pl.360 002 157.460 76.061 00215729.000 64.183 003 09.300 8'i.300 003 157.500 76.000 004 98.360 09.360 M4 160.360 71.010 utl8HTED AY6. 64.187 005 88.500 Bl.20 005 151.120 76.504 006 09.7:0 89.710 #6 157. 3 0 76.141 007 88.130 88.130 007 145.740 61.!!! 008 17.610 87.610 000 146.610 61.712 ed' 86.110 90.!!0 009 144.620 67.359 l-010 17.190 87.190 010. 141.970 60.277 011 - 17.m 17.330 012 09.810 M. Ole utl0HTEDAYS. 72.904 013 I?.7M 97.7M 014 - II.120 98.120 i015 84.030 94.030 -016 82.150 B2.150 017 94.150 84.150 018 Bl.630 65.630 019 69.000 69.000 020 69.660 69.660 021 68.910 64.919 022 69.250 69.250 023 69.450 69.00 1 024 69.320 69.320 l NEl6Hi[D AV6. 79.052 F 539.741 R t WATER VAPOR PAR 11AL PRitSURE: 0.400350 PS!t. ' Mall WilGHT:- 94268.8271 LBM

i

y

$$$ SENSOR READINGS AND AVERAGES 888 i litt Superloposed Illt { ~ fili POINT NURKR 4 CLitNT CarolinaPoser& Light 11ME OF READING: PLANT $li[I$runlufth Hits 02/19/90 ) Cli. I2 11ME:02:19 IRANSMIS$10N 7 RfD DENPOINT PRilSURE i SE 3 Al READ = CAllDR. S[h6 AS READ CALIBR. $Ent AS READ CALIBR. M1 B6.300 86.300 001 157.420 76.034 00104796.000 64.185 002 - 85.430 95.430 002 !$7.670 76.202 H205722.M0 64.178 i 003-99.290 99.290~ 003 157.5% 76.121 004. 88.340 98.340 M4 160.290 77.963 NEl6HIEDAV6. 64.181 005 - 88.590 98.$90 005. 150.270 76.605 006 09.940 39.940 M6 !$7.520 76.101 007 80.120 80.120 007 145.600 60.025 Mt 87.660 07.660 000 146.810 68.048 ~ Mt ' 08.100 SP.t40 009 144.460 67.251 . 010 87.190 Bia90 010 145.900 60.229 0!! : 87.330, 17.330, NE10HitDAV6. 72.919 012 - 99.810 19.010 ell 17.740 87.740 014 08.120 N.120 015 94.030 -84.030

016 82.1M 82.150 017 B4.1%

B4.150 016 85.629 85.620 019 69.000: 69.000 020 69.660 69.660 021 68J20 69.920 022 69.250 69.250 023 69.460 69.460 024 69.320 69.320 WEl6 HIED AVB. 79.057 F $30.747 R l W41[R VAPOR FA411AL PRESSURE: 0.4M562 PSIA MAS $WEl6HT: 94259.9934 LBM

i ses-SENSOR READINGS AND AVERAGES *st 'lill Superleansed till 1[$1 POINT llunt(R $ i ClifNT.

Carollha Power 6 light ilHE OF RE HIN6:

PLM1 $11Es trunselet Hi[102/19/90 CIT

2 I!ME:02:34

) Thesn!$510N 0 1 RfD MUF0!NT PR($SURE '{ 8t ] Al READ CAllDR. SEN0 Al RE M CALIBR. BENG AS R[AD CAllbR. C1 - N.280 B6.200 001 156.8 % 75.6 % 001 B4788.000 64.179 002 4.390 B5.380 002 AM.130 76.511 002B5715.000 64.172 003 99.200 89.200 003 157.260 75.926 M4 98.340 88.340 004 160.460 70.078 WI6Hi[DAVC. 64.176 M5 94.600 98.600 005 IX.000 76.477 0% 89.020 89.820 006 157.5% 76.121 j C7 ' N.120 88.120 007 145.690 64.007 + 000 87.610 87.610 000 146.730 68.793 009 80.090 08.090 009 144.710 67.421 010 87.190 87.190 010 146.M0 60.338 t til '87.330 87.330 f 012' 09.000 09.000 N(10NillAYt. 72.928 til ' 07.7M 87.7M r c 014 M.100.08.100 a 015 04.010 84.010 016 82.1 % B2.lM 017 84.1 % B4.1% 019 B5.620 85.620 019-69.000 69.000 020' 69.660 69.660 L 021 69.910 68.910 l' 022 69.2% 69.250 l. 023 69.460 69.460 i 024 69.310 69.310 NE16H1(0 AVG. 79.049F 538.73BR L l p l t l' + 1 i l.. NATER VAPOR PARilAL PR[SSURE: 0.400691iSIA MASS NEl6His '94253.0192 L M /* i

T u $$$ SENSOR READINGS AND AVERAGES.*** 1818 Superloposed !!!l TEli POINT NUMBER 6 CLllit

EarelinaPower& Light ilnE OF READ 14 :

PLC.i $11[a Brun6 mitt DATE:t?'19/90 C11 2 11ME 49 TRAND.;4'!DM 9 AfD ' MWPOINT PRESSURE $[M A$ READ. CAllM. SEM AS READ CMA. IE M AS READ EALIM. N1 E 250 66.250 001 !$7.490 ie.074 001 94781.000 64.174 i . j; '002 85.300 85.380 902 !$).b0 75.993 00285707.M0 64.167- . 003 89.270 89..'70 M3 - 157.200 7'u?40 M4 B8.320 B8,320 004 160.370, 78.017

EISHIED AV6. 04.170 OM 08.430 bl.430 005 158.270 74.6 %

0% 09.860 99.860. 0% ' 187.560 76.141_ G7~ 88.120 98.120 007 145.810 60.16B OM 87.570 87.570 NG 146.710. '69.780 -i ~C9 M.000 B8.000 009 144.640 67.373 + 610 81.150 B7.150 010 145.%0 68.2'/0 I ' > 0!! 07.820 Bl.120 012 09.906 M.000 WE10HTEDAYl. 72.941 til 97.7M 97.7M ~ t ' 014 - 88.100 48.100 'l -015' 84.029 84.020 1-016 B2.140 82.t40

017, 94.140 64.149 O!B 85,520' B5.620 019- '69.000- 49.000 5

020,69.670 69.670 021 68.900- 68.900 022 69.250 69.250 023.69.460 69.460 [ 024 69.320 69.320 WElGHTEDAV6. 79.044 F $30.734 R [ -i 'h WATER VMOR FAR11AL PRESSURE: 0.400664FSIA MASSWEISHT: 94245.2321L6R

] pS 7 m f', j m i %? (48 8 SENSOR READINGS AND AVERAGEE *** l '~ litt Superloposed-4 tit TEli itlRT NUMDIR 7 i 4 t i -CLIENT. : Carolin Power 6 light TIMEOFREHlW6: l 4 l L "PLMilitEtArmalck DATE: 02/19/90 [ Cli - 2 ilME: 03:M 1RANSMIB$10Ni 10 RfD DEWPOINT PRESSURE lE d M RE O Cr IM. SEH AS READ CALIBR. SEM AS READ CAllIR. d01: 66.230 86.230 001 157.330 75.973 001 64774.000 64.169 / A 002' 85.320.B5.320 002 157.310 75.960 002B5700.000 64.161 Y. 003 99.240 '.f.240. 003 117.360 75.993 ' M4 :.M.310 89.310. 004 :160. M 0 78.138 NE16HTED AV6. 64.165 605 ;98.420- -98.420 005 158.210 76.565 i M6 99.830 ? 09.830.006 157.620. 76.168 s, ! M7 99.100 98.'100 : 007 145.720 60.107 h 2 SOR < 87.30 67.5% 008-146.720 69.786 M9 '. 88.060 98.000 009 144.500 67.332 010 57.140 87.140 010 145.960 68.270 ' 0111 87,J10 17.31d -012 : 99.790 19.790 WEIMTED AVS. 72.934 til '57.730 87.730

014 90.096 '18.090 i ell H.010 H.010 i

, 016s 82.140.82.140 017 ' 94.140 94.140-0182 65.620 B5.620 i 019. 59.000- 69.000 s 020' -69.660-69.660 s 021 68.900 68.900 022 69.250 - 69.2% 023 69.450 69.450 , l 024 ~69.320-69.320 Wil6HIEDAVB. 79.037F

53B.727R l

r 3 i WATER VAPOR FAR111t FRESSURE: 0.400760 FSIA MASSWElBHis 94238.9016LBR n ~T

t 8 8 8' SENSOR READIf4GS AND AVERAGES *** list Superloposet till TEST POINT IUIRR 8 ' CLIENT tCarolinaPower&L18ht ilnt 0F READING: - PLANTlifE:Brunsoict-DAt[ 02/19/90 C11 .:2 TIMis03:19 TRANSM!$$10N 11 RfD MNPOINI PRESSURE i. 8tM AS READ CAL 18R. BENI AS READ cal!8R. SEN4 ' AS READ Call 8R. 001 86.200 86.200 901 156.660 75.523 001 84766.000 64.163 002 85.360 85.360 002 157.130 75,839 002 85692.000 64.155 003 - 89.230 89.230 003 157.590 76.148.- - M4' 88.300- 88.300 004 160.470 78.084 WE16 Hit 0AV6. 64.159 C',5 88.290 88.290 005 158.120 76.M4 - 006 89.600 89.680 006 157.510 76.094 C7 80.060 88.060 007 145.5M 67.991 000 87.570 87.570 000 146.720 68.786 - 009' 08.0 % 88.050 M9 144.M0 67.278 010 - 87.090 87.090 010 145.9M 68.263 011 87.310 87.310 - C2 89.790 89.791 til8HI(8AY8. 72.862 til-87.7M - 87.7M 014 l 48.lN. 80.120 015 H.010 84.010 016 - 82.130.- 82.130 017-84.140- 84.140 018.85.620.85.620

019 68.990- 68.990; f

020 69.660' 69.660 021 '68.900i - 68.900 - 022-69.250~ 69.250 - 023. 69.460 69.460 024 69.320. 69.320 . NEl6HTED AV6.~ 79.034 F' 538.724R i \\ WAi[R VAPOR FARilAL l'RISSURt ~ 0.399796 PSIA MASSWEIGHT: 94232.0418LBM t' '

l es*. SENSOR READINGS AND AVERAGES 888 tist Superloposed litt TEST Polut Nul'MR 9 CLl~~i 1CarollhaPoetr6 Light ilME DF READlW6: PLANT 511E Drumsnitt DATE: 02/19/90 Cif : 2 TIME:03:34 TRANSMIS$10N:12 3 RfD DEWPOINT PRESSURE SE D AS READ CALIDR. SEM AS READ CALIBR. SEM AB READ LALIM. l C1 ~06.170 86.170 001 157;400 76.020 001 64758.000 64.157 002-85.320 85.320 002 157.710 76.229 00285685.000 64.1 % ( 003 - 89.210- 89.210 00A iH.0(0 7;.91 004 98.200 88.200 004 160.680 78.226 NEl6HTEDAV6. 64.153 005 68.260 88.260 005 158.160 76.531 -. 006 89.700 89.700 006 157.H0 76.!!4 007 88.050 88.050 007 145.530 67.970 000 87.520 87.520 000 146.800 68.841 009' 88.040 68.040 009 144.600 67.400 010 87.040- 17.040 010 145.970 68.277 011.87.280 07.200 012 M.790 M.790 NE10HTEDAY8. 72.tH 013 87.7N 07.7M ' 014 08.000 II.000 Oll ' M.010 94.010 + 016.. C2.!30 82.130 017 84.130 84.130' 018 85.610 85.610 "019 68.990 68.990 020c 69.660 69.660 021-68.900.68.900 022'-69.250 69.250 023 69.460. 69.460 024 69.320 69.U0 WEIGHTED.AV6.. 79.026 F-538.714 R s [ WATER VAPDR PARilAL PRESSURE: 0.401043 PSIA RAS $ WE16HT: 94223.3476LDR

e ..sse CENSCR CECDINCB AND AVERCCEO ass j iets - suprispwd lat4 .itti Polui lluMMR 10

CLIENT

. CarolltePoser6L18ht 11ME OF RCA61b6: PLANT $liElBrunseitt Daft:02/19/90 C~IT - 2 ilnts03:49 TRAllSMISSION: 13 1 l RID D(WP0luf PRESSURE l 8(D AS RtAD Call 8R. SEN4 AS RtA8 Call'R. SENI AS RtAD Call 8R. l 001 86.150 86.150 001 !$6.520 71.429 00184751.000 64.151 002 85.270 85.270 002 158.150. 76.525 00285678.000 64.145 ' M3 - 09.190 89.190 003 157.500 76,.088 004-80.270 88.270 004 160.160 77.876 WE!6 HIED AV6. 64.140 005 88.240 88.240 005 158.090 76.484 'OM 89.720 89.720 0M 157.560 76.120 007 88.030 88.030 007 145.660 68.M6 000 87.470 87.470 000 146.770 68.820 -009: 88.020 88.020 009 144.570 67.325 010_. 87.040 87.040 010 145.890- 68.222 .0111 87.270 87.270 f12 89.7M 89.780 utl6Hi[DAVB. 72.893 813 87.7M B7.7M ^ 814 '08.188 88.188 . Oil - 84.000 - 84.000 016 82.130 82.130-017-84.130-84.130 018 85.610 85.610 019 69.000 69.000 020' 69.660 69460 021 68.910. 68.910 1 022 69.240 69.240 023 69.460 69.460 i 024 69.320 69.320 l-I WEIGHTED AV6. 79.022F 538.712R l' p .. i t bAl[R VAPDR FAR11AL FRIBSURE: 0.400213 FSIA MASS WEIGHT: - 94217.4027LBM

a. 'sas SENSOR READINGS AND AVERAGES *** till Superiaposed litt TEST POINT NOR8ER 11 CLIENT: CarolinaPoser6 Light-TIMEOFREADING: PL41II $1TE: Brunsmid DATE:02/19/90 " Clf 2 fille 04:04 1RAlllMIS$10N 14 P RfD MWPOINT PRESSURE . NWB AS READ C'.18R. BENB AS READ CALIM. SENB AS READ Call 8R. I 001 86.120 86.120 001 157.280 75.940 001 84744.6M 64.146 002-85.250 85.250 002 157.450 76.054 002 85671.000 64.140 003 89.190 A.190 003 157.520 76.101 004 88.250 88.250 004 160,490 78.098 WEl6HIEDAV6. 64.143 0M 88.240 88.240 005 158.200 76.558 ' M6 89.730 89.730 0M 157.640 76.182 M7 88.030 89.030 007 145.710 68.100 608 87.370' 87.370 000 146.740 68.8 % M9. 88.010 88.010 009 144.490 67.211 010 87.010 87.010 010 145.920 68.243 0!! 87.260 87.2M 012 99.7M 89.7M, WE18NTED AYO. 72 932 7 r ! 813 87.7M : 87.?M ~ ' 014 88.090 88.090 ' Oil 83.990 ' 83.990 016 82.120 82.120 017 84,120 84,120 018 85.6!0 85.610 019 68.990 68.990 020 - 69.660 69.660 021' 66.900 68.900 022 -694250 69.250 023 69.460 69.460 024-69.320 69.320-WEIGHTED AV6. 79.016 F l 538.706 R 1 1 1 l WATERVAPORPAR11ALPRES$ULE: 0.400735 PSIA MASS WEl6HT: ' 94209.9917 L M ] H

n + ~,8C8 SENSOR READINGS AND. AVERAGES *** lill Superieposed till TEST POINI NUNDER 12 CLIENT

CarolinaPoer6 Light TIME OF READIN6:

PLMi Slits Brunssid LATE:02/19/90 1211 '

2 ilHE 04:19 1RMSn!$$10N 15 RfD D(NP0lNT PRESSURE lE"3 AS READ CAlliiR. SENG AS READ CAllDR. SEN4 AS READ CAllBR.

=C?!' B6.100 86.!M 001 !?7.000 75.905 001 B4736.000 64.140 002 85.250 85.250 002 -157.700 76.276 002 85663.000 64.134 003. 65.170 89.170 003 157.750- F 2% 004 BB.240 B8.240 004 160.420 7B.051 NE16HTEDAV6. e4.137 005 l 88.240 B8.240 005 158.160 76.531 .006 09.730 09.730 0% 157.580 76.141 -007 96.020 B8.020 007 145.690 68.087 008.. 87.360 87.360 MB 146.770 68.920 009 99.M0 80.000 M9 144.520 67.291

010 86.970 86.170 010 145.930 68.250

- 0!! B7.2M 17.2M 012 -99.700.89.700 NE!OHTEDAV6. 72.929 013 17.7M B7.7M '+ 014 98.lM 98.1M

015- ' N.M0 94.M0

,016 82.120 82.120 017 84.120. 84,120 ' 018. 65.600 B5.600. 019 69.000 69.000 020 '69.660 69.660 021 68.900 68.900 022,(9.250 69.250 69.4% 023 69.450 .69.320 024-69.320 WE16HTEDAVB. 79.014F '538.704R l s WATER VAPOR FARilAL PRES $URE: 0.400698 PSIA ~ 'MASSNEl6HT: 94201.6428 LM 1

p ENSOR READINGS AND AVENAGES *** litt Superloposed litt Illi Polui NunMR 13 CarolinaPower& Light ilME OF READING: Bruns 2lti' DAlt 02/19I90 2 11ME:04t34 TRAN$nlSSION: 16 ft ' MNPOINI PRESSURE -n........i hl CAL 1 H. $EN0 Al READ Call H. SEN4 AS M AD. cal!6R. 50 86.050 001 157.690 76.215 001 04729.000 64.135 to 05.190 002 157.550 76.121 M2 65657.M0 64.129 60 : 99.160 003 157.910 76.363 20 : 98.220 M4 160.340 77.997 NEl6Hi[D AV6. 64.132 30 l98.230 M5 158.210 76.565 40 99.940 M6 !$7.540 76.114 00 98.000 007 145.720 68.107 30 87.430 008 14.790 68.834 1 00-bl.0M 009 144.530 67.298 i 30 84.930 010 145.9M 68.229 le 87.2M. M M.7M UE10NTES M8. 72.945 10 ' 07.730 B0 (D.000 00 04.0M 10 i 82.110 10 84.110 1 00 ~ 65.600 W 69.000 40 - 69.660 1 00 - 68.900 50 69.250 60 69.460-20 - 69.320 .V6. ' 79.000 F 538.698R 4 ' bATER VAPOR PARilAL PMSSURt 0.40PitPS14 MAsi x m wii 441P $n

4 I i 1t. sts SENSOR READINGS AND AVERAGES *** till Superisposed till j TEST POINI NUMK R 14 CLIENT

Carolina Power 6 Light 114 0F RE41W8:

e PLANT 51TE:Brunsulth DATE:02/19/90 ^ CIT-2 TIME: 04:49 TRANSM16610N 17 e AfD MNPOINT ' PRESSURE q , M D AS READ ~ CALIBR. SENG AS READ Ch iBR. SEN4 AS READ CAllBR. n 001 86.030 86.030 001 156.650 75.516 00184721.000 64.129 1 002 65.120. 83.120 002 157.530 16 JOB 00285648.000 64.123 L 003 89.150 89.150 003 !$8.180 76.5 % .004 88.210 88.210 004 160.430- 78.057 NE18HTEDAV6. 64.126 005 ' 08.200 88.200 005 158.360 76.666 ( b 004 89.f60. 89.860 0% 157. 3 0 76.128 007.88.000< 88.000 007 145.770 68.141 000 87.410 :87.410 008 146.690 68.766 '009 87.980 87.900 009 144.600 67.400 ~ 010 ' N.910 N.910 010 145.960 68.270 - 011', 07.240 87.240 012' 89.764 89.760 EIONTEIAVI. 72.948 . 013 87.720 87.720 014 II.080 - 88.080 , el5 83.990- 83.990 016 82.09C-- 82.090 E 017 84.110 - 84.110 - 018 85.590 85.590 019 68.990 48.990 020 69.660 69.660 021 68.900 68.900 022 69.250 - 69.750 ^ 023' 69.450 61.450 024 39.320 69.320 NElBHIED AYS. 79.000 F 538.690R l 1' 1 L ( 1 l: 1 1 NATER VAPOR PARilAL PRESSURE:= - 0.400951 PSIA RA!! Xi'NT: 94187.1351LBM t

_ ~ t ss* BENSOR READINGS AND AVERAGES *** lill Superisposed till TESTPOINTlluMER 15 4 CtlENT ' Carolina Power & Light

i!ME OF READIN8:

PL4lli SliEl Brunleith ' DATE: 02/19/90 Clif a2 11ME: 05:04 1RANSMIS$1DE: 10 RfD DENP0lWT -PRESSURE K M AS READ Cr48R. SEH AS READ C4lllR. SENG AS READ C4lllR. I M1 86.020 d6.020. 'll 156.900 75.617 001 84714.000 64.123 [ 002 85.160 85.160 002 157.600. 76.289 002 85641.000-64.118 C3 89.140 ft.140 003~ !$7.710 76.229 . M4 88.200 88.100 004 160.350 78.M4 WE!$NTEDAYB. 64.121 O 88.170 88.170 005 158.160- - 76.53! 0%- 89.820 89.820 004 157.510 76.094 O 87.990 87.990 M7 145.000 68.161 000 ' 87.3M 87.350 008 146.710 68.780 009 87.900 87.99C '009 144.410 67.217 010 86.920 86.920 010 145.090- 68.222 011 87.240 87.240 0 012 09.770 =99.770 WE18HTED AV8. 72.B98 til " B7.7M B7.7# '014 ' 08.000 It.000. .Oll: 13.990- 83.990 016 ~ 82.090 82.090. 017 64 !!0 1 84,110 ' 018 - 85.590 85.590 '019 68.990 68.990 020 69.660 69.660 .-021 - 68.900' 68.9M 022. 69.240 69.240 023 69.450 69.450-024 69.310 69.310 WE16HTEDAVG.- 78.997F 538.6B7 R 1 i r . ATER VAPOR FARilAL FRES$URE: 0.4 M279 FSIA-W o.. n 7-MASSWE18His 94180.9311 LBM is 5 'N 4

4-1 .388 SENSOR READINGS AND AVERAGES sss illi Superleposed till TEST POINT NUMBER 16 - CLIENT

Carolina Power 6 Light 11ME OF REAllN6:

- PLANT Slit Brunsuit! DATE:02/19/90 Clf a2 TIE:05:19 IAANSMIS$10N: 19 RfD DENPOINT-PRESSURE 4 BE J A6 READ CAlllR. SENI kl READ CAllbR. SENG AS READ CElpR. e M1 85.990 15.990 001 156.830- 75.637 001 B4707.000 64.!!9 M2 '85.1M '85.100 002 157.810 76.296 002 85633.000 64.112 ~ 003 89.120. 89.120 003 157.720 76.235 004 '80.170 88.170 M4 160.600 78.3% NE16HIEDAVS. 64.115 005-88.210 98.210 005 !$8.160 76.531 ON 99.710 89.710 006- !$7.580 76.141 M7 -87.990 87.990- 007 145.830 68.182 , 000 17.260 B7.260 M8 146.690 68.766 ~ #9 ' 07.900 87.900 009 144.450 67.244 1 010 86.930 86.930 010 145.920 68.243 i - 0!! 87.220 87.220 012.

M.7M 89.7M NEl6HIEDAV6.. 72.934 2 013~ 87.7M - 87.7M 014 II.070~ II.070 til 83.990 83.990 016 82.090 82.090 017 84.100 04.100 -

j -018-B5.590 95.590 019 69.0M 69.000 020: 69.650 69.650 . 021 68.900- 68.900

4 022.69.250 69.250

~N 023 '69.460-69.460 -024 69.320 69.320 NElBHIED AV6. 78.992f' l 538.682R l H l -i i i .WAIER VAPOR PAR 11AL FRESSURE: 0.400763 PSIA MASSNEl6HT: 94172.9087LBM

~ 1 L *Jsts. SENSOR' READINGS AND AVERAGES *** ~ ' Ifit Superieposed till TESTPOINTNUMBER 17 CLIENT Carclina f'ower 6 Light TIME OF REA41N6:- PLANT $ lits Drumseld DATE:02/19/90 .Clf - 2 TIME:05:34 IRANSMISSION: 20 r RfD MNPOINT PRESSURE 7 FO AS RFAO CALIM. SENG A$ REAS CAllDR. BEul AS READ CAlltR. '001-B',.950 85.950 001 1M.910 75.691 00184700.000 64.!!3 '002 % 180 85.180 002 !$7.850 76.323 002 BM25.000 64.106 s 003 99.100 99.100 003. 157.130 75.839 i ' 004't 88.160 88.160 004 160.300 77.970 NE10HTED AV6. 64.109 0 005 88.200 98.200 005 158.210 76.H5 '006-89.700 89.700 006 157.M0 76.121 007 87.950 87.950 007 145.400 67.944 l 008 87.330 B7.330 008 146.690 68.766 l %9- 07.960 87.960 00f 144.640 67.373 010 B6.910 86.910 010 145.990 68.222 i 011' 87.210 87.210 1. 0!!.09.760 09.760.NEiSHTEDAYS. 72.890

g L013-87.700 87.700

. 014 ' 08.090 48.090 015-53.990 83.990 016 B2.090 82.090+ 017 84.100 84.100 018 85.590 '85.5?0 019-68.990 68.990 020 69.660 69.660 .021 68.900 68.900 022 69.240 ~69.240 '023 69.450 69.450. ' 024' 69.320 69.320 .j . El'6Hi!D'AVS. 78.991 F W $30.681 R -i P g. i WATER VAPOR FARilAL PRESSURE: 0.400170 PSIA MASSNE16HT:J 94165.4952LBM

-..,7-.- 5 1 ? h e h 6 e b i ? APPENDIX F

SUMMARY

OF TYPE B & C LEAKAGE P a r i 1 a t t 'l k l l-f l l I:

A eeeeeeeeeeeeeeeeeeeeeeeee. *** e. Unit Two e Containment Running Total Log * ..****,......e****o* April 19, 1990 Leakage Equipment Test TCdt Date P1/PM No. Valve / Hatch Name Value Error Resultr. cocoooose eeeeeeeee..........................

- - - ees
      - eseo 43.316+4.440 0.000 O

9/09/08 CONT. LEAK. = Q/09/09 20.*e44 SOUTH TORUS HATCH 0.000 0.217 SAT E 9/13/09-20.?-69C CAC-V172 1.959 0.217 SAT -9/13/09 20.3-65 CAC-V170, V160 V162 2.394 0.217 SAT O/14/09 20.3-66 CAC-V171,V16),V163 0.604 0.218 SAT 9/10/09 20.3-114 E11-F0210 0.000 0.218 SAT 0.000 0.219 SAT 9/19/09 20.3-114A E11-FOl6H .9/10/09 20.3-163 G16-F019,FOBO O.000 0.219 SAT 9/21/89 20.3-1 PENETRATION X-100A O.000 0.219 SAT 9/21/04 20.3-2 PENETRATION X-100D O.000 0.219 SAT 9/21/09 20.3-3 PENETRATION X-100C O.000 0.219 SAT 9/21/09 20.3-4 PENETRATION y-103A O.016 0.220 SAT 9/27/G9 20.3-6 PENETRATION X-104A 0.000 0.220 SAT 9/&B/89 PO.3-5 PENETRATION x-1000 0.000 0.220 SAT 9/26/09 20.3-7 PENETRATION >-102A O.000 0.220 Sal 9/29/09 20.3-8 PE NE T R AT I ON Y-104P O.006 0 P14 SAT 9/E4/69 20.3-9 PENE TRAT I ON 3-1021-0.00A O.219 E, A T 9/29/00 20.3-79 CAC-SV-1260 0.000 0.214 5AT J 10/02/89 20.3-10 PENETRATION X-101A O.000 0.219 SAT 10/02/09 20.3-11 PENETRATION Y-101C O.000 0.219 SAT 10/03/09 20.3-12 PENET R AT ION y-105D O.000 0.219 SAT l I 10/03/09 20.3-13 PENE1RA1100 > - 105l (*. 00 3 0.219-Sol 10/O*.3/09 20.3-40 PERSONNEL LOCt: TO DRvWELL O.004 v.219 EA1 i U Page 1 L

w Apri1 18, 1990 Leakage Equipment Test TCat;Date PT/PM No. Valve / Hatch Name Value Error Results cocoocese eeeeeeeee e.........................

- - ...eee**ees eeeeee.

10/03/09-20.3-40 PERSONNEL LOCK TO DRYWELL O.064 0.219 SAT 1'C/C4/99' 20.3-14 PENETRATION X-102C O.000 0.219 SAT 10/04/89 20.3-16 PENETRATION X~105H 0.000 0.219 SAT l 1C/04/09 20.3-17 PENETRATION X-105G 0.000 0.219 SAT i

1C/O*7/P9 20.3-74 CAC-SV-1261 0.000 0.219 SAT t

-l 10/07/09 20.3-73 CAC-SV-12000 0.000 0.220 SAT 1 i 10/07/RG -20.3-77D 'CAC-SV-1227C O.000 0.220 SAT a 10/13/89 20.3-71 CAC-X200'V17 0.500 0.220 SAT i '10/14/89 20.3-41 DRYWELL HEAD BLANK O.000 0.219 SAT l 10/14/09 20.3-42 DRYWELL HEAD ACCESS HATCH 0.000 0.219 SA1 t 10/14/99 20.3-47 CAC-V49 INBOARD ORING O.000 0.219' SAT 10/14/99 20.3-72A CAC-V49 0.000 0.219 SAT

10/14/89 20.3-72B CAC-V50 0.000 0.219 SAT 10/15/09 20.3-83 CAC-SV-1211F 0.000 0.221 SAT 10/15/69' 20.3-04 CAC-SV-1262 0.000 0.221 SAT 10/1C/09 20.3-89 CAC-SV-1211C O.000 0.221 S A1 -

10/15/09 20.3-90 CAC-SV-3439 0.000 0.221 SAT 1 '10/16/69 EO.3-20 PENETRATION X-100F O.000 0.220 SAT '10/16/09 20.3-21 PENETRATION Y-100E O.000 0.220 SAT 310/1d/09 2o.3 E3 Pl.NC1 A AT !ON )- Imi

0. ( e

.F2n E.' 10/16/09 20.3-25 PENCTRATION X-104F O.000 0.220 SA1 10/17'/09 20.3-22 PENETRATION A-100G O.000 0.221 SAT =10/17/B9 20.9-24 PENETRATION Y-10FF O.000 0.221 SAT t 10/10/09 20.3-117 E 1 1 -F 022 '. F 023 0.000 0.220 SAT. t l 10/10/09 20.3-63 C41-F006 1.004 0.220 SAT l Page 2 h I r 1t 1

Apri1 18, 1990 Leckage Equipment Test Tcat Date PT/PM No. Valve / Hatch Name Value Error Results coco ***** ********* **************************

- - - - ********* ******i 10/21/89 20.3-64 C41-F007 0.000 0.221 SAT 1C/23/89 20.3-29 PENETRATION X-1053 0.000 0.221 SAT.

10/23/89 20.3-30 PENETRATION X-105K 0.000 0.221 SAT. 10/24/09 20.3-172 RXS-SV-4186 0.000 0.221 SAT 10/25/89 20.3-173 RXS-SV-4107 0.000

0. P'. !

SAT 10/26/89 20.3-49 CAC-V5 INBOARD O-RINGS 0.409 0.222 SAT 10/26/09 20.3-52 CAC-V16 INBGARD O-RINGS 0.000 0.'122 SAT . 10/26/09 20.3-53 CAC-V17 INBOARD O-RINGS 0.000 0.221 SAT 10/27/09 20.3-50 CAC-V7 INBOARD O-RINGS 0.000 0.220 SAT 10/29/89 20.3-49 CAC-V6 INBOARD O-RINGS 0.000 0.221 SAT 10/C8/89 20.3-51 CAC-V9 INBOARD O-RIi43S 0.000 0.221 SAT '10/31/89 20.3-81 CAC-SV-3440 0.000 0.221 SAT ~ 10/31/89 20.3-82 CAC-SV-12258 0.000 0.221 SAT 11/02/89 20.3-113 E11-F021A 1.000 0.221 SAT 11/03/09 20.3-113A E11-F016A 0.000 0.221 SAT 11/07/89 20.3-26 9ENETRATION X-1030 0.000 0.221 541 !!/07/09 -20.3-27 PCNETRATION X-104G 0.000 0.221 fiat 11/07/09 20.3-26 FENETRATICW K-10PH 0.510 0.P21 SAT 11/00/09 20.3-1*?9 TIP A DALL VALVE 0.000 0.222 SA1 1 14.P / Di; TM.? 100

] r !! F AL t.

vat vt o.6v i f?P %1 !!/08/09 20.3-101 'IP C DALL VALVE O 000 0,22P SAT 11/09/09-20.3-102-TIP D BALt. VALVE O.000 0.222 SAT 11/08/90 20.3-103 TIP d2 CHECM VALVE O.000 0.22D SAT 11/09/M 20.3-112B E11-FO17D 1.311 0.2P SAT I 11/10/89 20.3-60 E 32-r 019, r 020 0.820 0.222 SAT l' Page 3

q Apri1 10, 1970 Leakage Equipment Test , ?TC3t Date PT/.'M No. Valve / Hatch Name Value Error Results ocooce*** ********* ************************** L 11/11/89 20.3-61 B32-VB4 2.347 0.222 SAT . 11/16/09 20.3-18 PENETRATION X-102E 0.000 0.220 SAT 11/16/09 '20.E-19 PENETRATION X-104E 0.000 0.220 SAT

1'1/17/09 20.3-143B E21-F0040 0.023 0.223 SAT

<11/10/09 20.3-142B E21-F005P 0.000 0.222 SAT 11/20/09 20.3-119 E11-F0210,F027B,F0288 0.000 0.221 SAT 11/26/89 20.3-31 PENETRAT'.ON X-101F 0.v00 0.221 SAT. '11/29/89-20.3-160 RNA-SV-5262 0.000 0.221 SAT. 11/30/89-20.3-165 RNA-SV-5261 0.000 0.220 SAT 12/01/89 20.3-111B E11-F015B 0.815 0.P21 SAT. 12/Q1/09 '20.3-170 RNA-SV-5251 0.097 0.220 SAT- '12/01/89 20.3-171 RNA-SV-5253-0.199 0.220 SAT 10/03/99 20.3-33 PENETRATION X-105C 0.000 0.220 SAT .12/03/09 20.3-34 PENETRAT1bN X-1050 0.000 0.220 SAT 10/11/09 '20.3-35 PENETRATION X-2328 0.000 0.222 SAT 1r/11'/09.- 20.3 PENETRATION K-232A 0.000 0.222 SAT 12/13/09 20.3-36 PENETRATION'X-232C 0.000 0.220 GAT 12/13/09 20.3-30 PENElRAllON X-232D 0.000- 0.220 SAT '12/14/09 20.3-32 PENETRATION X-1010 0.000 0.221 SA1 12/14/06 20.D-67P CAC-VEb.V;6

0. 00= >

v.2F1 E /.1 l '1P/15/09 20.3-100 E 11 -F 000, F009 6.350 1.616 SAT. L '12/19/09 20.3-161 E51-F062,F066 0.000 0.221 GA1 12/27/09, 20.3-174 PkS-SV-41EB 0.000 0.223 SAT. I 12/20/09 20.3-175 RxS-SV-4109 0.000 0.223 SAT l-l 1/13/90 '20.3-55 B21-F0100 0.000 0.221 SAT l L i Page 4 a o L" i

] h -s t.: April 19, 1990 Leakage Equipment Test 'TCOt Date PT/PM No.- Valve / Hatch Name Value Error Results corco**** ********* **************************

- - - e** * * * + * * * * * *******

1/15/90 PM-87-170 RNA-V351 0.000 0.223 SAT 1/15/90 PM-89-018 G31-F004 0.000 0.264 SAT l'/15/90 PM-89-019 G31-F001 0.000 0.264 SAT 1/17/90. PM-F7-015 B21-FOl6 0.000 0.223 SAT 1/17/90. PF-89-015 B21-F019 0.620 0.223 SAT 1/20/90 20.?-166 RCC-V28, V52 4.059 0.283 SAT 1/23/90- 20.3-111A E11-F015A 2.540 0.222 SAT 1/26/90- 20.3-112A E11-F017A 2.721 0.222 SAT 1/23/90 20.3-167B 2-RCC-SV-1222B O.000 0.222 SAT

1/26/90, 20.3-167C 2-RCC-SV-1222C 0.000 0.222 SAT

~ t '1/27/90 20.3-56 821-F032A,E41-F006 3.566 0.222 SAT 1/29/90- 30.3-62 B32-V32 0.513 0.222' SAT 1/29/90 20.3-142A E21-FOO5A 0.000 0.222 SAT 1/30/90 20.3-143A E21-F004A O.915 0.221 SAT 1/29/90 20.3-110 E11-F024A,F0P7A,FOBOA 8.900

1. 6 P84 SAT 2/01/90- PM-87-170 RNA-V3bO' O.511 0.221 SAT P/02/90 EO.3-54 B21-F010A O.000 O.P2);

FAT I 2/07/90 20.3-598 D32-V30 0.000 0.270 S AT. 2 ' Mi < c n PM09-01" F S t - r o l 3,,. ;-rn P 0, c,0 r, age EA1 4 2/08/90 20.3-600 CAC-VPP O.000 0.222 SAT 2/13/90 BA.3-46 DRYWELL TO DRYWELL HEAD SE. 0.000 0.222 SA1 2/14/90: 20.3-15 PENETRATION y-104C O.200 0.221 BAT 2/1b/90 20.3-39 EQUIPMENT HATCH 0.000 0.221 SA1 ~'2/15/90 PO.3-162 016-FOO3.FOO4 0.000 O.PPP SAT I/lb/90 20.3-153 E41-FO75,F079 0.090 Q,Epp SA1 Pagt-5

m. April'18, 1990' i Leakage. Equipment Test i TCat Date PT/PM No. Valve / Hatch Name Value Error Results occoneeee ********* ee**,*******eseeeeee'ee.... 2/15/90 20.3-153 E41-F075,F079 0.098 0.222 SAT 2/20/90 20.3-6BA CAC-V7,V8 5.485 1.622 SAT i 2/20/90 20.3-69A CAC-V9,V10,V23 4.209 0.223 SAT s 2/20/90 20.3-67A CAC-V4,V5,V6,V15 11.409 1.622 SAT-2/21/90 PM89-017 E51-F000 0.616 0.222 SAT 2/22/90 20.3-59A B32-V22 0.000 0.249' SA1 P 2/24/90 20.3-70 CAC-V16,X20A 4. S 9 'e 1.6HS SAT 2/25/90 PMB9-017 E51-F007 0.822 0.222 SAT 2/28/90 20.3-43 CRD HATCH 0.000 0.222 SAT s ?% '90 20.3-45 NORTH TORUS HATCH 0.000 0.221 SAT 3, u YO 20.3B-PERSONNEL AIRLOCK BARREL 4.590 1.624 SAT. 4/d8/90 20.3-148 E41-F002,F003 4.552 1.610 SAT Acceptance Criteria <=159'.78 (SCFH) + eococeeeeeee**ee********e**********eeeeeeeeee**********ee******ee***eeee. o Containment Total Leakage (SCFH)= 78.6295 c-Containment Total Equipment Error = 5.26450 e .ococe..e***eeeeee****en.....eeeee......eeese*****...e**eeeeee*****...e Reviewed By: ty _. ),N.,... Dates _d_N.,//d/_f_O k r h ) ll F L c l L t Page 6 --}}

ML20042G590

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ML20042G590

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SUMMARY

9.0 REFERENCES

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2.0 INTRODUCTION

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