Text

Edwin I Hatch Nuclear Plant Unit 1 1988 Reactor Containment Bldg Integrated Leakage Rate Test, Final Rept
	ML20235T193
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Issue date:	11/30/1988
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7 GEORGIA POWER' COMPANY EDWIN I. HATCH NUCLEAR PLANT UNIT 1 1988 REACTOR CONTAINMENT BUILDING INTEGRATED LEAKAGE RATE TEST FINAL REPORT l

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Prepared By:

BCP Technical Services, Inc.

November, 1988

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9 BCP Technical Services, Inc.

Hatch 1988 ILRT final Report TABLE OF CONTENTS SECTION PAGE 1.

Introduction Page 1 2.

Summary Page 2 3.

Methodology Pages 3 - 5 3.1 Leakage Rate Calculation Pages 3 and 4 3.2 Test Measures Pages 4 and 5 4.

Procedures Pages 6 - 8 4.1 Plant Status Page 6 4.2 Pressurization Page 6 4.3 Stabilization, Test and Verification Pages 7 and 8 5.

Results Pages 9 - 11 5.1 8 Hour Test Page,s 9 and 10 5.2 Verification Test Page 10 5.3 Mass Point Results Page 11 6.

References Page 12 Tables Figures Appendix I - Computer Program Description Appendix II - Type B and C Local Leakage Rate Test Results Appendix III - Test Data

BCP Technical Services, Inc.

Hatch 1988 ILRT Final Report Page 1 1.

INTRODUCTION The containment integrated leakage rate test (ILRT) is performed as

.rsquiredby10CFR50/AppendixJ(Reference 1)todemonstratethatleakage through the containment boundary at design basis accident pressure does not exceed the Technical Specification limit. Test methods and procedures are specified in ANSI N45.4-1972 (Reference 2), which is referenced in Appendix J, and BN-TOP-1 (Reference 3), which contains specific test requirements acceptable to the USNRC. The conduct of the ILRT follows a plant surveillance procedure (Reference 4)whichcontainsdetailedinstructionsforalltest phases.

The Hatch Unit 1-1988 ILRT is described in detail in the following' sections of this report.

Section 2, Summary, summarizes test results.

describes measurements and calculations.

Section 4, Ssetion 3, Methodology,lant status, containment pressurization and test Procedures, describes p phases.

Section 5, Results presents the results of the measurements and calculationsfortheeight(8)hourtest,verificationtest,insadescription and the mass point results.

Section 6 lists references, and the Appendix conta of the ILRT computer program, a listing of Type B and C test results, and a listing of all data recorded during the test.

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Hatch 1988 ILRT Final Report Page 2 2.

SUMMARY

The ILRT was conducted on November 29 and 30, 1988. Pressurization was started at 3:45 a.m. on November 29 following the completion of all prerequisite activities and the containment was isolated at about 8:00 a.m.

when internal pressure had reached 59.4 PSIG. The 8 hour9.259259e-5 days 0.00222 hours 1.322751e-5 weeks 3.044e-6 months ILRT commenced at 12:45 p.m. following a stabilization period of just over 4.5 hours5.787037e-5 days 0.00139 hours 8.267196e-6 weeks 1.9025e-6 months during A verification flow of 1.2 which temp (erature stabilization criteria were met.verificat wt.%/ day 11.45 SCFM) was imposed just after 9:00 p.m.

The four 4) hour period. The containment was depressurized following the completion of the verification test. Test results are listed below.

95% UCL on total time leakage rate 0.57 wt.%/ day Acceptance limit (75% La) 0.90 wt.%/ day Extrapolated total time calculated leakage rate

<0.50 wt.%/ day Acceptance limit (75% La) 0.90 wt.%/ day Mean of measured leakage rates 0.50 wt.%/ day Acceptance limit (La) 1.20 wt.%/ day Total time calculated leakage rate, verification 1.63 wt.%/ day Upper limit 1.99 wt.%/ day Lower Limit 1.39 wt.%/ day The final as left leakage rate (UCL) is 0.57 wt.%/ day since penalties for penetrations in non-standard alignment add to zero.

The calculated as found leaka This is the sum of the as left rate (UCL)ge rate (UCL) is (0.77) wt.%/ day.plus (0.20) wt.l pathway leakage made during the Type B and C local testing program, i

BCP.. Technical Services, Inc.

Hatch 1988 ILRT Final Report Page 3 3.

METHODOLOGY 3.1 Leakaae Rate Calculation Integrated Leakage Rate is determined by calculating the average' rate of loss of dry air from the containment. The quantity of dry air in the containment is calculated using the ideal gas law and measurements of drybulb tem)erature, dewpoint temperature and absolute pressure. A single average dry))ulb temperature, T, is calculated as the sum of the products of fourteen-(14 measured temperatures and their associated weighting factors (discussed below).

Individual dew)oint temperatures are converted to vapor-pressures using the ASME Steam Ta)1e algorithm relating saturation pressures and.

temperatures. A single average vapor 3ressure is calculated as the sum of the

> products of individual pressures and t1eir assriated weighting factors. Dry

. air partial

>ressure, P, is measured total pressure less average vapor pressure. T1e quantity of air in the containment is computed using the~ ideal gas law, M = PV/RT where M is the quantity of air in pounds mass', V, is containment free air volume in cubic feet, R is the gas constant

for air and P and T are defined above. Containment free air volume used for ILRT calculations is 274,000 cubic feet.

The quantity of dry air is calculated so that evaporation of water and condensation of vapor, which are purely internal processas,.do not affect the computed leakage rate.

Assuming that leakage rate is constant, it is best defined as the slope of a line fitted to the air mass and time data sets. The slope of this line is the average rate of loss of air. Reference 3 takes a somewhat different approach to calculating leakage rate. The total time method described in Reference 3 is based on the premise that leakage rate varies linearly with time. A measured leakage is determined for air mass values evaluated from data collected at regular (15 minute) intervals. Measured rate is initial air mass less current air mass divided by current time less initial time. A straight line is fitted to the measured rate versus time data ue.ing the method of least squares. The calculated leakage rate is defined as the ordinate of

]

this line at the end of the test.

The measured leakage rates will exhibit some scatter about the fitted line with the result that there is a statistically determinable uncertainty as to the true rate. The uncertainty is quantified by calculating a 95% confidence band for the end of test measured leakage rate.

The upper limit of this confidence band is a very conservative bound on true leakage rate.

Reference 3 specifies three acceptance criteria. First, the upper limit of the 95% confidence band on the end of test measured leakage rate must be less than the acceptance leakage rate (per Reference 1, this acceptance rate is 75% of the maximum allowable leakage rate defined in the' Technical Specifications or,.75 x 1.2%/ Day = 0.9%/ Day).

l R = 53.35 (pounds force x feet)/(pounds mass x degrees Rankine) 1

BCP Technical Services, Inc.

Hatch 1988 ILRT Final Report Page 4 3.

METH0DOLOGY(cont) 3.1 j.eakaaeRateCalculation(cont)

Second, the calculated leakage rate extrapolated to a twenty-four hour test duration must be less than the acceptance leakage rate.

Finally, the mean of the measured leakage rates over the final five (5) hours of the test must be less than the maximum allowable leakage rate. The test may be terminated when all three criteria are met if the duration is at least six (6) hours (eight hours per Reference 4).

Following the conclusion of the test, the' calculational method is verified by imposing an additional leak (through a calibrated flow meter) on the containment and calculating the new leakage rate. The imposed leak, vented from the containment through a flow meter, is equal to the maximum allowable leakage rate. The new calculated leakage rate must equal the previously calculated rate plus the imposed rate plus or minus 25% of the maximum allowable leakage rate. This supplemental test also provides a rough check on pressure measurement since a large error in the measurement of pressure change will result in a a calculated leakage rate which differs significantly from the expected rate.

3.2 Test Measurements Leakage rate calculations are based on data taken from drybulb and dewpoint temperature sensors located inside the containment and absolute pressure transducers connected through temporary tubing to a containment instrument penetration. Ten drybulb and five dewpoint temperature sensors were located at approximately equally spaced elevations in the lower drywell the upper drywell to maintain reasonable weighting factors (g was increased in and increased vertical spacing in the upper drywell.

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cross-sectional area of the upper drywell is quite small compared to that of the lower drywell). One dewpoint and four drybulb temperature sensors were located in the torus.

Sensor locations and weighting factors (volume fractions) are listed in Table 1.

Dewpoint temperature sensor Number 6 (in the torus) failed during the test and was assigned a zero weighting factor.

This, in effect, assigned 100% weighting to the remaining dewpoint sensors since the mean vapor pressure is calculated as the sum of the products of individual pressures and weighting factors divided by the sum of the weighting factors.

Sensor locations and weighting factors were established by considering temperature distributions in past tests and the containment l

geometry.

Drybulb temperatures were measured using 100 Ohm platinum resistance temperature detectors (RTD's). Dewpoint temperatures were measured by chilled mirror dew cells.

These devices use a thermoelectric junction to cool a small mirror. The amount of light reflected by the mirror from a light source to a I

photodetector changes when the mirror cools to the dew)oint and collects condensation.

A small RTD senses mirror temperature w1ich is controlled at the dewpoint by the photodetector circuit. Absolute pressure was measured by a vibrating cylinder pressure transducer.

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Hatch 1988 ILRT Final Report Page 5 3.

METHODOLOGY (cont) 3.2 TestMeasurements(cont)

This device uses an electronic circuit to determine a modal frequency of a cylinder subjected to absolute (one side containment pressure /one side vacuum) containment pressure. The modal frequency varies approximately linearly with pressure. An internal microprocessor is programmed during calibration to convert frequency to true absolute pressure in engineering units.

The.

. pressure transducers have a resolution of 0.0001 PSI and a stability of better than 0.003 PSI (based on deviations between two transducers over the eight hour test duration).

A digital data acquisition system was used to collect data at fifteen (15) minute intervals and transfer that data to the ILRT computer over a serial (bit by bit transmission) link. The data system included the conditioning for the RTD's and converted resistance to temperature with a 0.01 degree F resolution.

The dew cell control unit provided an output of 1 mV per degree F to the data system. This voltage input was converted to temperature with a 0.01 degree F resolution. The pressure transducers provided a binary coded decimal output to the data system.

This was passed on to the computer in the same form (no conversion to engineering units in the data system due to a dynamic range limitation of 80,000 counts versus a pressure transducer output of over 740,000 counts at maximum pressure). The data system generated a printed tape record of each data set transmitted to the computer.

The ILRT computer was a small IBM compatible running a compiled Basic l

program.

The program is described in the Appendix.

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Other instrumentation included a 15 SCFM float type flow meter to measure imposed leakage during the supplemental test and two gages to measure containment gage pressure. All temporary instrumentation was calibrated to the I

l requirements of Reference 4 prior to the ILRT.

Permanent plant instrumentation was used to measure suppression pool and reactor vessel water levels / temperatures and the quantity of water pumped from the containment sumps.

Water quantities were tracked since a correction to calculated leakage rate may be required if total water inventory increases during the ILRT (a water injection is equivalent to a negative leakage which lowers the calculated leakage rate).

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Hatch 1988 ILRT Final Report i

Page 6 4

4.

PROCEDURES 4.1 Plant Status l

Plant systems were aligned for the ILRT as specified in Reference 4 which incorporates both FSAR and operational requirements.

Isolation valves were r

set in the post-LOCA positions specified in the FSAR except where the opposite positions were required to maintain the r'eactor in a safe shutdown condition or to allow pressurization for the ILRT. Piping was vented and drained to cxpose valve seats to containment and outside atmospheres per post-LOCA scenarios. All sources of gas at pressures above containment test pressure were isolated or vented to prevent leakage into the containment free air space during the ILRT. All Type B and C local leakage rate tests, including those on the airlock, were completed prior to the start of ILRT pressurization.

Containment sumps were pumped down just prior to the start of pressurization.

One loop of RHR was in continuous operation through the entire test period to remove core decay heat.

Drywell to torus communication was )rovided by blocking open two vacuum relief valves. The reactor was vented ay removing one main steam relief valve.

Prior to containment closure a temperature survey was performed, with fans off, to confirm the expected trend of drybulb and dewpoint temperatures. An in situ test on the in containment instruments was performed to de.nonstrate proper functioning with the long field cables connecting instruments to the data system. RTD in situ tests were done using an ice bath and verifying ice point temperature (plus or minus a tolerance) at the data system.

Dewpoint temperature sensor in situ tests were performed using a sling psychrometer.

The official test copy of Reference 4 documents plant status, including all exceptions to specified conditions.

It also documents the completion of all prerequisite activities.

4.2 Pressurization Temporary pressurization piping was connected to a flanged tee (normally blanked) on the purge and inerting system. The containment was pressurized by 4-1200 SCFM oil free compressors discharging to aftercoolers and r.e the chances of reaching t

refrigerated air dryers. Air was dried to mir-saturated conditions in the drywell. The coraoinment was pressurized to 59.4 PSIG in about four hours starting at 3:45 a.m. on November 29, 1988. The final increment of pressure was added using only one comaressor to insure close control, Pressurization was stopped about midway 3etween the maximum allowable value of 60 PSIG and the minimum start of test value of 59 PSIG.

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Isolation valves on the pressurization lines to the drywell and torus were closed following the completion of pressurization. Containment atmospheric condition data were recorded at thirty minute intervals during pressurization.

These data are included with the test data in the Appendix.

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Hatch 1988 ILRT Final Report-Page;7 s

4.

PROCEDURES (cont)

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'4.3-'Stabilizat' ion. Test and Verification-Containment atmosphere'wa's allowed to stabinze;for just overl4.5 hours5.787037e-5 days 0.00139 hours 8.267196e-6 weeks 1.9025e-6 months as required by Reference 3.

Table 2 summarizes containment. conditions during.

this stabilization period. As noted on the table, the' stabilization period

.cxtended from 8:15 a.m. (November 29) to 12:45 p.m.

Since the containment was, K

" isolated at just after 8:00 a.m., the total time for stabilization was somewhat over 4.5 hours5.787037e-5 days 0.00139 hours 8.267196e-6 weeks 1.9025e-6 months . Mean temperature during the stabilization period met the procedure. requirements on rate of change. Actual rates and maximum allowable values are listed below.

Rate.

Actual Maximum Allowable Average rate of change of mean temperature over the.

last 2 hours2.314815e-5 days 5.555556e-4 hours 3.306878e-6 weeks 7.61e-7 months of stabilization

=-(T at 1045 - T at 1245)/2

'0.11 Degrees F/ Hour 1 Degrees F/ Hour-Average rate o_f change of the above rate over the last 2 hours2.314815e-5 days 5.555556e-4 hours 3.306878e-6 weeks 7.61e-7 months of stabilization

= (T at 1045 - T at 1145) -

2 2

(T at 1145 - T at 1245) 0.07 Degrees F/ Hour 0.5 Degrees F/ Hour N an temperature during the stabilization period is graphed in Figure 1.

Reactor water level was increased to normal level during.the stabilization period to ensure adequate inventory during the.8 hour9.259259e-5 days 0.00222 hours 1.322751e-5 weeks 3.044e-6 months (expected duration) test.

Adequate verification test flow was demonstrated during the stabilization period by briefly venting 11.45 SCFM through the flow meter.

Suppression pool level was at 148 inches.

Since containment volume was calculated for this level, no correction to volume was required.

The 8 hour9.259259e-5 days 0.00222 hours 1.322751e-5 weeks 3.044e-6 months leakage rate test was started at 12:45 p.m. and concluded at 8:45 p.m.

Containment gage pressure at the start of the test was 59.2 PSIG.

' Containment atmospheric condition data were recorded at fifteen.(15) minute intervals during the test (as well as during stabilization and verification).

Reactor and suppression pool water levels were recorded at hourly intervals.

. Reactor level fell at two to three inches per hour during the test but torus level did not change.

Sumps were pumped down following the completion of

'depressurization -- the small accumulation in the sumps did not account for reactor level drop. The dewpoint temperature sensor in the torus indicated erratic swings of up to three degrees F during stabilization and the 8 hour9.259259e-5 days 0.00222 hours 1.322751e-5 weeks 3.044e-6 months test.

Data from this device were not used in leakage rate calculation. The weighting factor for this device was, in effect, prorated among the five dewpoint temperature sensors in the drywell. Failure of the torus dewpoint temperature sensor was probably due to condensation on electrical connections.

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BCP Technical Services, Inc.

Hatch 1988 ILRTl Final Report-

- Page 8 4.: PROCEDURES (cont)

~4.3 Stabilization.TestandVerification-(cont)

Figure 2 shows graphs of dewpoint temperatures indicated by sensor Number 1:(drywell)andsensorNumber6(torus). The erratic behavior of. Number 6 is evident when the two graphs are compared.

Following the' completion of the 8 hour9.259259e-5 days 0.00222 hours 1.322751e-5 weeks 3.044e-6 months ILRT, an 11.45 SCFM leak was-

.icposed through a flowmeter. This volumetric flow rate: corresponded to a leakage of 1.2 wt.% day at t e actual containment pressure of 73.7 PSIA (with

/

h no correction for temperature). The containment was allowed to stabilize for one hour.following the initiation of the imposed leak as required by Reference 3.

Reactor vessel level was increased to 60 inches during this stabilization.

period. The verification test commenced at 10:15 p.m. and was completed at

' 2:15 a.m. on November 30.

The containment was depressurized following the completion of.the-verification test. :The depressurization procedure is documented in the official. test copy of Reference 4.

Containment system restorations commenced when depressurization was complete.

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BCP Technical Services, Inc.

Hatch 1988 ILRT Final Report Page 9 5.

RESULTS 5.1 8 Hour Test The acceptance criteria specified in Reference 4 were met well before the completion.of the 8 hour9.259259e-5 days 0.00222 hours 1.322751e-5 weeks 3.044e-6 months test. The end of test leakage rate values and acceptance limits are listed below.

95% UCL on total time leakage rate 0.57 wt.%/ day Acceptance limit 0.90 wt.%/ day Total time calculated rate extrapolated to 24 hours2.777778e-4 days 0.00667 hours 3.968254e-5 weeks 9.132e-6 months

<0.50 wt.%/ day Acceptance limit 0.90 wt.%/ day Mean of measured leakage rates over the final 5 hours5.787037e-5 days 0.00139 hours 8.267196e-6 weeks 1.9025e-6 months of the test 0.50 wt.%/ day Acceptance limit 1.20 wt.%/ day Acceptance limits are based on the maximum allowable leakage rate of 1.2 wt.%/ day specified in the Technical Specifications. For return to power following an outage, the as left leakage rate must be less than 75% (per Reference 1) of the maximum allowable rate. The remaining 25% provides a margin for deterioration of the leakage boundary during the subsequent operating cycle. The 75% criterion is applied by Reference 3 to both the UCL and extrapolated rate values.

Since the mean of the measured rates is normally less than the UCL, the third criterion is generally not a factor in acceptance. The UCL rate shown above is the final as left value since penalties for penetrations with non-standard alignments add to zero.

Only the TIP purge penetration (35E) required penalty consideration since this penetration was not vented. However, minimum )athway leakage through this penetration was determined to be 0 SCCM and, t1erefore, no adjustment to calculated leakage rate is required.

One RHR loop was in service during the ILRT. This represents a conservative lineup (isolation valves open) and penalty is not a consideration.

Table 3 lists air mass and leakage rates (measured, calculated and UCL) foreachofthethirty-three(33)datasetsrecordedduringthe8 hour test. The extra olating the final twenty-one (21) polated rate is determined by manually extrap(24) hours.

calculated leakage rates out to twenty-four The final twenty-one (21) points show first a rising trend and then a falling trend. The net effect is an extrapolated rate below 0.50 wt.%/ day. How much below depends on the method of extrapolation which is not defined in Reference 3.

The mean of the measured rates is manually calculated using the final twenty-one (21) measured rate values.

The air mass values listed in Table 3 are graphed in Figure 3.

The various lines on the graph are annotated. The air mass decreased smoothly and linearly with time as expected.

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Si RESULTS(contj

-511'- 8 Hou'r Test (cont)--

' Containment mean temperature, total pressure and mean vapor, pressure are' listed;in Table 4"and graphed in Figures 4,' 5 and 6.

Vapor: pressure 'is-

. plotted to the same scale as total pressure and therefore shows little. change-

.over the test duration. The total pressure change (over the 8 hour9.259259e-5 days 0.00222 hours 1.322751e-5 weeks 3.044e-6 months test) ist

. 138 PSI _and' vapor pressure change over t e same per o - s

.0 0035 PSI.

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- The calculated leakage' rate of 0.49 (see Table:3) wt.4/ day is equivalent i

of about 56 cubic feet per hour.. The-1toawater. leak'(actualcubicfeet)from59'inchesto41'inchesbetween1:00-recorded reactor vessel level. drop

'and,nolmeasuraale rise in'. suppression )ool le(no significant riseLin sumrlevel p.m. and 9:00: ).mt equates'to an outleakage vel).of 48 cubic feet:per tour..

Thus,.more than-80% of containment._ lea cage is-accounted for by. loss of water in

.the primary system. This; water appears to have leaked back through'an RHR' connection to the refueling pool. Therefore;-there is very little air: leakage from the containment which is.the preferred condition since post-LOCA air leakage increases site. boundary dosage levels much more than equivalent water leakage.

If the water stays within the closed system / refueling pool boundary,.

.it adds'nothing to site boundary dosage levels.

The changes:in total time calculated and 95% UCL leakage rates with increasing test duration are illustrated in Figure 7.

The calculated rate is essentially constant after about three hours of test time as expected.

The UCL11s, as is-typical, asymptotic to the calculated rate.

5.2 Verification Test Verification test results are listed in Table 5 and graphed in Figure 7.

As' indicated by both the table and graph, the calculated leakage rate is'very close to the theoretical rate and well within the upper and lower limits..The final results and acceptance limits are listed below.

Upper Limit Rate

~-1.99 wt.%/ Day p'

- Total Time Calculated Rate 1.63 wt.4/ Day

Theoretics1 Rate 1.69 wt.%/ Day Lower Lin.it Rate 1.39 wt.%/ Day The theoretical rate is the. total time calculated leakage rate at the end of the 8 hour9.259259e-5 days 0.00222 hours 1.322751e-5 weeks 3.044e-6 months test, 0.49 wt.4/ day, plus the imposed rate, 1.2 wt.%/ day.

The.

upper and lower limits are set at 0.3 wt.%/ day (25% of the maximum allowable-LleakagerateperReference3)aboveandbelowthetheoreticalrate.

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BCP Technical. Services, Inc.

r Hatch.1988 ILRT Final Report

.Page 11' 1

I 5; RESOLTS-(cont)J 5.3 ' Mass Point Results.

Mass-point calculation results are listed for information in Tables 6 and 7; The mass: point calculated rate is the slope of the line fitted to the air n

mass / time data by;the method of least squares. Mass point UCL is the upper 95% confidence limit on the. slope (considering slope to be a positive number such that the absolute value of the UC1. exceeds the absolute value of the

-slope).

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BCP Technical Services, Inc.

Hatch 1988 ILRT Final Report

-Page 12

'6.. REFERENCES.

1.

Code of Federal Regulations, Title 10, Part 59, Appendix J,_ Reactor Containment Leakage Testing For Water Cooled Power Reactors.

r, 2.

ANSI N45.4-1972, Leakage Rate Testing.0f Containa nt Structures For Nuclear Reactors.

3. -Bechtel' Topical Report BN-TOP-1, Testing Criteria For Integrated' Leakage Rate Testing Of Primary Containment Structures For Nuclear Power Plants, Revision 1,-1972.

4.

HNP Surveillance Procedure 42SP-091688-0U-1-IS,. Primary Containment-Integrated Leakage Rate Test Procedure, Revision 0 and Revision 1.

BCP Technical Services, Inc.

Hatch 1988 ILRT Final Report TABLES AND FIGURES i

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LHatch 1988 TLRT Final; Report-h TABLE 1' b

-DRYBULB AND DEWPOINT TEMPERATURE' SENSOR LOCATIONS Sensor Tvoe Sensor Elev.*

. Azimuth

' Radius **-

Volume Number' Fraction'

-0 1'

118~Ft.

'90 degrees-19 Ft.

.059-

.Drybulb' Dr bulb 2-125 Ft.

320 degrees-25.ft.

.045-Dr bulb

'3

'130 Ft.

165 degrees 26 Ft.

.050 Dr bulb 4-

.135 Ft.

145 degrees 24 Ft.

.052

~Drybulb 141 Ft.

205 degrees.

24 Ft.

,.076.

Drybulb~

6 148 Ft.-

315 degrees.

20 Ft.

.075 Drybulb 7-159 Ft.

25 degrees 20 Ft.

.075-Drybulb 8

176 Ft.

200 degrees 16 Ft..

.036-

-Drybulb-

'9~

195 Ft.

135 degrees 14 Ft..

.050:

.Drybulb 10 209 Ft.

295 degrees

.13 Ft.

.030 Drybulb.

11***

-108 Ft.-

10 degrees.

57 ft.

.113-Drybulb-

'12***

108 ft.

90 degrees l 57 Ft.

.113 Drybulb-

'13***'

108 ft.

190 degrees 57 Ft.

.113'

.Drybulb 14***

108 Ft.

315 degrees 57.Ft.

.113 Dewpoint 1

121 Ft.

330 degrees' 26 Ft.

.104 Dewpoint 2.

132 Ft.

165 degrees 20 ft.

.102

-Dewpoint 3

147 Ft..

345 degrees 26 Ft.

.151-Dewpoint-4 169 Ft.

270 degrees 18 ft.

.111 Dewpoint 5'

201 Ft.

40 degrees 15 Ft.

.080 L.

Dewpoint 6***

108 Ft.

320 degrees 57'Ft.

0' Reference Elevations -- Drywell floor'at 114 Ft./ Head flange at 203 Ft.

o Out'from drywell centerline o*

o**

In torus t

I' L

1

> BCP Technical Services, Inc.

' Hatch'1988 ILRT Final Report'-

o TABLE 2-HNP Unit 1-1988 ILRT/ Stabilization DATA

SUMMARY

REPORT dsta. time ~date -temperature pressure' vapor-dry sir cet deg F psia pressure mass psia lbm 1

815. 1129 88.4699.

74.0705 0.4546 99325.'1 2'

830 1129 87.9070 74.0480 0.4552 99395.~ 9 ~

3 845 1129 87.6372 74.0057.

O.4548 99388.4 4:

-900.

1129.

87.4584 73.9789 0.4487 99392. 8-5 915 1129 87.3277-73.9567 0.4421.

99395.5 6

930 1129 87.2208 73.9371' O.4358 99396.9 945 1129 87.1498 73.9175 0.4363 99382.6 7. 1000 '1129 87.0680

'73.9018 0.42961 99385.4 8

9-1015' 1129-87.0079.

73.8868 0.4307.

99374.6 10 1030 '1129.

86.9505 73.8733 0.4305

.99366.9 1

11 1045 1129 86.9022 73.8609 0.4338 99354.5 11 2 1100 '1129 86.~8598 73.8492 0.4475 99327.81 13 1115 1129 86.8162 73.8383 0.4349 99338.0 14 1130 1129 86.7851 73.8281 0.4283 99338.9

)

15 1145 1129 86.7601 73.8192 0.4330 99325.0 16: 1200- 1129 86.7325 73.8103 0.4310 99320.7 17 1215 1129 86.7129 73.8021 0.4196 99328.6 18 1230 1129 86.7019 73.8430 0.4317

'99369.5 19 1245 1129 86.6831 73.8241 0.4272

.99353.5

l:f

, ~j,

,+

v:

' BCP ~ Technical Services, Inc.

Hatch 1988 ILRT Final Report TABLE 3 i

HNP Unit 1-1988 ILRT/ Test

. TOTAL' TIME LEAKAGE RATE REPORT data ~ time. date elapsed dry air' measured leakane uc1 cet time-mass rate ra{e

.. rate (hrs)

(Iba)

(%/ day)

-1 1245' 1129 0.00 99308.1 2

1300 1129 O.25 99300.8 O.7151-3 1315 1129

.O.50 99298.7 O.4576 0.4576 4.

1330 1129 0.75-99293.1 0.4851 0.4376-1.7538 5

1345 -1129 1.00 99287.5 0.4979 0.4453

-1.0190 6'

1400 1129 1.25 99280.8 0.5288' O.4704 0.8823 7

1415 1129 1.50-99277.3 0.4972 0.4686 0.7828 8

1430. 1129

'1.75 99271.5 0.5055 0.4726 0.7355 9

1445 1129 2.00 99265.9 0.5106 0.4779 0.7082 10 1500 1129-2.25 99260.8 0.5083 0.4810

.O.6873

11 1515 '1129 2.50-99255.6 O.5080 O.4835 O.6714 12 1530 1129 2.75 99249.8

-0.5126 0.4870 0.6610 13 1545. 1129 3.00-99244.4 0.5136 0.4901 0.6527

.14 1600 1129 3.25 99239.3.

0.5117 0.4921-0.6449

.15 1615 1129 l3.50 99233.8 O.5136 O.4942-O.6389 16 1630 1129 3.75 99229.O O.5104 O.4952-O.6326 17-1645 1129 4.00 99226.7 0.4921 0.4920 0.6226 18 1700- 1129 4.25 99220.0 0.5012 0.4914 0.6163 19.1715 1129 4.50 99211.7 0.5182 0.4944 0.6152 20: '1730. 1129 4.75 99207.8 O.5107 O.4955 O.6120 21 1745 '1129 5.00 99201.5 O.5157' O.4975 0,6102 22 1800 1129 5.25 99199.O' O.5026 0.4968 0.6058 23 1815 1129 5.50 99194.4 0.4997 0.4958 0.6013 24 1830 1129 5.75 99189.3 O.4994 0.4949 0.5973 25 1845 1129 6.00 99184.4 0.4986 0.4940 0.5936 26 1900 1129 6.25-99178.5 0.5013 0.4937 0.5906 27 1915-1129 6.50 99173.0 0.5026 0.4937 0.5882 28 1930 ~1129 6.75 99170.2 0.4939 0.4924 0.5846 29 1945 1129 7.00 99164.1 0.4972 0.4918 0.5819 30 2000 1129 7.25 99160.6 0.4918.

O.4905 0.5786 31 2015-1129 7.50 99156.9 0.4874 0.4889 0.5751 32 2030 1129 7.75 99152.5 0.4853 0.4872 0.5716 33 2045 1129 8.00 99144.1 0.4957 0.4870 0.5698 Allowable leakage rate, La =

1. 2OOO %/ day L

75% La 0.9000 2/ day 0.4870 X/ day Total time leakage rate

=

0.5698 %/ day Total time UCL r

l~

p; a

BCP)TechnicafServices,_Inc; f

k

' Hatch 1988 ILRT Final' Report d

d

,3 4

. TABLE 4 slNP Unit 1.-1988 ILRT/ Test DATA

SUMMARY

REPORT 1

data time date temperature pressure

. vapor dry air 1cet deg F.

psia pressure mass.

psia Ibm.

p

-99308.1-1.

1245 1129' 86.6831' 73.8241 0.4607

'2 1300 1129-86.6613-73.8157-O.4607 99300.8 m

~

3.

1315 1129 86.6313 73.8085

'O.4590

'99298.7

.4--1330 1129-86.6130 73.8020

'O.4591

99293.1 5.

1345-1129 86.5966-73.7954 0.4588 99287.5 6

1400 1129.

86.5844 73.7891' O.4591 99280.8 7

1415 1129 86.5718 73.7836' O.4579

'99277.3 8 -' 1430 1129 86'.5644

-73.7780 O.4575 99271.5 9 41445-1129 86.5497 73.7725 0.4582-99265.9 10- 15001 1129 86.5436

73.7678 0.4580 99260.8' 11, -1515 1129 86.5322 73.7629 O.4585 99255,6

12.'1530. 1129 86.5288 73.7583 0.4587

'99249.'8 13 '1545 1129 86.5219 73.7538 O.4591.

99244.4 14 1600 1129 86.5206 73.7493 0.4585

'99239.3

'15 1615 1129 86.5160-

-73.7456 O.4595.

99233.8 16 1630 1129 86.5129 73.7417 0.4596-99229.0

.17 - 1645 1129 86.5042 73.7380 0.4587 99226.7 18' 1700 1129 86.5057 73.7340 0.4595 99220.O~

19 1715 -1129 86.5141-73.7301 0.4606.

99211.7 20 1730- 1129' 86.5089 73.7267.

O.4608 99207.8 21 1745 1129 86.5114 73.7232 0.4616 99201.5~

22: 1800 1129 86.5041 73.7197 0.4609 99199.'O 23 1815 1129 86.5064 73.7163 0.4606 99194.4 24' 1830 1129 86.5058 73.7130 0.4611 99189.3 25 1 8 4 5 -- 1129 86.5030 73.7099 O.4621 99184.4

-26 1900 1129 86.5117 73.7067 0.4620 99178.5 27 1915 -1129 86.5169 73.7036 0.4623 99173.0 28 1930 1129 86.5092 73.7005 0.4623 99170.2 29 '1945 1129 86.5194 73.6978 0.4627 99164.1 30 2000 1129 86.5158 73.6949 0.4629 99160.6 31 2015 1129 86.5168 73.6918 0.4624 99156.9 32 2030 1129 86.5224 73.6893 0.4624 99152.5 33 2045 1129 86.533C 73.6863 0.4642 99144.1 i

d____._1_______

L lBCP Technical Services, Inc.

1 Hatch 1988 ILRT. Final Report TABLE 5 HNP Unit 1 - 1988 ILRT/ Verification-TOTAL TIME LEAKAGE RATE REPORT VERIFICATION data time date. elspeed dry air measured

' leak a' ge'-

set time mass rate rate

. %/ day) _

(%/ day)

'i

(

(hrs)

(Ibm) 1 2215

1129, O.00 99146.6 j

2 2230 1129 0.25 99128.7 1.7414 3.2245 1129 0.50 99113.7 1.5946 1.595-4 '2300 1129 0.75' 99096.1.

1.6323 1.602 5'

2315 1129-1.00 99080.5-1.6016-1.585 6

2330 1129 1.25-99062.9 1.6212 1.592 7

2345 1129 1.50 99044.7 1.6449 1.608 8

0 1130 1.75 99028.4 1.6354 1.614 9

15. 1130' 2.00 99010.3 1.6507 1.625 10 30 '1130 2.25 98994.5 1.6370 1.627 11 45 1130 2.50 98976.6 1.6468 1.631 12 100 1130 2.75 98961.7 1.6279 1.629 13

115. 1130 3.00 98942.7 1.6452 1.632 14 130 1130 3.25 98927.4 1.6332 1.632.

15 145 1130 3.50 98910.2 1.6352 1.631 16 200 1130-3.75 98892.8 1.6389 1.632 17 215 1130 4.00 98877.2 1.6308 1.631 Upper limit on leakage rate =

1.9870 %/ day 1.6313 %/ day Total time leakage rate

=

Lower limit on leakage rate =

1.3870 %/ day

4-1.

'BCP Technical Services, Inc.

Hatch 1988 ILRT Final Report TABLE 6 s

HNP Unit 1-1988 ILRT/ Test MASS POINT. LEAKAGE-RATE REPORT data time.date elapsed dry air leakage uc1 set time mass rate rate (hrs)

.(Ibm)

(%/ day)

(%/ day) 1 1245 1129 0.00 99308.1-

.2 1300 1129 O.25 99300.8 O.7151

.e 3-1315 1129 0.50 99298.7 0.4576 1.7298 4

1330 1129 0.75 99293.1 0.4566-0.6523 5

1345 1129

-1.00 99287.5 0.4724 0.5652 6

1400 1129 1.25 99280.8 0.6025 0.5690 7

1415 1129-

.1.50

-99277.3 O.4959

O.5409 8 ~1430 1129 1.75 99271.5

.O.4980 0.5305 9

1445;:1129 2.00 99265.9 O.5023 0.5272 10 '1500 ~1129 2.25

-99260.8 O.5037 0.5233

11 1515 1129 2.50 99255.6 O.5046 O.5204 12 1530- 1129 2.75 99249.8 0.5072 0.5205 13 1545 1129 3.00 99244.4 0.5093 0.5207 14 1600 1129 3.25 99239.3 0.5101' O.5197 15 1615 1129 3.50 99233.8 0.5113 0.5197 16 1630 1129 3.75 99229.0 0.5110 0.5184 17 1645 1129 4.00 99226.7 0.5052 0.5139 18 1700 1129 4.25 99220.0 0.5035 0.5114 19 1715 1129 4.50 99211.7 0.5071 0.5150 20 1730- 1129 4.75 99207.8 0.5079 0.5150 21 1745 1129 5.00 99201.5 0.5097 0.5165

22. 1800 1129 5.25 99199.0 0.5080 0.5143 23 1815 1129 5.50 99194.4 0.5059 0.5120 24 1830 1129 5.75 99189.3 0.5042 0.5100 25 1845 1129 6.00 99184.4 O.5026 0.5082 26 1900 1129 6.25 99178.5 0.5019

.O.5071 27 1915 1129 6.50 99173.0 0.5016 0.5064 28 1930 1129 6.75 99170.2 0.4996 0.5045 29 1945 1129 7.00 99164.1 0.4986-0.5033 30 2000 1129 7.25 99160.6 0.4968 0.5015 31 2015 1129 7.50 99156.9 0.4945 0.4994 32 2030 1129 7.75 99152.5 0.4922 0.4973 33 2045 1129 8.00 99144.1 0.4920 0.4968 Allowable leakage rate, La =

1.2000 %/ day 0.9000 1/ day

=

75% La 0.4920 1/ day Mass point leakage rate

=

0.4968 %/ day Mass point UCL

=

= _

i

/

~

'BCPTechhicalServices,Inc.

1 Hatch:1988 ILRT Final Report a

TABLE 7 1

'I HNP Unit'l - 1988 ILRT/ Verification MASS POINT LEAKAGE RATE REPORT l

VERIFICATION i

data time date elapsed dry air leakage set time mass' rate (hrs)'

(Ibm)

(%/ day) 1 2215 1129 0.00.

99146.6 2

2230 ~1129 0.25 99128.7 1.7414 3

2245 1129 0.50 99113.7-1.5946 4

2300 1129 0.75 99096.1 1.6139 5

2315 1129 1.00 99080.5 1.5969 i

I 6

2330 '1129 1.25 99062.9 1.6067 7 -2345. 1129 1.50:

99044.7-1.6270 8

0 1130 1.75 99028.4 1.6314 9

15 1130 2.00 99010.3 l'.6419:

10 30 1130 2.25 98994.5 1.6410 11 45 1130 2.50 98976.6 1.6447 12 100 1130 2.75 98961.7 1.6390 13' 115 1130 3.00 98942.7

.1.6420 14 130 1130 3.25 98927.4 1.6396 15 145 1130 3.50 98910.2 1.6385 16 200 1130 3.75 98892.8 1.6389 17 215 1130 4.00 98877.2 1.6367 Upper limit on leakage rate =

1.9920 %/ day 1.6367 %/ day Mass point leakage rate

=

Lower limit on leakage rate =

1.3920.%/ day

(.

BCP Technical Services. Inc.

Hatch 1988 ILRT Final Report y

88.5 I

E MPd Ee E's A1[

U R

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1000 1200 86.5 I

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FIGURE 1 NEAN TEMPERATURE DURING STABILIZATION t

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BCP Technical Services,.Inc..

Hatch 1988-ILRT Final Report

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H D Unit 1 - 1988 ILRT/ Test

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6 1400 1600 1800 2000 I

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FIGURE 2

BCP Technical Services, Inc.

Hatch 1988 ILRT Final Report i

IINP Init 1-1988 ILRT/ Test gg,gg_

i

's ACTUAL AIR MASS g

]

's STRAIGHT LINE R

7 FITTED TO.

g AIR MASS LOSSd %,

AIR MASS / TIME DATA MB t

AM g

EQUIVALENT TO 0.9%/ DAY's,

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1400 1600 1800 2000*

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FIGURE 3 AIR NASS - 8 WOUR TEST

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BCP Technical Services, Inc.

Hatch.1988 ILRT Final Report 1

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FIGURE 4 MEAN TEMPERATURE - 8 HOUR TEST

7 n.

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BCP Technical Services,. Inc.-

. Hatch 1988 ILRT Final Report.

w.

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MP Unit 1-1988 ILRT/ Test

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C_____--_-__.__

L BCP-Technical Services, Iric.

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FIGURE 6 VAPOR PRESSURE - 8 HOUR TEST

[

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Hatch 1988 ILRT Final Report NNP Init 1 - 19N IIM/ Test 2.00 I-0 i

g L

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1.00 75% La ga EY uct

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FIGURE 7 TOTAL TIME LEAKAGE RATE VS. TEST DURATION

'+

I BC'P. Technical Services, Inc.

Hatch 1988 ILRT final Report 4

r llNP hit 1 - 1988 ILRT/ Verification 99200

s'%,

's

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Hatt.h 1988.ILRT Final: Report F

(AppendixI' g.;

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','td I9x

,ine o,.

i.'

APPENDIX I i.

.i'

1 ILRT COMPUTER PROGRAM DESCRIPTION r

o i

r

. jl it i

L 1.

i' l

l l

l

BCP Technical Services, Inc.

Hatch 1988 ILRT Final Report Appendix I Page 1 APPENDIX I l

ILRT COMPUTER PROGRAM DESCRIPTION-c e

' calculates both BN-TOP-1 (program is a structured Basic program whichtotal time) and The BCP ILRT computer rates. The program accepts both keyboard and serial link data input (pre-data such as volume fractions, allowable leakage. rate, etc., must be input manually via the keyboard). Data is written to random access files. When a. program run is initiated, the user is queried for file information.

If a new file is s)ecified, screen prompts request pre-data.

If an existing file is specified, tie program calculates mean temperatures, mean vapor pressures and air masses and stores these in memory (not in the file). These quantities are l

recalculated whenever pre-data is changed. Once the. file information request is sat Sfied, the primary menu is displayed on the screen. Subsequent program functions are in response to menu selections. Menu choices allow the-

'following:

o Manual data entry

.o Serial link data entry o

Data set correction o. Pre-data set correction Datasetinsertionoutofsequence(e.g)inputtingthe3:15dataafter o

the 3:00 and 3:30 data have been entered o

Mass point. report.

i p

o Total time report L

o Trend (combinedmass/ total) report o

Listing of summary data Data rejection test perANSI56.8) i Changestartandend(timeforreports/ plots o

l o

i o

Delete a data set from calculations o

Restore a deleted data set o

Enter / exit verification test mode o

Branch to plot menu

.o Exit to system level I

i The plot menu allows plotting:

o Air mass l

.o Total time leakage rate o

Mass point leakage rate o

Individual or average temperature 4

o Individual or average pressure o

Individual dewpoint temperature or average vapor pressure Whenever pre-data or data is entered, the screen displays the data and asks the user if the data is correct.

If not, the user can correct any data Gntry.

When the user notes that the data is correct, it is written to the data file.

I u____---_.----_

BCP. Technical Services, Inc.

Hatch 1988 ILRT Final Report Appendix I Page 2 Leakage rate calculations are done in double precision since the regression line constants usually depend on the small difference of large l

numbers. Computer calculations were manually verified using a data file titled " Check". Check is always run following any program modification.

Various subroutines are modified to suit conditions unique to a particular test.

The routine which puts the initial display on the screen is modified to show job title and program revision date. The serial link routine is modified to accommodate the data system output format. The pressure transducer calibration table is changed to incorporate job specific calibration data.

l The generic program is written for dewpoint temperature inputs which are converted to vapor pressures using the ASME Steam Tables Polynomial. Several routines require modification if relative humidities or wet bulb temperatures are input instead of dewpoint temperatures.

BN-TOP-1 uses a very conservative procedure to calculate total time u)per l

confidence limit. The program calculates the more realistic 95% UCL on tie end of test total time calculated leakage rate if the test duration is twenty-four (24) hours or more. Otherwise, it uses the BN-TOP-1 formulation i

to determine the 97.5% UCL on end of test measured leakage rate.

l

References:

l 1.

Bechtel Topical Report BN-TOP-1, Testing Criteria For Integrated Leakage Rate Testing Of Primary Containment Structures For Nuclear Power Plants, i

Revision 1, 1972.

2.

ANSI /ANS 56.8-1987, Containment System Leakage Testing Requirements.

l l

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

___..---_.._-.--_a

L BCP Technica1' Services, Inc.

' Hatch 1988 ILRT Final Report.

Appendix II-APPENDIX II-TYPE'8 AND C LOCAL LEAKAGE RATE TEST'RESULTS

p

' BCP Technical Services, Inc.

Hatch 1988 ILRT Final Report :

Appendix II

. Page 1 The following tables list results for Type B and C local leakage rate tests )erformed between the completion of the.1986 ILRT.and the start of the

- 1988 I.RT.

Tables include data for all tests except those which are performed p

between the initial (or as-found). test at the start of a refueling outage and the final-(or as-left) retest at the end of the. outage. Other tests performet during the outage are considered to be diagnostic. Tables are arranged as e

follows:

o 1988 Type B test results including minimum pathway improvements o.1988 Type C test results including minimum pathway leakage improvements (TypeC,'TypeBandtotal) o 1987 Type B test results 1

o 1987. Type C test results o ' Personnel air lock test results o Results of tests performed between outages Minimum pathway leakage improvements for penetrations with simultaneously tested barriers are reported as half the as found/as left difference unless lesser numbers are justifiable based on diagnostic tests performed during the repair process.

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iI,

BCP Technical Services, Inc.

Hatch 1988 ILRT Final Report Appendix II t

Type B Test Results 1988 Refueling PENETRATION INITIAL TEST RETEST PENETRATION IDENTIFIER DATE LEAKAGE DATE LEAKAGE IMPROVEMENT 100C Electrical 9/26/88 0 acca N/A 100D Electrical 9/26/88 0 acem N/A 100E Electrical 9/26/88 0 acca N/A 101A Electrical 9/26/88 0 accm N/A 101B Electrical 9/26/88 0 acem N/A 101C Electrical 9/26/88 0 acem N/A 101D Electrical 9/28/88 0 accm N/A 101E Electrical 9/27/88 0 acem N/A 101F Electrical 9/26/88 0 accm N/A

-102A Electrical 9/27/88 0 acce N/A 103A Electrical 9/26/88 0 acca N/A 104A Electrical 9/27/88 0 acca N/A 104B Electrical 9/27/88 0 acca N/A 104C Electrical 9/27/88 0 acca N/A 104F Electrical 9/26/88

-0 acem M/A 104G Electrical 9/26/88 0 acca N/A 104H Electrical 9/26/88 0 acca N/A 105A Electrical 9/26/88 0 acca N/A 105C Electrical 9/27/88 0 acca N/A 106B Electrical 9/27/88

-0 aces 11/16/88 0 acca 200A Torus Hatch A 9/29/88 0 aces N/A 200B Torus Hatch B

.9/28/88 0 aces 11/28/88 0 acem 200C Torus Hatch C 9/28/88 0 acem N/A 202 Electrical 9/29/88 0 acca N/A 205 1T48-F310 A Test 10/06/88 0 accm M/A 205 1T48-F310 B Test 10/06/88 0 accm N/A 205 IT48-F310 C Test 10/06/88 0 acca N/A 205 IT48-F310 D Test 10/06/88 0 acca N/A 205 iT48-F311 A Test 10/08/88 0 acca N/A 205 IT48-F311 B Test 10/08/88 0 acca N/A l

205 1T48-F311 C Test 10/08/88 0 acca N/A 205 1748-F311 D Test 10/08/88 0 acca N/A 218B

'O' Rinus 10/21/88 0 acca N/A 220 1T48-F3I8 A Test 10/07/88 0 aces 11/09/88 0 seen 220 1748-F318 B Test 10/07/88 0 aces 11/09/88 0 seca 220 1T48-F318 C Test 10/07/88 0 aces 11/09/88 0 acem 220 1T48-F318 D Test 10/07/88 0 aces 11/09/88 0 aces 220 1T48-F326 A Test 10/07/88 28 aces 11/09/88 0 acca 14 acem 220 1T48-F326 B Test 10/07/88 79 accm 11/09/88 0 accm 40 acem 220 1T48-F326 C Test 10/07/88 0 acca 11/09/88 0 acca 220 1T48-F326 D Test 10/07/88 0 aces 11/09/88 0 aces Total Minimum Pathway Improvement -- Type B Tests 600 acem

1 i

.BCP Technical Services, Inc.

I Hatch 1988 ILRT Final Report

]

Appendix II j

Type C Test Results 1988 Refueling PENETRATION INITIAL TEST RETEST PENETRATION IDENTIFIER DATE LEAKAGE DATE LEAKAGE IMPROVEMENT 7A 1B21-F022A/028A (s) 9/29/88 67.7 scfh 11/04/88 0 scfh None-1 Valve Repaired 7B

'1B21-F022B/028B (s) 9/29/88 33 scfh 10/20/88 0 scfh None-1 Valve 7C IB21-F022C/028C (s) 9/30/88

<5 scfh N/A 7D 2B21-F022D/028D (s)

.9/29/88 5.1 scfh N/A 8

1B21-F016/019 (s) 9/30/88 8969 acca 10/18/88 0 acem None-1 Valve

9A 1B21-F010A 10/03/88 1050 acem N/A z e9A IB21-F032A/1G31-F039/ 10/01/88 2600 acem N/A 1E51-F013

98 1B21-B010B 10/13/88 0 acca N/A

+9B 1B21-F032B/1G31-F203/ 10/12/88

>10000 acce 11/03/88 220 acem(F006 only) 1E41-F006 10 1E51-F007/008 (s) 10/07/88 25 aces 11/05/88 133 aces 11 1E41-F002/003 (s) 10/04/88 83 acca 11/25/88 31 aces 26 acce 12 1E11-F008 10/14/88 1622 acce 10/30/88 559 acce 12 1E11-F009 10/14/88 31 acca N/A 13A

-1E11-F015A 10/16/88 36 acca 11/12/88 55 aces 13B 1E11-F015B 10/04/88 181 acca N/A 14 1G31-F001 10/15/88 81 acca N/A 14 1G31-F004 10/16/88 0 aces N/A 16A 1E21-F005A 10/13/88 0 acem N/A 16B 1F21-F005B 10/04/88 0 accm M/A 17 1E11-F022/023 (s)

-10/04/88 0 acca N/A 18

'1G11-F019 10/21/88 0 accm N/A 18 1G11-F020 10/21/88 2226 aces 11/04/88 61 acce 19 1G11-F003 10/31/88 0 acem M/A 19 1G11-F004 10/20/88 0 aces N/A 20&44 1P41-F049/050 (s) 11/C3/88 66241 acca 11/05/88 91 acca None-Cooler l

Leaks in CTMT.(1st Tes D

'21 1P51-F513 10/29/88 26 acca N/A-21

.1P51-F514 10/29/88 37 acca N/A 22 1P70-FOO4 10/22/88 0 accm M/A 22 1P70-F005 10/22/88

<20 acca N/A 23&24 1P42-F051/052 (a) 10/30/88 0 accm N/A 25 1748-F103/307/308/

10/08/88 38 accm 11/10/88 (200 accm 309/324 (s) 25 1T48-F113 10/18/88 0 acem N/A 25 IT48-F114 10/18/88 0 aces N/A 25 1748-F118A 10/18/88 0 acca N/A 23 IT48-F321 10/19/88 20 acca N/A 25 iT48-F322 10/18/88 0 acem N/A 25&205 1748-F104 10/17/88 0 acca N/A (a)= Valves Tested Simultaneously

= Water Test 1

l l

i

BCP Technical Services, Inc.

Hatch 1988 ILRT Final Report Appendix II Type C Test Results 1988 Refueling PENETRATION INITIAL TEST RETEST PENETRATION IDENTIFIER DATE LEAKAGE DATE LEAKAGE IMPROVEMENT 26 1P33-F002 10/06/88 0 accm N/A 26 1P33-F010 10/06/88 0 accm N/A 26 1T48-F319/320 (s) 10/05/88 14095 acem 11/07/88 20 acem 6081 acem 26 IT48-F334A 10/06/88 0 acem N/A 26 1T48-F335A 10/06/88 0 acem N/A 26 IT48-F334B 10/06/88 0 accm N/A 26 IT48-F335B 10/06/88 0 acem N/A 26 IT48-F340/341 (s) 10/31/88 0 acem N/A 27A 1D11-F051 10/25/88 0 acem N/A 27A 1D11-F053 10/25/88 0 acem N/A 27F iP70-F066 10/25/88 0 accm N/A 27F 1P70-F067 10/25/88 28 acem N/A 28A 1B31-F019 10/15/88 0 acem N/A 28A 1B31-F020 10'14/88 0 accm N/A 28F 1P33-F003 10/10/88 0 acem N/A 28F 1P33-F011 10/08/88 0 acem N/A 31D 1P33-F004 10/10/88 0 acem N/A 31D 1P33-F012 10/09/88 0 acem N/A 31F 1B31-F013A 10/17/88 173 acem 11/09/88 0 acem 31F 1B31-F017A 15: 18/88 0 neem N/A 33C 1D11-F050 lb/23/88

<20 acem N/A 33C 1D11-F052 10/23/88 (20 acem N/A 34E 1P33-F005 10/13/88 0 acem N/A 34E 1P33-F013 10/13/88 0 acem N/A 33A 1C51-J004B 10/09/88 0 acem N/A 35B 1C51-J004C 10/09/88 0 acem N/A 33C 1C51-J004A 10/09/88 0 acem N/A 35D 1C51-J004D 10/10/88 0 acem N/A 35E 1C51-F3012 10/12/88 16108 accm 10/21/88 0 acem 35E 1C51-F3017 10/10/88 0 acem 10/18/88 0 acem 31A 1E11-F016A 10/16/88 0 accm N/A 39B 1E11-F016B 10/03/88 ill accm N/A 40C iP70-F002 10/20/88 0 acem N/A 40C IP70-F003 10/20/88 0 acem N/A 42 1C41-F006 10/17/88 101 acem 10/27/88

<20 acem 42 1C41-F007 10/13/88 0 acem N/A 45F IT23-F004 10/20/88 (20 accm N/A 43F 1T23-F005 11/26/88

<20 accm N/A 46 IP21-F353 10/29/88 51 accm N/A 46 1P21-F420 10/29/88 38 acem N/A 52F 1B21-F111 10/20/88 0 accm N/A 92F IB21-F112 10/20/88 0 accm N/A 59A 1B31-F013B 10/17/88 106 acem 11/02/88 0 acem 59A 1B31-F017B 10/18/88 0 acem N/A (0) = Valvec Tested Simultaneously

j

>BCP Technica1' Services, Inc.

Hatch 1988 ILRT Final Report.

Appendix.II

-Type C Test Results 1988 Refueling PENETRATION INITIAL TEST-RETEST PENETRATION

' IDENTIFIER DATE LEAKAGE DATE' LEAKAGE IMPROVEMENT 1

205 IT48-F115 10/18/88 0 accm.

N/A 203 1748-F116 10/18/88 0 acem N/A l

205 1748-F118B-10/18/88

'O accm N/A 1

205 1T48-F310/328A (s) 10/06/88 303 accm N/A 203 1T48-F311/328B (s) 10/07/88 0 acem N/A 203 IT48-F325 10/19/88 30 acem N/A 205 IT48-F327 10/18/88 0 acem N/A 206A 1E41-F121 10/22/88 0 acem N/A i

206A 1E41-F122 10/21/88 0 acem N/A 210A&211A-1E11-F027A/028A (s) 10/17/88 314 acem N/A 210B&211B IE11-F027B/028B (s) 10/04/88 7551 acem 10/29/88 223 acem 3664 acem 212 1E51-F001/040 (c) 10/06/88

-O acem-N/A 213

.1E51-F002/028 (s) 10/04/88 0 accm N/A

-214 1E51-F021/049'(s)-

10/05/88 100 acem N/A 4

l 219 1E41-F022/040 (s) 10/05/88 0 acem N/A 217-IP33-F007 10/17/88 0 accm N/A i

217 iP33-F015

>10/11/88 0 accm N/A 220 IP33-F006 10/08/88 3030 acem

-11/02/88 0 accm 4

N/A 220 1P33-F014 10/08/88 0 accm

. 11/08/88 0 accm.

10 acem

220, 1T48-F318/326 (s) 10/07/88 20 accm

'220

'1748-F332A 10/11/88 0 acem N/A 220 IT48-F333A 10/16/88

<20 accm.

N/A

-l 220 1T48-F332B 10/17/88 0 accm N/A 220 IT48-F333B 10/16/88 (20 acem N/A l

220 1T48-F338/339 (s) 9/21/88 0 acem N/A 221A' 1E41-F104-10/04/88 0FF SCALE 10/27/88 36 acem

221A 1E41-F111 10/05/88 232 acem 11/14/88 20 accm 212 acem 22aC 1E51-F104 10/04/88 0 acem N/A l

d 321C 2E51-F305 10/04/88.

151 acem 10/28/88 38 acem 223A IT48-F342G 10/06/88 0 acem N/A l

J 223A iT48-F323G 10/06/88 30 acem N/A 223A IT48-F342H 10/06/88 0 acem N/A 223A 1T48-F323H 10/06/88 0 accm N/A i

i 223A IT48-F342I 10/06/88 0 accm N/A I

223A IT48-F323I 10/06/88 0 acem N/A 223A~

1T48-F342J 10/07/88 0 acem N/A 223A.

1T48-F323J 10/06/88 0 acem N/A 223A IT48-F342K 10/07/88 0FF SCALE 10/17/88 0 acem 223A IT48-F232K 10/07/88 0 acem N/A 223A

-1748-F342L 10/07/88 0 acem N/A

.1 223A iT48-F323L 10/07/88 0 accm N/A

'223B IT48-F342A 10/06/88 30 accm N/A i

223B IT48-F323A 10/05/88 0 acem N/A 233B IT48-F342B 10/06/88 0 acem N/A 223B 1748-F323B 10/05/88 0 acem N/A i

(0) = Valves Tested Simultaneoulsy

)

r d

l

1 y

BCP Technical Services, Inc.

Hatch.1988 ILRT Final Report-

-Appendix II Type C Test Results 1988 Refueling PENETRATION INITIAL TEST RETEST PENETRATION-IDENTIFIER DATE LEAKAGE DATE LEAKAGE IMPROVEMENT 223B-1748-F342C 10/06/88 0 accm N/A 223B 1T48-F323C 10/06/88 95 acca N/A 2238 1T48-F342D-10/06/88 0 acca N/A 223B IT48-F323D 10/06/88 0 acem N/A 223B 1T48-F342E 10/06/88 0 acca N/A 223B 1T48-F323E 10/06/88 0 aces N/A 223B 1T48-F342F 10/06/88 0 accm 12/22/88 0 accm 223B-1T48-F323F 10/06/88 0 acca N/A Total Minimum Pathway Improvement--Type C Tests 9993 acem

,-Type B Tests 600 accm Total Minimum Pathway Leakage Improvement 10593 acem 0.3741 acfm 538.7 acid For a Containment Free Air Volume of 274 000 FT3, the 538.7 acid Minimum Pathway Ln kage Improvement is equivalent to a Leakage Rate of $38.7/274000 = 0.13 + X/ day.

(c) = Valves Tested Simultaneouley l

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wN McCek M@HH0>m 0NwMNmb wOOb s00E WN0eNmb O W00E wN O3Wtk M@HH0>m 0NwMNmb MOO e00E WN0wNeb O W00E wM< McCek M%HH0>m 0NwMNmb eMw m00E WN0sNmb O W00E wM< O3#tk M%HH0>m 0NwMNmb wow a00E WN0wNmb NO E00E wMM Mccek M%HH0>m 0NwMNmb C s00E 2N4 wMM O3#%h M%HH0>m 0NwMNmb wO s00E 2N4 ww Mcc%h M%HN0>m 0NwwNmb O e00E 2N4 ww O3v4h M%HH0>m 0NwwNeb NO m00E 2N4 Il

.6yo. m bgu# Etm3w4M'.e O W6 m 4 % 3 & e W C. m AWXgEE<HMO2 MMM6M<. 6Wm'6 -

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TNNnNWb 0 s00E WNOwN@6 0 e00E NO m 66a9 wNNnNWb 0 e00E W%0wN@6 0 m00E wbTG keOm,u 64m9 wNNoNWb 0 m00E W%0wN@6 0 m00E NO wbTe,knOm NO.

NO wbv@,keOm o 64m4 wNNnNWb 0 e00E W%0wN@6 0 e00E NO.

wbw@,kmOb < 66m4 wxNnNWb 0 s00E W%0wN@6 0 s00R NO wbvm,kMOb m 64m4 wsNnNeb 0 s00E W%0wNW6 0 s00E NO wbve,kMOb u 64m9 wNNosmb 0 e00E W%0wNm6 0 e00S NG wbwm,kMOb c 64m4 wsNnNeb 0 s00E W%0wNe6 0 m00E NO wbvm,kMOm < 64m4 wNNnNmb 0 s00E W%0wNQ6 0 e00E NO wbTe,kMOe m 64m9 wNNnNeb 0 e00E W%0wN@6 0 s00E NO wbTG,kMOm u 64m9 wNNnNmb 0 s00E W%0wN@6 0 e00E NO wbfe,kMOe c 64m9 wNNnNmb 0 s00E W%0wN@6 0 s00E NO.

wbf@,kMOm < 64m9 fsNnNeb 0 e00E.

W%0wNG6 0 e00E NO wbT@,kMOm m 64m4 w%NnNeb 0 m00E W%0wNG6 0 s00E NO wb9e,kMOm u 64m4 w%NoNGb 0 e00E W%0wNG6 0 s00E NQ wb9W,kmOm o 64m4 T%NnNGb 0 s00E W%0wNG6 0 e00E NQ wb9G,kmNw < 64m9 wsNnNOb 0 s00E W%0wNW6 0 e00E

~ NO wb9@,kmNw m 64m4 wNNoNGb 0 e00E W%0wNW6 0 e00E NQ wbTe,kmNT.u 64m4 wNNnNGb 0 s00E W%0wNm6 0 e00E NA.

wbTm,kMNw c 64m4 wNNnNGb 0 e00E W%0aNm6 0 e00E NW wbwm,kMwm < 64m9 wNMoNeb M0 e00E W%0mNe6 Me e00E NW mbTe,kMwm m 64m9 wNmoNmb 0 e00E W%0mNG6 O s00E NW-ebT@,kMwm u 6%m@

fNmoNmb 0 e00E W%0mNG6 0 e00E NW wbTG,kmwm c 6%m@

fNMoNmb 0 e00E Ws0mNW6 0 s00E NW wbTe,kmNO < 6%mP wNMoNWb 0 e00E W%0mNW6 0 s00E NW wbWe,kmNO m 64m4 wNMoNWb 0 euUE WN0mNW6 0 e00E NW w6W@,kmNO u 66m4 wNMoNWb 0 e00E W%OmNW6 0 s00E NW w6T@,kmNO Q 64m9 wNMoNWb 0 e00E WNOmNW6 0 s00E Mn<

0*

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BCP Technical Services, Inc.

Hatch 1988 ILRT Final Report Appendix II Type.B Test Results 1987 Refueling PENETRATION INITIAL TEST RETEST IDENTIFIER DATE LEAKAGE DATE LEAKAGE i

100D Electrical 4/21/87 0 accm 100E Electrical 4/21/87 0 accm 101A Electrical 4/21/87 0 accm 101B Electrical 4/21/87 0 accm 101C Electrical 4/21/87 0 accm N/A 101D Electrical 4/21/87 20 accm N/A 1012 Electrical 4/22/87 20 accm N/A 101F Electrical 4/22/87 20 acem N/A 102A Electrical 4/21/87 0 accm N/A 103A Electrical 4/21/87 0 aces N/A 104A Electrical 4/21/87 0 accm N/A 104B Electrical 4/21/87 0 accm N/A 104C Electrical 4/21/87 0 accm N/A 104D Electrical 4/21/87 0 acem M/A 104F Electrical 4/21/87 0 accm N/A 104G Electrical 4/21/87 0 accm N/A 104H Electrical 4/21/87 0 accm N/A 105A Electrical 4/21/87 0 acem N/A 105C Electrical 4/22/87 20 accm N/A 106B Electrical 4/21/87 0 acca N/A 200A Torus Hatch A 4/22/87 0 acca 6/11/87 0 accm 200B Torus Hatch B 4/22/87 0 acem 6/11/87 0 acem 200C Torus Hatch C 4/22/87 0 accm 6/11/87 0 aces 202 Electrical 4/22/87 0 acca N/A 205 IT48-F310 A Test 5/01/87 0 acca 6/04/87 76 acca 205 1T48-F310 B Test 5/01/87 0 acem 6/04/87 0 acca 205 1T48-F310 C Test 5/01/87 0 acem 6/04/87 0 acem 205 IT48-F310 D Test 5/01/87 0 accm 6/04/87 0 acem 205 1T48-F311 A Test 4/29/87 0 accm 6/03/87 0 acca 205 IT48-F311 B Test 4/29/87 0 accm 6/03/87 0 acem 205 1748-F311 C Test 4/29/87 0 accm 6/03/87 0 accm 205 IT48-F311 D Test 4/29/87 0 acem 6/03/87 0 accm 218B

'O' Rings 5/05/87 0 acca N/A 220 1T48-F318 A Test 4/27/87 0 acca 6/10/87 0 acem 220 1T48-F318 B Test 4/27/87 0 acca 6/10/87 0 accm 220 1748-F318 C Test 4/27/87 0 acca 6/10/87 0 acem 220 1T48-F318 D Test 4/27/87 0 accm 6/10/87 0 aces 220 1T48-F326 A Test 4/27/87 0 acem 6/10/87 0 acem 220 1T48-F326 B Test 4/27/87 0 seen 6/10/87 0 accm 220 1T48-F326 C Test 4/27/87 0 acca 6/10/87 0 acca 220 1748-F326 D Test 4/27/87 0 acem 6/10/87 0 aces

BCP Technical Services, Inc.

Hatch 1988 ILRT Final Report Appendix II Type C Test Results 1987 Refueling PENETRATION INITIAL TEST RETEST

' IDENTIFIER DATE LEAKAGE DATE LEAKAGE 7A IB21-F022A/028A (s) 4/24/87 16 scfh 5/16/87 5 scfh 7B 1821-F022B/028B (s) 4/24/87 5 scfh N/A 7C 1B21-F022C/028C (s) 4/24/87 6 scfh N/A 7D 1B21-F022D/028D (s) 4/23/87

<5 scfh N/A 8

1B21-F016/019 (s) 4/27/87 352 acca 6/15/87 478 accm 09A 1B21-F010A 4/29/87 54377 accm 5/21/87 1130 accm c9A 1B21-F032A/1G31-F039/ 4/28/87 4186 acca 5/20/87 928 accm

.1E51-F013 09B IB21-F010B 5/10/87 400 aces N/A o9B IB21-F032B/1G31-F203/ 5/09/87 OFF SCALE 6/07/87 1500 acem 1E41-F006 10 1E51-F007/008 (s) 4/26/87 38 acca 5/30/87 111 accm 11 1E41-F002/003 (s) 4/26/87 70 acca 6/21/87 (20 accm 12 1E11-F008 5/15/87 1007 acca 5/30/87 906 accm 12 1E11-F009 5/16/87 35 accm N/A 13A 1E11-F015A 4/25/87 227 aces 5/22/87 81 accm 13B 1E11-F015B 5/20/87 1913 acca 5/31/87 0 accm 14 1G31-FOO1 5/12/87 0 acca N/A 14 1G31-F004 5/12/87 705 seen 5/24/87 25 aces 16A 1E21-F005A 4/29/87 22 aces N/A 16B 1E21-FOO5B 5/10/87 0 acca 6/20/87

<20 aces 17 1E11-F022/023 (s) 5/18/87 0 acca N/A 18 1G11-F019 5/08/87 1893 acca 5/26/87 0 acce 18 1G11-F020 5/09/87 2014 aces 5/26/87 26 aces 19 1G11-F003 5/16/87 0 acca N/A 19 1G11-F004 5/16/87 0 acca N/A

.20 & 44 1P41-F049/050 (s) 5/22/87 302 acem 5/24/87 303 accm 21-1P51-F513 4/28/87 20 acca M/A 21 1P51-F514 4/29/87 0 aces N/A 22 1P70-F004 4/27/87 0 acca N/A 22 1P70-F005 4/28/87 0 acca N/A 23 & 24 1P42-F051/052 (s) 6/12/87 0 acca N/A 25 1748-F103/307/308/

5/01/87 0 acem 5/31/87 507 acem i

309/324 (s) 25 1748-F113 4/29/87 0 acca N/A 25 1T48-F114 4/29/87 0 acca N/A 25 1T48-F118A 4/29/87 55 acca N/A 25 IT48-F321 5/03/87 20 acem N/A 25 1T48-F322 4/29/87 0 acem N/A 25&205 1T48-F104 5/03/87 0 acca N/A 26 1P33-F002 5/04/87 0 acca N/A 26 1P33-F010 5/04/87 0 acca N/A 26 IT48-F319/320 (s) 4/30/87 3232 acem 6/02/87 532 acem 26 1748-F334A 5/01/87 38 acca N/A 26 IT48-F335A 4/30/87

<20 acca N/A (c) = Valves Tested Simultaneously--Penetration Leakage Divided Equally Estvran Valve (e) = Water Test l

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'BCP Technical Services, Inc. -

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. Hatch 1988 ILRT Final' Report a

Appendix II

.4 i

Type C' Test Results 1987 Refueling PENETRATION INITIAL TEST RETEST-

. IDENTIFIER DATE LEAKAGE.

DATE LEAKAGE 126 1T48-F334B 5/01/87-

<20 aces N/A E ' 26 1748-F335B 4/30/87' 0 acca N/A

26 L 1748-F340/341 (s) 5/02/87

O aces N/A-27A

~1D11-F051 5/04/87

<20 accaL N/A 27A 1D11-F053 5/04/87 0 acca-N/A

27F-

.1P70-F066 4/30/87 0 acca N/A N/A

' :27F iP70-F067 4/30/87 0 acca~

5/29/87 0 accm.

28A=

1B31-F019

~5/08/87 35184 acem 28A

=1931-F020 5/08/87 0 aces N/A

-28F iP33-F003 5/06/87 71 acca 6/05/87 0 aces-

^ 28F.

1P33-F011

'5/06/87 808 acca 6/05/87 0 acce 131D

-1P33-F004/F012 (S) 5/04/87 0 acca N/A 31F 1831-F013A 5/07/87 0 aces N/A 31F 1931-F017A 5/07/87 0 aces N/A 33C-1D11-F050 5/04/87 0 acca

'N/A 33C 1D11-F052 5/04/87 0 acca N/A 34E

1P33-F005-5/05/87 25246 aces 6/11/87-O aces 34E-AP33-F013 6/11/87 0 aces N/A 35A 1C51-JOO4B:

5/07/87 58 acca 5/20/87 0 acca 358-1C51-J004C

-5/07/87 1913 acca 5/24/87 0 acca 35C-

'1C51-J004A 5/06/87 37 aces N/A

.35D' 1C51-J004D

.5/07/87 362 acca 5/23/87 0 acca 5/07/87 0 acca N/A 35EL 1C51-F3017 39A 1E11-F016A

.4/26/87 0 acca N/A 39B 1E11-F0168 5/19/87 0 acce 1 N/A

'42 1C41-F006 4/28/87 0 acca N/A 40C" 1P70-FOO2/F003 (s) 5/17/87 OFF SCALE 6/10/87 72 aces 5/06/87 0 acca

'N/A 42 1C41-F007

-4/30/87

<20 acca N/A 45F 1723-FOO4/005 (s) 46 1P21-F353 5/28/87 111 aces 5/28/87 30 aces 46 iP21-F420 5/11/87 3020 acca 5/21/87 20 acca

-52F:

11821-F111 5/04/87 0 acca 5/26/87 0 aces

'52F 1821-F112

-5/26/87 0 aces N/A 59A 1831-F0138 5/11/87 0FF SCALE 5/28/87 0 acem 59A 1B31-F0178 5/08/87 0 acca N/A 203 1E51-F031/003 (s) 4/24/87 (20 acca N/A 204A 1E11-FOO4A/030A (s) 4/23/87 300 aces

-5/21/87 450 acca 204B

.1E11-F004B/030B (s) 5/13/87 3662 acca 6/6/87 502 aces 204C-

.1E11-F004C/030C (s) 4/24/87 300 acca N/A

'204D 1E11-F004D/030D (S) 5/13/87 45 accm N/A

BCP Technical Services,.Inc.

Hatch 1988 ILRT Final Report Appendix II Type C Test Results 1987 Refueling PENETRATION INITIAL TEST RETEST IDENTIFIER DATE LEAKAGE DATE LEAKAGE 1

205 1T48-F115 5/02/87 (20 acca N/A 205 1T48-F116 4/30/87 0 acca N/A 203 1T48-F118B 4/30/87

<20 acem 6/06/87 0 accm 205 1T48-F310/328A (s) 4/29/87 0FF SCALE 5/17/87 40 acem 205 IT48-F311/328B (s) 4/29/87 9500 acem 6/01/87 179 accm 205 IT48-F325 5/02/87 0 acca N/A 205' 1T48-F327 4/30/87 0 acca N/A 206A 1E41-F121 5/03/87 20 acem N/A 206A 1E41-F122 5/03/87

<20 acca N/A 207 1E41-F042/051 (s) 4/24/87 0 accm N/A 208A 1E21-F001A/019A (s) 4/27/87 70 accm N/A 208B 1E21-F001B/019B (s) 5/09/87 0 acca N/A 210A 1E11-F007A 4/25/87 190 acem N/A 210A 1E11-F011A/026A (s) 4/24/87 1200 acem N/A 210A 1E11-F025A 4/30/87 0 accm 5/20/87 21 accm 210A 1E11-F029 5/20/87 0 acca N/A 210A 1E11-F055A/103A/3078A 4/27/87 2106 acca N/A 210A 1E21-F015A 4/28/87 0 acem N/A 210A 1E21-F031A 4/29/87 0FF SCALE 5/13/87 60 aces 210A 1E21-F044A 5/17/87 0 aces N/A 210A 1E51-F019/021 (s) 4/25/87 750 acca N/A

'210B 1E11-F007B 5/19/87 525 acca N/A 210B 1E11-F011B/026B (s) 5/13/87 37 acca M/A 210B 1E11-F025B 5/27/87 400 acca 5/27/87 40 acem 210B 1E11-F055B/103B/3078B 4/27/87 2106 acca 5/13/87 1103 acca 210B 1E11-F097-5/14/87 0 acca 5/19/87 63 aces 210B 1E21-F015B 4/15/87 55577 acca 6/03/87 0 accm 210B 1E21-F031B 5/11/87 0FF SCALE 6/11/87 431 aces 210B 1E21-F044B 5/09/87 0 acca N/A 210B 1E41-F012/046 (s) 4/25/87 0FF SCALE 5/05/87 115 acem 210AL 211A 1E11-F027A/028A (s) 4/26/87 0FF SCALE 5/19/87 232 aces 210B&

211B 1E11-F027B/028B (s) 5/19/87 7551 acem 6/08/07 856 aces 212 1E51-F001/040 (s) 4/25/87 8850 acca 4/30/87 81 aces 213-1E51-F002/028 (s) 4/25/87 7325 acca 5/07/87 700 acem 214 1E41-F021/049 (s) 4/25/87 0FF SCALE 6/05/87 1762 acca l

215 1E41-F022/040 (s) 4/26/87 0 acem N/A 217 1P33-FOO7 5/07/87 0 accm N/A 217 1P33-F015 5/07/87 0 accm N/A 218A IG51-F012 4/26/87 0 acca N/A 218A 1G51-F011 4/26/87 0 acca N/A 218A 1G51-F002 4/26/87 60 acca N/A 218A 1G51-D001 (Blind) 4/25/87 0 accm N/A l

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BCP Technical' Services, Inc.

Hatch 1988'ILRT Final Report Appendix II Type C Test Results 1987 Refueling i

PENETRATION INITIAL TEST RETEST IDENTIFIER DATE LEAKAGE DATE LEAKAGE l

l 220

-1P33-F006 5/05/8'7 50 acem N/A j

220 1P33-F014 5/05/87 (20 acca N/A 220 1T48-F318/326 (s) 4/29/87 84 accm-6/09/87 (20 accm 220 1T48-F332A 5/02/87 0 acca N/A 220 1T48-F333A 5/02/87 25 acca N/A 220 1T48-F332B 5/03/87 0 acca N/A 220 1T48-F333B 5/03/87 40 acca N/A 220 1T48-F338/339 (s) 5/02/87 0 acem N/A 221A 1E41-F104/F111 (s) 4/27/87 0FF SCALE 5/29/87 0 accm 221C 1E51-F104/F105 (s) 4/26/87 0 accm N/A 223A 1T48-F342G 5/01/87 0 acca 6/03/87 39 accm 223A iT48-F323G 4/30/87 0 accm 5/31/87 50 accm 223A 1T48-F342H 5/02/87 0 acem 5/31/87.

O acem 223A IT48-F323H 4/30/87 0 acem 5/31/87 0 accm 223A 1T48-F342I 5/02/87 0 acca 6/03/87 0 accm 223A 1748-F323I 4/30/87 0 acca 5/31/87 0 accm 223A IT48-F342J 5/01/87 81 acca 5/31/87 0 acca 223A iT48-F323J 4/30/87 0 scen 5/31/87 0 accm 223A IT48-F342K 5/01/87 0 acca 6/03/87 34 acca 223A 1T48-F323K 5/01/87 60 acca 5/31/87 50 acca 223A 1T48-F342L 5/01/87 85 acca 5/31/87 0 acco 223A iT48-F323L 5/01/87 72 acca 5/31/87 0 aces 223B 1T48-F342A 5/01/87 0 acca 5/31/87 30 aces 223B 1T48-F323A 4/30/87 0 acca 5/31/87 0 acca 223B IT48-F342B 5/01/87 0 acca 5/31/87 0 aces 223B 1T48-F323B 4/30/87 0 acca 5/31/87 22 accm 223B 1T48-F342C 5/01/87 0 acca 5/31/87 0 accm 223B 1748-F323C

'4/30/87 0 acca 5/31/87 48 aces 223B 1T48-F342D 5/01/87' 0 aces 5/31/87 0 aces 223B 1T48-F323D 4/30/87 0 acca 5/31/87 36 accm 223B 1T48-F342E 5/01/87 0 aces 5/31/87 0 accm 223B 1T48-F323E 4/30/87 0 acca 5/31/87 0 aces 223B IT48-F342F 5/01/87 0 aces 5/31/87 0 accm 223B 1T48-F323F 4/30/87 0 acca 5/31/87 0 acce 1

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ANNO 0 8s 0 e00E W%4wN.m e

0 e8s 0 s00E W%4wN m 0 s8n 0 s00E O%4 N e W%4wN 0e8e 0 e00E W%4NN m 0 s8s 0 e00E N0 8s 0 m00E COO eUUE c

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Hatch 1988 ILRT Final Report

' Appendix:II

)

-Miscellaneous.1ype B Test Results Performed Between Outages i

PENETRATION INITIAL TEST IDENTIFIER DATE LEAKAGE Dr 4/17/86 0 acem 0-kwellHead'0-ring'11/18/86 in s 0 accm 1A 1B DW Eq ipment Hatch 4/30/86 20 acem 78 MSIV ellows Outbrd 4/16/86 0 accm 200A Torus Hatch '0-rin ' 4/15/86 0 acem 200B Torus Hatch 80-rin ' 4/15/86 0 accm 200C Torus Hatch '0-rin

4/15/86 0 acem 200B Torus Hatch B 4/27/86 0 accm 200A Torus Hatch A 5/17/88 0 accm 200B Torus Hatch B 4/08/88 0 accm 200B Torus Hatch B 5/17/88 0 accm 1A Equipment Hatch A 4/09/88 0 acem 6

CRD Hatch 4/28/88 0 acem 6

CRD Hatch 5/17/88 0 acem A3 Found Results-Th7 calculated as found lenkene rate is the sum of the as left leakage rat? (UCL) and the improvements in minimum pathway leakages made during th) Type B and C local leakage testing program. The net minimum pathway 0.57 + 0.20 = 0.77vt%/ day. y. The calculated as found leakage rate is 1:provement is 0.20 wt.%/da

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' BCP Technical: Services, Inc.

' Hatch 1988 ILRT Final' Report

p. '

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i" APPENDIX III TEST DATA DATA SETS

- 1.

Pressurization 2.

Stabilization

.3.

Test 4.

Verification

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Hatch 1988,:ILRT Final Report.

"AppendixrIII-i l

c I

1, l:

- PRESSURIZATION' DATA SET-m 1

J

i; o

l' 1

'HNP Unit 1-1988 ILRT/ Pressurization j

DATA

SUMMARY

' REPORT L

(dzto' tise date temperature pressure

vapor, dry air set deg F psia pressure'

- sess psia lhe 1

'345 1129 82.2957' 14.8817 0.3585 19818.4 2 -400 1129 82.3674 14.8924 0.3491 19843.2 3

415 1129 83.1772-15.6092 0.3599 20775.4 4

430 1129 85.7229

.18.7114.

0.3583 24887.4 5

445 1129

'86.6382 22.7905 0.3654 30358.1 6

500 1129 86.9925 26.8552 0.3798 35818.1 7' ' 515 1129 87.3170 30.9132 0.3851 (1276.4 8

530 1129 87.5672 34.9742 0.3877 46742.3 9~

545 1129 87.8640 39.0268 0.3988 52175.9 10 600 1129 188.1589 43.0788 0.4059 57608.5 11-615 1129 88.4392 47.1041 0.4144 62998.9 12 630 1129 88.6938-51.1304 0.4232 68386.0 13 665 1129

'68.9315 55.1436 0.4367-73750.3 14 700 1129 89.1442 59.1363 0.4297 79111.7 15 715 1129 89.3695 63.1129 0.4430 84417.9 16 730 1129 89.5928 67.D643 0.4513 89692.7 17 745 11129' 89.7707 71.0062 0.4540 94966.1

.18 800 1129 89.4960 73.7050 0.4593 98641.0

_.--_.a-..-

6 a.

i HNP Unit 1-1988 ILRT/ Pressurization

.I detaiset i

time'=

345 date = 1129-sensor raw data value

' temperature 1( 77.040 ) = ~ 77.040 deg. F 77.290 deg. F-

. temperature 2( L77.290 )

=

78.880 deg. F temperature 3 ( 78.880 )-

=

81.130 deg. F' temperature 4(

81.130 ) =

83.820 deg. F

. temperature 5( 83.820 )

=

88.480 deg. F

. temperature 6 (-

88.480 ) =

94.000 deg. F-j..

. temperature 71(. 94.000 )

=

.98.130 deg. F temperature ~8 ( 98.130-)

=-

104.820 deg. F temperature 9 (.104.820 ) =

104.590 deg. F temperature 10 ( 104.590 ) =

ten.perature 11 ( 75.380 ) =.

75.380 deg. F-75.670 deg. F temperature 12 ( 75.670 ) =

75.210 deg. F

' temperature 13 (~

75.210 ) =

75.880 deg. F temperature 14 ( 75.880 )

=

68.980 deg. F, 0.3505 psia

derpoint 1

.(.. 68.980-)

=

68.180 deg. F, 0.3410 psia dewpoint 2

(: 68.180 )~

=

66.600 deg. F, 0.3229 psia, dewpoint 3

( 66.600 )'

=

66.790 deg. F, 0.3250 psia

' dewpoint 4

( 66.790 ) =

67.860 deg.' F, 0.3373 psia dewpoint 5

(-

67.860 ) =

'71.980 deg. F, 2.3882 psia

'derpoint 6 L( 71.980-)

=

14.8826 psia pressure 1

(

148826 )

=

'14.8817-psia

-pressure 2

( 148817 ) =

weighted averages, volume and air mass 82.29570 deg. F temperature

=

s' 14.88170 psia pressure 0.35849 psia

=

vapor pressure volume

=

274000 cu. ft.

19818.4 lba dry air mass

=

7_- -

.f 4;).:

r_

HNP Unit 1-1988 ILRT/ Pressurization

. data set-2 time = 400 date = 1129 sensor raw data value 77.150 deg. F

' temperature 1~( -77.150 )

=

77.440 deg. F-temperature. 2( 77.440 )

=

temperature 3( 79.040 )

=. 79.040 deg. F-81.330 deg. F temperature 4( 81.330 ).

=

83.930 deg. F temperature 5( 83.930 )

=

88.570 deg. F temperature 6( 88.570 )

=

94.220 deg. F temperature 7( 94.220 )

=

98.440 deg. F temperature 8( 98.440 )

=

104.970 deg. F temperature 9( 104.970 )

=

104.590 deg. F temperature 10 ( 104.590 )

=

75.350 deg. F temperature 11 (. 75.350 )

=

75.650 deg. F temperature 12 ( 75.650 )

=-

75.190 deg. F temperature-13 ( -75.190 )

=

75.860 deg. F-temperature 14 ( 75.860 )

=

69.360 deg. F, 0.3551 pais dewpoint 1

( 69.360 )

=

-68.540 deg. F, 0.3452 psia dewpoint 2

( 68.540 )

=

66.380 deg. F, 0.3205 psia dewpoint 3 66.380 )

=

67.110 deg. F, 0.3287 psia dewpoint 4

( 67.110 )

=

68.020 deg. F, 0.3391 psia dewpoint 5

( 68.020 )

=

70.170 deg. F, 0.3650 psia despoint. 6

( 70.170 )

=

14.8935 pais pressure 1

(

148935 )

~=

14.8924 psia pressure 2

(

148924 ) =

weighted averages, volume and air mass 82.36744 deg. F temperature

=

14.89240 psia

=

pressure.

0.34912 psia

=

vapor pressure 274000 cu. ft.

volume

=

19843.2 lbm dry air mass

=

l l

= - - _

g

- -y

~.

+

,p'

[

HNP Unit 1-1988 ILRT/ Pressurization' i

. data' set:

4.+

time.=' 430 date = 1129 sensor rev. data; value l

N, 79.710 deg. F

,: temperature-1:(? 79.710.-)-

=-

80.640 deg. F

(

temperature ' 2l(l-'80.640 ).

'82.550 deg. F.

/

=

temperature. 3't 82.550 )

=

85.890.);:=.

85.890,deg. F temperature 4 (:

~

87.070 deg. F1 temperature:: 5. _ (.' ; 87. 070 ) ' ' =-

89.870 deg. F

. temperature-6 ( '89.870 )

=

temperature 7( 98.010 ).

=,.98.010 deg. F i'-

' temperature '8L( 101.680-) = 101.680 deg.~~F 107.600 deg.-F temperature _. 9:(-'107.600 )

-=-

' temperature l10.('107.250 ).= ' 107.250 deg.' F temperature 11-( 79.320 ).

79.320'deg. F

=

81.060 deg. F

/ temperature 12 (~ 81.060_)

=.

=-temperature 13-(. 79.620-):,;=.

79.620 deg.' F.

temperature-14 ( ~77.090 l' = -77.090 deg. F 70.310 deg.

F., 0.3668 psia devpoint 1:.

. ( 70.310 )

=

63.810 deg. F, 0.2930 psia devpointo 2?

( 63.810 )-

=

72.360 deg. F, 0.3932 psia devpoint 3.

( 72.360 )

=

73.470 deg.-F,_0.4082 psia devpoint. 4, f( 73.470 ): -=

73.400 deg.'F, O.4072 psia devpoint S,

( 73.400 ).

=.

67.990 deg. F, 0.3388 psia.

devpoint 6

( ~67.990')-

=

1 18.7168 psia-

-pressure 1

(,187168 )

=

18.7114 psia pressure..2-( -- 187114 ).

=

. weighted averages,' volume and air mass 85.72295 deg. F temperature

=

18.71140 psia

=

pressure 0.35827 pois

=

vapor pressure 274000 cu. ft.

volume.

=

24887.4 lba dry air mass

=

I

n w,

l

Nk.'.

$i.

+

NNP' Unit 1-1988 ILR7/ Pressurization 1

T ata set'

-6 d

4

. time =.500" date = 1129 9'

.1 ft',D sensoro raw data-

'value.

~

79.480 deg.IF-temperature 1-~ ( o79.480")

=:

p 3

80.530'deg..F-temperature '2 (.

80.530

)--

=

"g 1

83.520 deg. F-

= temperature - 3 (. 83.520:)

=

temperature 4.(1 87.280-)

=- 87.280 deg. F r

Temperature 15'( _ 89.290 ) =: 89.290 deg. F L

-temperature 6

(-

90.550 ).=-

90.550 deg. F~

temperature 77-( 99.700 )

1=1 99.700 deg. F.

[

. temperature 8-( 102.860 )-

=

'102.860 deg. F temperature 9-( 109.820-); m: 109.820 deg. F temperature 10 ( 109.720:). si'1D9.720 deg. F 80.730 deg.' F temperature 11:( 80.730 )

=

n 83.080 deg.' F-g

' temperature 12 (;-83.080 )

=-

-- 81.410 deg. F

._ temperature 13 ( 81.410 ).*

77.120 deg. F temperature 14 (' 77.120 )-

=-

l.[,

dewpoint. 1 g.(; 71.560 ) ~= '71.560 deg. F,.0.3827. psia 60.370 deg.

F', 0.2595 psia

(.'60.370 ).

dewpoint'l2 L

=

76.770 deg. F, 0.4557 psia dewpoint 3

( 76.770 ) =

80.060 deg..F', 0.5078 psia dewpoint 4-( 80.060 ) =

p,

despoint 5

( 76.870 ).

76.870 deg. F, 0.4572 psia-

=

67.770 deg. F, 0.3362 psia L'

dewpoint'"6,

(-

67.770 ); =-

pressure 1

( '268559 l' =

26.8559 psia 26.8552 pois

. pressure 2

- ( 268552 ) =

L.

! weighted averages, volume and air mass 86.99252 deg. F temperature

=

26.85520 psia

=

pressure 0.37975 pais

=

vapor pressure a

volume

=

274000 cu. ft.

=

35818.1 lba dry air mass o.

t

.___-._-.-m._

HNP Unit 1-1988 ILRT/ Pressurization 1 data set 8

time = 530 date = 1129 l

' sensor rav data value 79.590 deg. F temperature 1( 79.590 )

=

80.810 deg. F

temperature 2 ( 80.810 ) =.

84.180 deg. F temperature 3-(

84.180 ) =

87.870 deg. F temperature 4 (87.870 )

=

89.950 deg. F

-temperature 5( 89.950:)

=

91.450 deg. F

temperature 6'(

91.450')

=-

100;170 deg. F temperature 7( 100.170 )

=

103.270 deg.' F temperature-8( 103.270')

=

111.390 deg. F.

temperature 9 ( 111.390-)

=

111.620 deg. F temperatt;e 10-( 111.620.)

=

81.190 deg. F temperature'11 ( 81.190-)

=

83.380 deg. F temperature 12 ( 83.380 )

=

82.020 deg. F temperature 13 ( 82.020 )

=

temperature 14 ( 77.420 ).

'77.420 deg. F

=

69.530 deg. F, 0.3571 psia devpoint 1

'(

69.530 )

=

61.390 deg. F, 0.2691 psia devpoint. 2

.i 61.390-)

=

77.570 deg. F, 0.4679 psia.

devpoint 3

( 77.570 )

=

81.860 deg. F, 0.5385 psia devpoint 4

( 81.860 )

=

77.880 deg. F, 0.4727 psia devpoint 5

( 77.880 )

=

68.350 deg. F, 0.3430 psia devpoint 6

( 68.350 )

=

34.9771 psia pressure 1

(-

349771 )

=

34.9742 psia pressure 2

( 349742 )

=

weighted' averages, volume and air mass 87.56715 deg. F temperature

=

34.97420 psia

=

pressure 0.38769 psia

=

vapor pressure 274000 cu. ft.

volume

=

46742.3 lba dry air mass

=

5

.HNP Unit'l-1988 ILRT/ Pressurization data set 10 time = 600 date = 1129 sensor-raw data value 79.640 deg. F temperature 1( 79.640 ) -=

a temperature 2( 81.530 ).

=

81.530-deg. F-84.790 deg. F ll temperature 3( 84.790 ) -=

88.350 deg. F

. temperature '4 (' 88.350 )

=

90.580 deg. F temperature 5(~ 90.580 l' =

92.260 deg. F temperature 6( 92.260 ) =

100.590 deg. F temperature 7( 100.590 ) =

103.640 deg. F temperature 8 ( 103.640-)

=

112.570 deg. F temperature 9 (:112.570 )

=

113.290 deg. F-temperature 10 ( 113.290 )

=

81.620'deg. F temperature 11 (.81.620 )

=

83.620 deg. F temperature 12 ( 83.620

)-

=

82.260 deg.-F temperature 13 ( 82.260 )

=

78.620 deg. F temperature 14 ( 78.620 )

=

dewpoint 1

( 73.920 )

73.920 deg. F, 0.4144 paia

=

62.660 deg..F, 0.2814 psia dewpoint 2~

( 62.660.)

=

78.240 deg. F, 0.4784 psia dewpoint 3

( 78.240 ) =

82.800 deg. F, 0.5551 psia dewpoint 4

( 82.800 )

=

79.180 deg. F, 0.4934 psia

- dewpoint 5

(; 79.180 )

=

69.450 deg. F, 0.3562 psia dewpoint 6

( 69.450 )

=

43.0684 psia pressure 1

( 430684 ) =

43.0788 psia pressure 2

( 430788 )

=-

weighted averages, volume and air mass 88.15894 deg. F temperature

=

43.07880 psia

=

pressure 0.40585 psia

=

vapor pressure 274000 cu. ft.

volume

=

57608.5 lba dry air mass

=

I HNP Unit /1-1988-ILRT/ Pressurization f

Ldata set-12 time s,'630

'date = 1129 E

s

(.;

sensor raw data value

~3

-temperature-l' ( 79.780 ) =.

79.780 deg..F j

82.240 deg. F j

temperature 2( L82.240 )

,=

85.160;deg. F j

temperature'-3 ( 85.160 )

-=

88.770 deg. F i

temperature' 4-(

88.770 ).=

91.170 deg. F j

temperature 5 - ('

91.170 ).

=-

93.310 deg. F.

temperature 6=(

93.310 l'

=

. temperature 7 ( 100.980,). =. 100.980 deg. F temperature. 8 ( 104.060.)

1=. 104.060 deg. F 113.580 deg. F temperature 9 ( 113.580_-)

=

114.860 deg.

F-.

l.

temperature 10-(,114.860 )

=

temperature.11 ( 81.940;)..

81.940 deg. F

=

temperature 12 ( 83.840 ) =. -83.840 deg. F 82.380 deg. F temperature 13 ( 82.3804)

=

79.630 deg. F temperature.14 ( '79.630-)

=

.72.510 deg. F, 0.3952 psia dewpoint. 1-(' -72.510 )

=-

dewpoint. 2

-(.

64.720 ).

64.720 deg.-F, 0.3025 psia

=

78.740 deg. F, 0.4863 psia

.devpoint 3

(-

78.740 )

=

83.280 deg. F, 0.5638 psia devpoint'_ 4

( 183.280 )

=

80.310 deg. F, 0.5120 psia-devpoint.: 5-( -80.310 )

=

71.810 deg. F, O.3859 psia devpoint.~6-( 71.810 )

=

51.1343 psia pressure 1

( 511343 )

=

51.1304 psia pressure 2

( 511304 )

=

weighted averages, volume and air mass 88.69377 deg. F temperature

=

51.13040 psia-

=

pressure 0.42319 psia.

=

vapor pressure 274000 cu. ft.

volume

=

68388.0 lba dry air mass

=

j l

HNP Unit 1-1988 ILRT/ Pressurization-data set 14 time =' 700 date = 1129 sensor raw data

.value 80.040 deg. F temperature 1( 80.040 )

=

82.940 deg. F temperature 2( 82.940 )

=-

85.500 deg. F-temperature 3 (-

85.500 ).

=

89.170 deg. F temperature 4;(

89.170 )

=

91.730 deg. F temperature 5'( ~91.730

).

=

temperature 6( 94.210 )

=..94.210 deg. F 101.290 deg. F temperature 7.( 101.290-)

=

104.420 deg. F temperature 8( 104.420 )

=

temperature 9 ( 114.390 )

=. 114.390 deg. F 116.120 deg. F temperature 10 ( 116.120 )

=

82.180 deg. F temperature 11 ( 82.180 ).

=

84.040 deg.cF temperature 12 ( 84.040 )

=

82.540 deg. F temperature 13 ( 82.540 )

=

80.280 deg. F temperature 14

(-

80.280 )

=

71.010 deg. F, 0.3756 psia dewpoint-1

(.

71.010 )

=

66.330 deg. F, 0.3199 psia dewpoint' 2

(- 66.330 )

=

78.920 deg. F, 0.4892 psia dewpoint 3

( 78.920 )

=

83.750 deg. F, 0.5724 psia davpoint 4

'(

83.750 )

=

81.420 deg.'F, 0.5308 psia-dewpoint 15

( 81.420 )

=

72.440 deg. F, 0.3943. psia dewpoint 6

.(

72.440 )

=

59.1406 p'sia pressure 1

( 591406 )

=

59.1363 psia pressure 2

( 591363 >-

=

weighted averages, volume and air macs 89.14423 deg. F-temperature

=

59.13630 psia

=

pressure 0.42966 psia

=

vapor pressure 274000 cu. ft.

volume

=

79111.7 lba-dry air mass

=

l

ny

>\\

i

HNP Unit 1-l'988'ILRT/ Pressurization -

q data' set 16 time = 730".date = 1129

)

sensor raw-data value temperature 1( 80.470

)~

=1 80.470 deg. F 83.690 deg. F

temperature :2 ( 83.690 ) =

86.010 deg. F temperature. 3:( 86.010-) =

temperature. 4 (.89.670 )

89.670 deg. F

=

92.250 deg. F.

1 temperature. 5 ('.92.250 ) =-

95.060 deg. F

' temperature 6

(-

95.060 )

=

101.560 deg.'F temperature 7( 101.560 ) =

104.690 deg. F temperature 81('104.690 )

=

temperature 9( 115.180 ) = 115.180 deg..F temperature. 10 ( 117.220 1

= 117.220'deg. F.

82.450.deg. F temperature 11

(-

82.450 );

=

84.170 deg. F temperature 12 ( '84.170 )

=

82.690 deg. F temperature 13 ( 82.690 )

=

' temperature 14 ('.80.900 ).

80.900 deg. F

=

77.610 deg. FE, 0.4685-psia dewpoint 1

( 77.610 ) =

67.090 deg. F, 0.3284 psia devpoint~:2-( 67.090 ); =

80.220 deg. F,-0.5105 psia-dewpoint 3-( 80.220:)

=

84.220 deg. F, 0.5811 psia devpoint 4-

'(

84.220 ) =

82.470 deg. F, 0.5492 psis devpoint -5

. ( 82.470 ) =

73.370 deg. F, 0.4068 psia devpoint 6.

. ( 73.370 ) =-

67.0642 psia pressure -1

( 670642 ) =

67.0643 psia pressure 2

-(

670643 ) =

weighted averages, volume and air mass 89.59280 deg. F temperature'

=

67.06430 psia

=

pressure 0.45135 psia vapor pressure =

volume

=

274000 cu. ft.

=

89692.7 lba dry air mass l-l L-______-__-______-__,_-___

o

( l..

HNP Uniti14988'ILRT/ Pressurization

-dat's set 18 i

time = :800' date = 1129 j

sensor' rav' data' value p.

j temperature.1-( L80.330 )-

80.330 deg. F'

.-]

=-

83.850 deg. F j

temperature' 2 (.

83.850 )-

=

86.180 deg. F;

-l temperature 3( 86.180 )

=

temperature ' 4.(. 89.470.)

s' 89.470 deg. F i

temperature 5( 92.230 )

=.

92.230 deg. F

' temperat ure'.. 6 ( 195.440-)-.=

95.440 deg. F 101.420 deg. F-temperature

7. ( 101.420-)

=

104.'470 deg. F temperature 8 (: 104.470') '=

115.400 deg'.-F

. temperature 9( ~115.400 )

=

temperature 10 ('117.660c) := 117.660 deg. F 82.020 deg. F

' temperature 11 (

82.020.)-

=

83.630 deg. F.

temperature 12 (.83.630.)

=,

82.160 deg. F

-temperature 13 (: 82.160 )

=

-81.280 deg. F temperature'14-( :81.280 )

=

77.940 deg.- F, 0.4737 psia devpoint 1_

( 77.940 )

=

67.310 deg. F, 0.3309 psia Jderpointi~2

-( '67.310-)

=

81.330 deg. F,'O.5293 psia

-devpoint '3

(-

81.330 )

=

84.300 deg. F, 0.5826 psia devpoint

'4-( 84.300 )

=

82.730 deg. F, 0.5539 psia.

. dewpoint 5-(.. 82.730 )

=

73.970 deg. F, 0.4151 psia devpoint 6

( 73.970 )

=-

73.7002 psia pressure l'

(. 737002-)

=

73.7050 psia pressure 2

( 737050 )

=

weighted-averages, volume and air mass 89.49603 deg. F temperature

=

73.70500 psia

=

pressure 0.45925 psia

=

vapor pressure 274000 cu. ft.

volume

=

98641.0 lba dry air mass

=

gx z j

.I

[,. i - ~

r p f t

,< ; p f

4

.BCPDTechnical-Services, Ince '

a Hatch.1988 ILRT. Final Report

- AppendixIII:

L

[., +

>J 4

u..

2

STABILIZATION 4

. DATA SET T

4 p,.'. '

t

,T-l l~

HNP Unit 1-1988 ILRT/ Stabilization DATA

SUMMARY

REPORT d:ta time -date temperature pressure vapor dry air; cat deg F

' psia pressure-mass psia Ibn 1

815 1123 88.4699 174.0705 0.4546 99325.1' 2

830 1129 87.9070

-74.0480 0.4552 99395.9' 3

845 1129 87.6372 74.00571

'O.4548 99388.4 4

900 '1129 87.4584 73.9789.

0.4487-99392.8:

5 915 1129' 87.3277 73.9567 0.4421 99395.5 6.

930' 1129 87.2208 73.9371 0.4358' 99396.9 7

945. 1129-87.1498 73.9175 0.4363

~99382.6 8 1000 1129 87.0680 73.9018.

0.4296 99385.4 9 1015 1129 87.0079 73.8868 0.4307 99374.6 10 1030 1129 86.9505 73.8733-0.4305.

99366.9 11 1045 1129 86.9022 73.8609 0.4338 99354.5 12 1100- 1129 86.8598 73.8492 0.4475 99327.8 13 1115.1129-86.8162

.73.8383 0.4349 99338.0 14-1130 1129.

86.7851 73.8281 0.4283 99338.9 15 1145 1129 86.7601

-73.8192

'O.4330 99325.0

'1 Ei 1200 1129' 86.7325 73.8103 0.4310 99320.7-

'17 1215 '1129 86.7129 73.8021 0.4196 99328.6 18 1230 1129 86.7019 73.8430 0.4317

'99369.5 19 1245 1129 86.6831 73.8241 0.4272 99353.5.

L l

l l

i

J HNPUnit1-1988ILRT/ Stabilization 08.47 b

q i

i h.

.l

=

c LF I

}.

s 86.68 i

i i

i 8151129 FINE 12451129 i

h-

__________m._.--______.____

Unit 1-1988ILRT/ Stabilization f4.87 p.

M P

l S

I A

W W

D 78.89 i-i i

8151129 rig 12451129-i

HNPUnit1-1988ILRT/ Stabilization 993$.

\\_

.~s;...

s s s

s s

h s

's s

L

's

) B-

's iM

's j.

~

s

's s s s

s 99229 I

8151129 TIE 12451129 I

l l

4 1

)

ilNPUnit1-1988ILRT/ Stabilization-85.65 l

1./

L.D A

'y

~

s 1

1 l-l

-6,84 8151129 fIE 12451129 l

HNP Unit 1-1988 ILRT/ Stabilization 81.75 I';

.e 7

r i

l

. sf "

1 f.

.)

l-

[ Al

____j__________________

g 7

l

(.

u L

r 3:

-g,84 I

I I

I 8151129 fIE 12451129

_--.,---____------------_--------------------a-

[2 l.g i

p.

L HNP Unit 1-1988 ILRT/ Stabilization i

data set' 1

time-=' 815:

date = 1129 sensor:

-raw' data

'value I

temperature'!1-(- 80.100 )

=

80.100 deg.'F

.{

temperature 2'(

83.140 l' 83.140 deg. F.

=

temperature--3:(

85.380')

85.380 deg. F

=

~ temperature' 4 ( '88.350 )

=-

88.350 deg. F temperature? 5 (

91.180-)

=

91.180 deg. F temperature 6(. 94.960 ).

94.960 deg.' F

=

temperature :7 ( 100.220 1

=

100.220 deg. F g

Temperature 8.( 103.820 )

103.820 deg. F

=-

temperature.- 9 ('114.560 )

' 114.560 deg. F

=

l.

temperature 10 ( 117.100 )-

=

117.100 deg. F-temperature 11 ( 80.650 )

80.650 deg. F

=

V-temperature.12'( 81.910 )

81.910 deg. F

=

' temperature 13 ( 80.330 )

=

80.330 deg. F

temperature 14-( '80.940 )

80.940 deg. F

=

77.670-deg. F, '.4695 psia-dewpoint-l'

( 77.670 )

=

O

'derpoint' 2

(.70.800 )

=

70.800 deg. F, 0.3729 psia dewpoint' 3

. ('

81.420 )

81.420 deg. F, 0.5308 psia

=

dewpoint 4-

.('

83.330 )

83.330 deg. F, 0.5647 psia

=

dewpoint 5

-(

81.950 )

=

81.950 deg. F, 0.5401 psia

'derpoint 6

( '73.040 )

=

73.040 deg. F,-0.4023 psia.

s pressure 1

'( '740673 )

74.0673 psia

=

pressure 2L

( 740705 )

74.0705 psia

=

weighted averages, volume and air mass temperature

'=

88.46989 deg. F 74.07050 psia pressure

=

0.45456 psia vapor pressure

=

volume 274000 cu."ft.

=

dry air mass 99325.1 lba

=

__________.__.______m.__a

e i

(-

HNF. Unit 1-1988ILRT/ Stabilization data set 2

. time = 830. date = 1129-sensor raw. data value' t

temperature' 1( 79.940')

79.940 deg. F

=

' temperature. 2(

82.950 )

=- 82.950 deg. F temperature.3

('

85.080 )

= '

85.080 deg. F 88.030 deg. F temperature" 4.( -88.030 )

=

90.840 deg. F temperature 5 (

90.840 1

=

temperature' 6 (

94.760 )

=-

94.760 deg. F 99.620 deg. F temperature 7

(-

99.620 )

=

-J temperature 8( 103.660 ).

103.660 deg. F

=

114.270 deg. F temperature 9( 114.270 ).

=

temperature 10 ( 116.900 )

116.900 deg. F'

=

temperature 11 ( 79.930 )

'79.930 deg. F

=-

80.760 deg. F temperature 12 (

80.760 *

=

temperature 13-(. 79.350')

79.350 deg. F

=

80.240 deg. F'

temperature 14 (

80.240 )

=

.derpoint 1

(

78.'280 )

78.280 deg.'F, 0.4790 psia

=

.71.750 deg. F, 0.3852 psia

' dewpoint 2

(

71.750 )

=

dewpoint3

(

80.660 )

80.660 deg. F, 0.-5179 psia

=

82.440 deg. F, 0.5487 psia dewpoint 4

(

82.440 1

=-

81.560 deg. F, 0.5333 psia dewpoint 5

(-

81.560 )

=

73.480 deg. F, 0.4083 psia dewpoint 6 (t 73.480 )

=

74.0454 psia pressure 1

( 740454 F =

. pressure 2-( 740480 )'

74.0480 psia

=

weighted averages, volume and air mass 87.90702 deg. F temperature

=

74.04800 psia pressure

=

0.45524 psia

=

vapor pressure 274000 cu. ft.-

volume

=

99395.9 lbm dry air mass

=

l I

4

..'(-

HNP Unit l-1988 ILRT/ Stabilization

)

datat set 3

. time = 845 date = 1129 sensor-raw data value 79.900 deg. F temperature--11( 79.900 )

=

82.910 deg. F

' temperature. 2 (

82.910 )

=

85.000 deg. F temperature: 3(

85.000 )

=-

87.900 deg. F temperature 4 ('

87.900 )

=

temperature 15 (

90.710.)

=.

90.710 deg. F

. temperature 6'(

94.680.)

's 94.680 deg.'F 99.460 deg. F temperature 7(

99.460')

=-

103.620 deg. F

-temperature 8 (:103.620 )

=

114.180 deg. F temperature. 9-( 114.180

)-

=

116.800 deg. F temperature 10 (.116.800 )

=

temperature'11 ( 79.410 ),=

79.410 deg. F 80.150 deg. F temperature 12 (

80.150 )

=

78.880 deg. F temperature 13 ( 78.880 )

=

temperature 14 ( '79.910

).

79.910 deg. F

=

78.640'deg. F, 0.4847 psic dewpoint 1

( '78.640 )

=

72.900 deg. F, 0.4004 psia dewpoint 2

( 72.900 )

=

79.160 deg. F, 0.4931 psia dewpoint 3

(.79.160 )

=

81.680 deg. F, 0.5353 psia dewpoint 4

(

81.680 )

=

81.100 deg. F,-0.5253 psia dewpoint 5

(

81.100 )

=

74.000 deg. F.,'O.4155 psia dewpoint 6

(-

74.000 )

=

74.0032 psia pressure 1

(-

740032 )

=

74.0057 psia pressure 2

( 740057

).

=.

weighted averages, volume and air mass 87.63718 deg. F

-temperature

=

74.00570 psia pressure

=

0.45480 psia

=-

vapor pressure 274000 cu. ft, volume

=

99388.4 lbm dry air mass l

l i

N 1

L e

L

.HNP Unit 1-1988 ILRT/ Stabilization data set.

4' timeJ=- 900 date = 1129-f '

-sensor r a w'_. da t a value.

temperature 1-(

79.890 )

79.890 deg. F

=

temperature ;2 (

82.910 ).

'82.910 deg..F

=

temperature: 3 (-

84.980 )

=

84.980 deg.'F temperature

,4 ~ ( - 87.~870 )

='

87.870 deg. F 90.680 deg. F temperature 5(

90.680 )

=

94.620 deg. F.

temperature 6

(-

94.620 )

='

99.370 deg..F temperature 7

(-

99.370 )

=.

-temperature 8 (: 103.630 )

=

103.630 deg. F 114.200 deg. F temperature. 9 ( 114.200 )-

=

~116.700 deg..F temperature 10 ( 116.700 ):

=

temperature,11-(- 79.060 )

.79.060 deg. F

=

.79.780 deg. Ff

' temperature 12.(

79.780 );

=

temperature 13 ('

78.540-)

=-

78.540-deg. F i

79.550 deg. F

= temperature 14'(. -79.550 )

=

L dewpoint'~ 1

(

78.290.)

= '

78.290 deg. F, 0.4792 psia 72.580 deg. F, 0.3961. psia dewpoint' 2~

( ~ 72.580 )

=

78.490 deg. F, 0.4823 psia

' dewpoint. 3

. (-

78.490 )

=

81.070 deg. F, 0.5248 psia dewpoint 4'

-(

81.070 )

=

80.660 deg. F, 0.5179 psia dewpoint

.5

(

80.660.)

=

73.730 deg. F, 0.4118 psia dewpoint 6

( ~73.730.)

=

pressure 1.

( 739763')

73.9763 psia

=

73.9789 psia pressure' 2

( 739789 )

=

weighted averages, volume and air mass 87.45841 deg. F temperature.

=

73.97890 psia pressure

=

0.44870 psia vapor pressure

=

volume 274000 cu. ft,

=

99392.8 lbm dry air mass

=

_=__-_____:__' _ - - _ _ - _ _ -..

a 4

lHNP Unit'.1-1988 ILRT/ Stabilization i

data set-4 (W

' time = 915-date'='1129.

i.

sensor.

raw data value-4 4

temperature.1 ? ( '79.900I)=

79.900 deg. F temperature - 2 ( '82.940 )

=: 82.940 deg. F" temperature-3.('

84.980 ); =

84.980 deg.'F.

temperature 4 ( '87.850;).

87.850 deg. F

=

[

~ temperature.5~(

90.680-):

90.680;deg. F

=

.i b

. temperature ~ 6 (L'94.600 )

94.600 deg. F

=

. 99.300'deg. F temperature;.7 (

99.300:)' =

temperature. 8 (1103.670 )

103.670 deg.-F

=

114.180 deg. F l.:-

. temperature.9'(

114.180 )

=

-temperature 10;(t 116.630 )

-116.630 deg. F

=

78.780 deg.~F temperature 11:(. 78.780 )

=

temperature;12;(; 79.510 )

='

79.510 deg.'F' j

-78.300 deg. F.

temperature 13 ( '78.300 )

=-

. temperature 14-( ~79.250 )

=

79.250 deg; F dewpoint 1

~(

78.500'.)

78.500 deg. F, 0.4825 psia

=-

dewpoint' 21

( 73.000 1 173.000 deg. F,;0.4018 psia

=

b Edewpoint 3'

(

78.300 )

78.300 deg. F, 0.4793. psia

=

' dewpoint 4

(-

80.630 )-

80.630 deg. F,7 0.5174 psia

=

80.180 deg. F, 0.5098 psia

dewpoint 5

(: 80.180 )

=

devpoint' 6

-(

72.820 )

72.820 deg. F, 0.3993 psia

=

pressure 1

(;:739541 )

73.9541 psia

=

pressure 2

( 739567-)

73.9567 psia

=

weighted averages, volume and air mass

' temperature 87.32772 deg. F

=

pressure

.=

73.95G70 psia vapor pressure.=

0.44209 psia-volume

=

274000 cu. ft.

99395.5 lba dry air mass

=

?!(.

r

" -HNP' Unit 1-1988:ILRT/ Stabilization dat's set ' 6

time =L 930' date = 1129 sensor

. raw data'

- value

. temperature 1)(. 79.970.)-

79.970 deg. F

=-

temperature 12 ( 82.980;)

82.980 deg. F'

=

s temperature 3j(.. 85.000 )

~

=>

85.000 deg. F' temperature -4'(

87.8701)' =

87.870 deg. F temperature 5( 90.690:)

1=

190.690-deg. F temperature ~-6f(-:94.6001).

.94.600ldeg. F-

=

temperature 7( l99.240 )

=

99.240 deg. F-

temperature: 8( 103.720 )

103.720;deg. F

=-

. temperature. 9 ( 114.200-)- =.,114.200'deg. F-temperature 10 ( 116.560;)':='

temperature 11

(- 78.560L) '

116.560 deg. F.

78.560.deg. F

=

temperature 12.(

79.260 )

79.260 deg. F.

=

temperature 13 (1 78.060 ). =

78.060 deg. F temperature 14 ( 78.970 )

78.970 deg. F

=

dewpoint' 1

( 77.880 )'

=

77.880 deg. F, 0.4727 psia

. dewpoint.

2.

-(-

73.570 )

73.570 deg. F, 0.4095 psia-

=

' dewpoint 3

( 77.990 ):.=

'77.990 deg. F, 0.4745 psia-

-dewpoint 4

(: 80.160-)- =

80.160.deg. F, 0.5095 psia dewpoint 5

'(

80.220 ) ' =

80.220 deg. F, 0.5105 psia dewpoint 6

( 72.070 )

=

72.070 deg.-F, 0.3894 psia ~

pressure 1

( 739346 )

=

73.9346 psia pressure 2

( 739371 )

=

73.9371 psia weighted averages, volume and air mass temperature 87.22079 deg. F

=

73.93710 psia pressure

=

0.'43584 psia vapor pressure

=

volume 274000 cu. ft.

=

99396.9 lba dry air mass

=

l-l 1

l I

-j ;

e i'I

[HNP Unit 1-1988 ILRT/ Stabilization i data set 7

l',

time =~ 945 date = 1129 p

sensor:

raw data' value temperature 1,(

80.070 )

=-

80.070 deg. F temperature 2(

83.020 )

83.020 deg. F

=

temperature 3( 85.050 )

85.050 deg. F

=

temperature 4 ( 87.930 )

=

87.930 deg. F temperature 5( 90.730 )

=

90.730 deg. F temperature -6 ( 94.610 )L =

94.610 deg. F temperature. 7( 99.220 )

99.220 deg. F

=

temperature 8( 103.790 )

103.790 deg. F.

=

temperature 9( 114.240.)'~=

114.240 deg. F temperature 10 (-116.460 )

116.460 deg. F

=

temperature 11 (

78.370.)

=

78.370 deg. F temperature 12 ( 79.070 )

=

79.070 deg. F temperature 13 ('.77.880 )

77.880 deg. F

=

. temperature 14

(~ 78.750

)~

78.750 deg. F

=

.derpoint 1

(-

78.080 )

78.080 deg. F, 0.4759 psia

=

' dewpoint 2

( '74.140 )

74.140 deg. F, 0.4175 psia

=

dewpoint 3

( 77.680 >-

77.680 deg. F, 0.4696 psia

=

79.730 deg. F,'O.5024 psia dewpoint 4

.. 79.730 )

(

=

dewpoint 5

( 79.700 )

=

79.700 deg.

F, 0.5019 psia

' dewpoint 6

( 72.330 )

72.330.deg. F, 0.3928 psia

=

pressure 1

( 739149 )

73.9149 psia

=

pressure 2

( 739175 )

73.9175 psia

=

weighted averages, volume and air mass temperature 87.14977.deg. F

=

73.91750 psia pressure

=

0.43633 psia vapor pressure =

volume 274000 cu. ft.

=

dry air mass

=

99382.6 lba f

(

)

~ _ _ _ _ _ - _ _ _ _ -

m, =w-

--3--------------=-

.~ m ff-(,

1 r,

1 r

NNP-Unit 1-1988 ILR7/ Stabilization'

.v 1

^

e

l

.. i

.8,.

w,': data set' rtime'=2 1000-date = 1129, sensor'

. raw' data

'value.

7 temperature.<1 (.80.'180 ).

=;

80.180'deg. Fr (temperature ~2'(

i83.040 ).=

- 83.040 deg. F-

'= '

85.070 deg.' F-

" temperature. 3 (: '85.070 )

temperature 4 ( L87!930;).

87.930 deg. F

=- '

1 temperature 5'(

90.770 )

90.770 deg. F

=

= '

94.610 deg. F 2 temperature,.6 ( l94.610;)-

~ temperature _7 ( 99.200') :=

99.200 deg.1F temperature - 8 ( 103.820-)

=.:103.820 deg.~-F.

l temperature 9 ( 114.280.): = 114.280'deg.JF

temperature 10 (,116.390 )

= 116.390 deg. F-temperature 111.(- 78.160-)

=

. 78.160. deg. F -

78.860 deg. F

-g

' temperature 12 ('

78.860 )

=

temperature 13.(2 :. 77. 690 ' ) '=

177.690,deg. F l temperature'14

(~

78.540-)' =

78.540 deg. F '-

o?

Ldewpoint!.1:.

78.200 deg. F, D.4778 psia

( 78.200')L

=

(dewpoint 2

( '. 74.760

).

=. T74.760 deg. F, O.4262 psia 3

.' dewpoint : 3

(

_77. 520 : ).

despointL4

(; 79.'270 ):.

-77.520 deg.

F_, 0.4672 psie

=

'79.270 deg. F, O.4949 psia

' dewpoint. 5

(-l79.380 )-

=. ~79.380 deg. F, O.4966 psia;

-.71.280 deg. F,-O.3791 psia

' dewpoint. 6

(

71.~280 3

=.

73.8990.pois pressure 1

( 738990 );

=

pressure 2'

, (.739018 )

73.9018 psia

=

weighted. averages,-volume and.' air mass 87.06803 deg. F temperature

=

73.90180 psia pressure

=

0.42960 psia vapor pressure =

274000 cu. ft, volume

=

99385.4 lba dry air. mass

=

f.

.,,l'-

I'

.m

___m..i_5._..L_.______._

_.._____m_

L l

HNP Unit 1-1988 ILRT/ Stabilization data set

'9-time ='1015 date =-1129 sensor raw data value temperature. 1 ( 80.260 ).

183.100 deg. F 80.260 deg. F

=

2( 83.100 )

temperature ~ 3.( -85.120 )

=

85.120'deg. F-temperature

=

88.040 deg.'F temperature 4( 88.040 ) ' =

temperature 5( 90.810

)-

=.

90.810 deg. F 94.600 deg. F

- temperature;-6 ( 94.600 )

=

temperature 7 ( 99.190 )

99.190 deg. F

=

temperature 8( 103.890 )

103.890 deg. F

=

temperature 9( 114.270.)

114.270 deg. F

=

temperature:10 ( 116.270 1-116.270 deg. F

=

temperature 11'(

77.'990 )

77.990 deg. F

=

temperature 12 (

78.690.)

78.690 deg. F

=

temperature'13 ( 77.530 1 77.530 deg. F

=

temperature 14 (.

78.370 )

=

78.370 deg. F'

' dewpoint -1

( '77.780 )

=

77.780 deg. F, 0.4712 psia dewpoint 2-( 75.110 )

=

75.110 deg. F, 0.4312 psia dewpoint 3

(-

77.410.)

=

77.410 deg. F, 0.4655 psia despoint 4

( 78.950 )

=

78.950 deg. F, 0.4897' psia 79.050 deg. F, 0.4913 psia dewpoint 5

(

79.050-)

=

dewpoint 6

( 71.700 )

=

71.700 deg. F, 0.3845 psia pressure 1

( 738846 )

=

73.8846 psia pressure 2

( 738868 )

73.8868 psia-

=

weighted averages, volume and air mass 87.00792 deg. F temperature.

=

73.88680 psia pressure

=

0.43065 osia vapor pressure.

=

volume

=

274000 cu. ft.

dry air mass 99374.6 lbm

=

l u

o l

)

i J

_-------,-------__----------u--

---,---,-_---1.--a-

i 7

i

.i m

1 HNP' Unite 1 1988 ILRT/ Stabilization data wet $.liOI

. time = 1030 date =:1129 b sensori

!rav data value

, temperature'c1 (

.80.340')

s' 80.340fdeg. F Temperature 2?(

83.140').=:

83.140 deg. F'

=

- 85.170 deg. F Temperature 3( 85.170;):

. temperature 4;(- 88.100 ): =

88.100'deg. F

[

-temperature,5 ( 90.890')1 90.890 deg. Ff

=

. temperature 1 6 ( 194.610 ):

94.610 deg. F

=

temperature ;7L(' 99.190!);.=. '.99.190 'deg. F-0

. 103.970'deg.7F-temperature 8!().103.970 )

=.

Temperature'.9 ('114.3001); =' 114.300 deg. F-temperature 10 ( 116.140 ) ~".: 116.140 deg. F

~

=

- L

772830ldeg. F temperature 11-(;'77.830 )

=

' temperature 12 ( 78.510.)

=

- 78.510ldeg. F:

temperature;13

(-

. 77. 370 ; )'

77.370 deg. F.

='

1

. temperature 14

(-

78.190.). '=. -78.190,deg. F i

l'-

('-77.740.)

77.740 deg.: F','0.4706. psia:

sdewpoint

=.

.. dewpoint 2L

( L75.550 )

=:

75.550 deg. F, 0.4376 psia-dewpoint 3

'(

'77.120 )

=

. 77.120'deg. F,-0.4610 psia:

despoint ;4

-(.

78.660 ):

78.660_deg. F, 0.4850 psia

=-

dewpoint 5

( '78.840:)

=

78.840 deg. F=,,0.4879 psia dewpoint.L6'

(~

71.820 )

=

71.820 deg. F, 0.3861 psia pressure 91(

( 738708 )

=

73.8708 psia 73.8733 psia pressure 2

.(

738733 )

=

weighted averages,. volume and air mass

. temperature 86.95053 deg..F

=

pressure

. 73.87330 psia

=

0.43050 psia vapor pressure

=

-volume

=

274000 cu._ft.-

4 99366.9 lbe

. dry air mass

=

L m

a 1

i i

l 1

4 i

h. s.

'HNP Unit 1-1988 ILRT/ Stabilization

-data. set 11

. time = 1045 date = 1129 sensor.

rev' data value temperature l'('

80.4'10 ).

-80.410 deg. F

=

83.200 deg. F temperature 2( 83.200 )

=

l temperature _3 ( '85.230 )

85.230 deg. F

=

-+*mperature 4(

88.150 )

88.150 deg. F

=

~.emperature 5( 90.950 )

90.950 deg. F

=

94.650 deg. F

-temperature 6( 94.650 )

=

. temperature 7( 99.200 )'

99.200 deg. F

=

. temperature 8 ( 104.030 )

104.030 deg. F

=

114.310 deg. F temperature 9( 114.310.)

=

116.010 deg. F temperature 10 ( _116.010 )

=

temperature 11 ( 77.670 )

=~

77.670 deg. F temperature 12 ( 78.360 ) ' =

78.360 deg. F

. temperature 13 (

77.230')

77.230 deg. F

=

temperature 14-(- 78.040 )

=

78.040 deg. F dewpoint 1-

-(

'78.010-)

=.

78.010 deg. F, 0.4748 psia dewpoint 2

('

75.640 )

75.640 deg. F, 0.4389 psia

=

derpoint 3

( 76.980 )

76.980 deg. F, 0.4589 psia

=

78.360 deg.

F, 0.4803 psia dewpoint 4

. (

78.360 1.

=

78.570 deg.

F, 0.4836 psia dewpoint 5

( 78.570 )

=

72.480 deg.

F, 0.3948 psia dewpoint 6

(

72.480-).=

'l 73.8585 psia pressr e 1

( 738585 )

=

73.8609 psia pressure 2

( 738609 )

=

weighted averages, volume and air mass 86.90223 deg. F temperature

=

73.86090 psia pressure.

=

0.43381 psia vapor pressure

=

274000 cu. ft.

4 volume

=

99354.5 lbm l

dry air mass

=

l 1

2 l

l 1

y l@..

s m

e~~~

q)

+ ',.

HNP Unit'l-1988 ILR7/ Stabilization-Idata set"'.12 1 Itime. =.'1100 ~

date:=L11291

'i

_ sensor :.

. raw data' value 80.470 deg. F

temperature; 1 (

80.470 )

-=

temperature :2 (3 83.250 )'

83.250 deg. F-

=

' temperature - 3>(;-85.290;).'=

85.290 deg. F 88.230 deg.:F temperature (4.( 188.230')-

' '91.030 deg. F

=-

temperature 5 m (: 91'.030.)

=

temperature,6 ( '94.660

)~

94.660 deg.-F

=

, temperature 7

(- 99.210.): 1=-

99.210'deg. F

104.090 deg. Ff temperature 8;( -104.090.)'

=

temperature,' 9 -. ( 114.340

);~=~

114.340ldeg F.-

._ temperature 10.(.115.900.L).= 115.900 deg. F temperature.11-(-.77.540 )

s'

_77.540 deg. F Temperature 12L(, 78.190 1-

=,

78.190.deg. F temperature.13_(.77.~110 ). = -

77.110_deg. F temperature l14i(

77.900-_)

177.900 deg. F.

=.

'devpointi.1

-(

.- 77. 940. )

77.940 deg.

F.,

O.4737 psia-

=-

dewpoint 2-

'('.75.810 )

75.810 deg.~F, O.4414 psia

=

, dewpoint: 3-(f 76.740 )- ' =

76.740 deg. F,. O.4553 psia 78.140 deg. F, O.4768 psia

. dewpoint 4-

-(.

78.'140 )'

'=-

.78.440 deg. F,.O.4815 psia

_ dewpoint 5

.(

-78.440 ) ' =

74.830 deg. F,. O.4272 psia.

dewpoint-6-

(. -_74. 830 - )

=

73.8467 psia pressure 1

-(-

738467 )

=

-73.8492 psia pressure 12

(

736492 )

=

weighted averages,. volume and air-mass 86.85984 deg. F temperature'

=

-73.84920 psia

-pressure.

=

vapor pressure = '

0.44751 psia

-274000 cu. ft.

volume

=-

99327.8 lba dry air mass

=

N gg W

gp w

r a

i e

o.,

HNP! Unit 11-1988'ILRT/ Stabilization A dhts.seti 13 j

time = 1115

? date~ '= L1129 :

n

. sensor

. rav: data value-O^

. temperature 1 (L;80.540')- ' =-

80.540 deg..F-

=.

temperature.~2 (.

83.- 300 - ) -

83.300'deg. F

. temperature 113 ( '85.3507)~:=L. 85.350 deg.

F--

3l temperature 4' ( -88.350'):

88.350'deg. F

=

Temperature 6.( '94.680.). = '

91.090 deg.2 F'

~

. temperature 5i(

91.090~). * ~

94.680 deg. F-

-7

. temperature' 7.(

99.220.)

" 99.220.deg. F-

=

=. temperature. 8 (:104.130 )

=. 104.130 deg. F:

temperature 1 9 (:114.340 );

114.340 deg. F

='

temperature.10-( 115.760;)

115.760'deg. F

=

temperature 11 ('

77.400')'

=

- 77. 400 deg. F.

,e,

i emperature 12 _(: 78.040 )'

. 78.040 deg. F' t

=-

temperature 13-('

76.980 ).= ~ 76.980 deg. F temperature ~14'( '77.760:). =

77.760 deg.LF.-

e

~

77.730 deg..F", 0.4704 psia.

sdewpoint.'1-( :77.730 ).= ' ' 76.100 deg. F. 0.4457 psia dewpoint 2 (fq76.100-).

76.750.deg. F, 0.4554l psia

' =

idewpoint.

3-( 76.750;)

=

dewpoint. 4

-(

77.920 ).=

. 77.920 deg. F, 0.4734 psia dewpoint 5-( 78.170 ).

=.

78.170'deg. F, 0.4773 psia dewpoint 6

(. 72.9201)'

72.920 deg. F,n0.4007 psia

=

. pressure 1.

(

738359 )

=

- 73.8359 psia 73.8383 psia

,= pressure 2-(- 2 738383 )

=

.- o tweighted' averages, volume and air mass l

temperature.

86.81622 deg. F.

=

73.83830 psia pressure

=-

0.43494 psia

=

vapor pressure i.c

. volume

=;

.274000 cu. ft.

H dry.mir mass 99338.0.1be

=

p.

i-l 1:

[.'

l:

1

'U HNP Unit 1-1988 ILRT/ Stabilization

.i

. data set. 14'

'l Ltime =L1130 date = 1129 sensor

rav data value temperature 1

(.

80.610 )

=

80.610 deg. F temperature 2(

83.370 )

83.370 deg. F

=

temperature 3( 85.420 )

85.420 deg. F

=

temperature 4 ( 88.400 )

88.400 deg. F

=

temperature.5'(

91.160 ) -=.

91.160 deg. F temperature ~ 6( 94.710 )'

'94.710 deg. F

=

. temperature. 7(

99 230 )

99.230 deg. F

=

temperatu:e 8( 104.210-)

104.210 deg. F

=

temperature 9( 114.320

)-

114.320 deg. F

=

temperat'ure 10 ( 115.630 )

115.630 deg. F

=

temperature 11

(.

77.280 )

77.280 deg. F

=

temperature 12 ( 77.910 )

77.910 deg. F

=

temperature 13 ( 76.890 )

's 76.890 deg. F temperature 14 (. :.77. 650

).

77.650 deg. F

=

dewpoint 1

(

77.640-)

=

77.640 deg.'F, 0.4690 psia dewpoint-2

(-

76.060 )

=

76.060 deg. F, 0.4451 psia dewpoint 3

( 76.580

).

76.580 deg. F, 0.4528.psis

=

dewpoint 4

( '77.690 )

=

77.690 deg. F,.0.4698 psia dewpoint 5-( 78.020 )

=

78.020 deg. F, 0.4749 psia

' dewpoint 6

( 72.010 )

72.010 deg.

F.,

0.3886 psia

=

pressure 1

( 738259

)-

73.8259 psia

=

pressure-2

( 738281-)

73.8281 psia

=

weighted averages, volume and air mass temperature 86.78506 deg. F

=

73.82810 psia pressure

=

0.42828 psia vapor pressure

=

volume

=

274000 cu. ft.

dry air mass

=.

99338.9 lbm

[.

A HNP Unit 1-1988 ILRT/ Stabilization ~

p data set 15

-time = 1145-date = 1129 sensor.

rav'dnta value temperature l' (

80.680 )

=

80.680 deg. F

. temperature 2(.83.430 )

=

83.430 deg. F

' temperature. 3(

85.480 )

temperature. 4 (

88.460 )

= '

85.480 deg. F.

=

88.460 deg. F temperature 5(

91.250 )-

91.250 deg. F

=

temperature l6 ( 94.740 )

94.740 deg. F

=

temperature

'7 ( 99.250 ).

99.250 deg.'F

=

temperature 8-( 104.280

).

104.280 deg. F

=

temperature 9( 114.320 )

=

114.320 deg. F temperature 10 ( 115.510-)

=

115.510 deg. F temperature 11 ( 77.180 )

=

77.180 deg. F temperatur>? 12 (

77.800 )

=

77.800 deg. F temperature 13 (

76.790 )

=-

76.790 deg. F' temperature 14 ( 77.540 )

77.540 deg. F-

=

dewpoint 1-(

77.700 ')

77.700 deg.:F, 0.4699 psia

=

dewpoint 2

(

76.350 )

76.350 deg. F, 0.4494 psia

=

dewpoint 3

( 76.610 )

=

76.610 deg. F, 0.4533 psia dewpoint 4

( 77.560 )

77.560 deg. F, 0.4678 psia

=

dewpoint 5

( 77.960 )

77.960 deg. F, 0.4740 psia

=

dewpoint 6

( 72.740 )

72.740 deg. F,;0.3983 psia

=

pressure 11

( 738165 )

73.8165 psia

=

pressure 2

(

738192 )

=

73.8192 psia weighted averages, volume and air mass temperature 86.76006 deg. F

=

73.81920 psia pressure

=

0.43298 psia vapor pressure

=

volume

=

274000 cu. ft.

99325.0 lbm dry air mass

=

..)"

s

a. i,i HNP_ Unit:1-1988 ILRT/ Stabilization

datalset. 16 timef= 1200 date = 1129 sensor:

' raw data value temperature; 1 ( 80.750 )

80.750 deg. F-

=

temperature 2( '83.490 )

83.490 deg. F

=

temperature 3-( -85.560-): =

85.560 deg. F temperature 4-(.

88.540 ). =

88.540 deg..F'

temperature ~' 5'('"91.330')~ =

91.330 deg. F temperature-6 (~-94.740')

='

94.740 deg. F

~

temperature 7- (_ '99.270 )

=

99.270 deg. F temperature 8 ( 104.330 )

n 104.330 deg.-F

=

. temperature. 9.(-114.320

);'=

114.320 deg. F temperature 10 ( 115.360 ) -=

115.360 deg. F

. temperature 11 ( 77.070,)

77.070 deg. F

=

temperature 12,(

77.670 )

=,

77.670 deg. F temperature 13'(

76.710

)-

=.

76.710 deg. F temperature 14-(: '77J440')

=

77.440 deg. F dewpoint-1

('

77.800 )

=

77.800 deg.' F, 0.4715 psia dewpoint 2

( -76.410 )

=

'76.410 deg. F, 0.4503 psia dewpoint 3

( 76.500 )

=

'76.500 deg. F, 0.4516 psia dewpointf 4

( '77.380 l' 77.380 deg. F, 0.4350 psia

=

dewpoint 5

( 77.830 )

=

77.830 deg. F, 0.4720 psia dewpoint 6

( 72.490 )

72.490 deg. F, 0.3949 psia

=

pressure l'

(-

738076 )

73.8076 psia

=

pressure 2

( 738103 )

73.8103 psia

=

weighted averages,. volume and' air mass 86.73246 deg. F temperature

=

73.81030 psia pressure

=

0.43100 psia vapor pressure =

volume 274000 cu. ft.

=

dry air mass

=

99320.7 lbm i

l 1

I l

l 1

__________________._a

j HNP Unitil-1988'ILRT/ Stabilization

'l data set 17 i

Ltime = 1215' date'= 1129 L

sensori raw data'.

value temperature 1)(

80.810 )

=

80.810 deg.' F'

temperature 2(

83.540 )

'83.540 deg.:F

=

temperature 3.( ;85.620'). ='

85.620 deg. F temperature 4:( 188.620 )

88.620 deg.'F

=

-temperature. 5

(.

91.410 )-

91.410 deg.' F

='

temperature 6

(-

94.790.)

94.790 deg..F

=

temperature 7 (: 99.290-).= '

99.290 deg. F' temperature 8( 104.400 ) ' =

104.400 deg. F temperature' 9( 114.270.)'

114.270 deg. F

=

temperature 10 ( 115.330 )

115.330 deg. F

=

temperature 11.(

76.980 )

=

76.980 deg. F temperature 12 ( 77.560 ).~=

77.560 deg. F temperature 13 ( 76.610 l' 76.610 deg. F.

=

temperature 14 ( '77.360 )c 77.360 deg. F

=

dewpoint 1

( 77.860 )

=

77.860'deg. F, 0.4724 psia dewpoint, 2

(.

76.470.)

76.470 deg. F,-0.4512 psia

=

. dewpoint' 3

(

76.390 )

=

76.390 deg. F, 0.4500 psia dewpoint.4

( 77.300 )

=

77.300 deg. F, 0.4638 psia dewpoint-5

-(

77.750 )

77.750 deg.' F, 0.4707 psia

=

dewpoint 6

('

70.590 )

=

70.590 deg. F,.0.3703 psia pressure l'

( 738030 )

73.8030 psia

=

pressure 2

(' 738021-)

=

73.8021 psia weighted averages, volume and air mass temperature 86.71293 deg. F

=

73.80210 psia-

. pressure

=-

0.41957 psia vapor pressure

=

volume 274000 cu. ft.

=

dry air mass

=

99328.6 lbm

_-___a

L.

l HNPUnitk-1988ILRT/ Stabilization sj s

L-i

/ data set' 18 1

-time = 1230

-date = 1129 L

sensor raw data value temperature' 1(

80.880 )

=

80.880 deg. F

- temperature 2 (.

83.620')

=

83.620 deg. F temperature 3:(- 85.710 )

85.710 deg. F

=

t-

. temperature :4:(-.88.740 )

=

88.740 deg. F temperature.

5'('

91.500')

91.500 deg. F

=

temperature 6(.-94.860 )

94.860 deg. F

=

temperature _ 7 (. 104.470 )

99.220 )'

99.220 deg. F

=

temperature 8(

=

104.470 deg. F

- temperature '9 ( 114.230-)~

114.230 deg. F-

=

temperature 10.( 115.270:)-

115.270 deg. F

=

-temperature 11 (

76.910 1-

=

76.910 deg. F

. temperature 12 ( 77.470 )

=

77.470 deg. F temperature 13 (

76.550 )

=

76.550 deg. F temperature 114-(- 77.270 ) ' =

77.270 deg. F dewpoint 1

(

77.760 )

77.760'deg. F, 0.4709 psia

.=

dewpoint 2

(

76.570-)

-76.570 deg. F, 0.4527 psia

=

dewpoint 3 76.260 )

=

(.

76.260 deg. F, 0.4481 psia dewpoint 4-(-

77.200

).

77.200 deg. F, 0.4622 psia

=

. dewpoint 5

-(

77.630.).=

77.630 deg. F, 0.4689 psia dewpoint 6

( 72.760 )

72.760 deg. F, 0.3985 psia

=

l pressure 1

( 738435-)

.73.8435 psia

=

pressure 2 i 738430 )

73.8430 psia

=

weighted averages, volume and air mass

. temperature 86.70193 deg. F

=

73.84300 psia

. pressure'

=

0.43172 psia vapor pressurt

=

volume 274000 cu. ft.

=

99369.5 lbm dry air mass

=

~

HNP Unit'1-1988 ILRT/ Stabilization.

, data set 19.

time =-1245 date = 1129 sensor.

raw data value 80.940 deg..F Temperature 1

(~

80.940 )

=

83.670 deg. F temperature 2( 83.670 )

=

85.770 deg. F.

temperature 3'(

85.770 )

=

temperature 4

(-

88.810 )

88.810 deg. F

=-

91.570 deg. F temperature 5( 91.570 )

z.

94.850 deg. F temperature 6 ( ;94.850

).

=

temperature 7( 99.320

).

99.320 deg. F

's 104.520 deg. F temperature 8( 104.520.)

=

temperature 9( 114.170 1

= 1114.170 deg. F 115.110 deg.- F.

temperature 10 ( 115.110 )'

=

76.820-deg. F temperature 11-(

76.820 )

=

77.390 deg. F temperature 12_(

77.390 ).

=

76.470 deg. F temperature 13 ( 76.470 )

=

77.190 deg. F-temperature.14 ( -77.190 ).

=

77.950 deg. F, 0.4738 psia dewpoint 1

( 77.950 )

=

76.890 deg. F, 0.4575 psia dewpoint 2

( 76.890 ),

=

76.410 deg.

F.,

0.4503. psia dewpoint 3

( 76.410 )

=

77.060 deg. F, 0.4601 psia dewpoint 4 t 77.060 l'

=

77.590 deg. F, 0.4682 psia dewpoint 5

(

77.590.)

=

71.860 deg. F, 0.3866 psia dewpoint '6

(

71.860 )

=

73.8242 psia pressure 1

( 738242 )

's pressure 2 t 738241 )

73.8241 psia

=-

weighted averages, volume and air mass 86.68314 deg. F-temperature

=

73.82410 psia-pressure

=

0.42718 psia

=

vapor pressure 274000 cu. ft.

volume

=

99353.5 lba dry air mass

=

1 r

1 l

l 1

l

c BCP Technical' Services', Inc.

Hatch 1988 ILRT Final Report Appendix III TEST DATA SET I

1 l

1 1

l'.

1

.. (.

-HNP Unit 1-1988 ILRT/ Test t

DATA

SUMMARY

REPORT d to;ltise.'date temperature pressure vapor dry air set-deg F-psia- ' pressure

. sass-psia.

Ibs 21 1245 1129-86.68311 73.8241 0.4607

^99308.1 2 1300 1129

'86.6613'

'73.8157

-0.4607 99300.81 3 1315 1129-86.6313 73.8085 0.4590-99298.7-

'4. 1330:.1129

'86.6130-73.8020 0.4591' 99293.1 5 :1345.1129 86.5966

.73.7954 0.4588 99287.5 6.1400 1129 06.5844 73.7891 0.4591

'99280.8.

7 J1415. 1129 86.5718

'73.7836-0.4579-99277.3

,8' 1430 1129

'86.5644 73.7780 0.4575 99271.5-s 9' 1445 1129-

'86.5497 73.7725 0.4582:

99265.9' 10 1500 1129'

'86.5436

'73.7678 0.4580' 99260.8 11 1515 1129 86.5322 73.7629 0.4585 99255.6 12 -1530- 1129

'86.5288' 73.7583 0.4587 99249.8 13 1545-1129 86.5219 73.7538-0.4591 99244.4

'14. 1600' 1129-

'86.5206 73.7493 0.4585.

99239.3

15-1615 1129-

-86.5160 73.7456 0.4595 99233.8 16 1630- 1129-86.5129-73.7417-

-0.4596' 99229.0 17 1645 1129-86.5042 73.7380 0.4587 99226.7

'18' 1700 1129 86.5057 73.7340 0.4595 99220.0 19 1715 1129

'86.5141 73.7301 0.4606:

99211.7-20' 1730' 1129 86.5089 73.7267.

0.4608 99207.8

.21-1745L11129

.86.5114 73.7232 0.4616-99201.5 22 1800 1129 86.5041-73.7197 0.4609-99199.0

-23 1815 1129' 86.5064 73.7163 0.4606i 99194.4

24 1830.1129 86.5058 73.7130 0.4611 99189.3 25 1845 1129 86.5030 73.7099 0.4621 99184.4 26 1900' 1129 86.5117 73.7067 0.4620 99178.5 27 1915 1129' 86.5169 73.7036 0.4623 99173.0 3'28 1930 1129g 86.5092 73.7005 0.4623 99170.2 29 1945 1129-

'86.5194

'73.6978 0.4627 99164.1 30 2000 1129 86.5158 73.6949 0.4629 99160.6 31 2015 1129 86.5168 73.6918 0.4624 99156.9 32 2030 1129 86.5224 73.6893 0.4624 99152.5

'33 2045 1129 86.5330 73.6863 0.4642 99144.1 l'

l

'HNP Unit'1-1988 ILRT/ Test-TREND REPORT leakage rates total. time.

mars point

. dr.to time date elapsed measured leakage uc1 leakage

uc1,

. c;t "

time rate rate-rate

' rate rate thrs).

(%/ day)'

(%/ day)-

(%/ day)

-(%/ day)

~1 1245 1129 0.00=

0.0000 0.0000 0.0000 0.0000 0.0000 2 1300. 1129-0.25 0.7151.

0.7151 0.7151 0.7151 0.7151 3 1315 1129 0.50 0.4576 0.4576 0.4576 0.4576 1.7298 4 1330 '1129 0.75 0.4851 0.4376 1.7538 0.4566 0.6523 5' -1345 '1129 1.00 0.4979 0.4453 1.0190

'O.4724 0.5652U 6 '1400 1129' 1.25 0.5288 0.4704 0.8823 0.5025 0.5690

-7 1415 1129-1.50 0.4972 0.4686-0.7828 0.4959 0.5409 8 1430 1129

-1.75 0.5055 0.4726 0.7355 0.4980 0.5305 9 1445 1129 2.00 0.5106 0.4779 0.7082 0.5023 0.5272

.10 1500 1129 2.23 0.5083 0.4810.

0.6873 0.5037-0.5233 11' 1515 1129

'2.50 0.5080 0.4835 0.6714 0.5046 0.5204 12 1530 1129 2.75 0.5126 0.4870 0.6610 0.5072 0.5205 13 '1545 1129 3.00 0.5136 0.4901 0.6527 0.5093 0.5207 14 1600 1129' 3.25-0.5117 0.4921 0.6449 0.5101 0.5197 15' 1615 1129 3.50 0.5136.

0.4942 0.6389 0.5113 0.5197 16 1630 1129 3.75 0.5104 0.4952 0.6326 0.5110 0.5184 17 1645.1129-4.00' O.4921 0.4920 0.6226 0.5052 0.5139

, - 18 1700 1129

'4.25 0.5012 0.4914 0.6163 0.5035 0.5114 19 1715 1129 4.50 0.5182 0.4944 0.6152 0.5071 0.5150 20 1730 1129 4.75 0.5107 0.4955 0.6120 0.5079 0.5150 21 1745-1129 5.00 0.5157 0.4975 0.6102 0.5097 0.5165 22-1800 1129 5.25-0.5026 0.4968 0.6058 0.5080 0.5143 23 1815' 1129 5.50 0.4997 0.4958 0.6013 0.5059 0.5120 24' 1830 1129 5.75 0.4994 0.4949 0.5973 0.5042 0.5100 25 1845 1129 6.00 0.4986 0.4940 0.5936 0.5026 0.5082

-26 1900 1129 6.25 0.5013 0.4937 0.5906 0.5019 0.5071 27 1915 1129 6.50 0.5026 0.4937 0.5882 0.5016 0.5064 28 1930~ 1129 6.75 0.4939 0.4924 0.5846 0.4996 0.5045 29 1945-1129 7.00 0.4972 0.4918 0.5819 0.4986 0.5033 13 0 2000 1129 7.25-0.4918 0.4905 0.5786 0.4968 0.5015

31. 2015 1129 7.50 0.4874 0.4889 0.5751 0.4945 0.4994 32 2030 1129 7.75 0.4853 0.4872 0.5716 0.4922 0.4973 33 2045 1129 8.00 0.4957 0.4870 0.5698 0.4920 0.4968

?

i

_a

n.tr.

n

.:f HNP Unit 1-1988 ILRT/ Test:-

l'

' TOTAL TIME LEAXAGE RATE REPORT:

idit3L: time: dateL elapsed-dry air imeasured leakage uc1

c;t,,

time mass

-rate rate rate (hrs)-

(Ibs).

(%/ day)

(%/ day)~

~1-1245 1129 0.00:

99308.l.

.0.0000-0.0000 0.0000 2 1300 1129 0.25

'99300.8 0.7151 0.7151 0.7151 3.1315 1129-0.50 99298.7'

0.4576 0.4576 0.4576 4 1330 1129-0.75 99293.1 0.4851 0.4376-1.7538 5 1345 1129 1.00:

99287.5 0.4979 0.4453 1.0190 6-1400. 1129 1.25 99280.8 0.5288

'O.4704 0.8823' 7 1415 1129' 1.50.

99277.3 0.4972.

0.4686 0.7828 8; 1430 1129 1.75

'99271.5 0.5055 0.4726 0.7355-9 1445. 1129 2.00 99265.9-0.5106 0.4779 0.7082 10- 1500: 1129'

.2.25 99260.8 0.5083 0.4810 0.6873

.11 1515 1129; 2.50 99255.6 0.5080 0.4835 0.6714

.12 1530 1129!

2.75 99249.8 0.5126 0.4870 0.6610

.13-1545 1129 3.00 99244.4 0.5136 0.4901-0.6527-14 1600 ~1129 3.25 99239.3 0.5117 0.4921 0.6449 15 '1615 1129 3.50 99233.8 0.5136 0.4942 0.6389 16 1630 1129 3.75.

99229.0 0.5104 0.4952 0.6326 17' 1645 1129 4.00 99226.7 0.4921 0.4920 0.6226

' 18 - ),700 1129 4.25 99220.0

~0.5012 0.4914 0.6163-

19. 1715.1129~

'4.50 99211.7.

0.5182 0.4944 0.6152 20 1730 1129 4.75 99207.8 0.5107

-0.4955 0.6120

~21 1745 1129 5.00 99201.5 0.5157 0.4975 0.6102-22 1800 1129 5.25 99199.0 0.5026 0.4968 0.6058 23 1815 1129 5.50 99194.4 0.4997 0.4958 0.6013 1830 1129 5.75 99189.3 0.4994 0.4949 0.5973-25 1845 1129 6.00 99184.4 0.4986 0.4940 0.5936 26 1900 1129 6.25 99178.5 0.5013 0.4937 0.5906

27 1915 1129 6.50 99173.0 0.5026 0.4937 0.5882

.28 1930 1129 6.75 99170.2 0.4939 0.4924 0.5846

-29 1945 1129-7.00 99164.1 0.4972 0.4918 0.5819 30 2000 1129

-7.25 99160.6 0.4918 0.4905 0.5786 31 2015 1129 7.50 99156.9 0.4874 0.4889 0.5751 32 2030 1129 7.75 99152.5 0.4853 0.4872 0.5716 33 2045 1129 8.00 99144.1 0.4957 0.4870 0.5698 Allowable leakage rate, La =

1.2000 %/ day 75% La 0.9000 %/ day

=

Total time leakage rate 0.4870 %/ day

=

Total time UCL 0.5698 %/ day

=

HNP Unit 1-1988 ILRT/ Test MASS POINT LEAKAGE RATE REPORT j

j data time date elapsed dry air leakage uc1 j

set time mass rate rate

{

(hrs)

(1bm)

(%/ day)

(%/ day) 1 1245 1129 0.00 99308.1 0.0000 0.0000 2 1300 1129 0.25 99300.8 0.7151 0.7151 3 1315 1129 0.50 99298.7 0.4576 3.7298 4 1330 1129 0.75 99293.1

'O.4566 0.6523 5 1345 1129 1.00 99287.5 0.4724 0.5652 6 1400 1129 1.25 99280.8 0.5025 0.5690 7 1415 1129 1.50 99277.3 0.4959 0.5409 8 1430 1129 1.75 99271.5 0.4980 0.5305 9 1445 1129 2.00 99265.9 0.5023 0.5272 10 1500 1129 2.25 99260.8 0.5037 0.5233 11 1515 1129 2.50 99255.6 0.5046 0.5204 12 1530 1129 2.75 99249.8 0.5072 0.5205 13 1545 1129 3.00 99244.4 0.5093 0.5207 14 1600 1129 3.25 99239.3 0.5101 0.5197 15 1615 1129 3.50 99233.8 0.5113 0.5197 16 1630 1129 3.75 99229.0 0.5110 0.5184 17 1645 1129 4.00 99226.7 0.5052 0.5139 18 1700 1129 4.25 99220.0 0.5035 0.5114 19 1715 1129 4.50 99211.7 0.5071 0.5150 20 1730 1129 4.75 99207.8 0.5079 0.5150 21 1745 1129 5.00 99201.5 0.5097 0.5165 22 1800 1129 5.25 99199.0 0.50B0 0.5143 23 1815 1129 5.50 99194.4 0.5059 0.5120 24 1830 1129 5.75 99189.3 0.5042 0.5100 25 1845 1129 6.00 99184.4 0.5026 0.5082 26 1900 1129 6.25 99178.5 0.5019 0.5071 27 1915 1129 6.50 99173.0 0.5016 0.5064 28 1930 1129 6.75 99170.2 0.4996 0.5045 29 1945 1129 7.00 99164.1 0.4986 0.5033 30 2000 1129 7.25 99160.6 0.4968 0.5015 I

31 2015 1129 7.50 99156.9 0.4945 0.4994 32 2030 1129 7.75 99152.5 0.4922 0.4973 33 2045 1129 8.00 99144.1 0.4920 0.4968 Allowable leakage rate, La =

1.2000 %/ day 0.9000 %/ day l

75% La

=

0.4920 %/ day i

Mass point leakage rate

=

0.4968 %/ day Mass point UCL e

l I

l l

HNP Unit 1-1988 ILRT/ Test l6.68 W

d-e.

.9

'y N

g 12451129 IINE 29451129 I

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W I

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i 12451129 TIE 29451129

\\'

HNP Unit 1-1988 IIAT/ Test 9,6 W

D p

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1 I

I 26 1129 TIME 2 M H29

HNP Unit 1-1988 ILRT/fest d9398 s s s s

s

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s x

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's. s s

's

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1245 1129 TIME 20451129 1

1

i HNPUnit1-1988ILRT/ Test

)

8.73

)

1

/.

y A

y W

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I I

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1245 1129 TIE 2945 1129 4

1 l

HNPUnit1-1988ILRT/fest

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}.

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p A

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Ik -

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I i

i i

12451129 FINE 2945 1129 i

e 16 f

i, i-HNP..UnitL1-1988 ILRT/ Test:

- data - set i 1'

V itime:= 1245 ;date =:1129

~

sensor-raw data'.

value m

. temperature L2-(< 83.670-)

. 80.940 deg. F

,; temperature; 1:( 80.940"L =.

83.670'deg.~ F

=

Temperature; 3 ( ;85.770 )

!=.

65.770 deg. F 88.810 deg. F W

-temperature E4 ('

88.810 )-

=

temperature-'5-(

91~.570 T =

91.570 deg. F

. temperature "6-(..94.850 ).=-

94.850 deg.:F-temperature 7 (i.99.320-)? =. 99.320 deg. F 104.520 deg. F temperature 8J( 104.52011.

=

t Temperature 9 (:114.170 ):

114.170 deg. F

=

_115.110 deg. F.

temperature 10 (:115.110')

=

.76.820 deg. F

!i (temperature 11<( 76.820:)

=

77.390 deg. F temperature 12~(' 77.390 )

=

temperature 13.(

76.470 L 76.470 deg. F.

=

77.190 deg. F-temperature 14_(

77.190 )

=-

1

.77.950 deg. F,.0.4738 psia dewpoint 1

. (?'77.950 )

=

176.890 deg. F, 0.4575 psia dewpoint 2

(; 76.890

)-

=

76.410 deg. F, 0.4503 psia dewpoint 3

>!.l76.410,).

=-

77.060 deg. F, 0.4601 psia dewpoint 4

( 77.060 )

=

dewpoint 5.

(.77.590-)1 =

77.590 deg.'F, 0.4682 psia

-71.860 deg.

F.,

0.3866 psia dewpoint' 6

( 71.860 )

=-

. pressure 1-

.( -738242 )

=' 73.8242 psia 73.8241. psia pressure.2

'(

738241 )

=

weighted averages, volume and air mass-86.68314 deg.fF-temperature.

=

73.82410 psia

=

pressure 0.42718 psia i

vapor pressure =

volume

=

274000 cu. ft.

99353.5 lbm dry air mass

=

?

1

p i

i-

.HNP. Unit 1-1988 ILRT/ Test i

data set 2

-time = 1300.date = 1129-sensor.

l raw data value

' temperature 1(

81.000 )

81.000 deg. F

=

. temperature. 2 '(

83.730 )

83.730 deg. F

=

temperature

'3'( ^85.840-)-

85.840 deg. F

=

temperature 4'(

88.8901) 88.890 deg. F

=

91.630 deg. F temperature 5(

91.630 )

=

temperature '6 (-

94.870 )

94.870 deg. F

=

temperature 7( 99.340 )

=' -99.340 deg. F temperature 8-(~104.580 )

'104.580 deg. F

=

temperature 9 (,114.140 )

.114.140 deg. F

=

temperature 10 ( 115.000 )

115.000 deg. F

=

temperature.11'( 76.740 )

76.740 deg..F

=

77.280 deg. F l

temperature 12 ( 77.280 )

=

temperature.13 (

76.380 ) '=

76.380 deg. F.

77.110 deg. F

' temperature 14 (

77.110 )

=

-jdewpoint' 1

.(

78.210 )

=

78.210 deg. F, 0.4779 psia dewpoint 2

-(

76.730.)

'76.730 deg. F, 0.4551 psia

=

dewpoint 3

(

76.370 )

76.370 deg. F, 0.4497 psia

=

dewpoint 4

(

77.040 )

77.040 deg. F, 0.4598 psia

=

dewpoint 5

(

77.560 )

77.560 deg.

F, 0.4678 psia

=

dewpoint 6~

(

71.000 )

.71.000 deg.

F>,

0.-3755 psia j

=

pressure 1

(

738156 )

=

73.8156 psia pressure 2

(

738157 )

=

73.8157 psia l

weighted averages, volume and air mass-86.66129 deg. F temperature

=

'73.81570 psia i

preesure

=

.0.42216 psia

.j vapor pressure

=

volume

=

'274000 cu. ft.

i 99352.9 lbm j

dry air mass

=

1

___=

'HNP' Unit'.1-1988 ILRT/ Test'

-dati set-3 time = 1315 date = 1129-sensor.

raw data value temperature 1)(

81.030-->

=-

81.030 deg..F temperature 2.(.

83.770 )

83.770 deg. F

=

temperature 3 (

85.890 ) ' =

85.890 deg. F l

temperature -4 (

88.970 )

88.970 deg. F

=

temperature 5 ('

91.690 )'

=.

91.690 deg. F

' temperature 6 ( -94.880 )

94.880 deg. F-

=

temperatur e 7( 99.360 )

=

99.360 deg. F temperature 8 (~104.620 )

104.620 deg. F

=

temperature 9( 114.070 )

114.070 deg. F

=

-temperature 10.( 114.820 >

114.820 deg. F.

=

temperature 11 ( 76.640 )

76.640 deg. F

=

temperature 12 ( 77.190 )

=-

77.190 deg. F temperature 13 -(

76.300-)

76.300 deg. F

=

temperature 14 (.77.030 )

77.030 deg. F-q

=

dewpoint :1

-(

77.950 )

77.950 deg. F, 0.4738 psia-

=

dewpoint 2

( 76.910 )

=

76.910 deg. F, 0.4578 psia 76.180 deg. F, 0.4469 psia dewpoint 31

( 76.180 )

=

dewpoint 4

'(

76.940 )

=

76.940 deg. F, 0.4583 psia j

. dewpoint 5

( 77.420 )

77.420 deg. F, 0.4656 psia

=

4 dewpoint 6

(

73.300 )

73.300 deg. F, 0.4058 psia

=

pressure 1

('

738083 )

=-

73.8083 psia pressure 2

(

738085 )

=

73.8085 psia weighted averages, volume and air mass temperature 86.63131 deg. F

=

73.80350 psia pressure

=

0.43498 psia vapor pressure =

volume 274000 cu. ft.

=

L dry air mass 99331.2 lba

=

l l

.l 4

a a

--s-

,e Q?ns i

HNP. Unit 1-1988 ILRT/ Test:

7 (data' set I 4' Ltimef= 1330' date.='1129s

-q sensor

'rav'date:

-valuez temperature?!1 (

81.100l);'=.

81'.'100 deg. F pf 1 temperature; 3t(- 85.960-)

=~

83.S30'deg.;F' temperature '2 ( -83.830l)

=-

s, 85.960'deg. F-temperature. 4( :89.050')

89. 050 deg. F

=

Temperature? 5-(-

91.770 )-'=-

91.770 deg. F.

temperature ~ 6 :(' 94.900,)s 94.900.deg. F

=

Temperature 7L (-

99.380s)'Je 99.380 deg. F L emperature8: 8.(~104.660 );1= 104.660 deg. F.

t temperature; 9-(.114.010-):

114.010 deg. F

=

temperature.10ct 114.680 ):, =

114.680 deg. F stemperaturef11.( 76.560:)

76.560 deg. F

=

temperature 121(

77.100-) - =

.77.100 deg. F temperature:13 (. 76.230 )

76.230 deg. F

=

temperature 14.(

76.950 )

=

.76.950 deg. F'

dewpointi 1

( 78.030 ')l

.78.030 deg.

F',

0.4751 psia

=-

!dewpointi.2-(-

76.970 F.=-

76.970 deg.'F, 0.4587 psia dewpoint.3

. (. 76.100 )-

76.100 deg. F, 0.4457 psia

=

dewpoint' 4-(

76.930.):

76.930 deg. F-,-0.4581 psia

=

dewpoint:15

( ;77.440 )

77.440 deg..F, 0.4659 psia

=

dewpoint _ 6

. (

71.790-)

71.790 deg. F, 0.3857 psia

=

. pressure' 1"

.(

738015 ). : =

73.8015 psia pressure-2

( '738020 )

=

73.8020 psia

weighted averages, - volume and air mass

'86.61295 deg. F temperature

=

73.80200 psia pressure

=

vapor pressure =

0.42592 psia volume 274000 cu. ft.

=

dry' air mass 99338.0 lbe

=

g l

o j

4 HNP Unit 1-1988 ILRT/ Test

. data set 5<

- time;= 1345c date =-1129 sensor-raw data value temperature' l't: 81.150 )

e' 81.150'eg. F d

' temperature.2.(

83.880 )

=

83.880 deg. F temperature. 3:(

86.030-),=-

86.030 deg. F temperature 4 (.

89.100 )

89.100 deg. F

=

temperature 5 (' 91.830 )

91.830 deg. F.

=

- temperature. 6 (

94.940.)

94.940 deg. F

=

temperature 7-(

99.400 )

99.400'deg. F

=-

temperature 8( 104.690 )

104.690 deg. F

=

- temperature-9 (-113.960 )

113.960 deg. F

=

temperature 10 (-114.520 1

=

114.520 deg. F.

temperature 11

(.

76.500 )

76.500 deg. F

=

temperature 12.(".77.010-)

77.010 deg. F

=

' temperature 13 (

76.170-)

=

76.170 deg. F

temperature 14 (L 76.890 )

=

76.890 deg. F dewpoint. 1

(-

78.100 )

78.100 deg. F. 0.4762 psia

=

dewpoint 2'

-(

77.110 )

=

77.110 deg.

F.,' O.4609 psia dewpoint 3

(_ 75.950 )

75.950 deg. F, 0.4435 psia

=

dewpoint 4

( 76.860 )

76.860 deg. F, 0.4571 psia

=

-dewpoint 5

. ( 77.400 )

=

-77.400 deg..F, 0.4653 psia dewpoint 6

( 70.740 )

70.740 deg. F, 0.3722 psia

=

. pressure. 1

( 737950.).

73.7950 psia

=

pressure 2

( 737954 )

73.7954 psia

=

weighted averages, volume and air mass temperature

86. 59659 deg. F -

-=

73.79540 psia

. pressure

=

0.41965 psia vapor pressure

=

volume 274000 cu. ft.

=

l dry air mass 99340.6 lbm

=

l l

i s.

HNP,Unitt1-1988 ILRT/ Test data set 6

ttime:=j1400'.date =.1129' sensor-

. raw data

. values l

temperature l' ( 81.200 )

s' 81.200 deg. F-83.930 deg. F temperature-2 (; 83.930 )-

=-

86.100 deg. F-tempe sture'.s3

(-

86.100 1'

=

temperature 4 (

83.180.)

=-

89.180 deg. F temperature 5-(

91.9001);~=.

91.900 deg. F-94.960 deg..F temperature' 6 ( 94.960 )

=

99.430 deg. F temperature 17

(-

99.430.). =

temperature 8'( 104.710 )

= >104.710 deg..F

'4

temperature-9-( 113.930 )

=.'113.930Ldeg. F-

temperature-- 10'(-114.350-)

={

114.350 deg. F 76.420.deg. F temperature <11"(

76.420_)

=

76.960 deg. F temperature 12 ( 76.960 )

=

76.100 deg. F' temperature?13 ( 76.100 )

=

76.840 deg. F-

.teraperature.14 ( - 76.840 )

=

78.120 deg. F, 0.4765 psia Ldewpoint,.it E(-

78.120 )

=

77.140 deg.

F.,

0.4613 psia-dewpoint 2-

.(77.140

)-

=

dewpoint 3

-(

76.020 ).=

76.020 deg.

F.,

0.4445 psia 76.810 deg..F,'O.4563 psia-

~ dewpoint. -4

(

76.810-)

=

77.420.deg. F, 0.4656 psia-1 dewpoint

.5..

( 77.420 )

=

.72.670 deg.iF, 0.3973 psia-dewpoint 6-(.72.670 )

=

73.7887-psia.

pressure l'

( 737887 )

=

73.7891 psia

' pressure-2.

( L737891 )

=-

weighted averages,. volume and air mass 86.58438 deg. F temperature

=.

73.78910 psia

=

pressure 0.43119 psia

=

vapor pressure 274000 cu. ft.

volume

=

99318.6 lba dry air mass

=

]

.l

.]

l

)

_---_-_--_-__--_____-________-____n

I f

i HNP Unit 1-1988 ILRT/ Test Ldata set 7

j time = 1415 date.= 1129 sensor raw data value y

h

. temperature 1(

81.250')

'81.250 deg. F a

=

83.980 deg. F

]

temperature 2 ('

83.980 )

=

temperature-3 (

86.180-)

86.180 deg. F j

=

temperature 4(

89.250

')

89.250 deg. F

=

temperature 5( 91.960 )

=

91.960 deg. F' temperature, 6.(

94.990

).

94.990 deg. F

=

temperature 7(

99.450.)

99.450 deg. F

=

temperature 8( 104.760 1 104.760 deg. F

=

temperature 9 ('113.890 )

=

113.890 deg. F temperature 10 ('114.210 ).' ='

114.210 deg. F temperature 11

(-

76.360 )

76.360 deg. F

=

temperature 12 ( 76.880 )

76.880 deg. F

=

temperature 13 (

76.050 )

=

.76.050 deg. F.

temperature 14 (

76.770-)

76.770 deg. F

=

, dewpoint' 1

( 78.100 ) is 78.100 deg. F, 0.4762 psia dewpoint 2

.- 76.970 )

76.970 deg. F, 0.4587 psia

(

=

dewpoint 3

( 75.960 )-

75.960 deg. F, 0.4436 psia

=

dewpoint 4

(

76.760 )

76.760 deg. F, 0.4556 psia

=

dewpoint 5

(-

77.300 )

77.300 deg.

F',

0.4638 psia

=

dewpoint. 6

'(

71.580 )

71.580 deg. F, 0.3830 psia

=

pressure 1

( 737829 )

73.7829 psia

=

pressure 2

( 737836 )

73.7836 psia

=

weighted averages, volume and air mass 86.57176 deg. F temperature

=

73.78360 psia.

pressure

=

0.42403 psia vapor pressure =

volume 274000 cu. ft!

=

dry air mass 99323.2 lbs

=

.m7

_ y e

t.g <

-n

x HNP Unit-l'1988 1LRT/ Test) data set 8

time = 1430 date'= 11'29:

sensor-raw data value

-. temperature.1-(.

81.310-):.=.

81.310 deg. F temperature.:2 ( :84.040 l' 84.040 deg. F

=

temperature 3 (-

86.230

).

'86.230 deg. F

=

89.370 deg.~F temperature 4( 89.370 )

=

92.040 deg.' F'

- temperature = 5 (

92.040-)- =

temperature 6 '(

95.020 )

95.020 deg. F

=

99.470 deg._F-temperature 7

(.

99.470 >- =-

104.810'deg..F

' temperature: 8,( 104.810 )

=

g temperature.9 ( 113.850 )

113.850-deg. F

=

' temperature 10 ( 114.050 )

=

114.050 deg. F

^ temperature 11 ( 76.310

)-

=- -76.310 deg. F 76.820 deg.'F temperature 12 (

76.820.)

=

temperature 13 ( 75.980

)~

='

75.980.deg. F temperature 14.(. 76.710 );

76.710 deg. F

=

,e dewpoint.'1

(~ 78.150.)

=.

78.150'deg. F, 0.4770 psia 76.840 deg.

F',

0.4568 psia dewpoint' ~2

( 76.840 )

=

75.940 deg. F, 0.4433 psia dewpoint.3

( 75.940

)-

=

'76.740 deg. F, 0.4553; psia -

dewpoint' 4

( 76.740 )

=

177.300 deg. F,_0.4638 psia devpoint;l5-( 77.300 )

=-

71.860 deg. F, 0.3866 psia

-dewpoint 6 t

71.'860 )

=

pressure 1

(-

737771-).

-73.7771 psia

=

pressure 2

( 737780 )

73.7780 psia

=

weighted averages, volume and air mass 86.56445 deg. F temperature'

=

73.77800 psia pressure

'=

0.42547-psia vapor pressure =

274000 cu. ft.

volume

=

99314.9 1ha dry air mass

=

I h

1

+

.f

^

f

HNP Unit l'-1988 ILRT/ Test j

data set' 9 '.

l j

i

time;=;1445 date.= 1129 j

' sensor raw' data

.value

~

81.340 deg. F

]

n

' temperature 1(

81.340 )

=

l

- temperature ' 2.(. 84.100 )

84.100 deg. F

=

86.290 deg. F

' temperature 3( 86.290 )

=

temperature 4( 89.460 )

=

89.460 deg. F temperature ~5 ( ~92.100 )

=. 92.100 deg. F temperature 6( 95.040 )

= '

95.040 deg. F t

temperature. 7( 99.490 )

99.490 deg. F

=-

L temperature' 8.(f104.860 )

104.860.deg. F

=

temperature 9 ( 113.820')-

113.820 deg. F

=

. temperature 10 ('113.870 )

113.870 deg. F

=-

' temperature'11 ( '76.240 )

=

76.240 deg. F

, temperature 12 ( 76.750 ) ' =

76.750.deg. F temperature 13.(

75.930 )

=

75.930 deg.:F temperature 14:( 76.640 )

=

-76.640 deg. F dewpoint? 1

( !78.150 )

78.150 deg. F, 0.4770 psia

=

dewpoint. 2

(.~77.230 )

77.230 deg. F,.0.4627 psia-

=

dewpoint 3

't 75.850')

75.850 deg. F, 0.4420 psia

=

76.690 deg. F, 0.4545 psia dewpoint 4.

( 76.690 )

=

77.320 degi-F, 0.4641: psia dewpoint 5.

-(

77.320 )

=

dewpoint-6

( 71.300 )

71.300 deg. F, 0.3793 psia

=

. pressure 1

( 737716 )

73.7716 psia

=

73.7725 psia preesure 2

( 737725 )

=

veighted averagee, volume and air mass 86.54967 deg. F temperature

=

73.77250 pria' q

pressure

=

0.45819 psia vapor pressure

=

> volume 274000 cu. ft.

=

99265.9 lbm dry air mass.

=

l+

L t

y : 3 _r;:

3

$g3

/Ni ",

i >

%.g.,

jHNP_ Unit'_1-1988 ILRT/TestL M.

idata: set J10; time.= 1500':

date =._1129 os sensor raw data l valuel-.

temperature.'l.(i i815400 ).i=

81.400'deg. F l temperature, 2_._ ( : 84.170').=

84.170 deg. F temperature : L 3 - ( ;86.350 );'=

86. 350 deg. : F' 1

temperature '4 ( :89.510 )-_'=.

89.510 deg. F 92.180 deg.- F

. temperature' 5-(. 92.180 )

=,

' temperature-6

(< 95.060

).

95.060 deg. F-

=

, temperature,'7-(

99.510~) :=.

99.510:deg. F temperatures.8 ( 104.900.);

104.900 deg.1 F'

=.

temperature-9 (,113.790

)_- =' '113.790 deg. F-temperature 10'( 113.7101) 113.710.deg. F:

=

76.190 deg.EFE Temperature 11 (

76.190:)

=-

temperature:12 (

76.690-)- =-

76.690.deg.'F 75.880 deg..F temperature.13 (

75.880-) '=-

temperature 14 ( 76.600-)

=-

76.600 deg. F dewpoint

'1

(; 78.170.)

^8.170Ldeg. F, 0.4773 psia

=

77.200 deg. F, 0.4622' psia dewpoint: 2

.('

77.200 )

=

dewpointi 3

(- '75.860 )

='

75.860 deg. F, 0.4421 psia

dewpoint

<4 '

(

76.670-) ~=- -76.670 deg. F;, 0.4542 psia

- dewpoint' 5._

(~

77.280,)

=

77.280_deg. F, 0.4635 psia

'4;_

cdewpoint 6,

( _71.480 )

=J 71.480 deg. F,s0.3817 psia, 73.7666 psia.

pressure l'

'(

737666 )

=

pressuref 2

(-

737678 ).=

73.7678 psia weighted averages, volume and air mass 86.54359 deg. F temperature

=

73.76780_ psia-h pressure

=

0.45805 psia-j

. vapor. pressure

=

volume.

'274000 cu. ft.

=

99260.8 lbe dry air mass

=

I

I),:

' ][/,

i

'HNP Unit 1-1988 ILRT/ Test'

[ data set 11,'

y time = 1515. date ='1129' U

' sensor ra'v data value temperature 1'( '81.440 )-

81.440 deg. F-

=

~. temperature 2'(. :84'.200 )'

=: 84.200 deg. F' i

~ temperature. 3 (f.86.430')-

86.430 deg. F

=-

l temperature.:4

(.

89.570-);

89.570 deg. Fi

=

92.230.deg. F=

~ temperature. 5 (

92.230

)-

=

95.110 deg. F

temperature-6.(

95.110.)

=

99.520 deg. F'

-temperature-7.(

99.520')

=

104.940 deg. F

~

temperature 8 (,104.940 )

=

temperature 9-(~113.750 )

= 113.750 deg. F 2

temperature 10 ( 113.540 ).= 113.540 deg. F 76.120 deg. F temperature li'(

76.120

)-

=

76.640 deg. F-temperature 12

('

76.640 )

=

75.830 deg. F temperature 13 ('

75.830 )-

=

76.550 deg. F

. temperature 14-(

76.550: ) ' =

dewpoint

. (

78.380 ). = '

78.380 deg. F, 0.4806 psia fdewpoint.2

( -- 77.200 )

77.200 deg. F, O.4622 psia

=

75.830 deg. F, 0.4417 psia dewpoint.'3

(-

75.830 )

=

76.670 deg..F, 0.'4542 psia

-dewpoint-4

(

76.670 )

=-

77.280 deg. F, 0.4635 psia

~ dewpoint' 5'

(

77.280 )

=

70.930 deg. F,-0.3746 psia dewpoint -6

(. 70.930 )

=

pressure -1L

(' '737616').

73.7629 psia 73.7616 psia

=-

pressure 2'

(

737629') _

=

weighted averages,-volume and air mass

86.53219 deg. F temperature

=

'73.76290 psia

=

pressure.

0.45854 psia

=

vapor pressure volume

=

274000 cu. ft.

99255.6 lba dry air mass

=

t-1 HNP. Unit 161988.ILRT/ Test

' data set 12

- time.=~1530 date = 1129l

sensor raw data.

value; temperature 1_ (

81.490 )

=

81.490 deg. F.

temperature _ 2 0 84.260 )

=

84.260 deg. F-temperature 3.(

86.480

),.

m.

86.480 deg. F-temperature _, 4

(-

89.650

)-

=

89.650 deg.'F

. temperature' 5-(.

92.290 )

'92.'290.deg. F

=

temperature 6(

95.150L)- ='

95.150 deg. F temperature 7(. 99.560 )

's 99.560 deg. F temperature 8( 105.000 )

=

-105.000 deg. F temperature 9 ('113.690-)- ~= 113.690 deg._F-temperature 10 ( 113.370 )

=

113.370 deg. F temperature 11 ( -76.060 )

=

76.060 deg. F temperature 12-( ~76.600 )-

=

76.600 deg. F temperature 13 ( -75.790 )

=

75.790 deg. F temperature: 14 -(

76.510 )

76.510 deg. F

=-

d' ewpoint - 1

(; 78.150 )

78.150 deg. F, 0.4770 psia.

=

dewpoint-2

( 77.410 ).

=

77.410 deg. F, 0.4655 psia dewpoint 3

('

75.880 )

=

75.880 deg. F, 0.4424 psia

- dewpoint 4

( 76.650 )

=

76.650 deg. F, 0.4539 psia dewpoint 5

'(

77.300 )

=-

.77.300 deg. F, 0.4638 pain-

- dewpoint 6

( _70.590 )

70.590 deg. F, 0.3703. psia

=

pressure 1

(

737570

)-

73.7570 psia

=-

pressure 2

( 737583 )

=

73.7583 psia weighted averages, volume and air mass temperature 86.52879 deg. F

=

73.75830 psia pressure

=

0.45867 paia vapor pressure

=

volume 274000 cu.-ft,

=

dry air mass 99249.8 lba

=

i l

l i

HNP Unit 1-1988 ILRT/ Test

' data set 13 time = 1545-date = 1129' sensor raw data value 81.540 deg. F temperature 1( 81.540

).

=-

84.300 deg. F.

temperature 21 ('

84.300 )

=

86.550 deg. F temperature

'3 (

86.550.)

=

89.700 deg.'F temperature 4(

89.700 )-

=

92.360 deg. F temperature 5( 92.360 )

=:

95.180 deg. F temperature 6( 95.180 )

=

99.580 deg. F temperature 7( 99.580 )

=-

105.040 deg. F

-temperature 8( 105.040 )

=

113.650 deg. F

-temperature 9( 113.650 )

=

113.210 deg. F temperature 10 ( 113.210

)-

=

76.030 deg.-F temperature 11

('

76.030 )

=

76.540 deg. F temperature 12 (

76.540 )

=

75.750 deg. F temperature 13 ( :75.750 )

=

76.450 deg. F temperature 14 ( 76.450 )

=

78.230 deg. F, 0.4782 psia dewpoint 1

( 78.230 )

=

77.510 deg.

F',

0.4670 psia dewpoint-2

( 77.510 )

=

75.860 deg. F, 0.4421 psia dewpoint 3

(

75.860 )

=

76.660 deg. F, 0.4540 psia dewpoint 4

('

76.660 )

=

77.280 deg. F, 0.4635 psia dewpoint 5

( 77.280 )

=

71.420 deg. F, 0.3809 psia dewpoint 6

(

71.420 )

=

'73.7525 psia pressure 1

( 737525 )

=

73.7538 psia pressure 2

( 737538 )

=

weighted averages, volume and' air mass 86.52188 deg. F temperature

=

73.75380 psia

=

pressure 0.45910 psia

=

vapor pressure 274000 cu. ft.

volume

=

99244.4 lbe dry air mass l

l l

I

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

. _ _ _ _ _ _ _ _ ~

y 73 HNP Unit'1-1988 ILRT/ Test data set 114 -

time =.1600

'date = 1129 sensor-raw data value

, temperature'.1 : ( ' 81.580 )

81.580 deg..F

=

. temperature 2

(.

84.350-)

!='

84.350 deg.- F temperature 3L(

86.600 )

86.600 deg. F

=

. temperature 4-(-

89.800 )

89.800 deg. F

=

temperature 5'(

92.410 )

=

92.410 deg. F temperature-6 ;-(

95.210 )

95.210 deg. F.

.=

. temperature 7'(

99.610 )-

99.610 deg. F

=

temperature 8( 105.090 )

=

105.090 deg. F temperature: 9 (.113.600 )

=.113.600 deg. F

. temperature 10 (1113.030 )-

' 113.030 deg. F

=

temperature'11 (

.75.990-)~.=

75.990 deg. F

. temperature 12

('

76.500 )

=

76.500'deg. F-temperature.13.( 75.720 )

75.720 deg. F

=

temperature 14 (.'76.420 )

76.420 deg.'F

=

dewpoint 1

('

78.370 )

78.370 deg. F, 0.4804 psia-

=-

dewpoint 2

(.

77.320 )

=

77.320 deg.

F',

0.4641 psia dewpoint.3

( 75.770 )

75.770 deg. F, 0.4408 psia-

=

dewpoint 4

( 76.640 )

76.640 deg. F, 0.4537 psia

=

dewpoint 5

( 77.270 )

=

77.270 deg. F, 0.4633 psia dewpoint 6

-(

73.330 )

=

-73.330 deg. F,,0.4063 psia pre 9sure 2

( 737493

).

73.7481 psia pressure 1

( 737481 )

=

73.7493 psia

=

weighted averages, volume and. air mass 86.52056 deg. F temperature

=

73.74930 psia pressure

=

0.45851 psia

=

vapor pressure 274000 cu. ft.

volume

=

99239.3 lbe dry air mass

=

O R

l' 1

r A

- o y

HNP Unit 1-1988-ILRT/ Test ae 1

3'.

as

~

15

' data? set?

i time'= 1615 date =J1129 sensor rav ' data :.

value:-

81.630 deg. F temperature

'1-('

81.630 1'

=

84.420 deg..F t emperature 2 (: 84.420 >-

=

i 86.670 deg.'F

-temperature 3(

86.670 )

=

89.860 deg. F2 temperature E4.(

89.860 )

=

92.490 deg.? F.

temperature ! 5.(-:92.490:)

=

95.240 deg. F-temperature; 6 ( 95.240;)

=

temperature 7.(

99.640 ).

99.640 deg. F

=

105.130 deg. F.

Temperature ~8 ( 105.130-)-

=

113.540'deg. F

. temperature - 9'(-113.540 )-

=

= temperature 10-( 112.870l) := 112.870 deg.'F

.75.940 deg. F temperature;11.( 75.940 )

=

temperature-12c(- 76.440 )f'=.

76.440,,deg. F1 75.680 deg. F temperature 13-(

75.680')

=

temperature 14 ( 76.380 ).=

76.380 deg. F.

.78.260 deg. F, 0.4787 psia l '.

' dewpoint 1

'(

78.260');

=-

77.570'deg. F,.0.4679 psia dewpoint;.2

(( 77.570 ).=

75.890.deg. F,'O.4426 psia

dewpoint, 3'

t(? 75.890:)

=

76.660.deg. F, 0.4540' psia dewpoint.4

-(.;76.660 );

77.300 deg.

F.,

0.4638 psia

=

dewpoint 5

( 77.300 )

=

69.970 deg. F, 0.3626' psia dewpoint. 6

( 69.970 )

=

pressure 1

(.

737441

)'-

73.7441' psia

=

73.7456 psia pressure 2

( -737456.)

=

weighted-averages, volume and air mass 86.51605;deg. F temperature'

=

73.74560 pais

=

pressure 0.45953 psia

=

vapor pressure 274000 cu. ft.

volume

=

99233.8 lba dry air mass

=

L-

HNP Unit 1-1988 ILRT/ Test data set 16 time = 1630 date = 1129 senser raw data value 81.670 deg. F temperature 1(

81.670 )

=

84.470 deg. F temperature 2(

84.470 1

=

86.720 deg. F temperature 3(

86.720 )

=

89.910 deg. F temperature 4( 89.910 )

=

92.540 deg. F temperature 5(

92.540 )

=

95.260 deg. F temperature' 6(

95.260 )

=

99.670 deg. F temperature 7(

99.670 )

=

105.170 deg. F temperature 8( 105.170 )

=

113.510 deg. F temperature 9( 113.510 )

=

112.720 deg. F temperature 10 ( 112.720 )

=

75.900 deg. F temperature 11 ( 75.900 )

=

76.420 deg. F temperature 12 ( 76.420 )

=

75.640 deg. F temperature 13 (

75.640 )

=

76.340 deg. F temperature 14 (

76.340 )

=

78.220 deg. F, 0.4781 psia dewpoint 1

( 78.220 )

=

77.730 deg. F, 0.4704 psia dewpoint 2

( 77.730 )

=

75.810 deg. F, 0.4414 psia dewpoint 3

( 75.810 )

=

76.660 deg. F, 0.4540 psia dewpoint 4

( 76.660 )

=

77.320 deg. F, 0.4641 psia dewpoint 5

( 77.320 )

=

71.590 deg. F, 0.3831 psia dewpoint 6

( 71.590 )

=

73.7401 psia pressure 1

(

737401 )

=

73.7417 psia pressure 2

( 737417 )

=

weighted averages, volume and air mass 86.51292 deg. F temperature

=

73.74170 psia

=

pressure 0.45960 psia vapor pressure

=

274000 cu. ft.

volume

=

99229.0 lbm dry air mass

=

~

n i-HNP Unit 1-1988 ILRT/ Test

dets set 17 tiee = 1645 date = 1129-sensor raw data ~

.value 81.700 deg. F

_ temperature 1 ( 81.700 )

=

temperature ~ 2 (

84.510 ).

84.510 deg.' F

=

86.790 deg. F temperature.31(

86.790 )

=

89.960 deg. F

[;

temperature 4( :89.960 )

=

92.600 deg. F N

temperature 5( 92.600 )

=

L 95.290 deg. F

' temperature' 6( 95.290-)

=

99.690 deg. F temperature 7( 99.690 )

='

105.200 deg. F temperature 8( 105.200 )

=

113.440 deg. F temperature 9.(_113.440 )

=

112.550 deg. F temperature 10 ( 112.550 )

=

75.850 deg. F

' temperature.11 ( 75.850 )

=

76.360 deg. F temperature 12 (.76.360 )

=

75.600 deg. F temperature 13 (.75.600 )

=

.76.320 deg. F temperature 14 ( '76.320 )

=

78.320 deg. F, 0.4796 psia dewpoint 1_

( 78.320 )

=

77.450 deg. F, 0.4661 psia dewpoint 2:

( 77.450 ) =

75.760 deg. F, 0.4407 psia dewpoint 3

(

75.760')

=

76.640 deg. F, 0.4537 psia dewpoint 4

( 76.640 )

=

77.290 deg. F, 0.4636 psia dewpoint 5

(.77.290 )

=

72.830 deg.

F_,

0.3995 psia dewpoint 6

.(

72.830

).

=

73.7360 psia pressure 1

( 737360 )

=

73.7380 psia pressure 2

( 737380 )

=

weighted averages, volur.e and air mass 86.50417 deg. F temperature

=

73.73800 psia

=

pressure 0.45874 psia

=

vapor pressure 274000 cu. ft, volume-

=

99226.7 lba dry air mass

=

s

~

w HNP Unit-1-1988 ILRT/ Test idata set; 18 U

-time = 1700 dateL= 11'29'

~

sensor rav1 data

-value

~

81.750 deg. F temperature' 1-(

81.750.1

=

temperature 2 (1 84.560;)

84.560 deg. F

=

temperature. 3 (' 86.850:).

86.850 deg. F-

=

temperature 4( 90.060 )

=.

90.060 deg. F 92.660 deg. F temperature '5

(.

92.6601)

=

temperature 1;6 ( 95.320 )

95.320.deg. F

=

99.710'deg. F.

temperature ( '99.710 )

=

.temperstbre;18!( 105.240

)-

=

105.240 deg.JF.

' temperature 9 (L113.380 ) := '113.380 deg. F temperature 10.( 112.380.)~ =

'112.380 deg. F 75.820 deg..F temperature :11- (

75.8201)-

=

. temperature 12.(- 76.330')

76.330 deg.-F

=

temperature 13

(.

75.580.)-

75.580 deg. F

=

temperature 14 (l!76.280 ) ' =

76.280 deg. F dewpoint 'l

(

78.310')

78. 310 deg. : F, 0.' 4795 psia

=

77.480 deg. F1, 0.4665 psia dewpoint 2

(.77.480 )-

=

75.870 deg. F, 0.4423 psia dewpoint -3

.(

75.870 )

=

dewpoint' 4

( 76.680 ).

76.680 deg. F, 0.4543 psia

=

77.340 deg.

F.,

0.4644 psia dewpoint 5

(

77.340..)

=

70.150 deg. F, 0.3648 psia dewpoint 6:

( 70.150

)~

=

pressure. 1

( 737321 )'

73.7321 psia

=

pressure 2

( 737340 )

=-

73.7340 psia weighted averages,. volume and air mass temperature 86.50565 deg. F

=

73.73400 psia

=

pressure vapor pressure.=

0.45948-psia-volume 274000 cu. ft.

=

99220.0 lba dry air mass

=

l E________----

i

l

'ij HNP Unit 1-1988 ILRT/ Test J7:a' set 19=

j l

time = 1715 date = 1129 sensor raw data value I

a

-81.800 deg. F temperature 1 -(

81.800 )

=

84.630 deg. F temperature 2(

84.630-)

=

.86.910 deg. F

' temperature 3(. 86.910-)

=

~

' 90.140 deg. F.

temperature 4

(-

90.140 )

=

92.730'deg..F temperature 5( 92.730 )

=

95.350 deg. F temperature 6( 95.350 )

=

'99.750 deg. F temperature 7( 199.750 )

=

105.290 deg. F temperature 8( 105.290 )

=

113.340 deg. F temperature 9( 113.340-),

=

112.250 deg. F temperature 10 ( 112.250 )

=

75.800 deg.' F

' temperature 11.(

75.800 )

=

76.300 deg. F temperature 12.(

76.300 )

=

75.550 deg. F temperature 13 ( e75.550 )

=

.76.260 deg. F temperature 14

(-

76.260 )

=

78.340 deg. F, 0.4800 psia dewpoint 1

( 78.340 ).

=

dewpoint 2

.(- 77.880 ).

.77.880 deg.-F, 0.4727 psia

=

dewpoint.3

(

75.850 1 '=

75.850 deg. F, 0.4420 psia 76.680 deg. F, 0.4543 psia dewpoint 4

( 76.680 )

=

77.320 deg. F., 0.4641 psia dewpoint 5

(

77.320 )

=

71.610 deg. F, 0.3833 psia dewpoint 6

( 71.610 )

=

73.7284 psia pressure 1

( 737284 )

=

73.7301 psia pressure 2

( 737301 )

=

weighted averages, volume'and air mass 86.51408 deg. F temperature

=

73.73010 psia

=

pressure 0.46062 psia

=

vapor pressure 274000 cu. ft.

volume

=

99211.7.lbm dry air mass

=

L-

_HNP Unit 1-1988 ILRT/ Test i.-

20.

data set time.= 1730 date = 1129 sensor raw data value 81.830 deg. F temperature 1(

81.830 )

=

84.670 deg. F

. temperature 2

(' -84.670 )

=

86.980 deg. F temperature 3( 86.980 )

=

temperature' 4 (

90.180')-

90.180 deg. F

=

.92.780 deg. F

' temperature' 5( 92.780 )

=

95.370 deg. F temperature 6.(

95.370 )

=

temperature '7 (

99.780')

99.780 deg. F

=

105.330 deg. F temperature. 8( 105.330.)- =

113.280 deg. F temperature 9 ('113.280 )

=

112.100 deg. F temperature 10 (-112.100 )

=

75.760 deg. F temperature 11 ( 75.760 )

=

76.270 deg. F temperature 12 (

76.270 )

=

75.530 deg. F temperature 13 ( '75.530 )

=

76.210 deg. F temperature 14 (

76.210 )

=

dewpoint 1 78.510

).

=

(

78.510 deg.

F.,

0.4827 psia 77.720 deg. F, 0.4703 psia dewpoint 2

( 77.720

)-

=

75.840 deg. F, 0.4418 psia dewpoint 3'

. ( 75.840 )

1=

76.690 deg. F, 0.4545 psia dewpoint 4

( 76.690 )

=

77.380 deg. F, 0.4650 psia dewpoint 5

( 77.380 )

=

72.530 deg. F, 0.3955 psia dewpoint 6

'(.'72.530 )

=

73.7247 psia pressure 1

(

737247 )

=

73.7267 psia pressure 2

(

737267 )

=

weighted averages, volume and air mass 86.50891 deg. F temperature

=

73.72670 psia pressure

=

0.46077 psia vapor pressure =

274000 cu. ft.

volume

=

99207.8 lba dry air mass

=

1:

l

-HNP Unit 1-1988 ILRT/ Test

' data set 21 time =L1745 'date = 1129 sensor

. raw data value 81.880 deg.~F temperature: 1(

81.880 )

=

84.730 deg. F temperature '2 ( 84.730 )

=

temperature.

3.(.

87.030 ).=

87.030 deg..F

'90.250 deg. F j

temperature' 4( 90.250 )

=

92.840 deg. F temperature.

5.(

92.840 )

=

.95.400 deg. F temperature 6(

95.400 )

=

99.810 deg. F temperature 7

(-

99.810 l'

=

105.370 deg. F temperature. 8( 105.370.)

=-

113.240 deg..F temperature 9 (.113.240 )

=

111.920 deg. F temperature 10.( 111.920')

=1 75.740 deg. F

' temperature 11.(

75.740.)

=

76.240 deg. F temperature'12 ( '76.240 )

=

75.500 deg. F-temperature 13 ( '75.500 ).

=

76.180 deg. F temperature 14 (.76.180 )

=

dewpoint! 1

(

78.540')

='

78.540 deg. F, 0.4831 psia' dewpoint 2

( 77.820 )

J=

77.820 deg. F, 0.4718' psia 75.940 deg. F,.0.4433 psia dewpoint 3

( 75.940 ) = 1 76.730 deg.' F, 0.4551 psia dewpoint 4

( '76.730

)"

=

.77.350 deg. F, 0.4645 psia dewpoint 5

-(

77.350 )

=

70.170 deg. F, 0.3650 psia dewpoint 6

( 70.170 )

=

-73.7210 psia pressure 1

( 737210 )

=

73.7232 psia pressure 2

( 737232 )

=

weighted averages, volume and air mass 86.51137 deg. F temperature

=

73.72320 psia

=

pressure 0.46162 pain

=

vapor pressure 274000 cu. ft.

volume

=

99201.5 lbm dry air mass

=

h Lj.

1.

i. -

t HNP Unit 1-1988 ILR7/ Test-data set-22 time = 1800 :date =,1129 sensor raw data value.

' temperature :1 ( 81.910 )_

81.910 deg. F'

=

84.770 deg..F temperature' 2( 84,770 )

=

temperature '3 (- 87.080 ) ' =

87.080 deg. F temperature 4.(

90.280 )

90.280 deg. F

=

92.890 deg. F-temperature 5;(- 92.890 )

=

temperature6 (.95.450 ).

s.

95.450 deg. F

,99.820 deg. F.

temperature 7(.99.820 )-

=

.105.400 deg. F temperature 6( 105.400 )-

=

113.160 deg. F temperature. 9( 113.160 ).

=

temperature 10 (1111.770 ).

111.770.deg. F

=

75.710 deg. F:

temperature 11-(. 75.710~)

=

76.200 deg. F temperature 12-(

76.200-)

=

75.460 deg. F temperature'13;( -75.460 )

=

76.150 deg. F.

temperature 14 (.76.150 )

='

78.520 deg. F, 0.4828 pais dewpoint'. 1

( 78.520

)'

=

devpoint.2

( 77.670 ).'=

.77.670 deg; F, 0.4695 psia 75.860 deg. F, 0.4421 psia dewpoint-3

( '75.860 );

=

76.750 deg. F, 0.4554. psia devpointi 4

-(

76.~750 )

=

77.390 deg. F, 0.4652 psia dewpoint; 5

( 77.390 )

=-

71.630 deg. F, 0.3836 psia devpoint' 6

(. 71.630 )

=

-73.7175 psia pressure 1

( 737175-)

=

73.7197 pois pressure 2

.(

737197 )

=

weighted averages, volume and air mass

~86.50405 deg. F temperature

=

73.71970 psia

=

pressure 0.46094 psia

=

vapor pressure 274000 cu. ft.

volume

=

99199.0 lba dry air mass

=

1 I

l i

l 1

)

l

i HNP Unit 1-1988 ILRT/ Test 1

<%&i:p data set 23

(

fg!;' M j

time = 1815 date = 1129 value j

raw data sensor 81.950 deg. F temperature 1( 81.950 )

=

84.820 deg. F j

temperature 2( 84.820 )

=

i 87.140 deg. F temperature' 3 ( 87.140 )

=

90.330 deg. F temperature 4( 90.330 )

=

92.950 deg. F temperature 5( 92.950 )

=

95.470 deg. F temperature 6( 95.470 )

=

99.860 deg. F temperature 7 ( 99.860 )

=

, gy,,

105.450 deg. F

4. ;A temperature 8( 105.450 )

=

113.130 deg. F temperature 9( 113.130 )

=

111.610 deg. F temperature 10 ( 111.610 )

=

75.680 deg. F temperature 11 ( 75.680 )

=

76.170 deg. F temperature 12 ( 76.170 )

=

75.450 deg. F temperature 13 ( 75.450 )

=

76.110 deg. F temperature 14 ( 76.110 )

=

78.410 deg. F, 0.4811 psia devpoint 1

( 78.410 )

=

7.'.620 deg. F, 0.4687 psia devpoint 2

( 77.620 )

=

75.900 deg. F, 0.4427 psia devpoint 3

( 75.900 )

=

76,740 deg. F, 0.4553 psia devpoint 4

( 76.740 )

=

77.380 deg. F, 0.4650 psia devpoint 5

( 77.380 )

=

71.890 deg. F, 0.3870 psia devpoint 6

( 71.890 )

=

73.7140 psia pressure 1

( 737140 )

=

73.7163 pais pressure 2

( 737163 )

=

i veighted averages, volume and air mass 86.50639 deg. F

=

temperature 73.71630 psia

=

pressure 0.46058 psia

=

vapor pressure 274000 cu. ft.

(( ],

volume

=

99194.4 lba dry air mass

=

1

f. s

U ' "

c, 3 g

HNP Unit 1-1988 ILRT/ Test data set 24 time s.1830 date = 1129 sensor rav' data value-81.990 deg. F temperature 1(

81.990 )

=

84.860 deg. F temperature 2( 84.860 )

=

87.200 deg. F temperature 3(

87.200 )

=

90.420 deg. F temperature 4( 90.420 1

=

93.000 deg. F temperature 5( 93.000 )

=

95.490 deg. F temperature 6 (. 95.490 )

=

99.880 deg. F temperature 7(

99.880 )

=

105.480 deg. F temperature 6( 105.480 )

=

113.080 deg. F temperature 9( 113.080 )

=

111.430 deg. F temperature 10 ( 111.430 )

=

75.660 deg. F temperature 11 ( 75.660 )

=

76.140 deg. F temperature 12 ( 76.140 )

=

75.410 deg. F temperature 13 ( 75.410 )

=

temperature 14 ( 76.090 )

' 76.090 deg. F

=

78.700 deg. F, 0.4857 psia devpoint l'

( 78.700 )

=

77.410 deg. F, 0.4655 psia devpoint 2

( 77.410 )

-=

75.950 deg. F, 0.4435 psia devpoint 3

( 75.950 )

=

76.730 deg. F, 0.4551 psia devpoint 4

( 76.730 )

=

77.440 deg. F, 0.4659 psia devpoint 5

(

77.440 )

=

69.940 deg. F, 0.3622 psia devpoint 6

( 69.940 )

=

73.7105 psia pressure 1

( 737105 )

=

73.7130 psia pressure 2

( 737130 )

=

weighted averages, volume and air mass 86.50578 deg. F temperature

=

73.71300 psia

=

pressure 0.46113 psia

=

vapor pressure 274000 cu. ft.

volume

=

99189.3 lba dry air mass

=

1

l 1

HNP Unit 1-1988 ILRT/ Test data set 25 time = 1845 da'te = 1129 raw data value sensor l

82.020 deg. F temperature 1( 82.020 )

=

84.920 deg. F

^

temperature 2( :84.920 )

=

87.260 deg. F temperature 3( 87.260 )

=-

90.460 deg.tF

' temperature 4( 90.460 )

=

93.050 deg.:F temperature 5( 93.050-)

=

95.510 deg. F temperature 6( 95.510 )

=

99.900 deg. F temperature 7( 99.900 )

=

105.510 deg. F temperature 8( 105.510 )

=

113.020 deg. F temperature 9( 113.020 )

=

111.270 deg. F temperature 10 ( 111.270 )

=

75.630 deg. F temperature 11 ( 75.630 )

=

76.110 deg. F temperature:12 ( 76.110 )

=

75.390 deg. F temperature 13 ( 75.390 )

=

76.060 deg. F temperature 14 ( 76.060 )

=

78.660 deg. F, 0.4850 psia dewpoint 1-(

78.6'60-)

is 77.680 deg. F, 0.4696 psia

.derpoint 2

( 77.680 )

=

75.990 deg. F, 0.4441 psia devpoint 3

( 75.990 ).

76.780 deg. F, 0.4559 psia

=.

devpoint 4

( 76.780 )

=

77.420 deg. F, 0.4656 psia devpoint 5

( 77.420 )

=

71.680 deg. F, 0.3843 psia devpoint 6

( 71.680 )

=

73.7105 psia pressure 1

( 737105 )

=

73.7099 psia

. pressure 2

( 737099 )

=

weighted averages, volume and air mass 86.50299 deg. F temperature

=

73.70990 psia

=

pressure

[

0.46207 psia

=

l vapor pressure 274000 cu. ft.

=

volume

{

99184.3 lba

=

dry air mass

a 3

n-I J.

ij,'

,=

-n A

nit 1 1988'ILRT/ Test' HNP

-data set _J26

.i d

V

' timeL= 1900 date =-1129-I

sensor, raw data.

value 82.070 deg. F g

temperature 1(

82.070-)-

=

84.970 deg. F

! temperature 2-(- 84.970 )

=

87.320 deg.'F t

temperature.3 ( 87.320 )-

=

I 90.520 deg. F 1 emperature 4( L90.520-)

t

=-

temperature ~ 5 ('

93.100:).

=1 93.100 deg. F temperature 6(- 95.550 )

!=-

95.550 deg. F f '

99.940 deg. F

' temperature '7'(

99.940.)

=

112.940'dtg./P,(1 105.530 d(g.

temperature 8 ( 105.530 )

=

FF.'

-temperature 9( 112.940 )

1,;,g[

=

'5)

~

111.230 typ.' F-;

temperature 10'( 111.230 )-

=

75.620 dDgy FF. L N./ 3 temperature 11'( :75.62P ),

=

3

76.080 dig (f;"O temperature 12 (' '76.080 )

=

75.360 deg?

i temperature 13 ( 75.360 ).=

76.060 deg.' F temperature 14 ( 76.060 )

=

i 78.470 deg. F, 0.4820 psia devpoint 1

( 78.470 )

=

77.900'deg. F, 0.4731 psia devpoint 2

( 77.900 )

=

75.990 deg. F, 0.4441. psia devpoint. 3

-(

.75.990-)

=

76.780 deg. F, 0.4559 psia despoint 4

-(

76.780?)

=

77.360 deg. F,.O.4647 psia devpoint 5

(.77.360 ) '=

71.030 deg. F, 0.3759 psia devpoint 6

.(

71.030 ) =

73.7070 psia pressure 1

( 737070 )

=

73.7067 psia pressure 2

( 737067 )

=

weighted averages, volume and air mass 86.51171 deg. F temperature.

=

73.70670 psia-

=

pressure

.0.46203 psia

=

vapor pressure 274000 cu. ft.

volume

=

99178.5 lba dry air mass

=

f

cHNP.Unitil-1988Ik.RT/TestL

' ati data set :27-itime = 1915? -date =.1129 y

sensor.

raw data' value

'82.100.deg. F-l temperature: 1(

82.100-)'

=

85.020 deg..F temperature 2 ( '85.020 ) ' =

temperature.3;(.

87.'380 );'=

87.380 deg. F

temperature 4'((.90.600:). =; '90.600.deg. F'

~ temperature 5:( ~93.160 )

=:

93.160 deg.

F

95.580 deg. F temperature 6-( ;95.580 )

=

temperature 7 (-

99.960 ) ~=

.99.960 deg. F 105.590 deg. F-temperature-8 ( 105.590 )

=

. temperature.9.( 112.880-) ' = ' -112.880 deg. F L111.120.deg. F temperature 10 (;111.120L)

~=

'75.590 deg. F temperature.11:(- :75.590 )-

=:

temperature 12 ( '76.060 ).

~76.060 deg..F

=-

. temperature 13 ( 75.350 )

=

-75.350 deg. F 76.030'deg. F temperature:14 ( ~76.030 )

=

78.550'deg. F, 0.4833 psia despointi.1

( 78.550 ).

=

77.880 deg.- F, 0.4727 psia devpoint 2 l( 77.880')

-=

75.910 deg. F, 0.4429 psia ~

~derpoint. 3

. ( -75.910-)

=-

.76.830 deg.'F~,10.4566 psia

-despoint 4

(- 76.830-) ~=

77.480 deg. F, 0.4665~ psia

'derpoint 5

( 77.480 )-

=

70.620 deg.:F, 0.3707, psia

'despoint: 6

( 70.620.)

=

73.7037-psia pressure. 1

( 737037 ) =

73.7036 poin pressure 2

..(

737036 )

=

weighted averages, volume and air mass 86.51690 deg. F-temperature

=

73.70360 psia

=

pressure 0.46230 pois

=

vapor pressure volume

=

274000 cu. ft.

=

99173.0 lba dry air mass i

i L-m

..7-

.HNP Unit:1-1988 ILRT/ Test data set 28 time = 1930

-date = 1129

< sensor-

.rav data value

. temperature 1 ('

82.140 )

82.140~deg. F

=

85.080 deg. F temperature 2(

85.080 )

=

87.420 deg. F temperature 3.(

87.420 )

-=

190.630 deg. F

- temperature 4 ( -- 90.630 )

=

93.120 deg. F

' temperature 5

(-

93.120')

=

95.610 deg. F temperature 6( 95.610

)-

=

-100.000 deg. F temperature

-7 (-100.000 )-

=

-temperature '8 ( 105.620 ).

= ' 105.620 deg. F 112.810 deg. F

- temperature '9 ( 112.810 )

=

110.960 deg. F temperature 10-( 110.960 1

=

75.570 deg. F

. temperature 11-(.75.570 )

=-

76.050 deg. F temperature-12'(

76.050 ).

=

75.320 deg. F

- temperature 13.(-

75.320 )

=

75.990 deg. F' temperature 14 ( 75.990 )

=

78.640 deg. F, 0.4847 psia dewpoint

'l

(

78.640-)

=

77.880 deg. F, 0.4727 psia dewpoint 2

( 77.880 )

=

75.870 deg. F, 0.4423 psia dewpoint 3

( 75.870 )

=

dewpoint 4

( 76.800

)_

76.800 deg. F, 0.4562 psia

=

77.470 deg. F, 0.4664 psia dewpoint 5

-(

77.470 )

=

72.360 deg. F, 0.3932 psia dewpoint 6

( 72.360 )

=

73.7003 psia pressure 1

( 737003-)

=

73.7005 psia pressure 2

( 737005 )

=-

weighted averages,-volume and air mass 86.50921 deg. F temperature

=

73.70050 psia

=

pressure 0.46229 psia vapor pressure

=

274000 cu. ft, volume 99170.2 lba dry air mass

=

1-

F ll~.

HNP Unit 1-1988 ILRT/ Test

~ data set 29 time = 1945. date = 1129 sensori raw data value 82.170 deg. F temperature 1( 82.170 )

=

85.120 deg. F

' temperature 2(- 85.120 )

=

87.480 deg. F temperature 3( 87.480 )

=

90.700 deg. F temperature 4( 90.700 )

=

93.270 deg. F temperature 5( _93.270 )

=

95.640 deg. F temperature 6( _'95.640 )

=

100.020 deg. F

-temperature 7( 100.020 )

=

105.640 deg. F temperature 8-( 105.640 )

=

112.740 deg. F temperature 9 ( 112.740 )

='

110.810 deg. F temperature 10 ( 110.810 )

=

75.550 deg. F 75.550 )

temperature 11 (. '76.020.)'

=.

76. 020 deg. F -

temperature.12 (

e 75.320 deg. F temperature 13 ( 75.320 )

=

75.970 deg. F

-temperature 14 ( 75.970 ) =

Jdevpoint 1-( 78.6601)

.s 78.660 deg. F, 0.4850 psia 77.710 deg. F, 0.4701 psia devpoint-2

( -77.710 )

=

76.050 deg. F, 0.4449 psia devpoint 3

( '76.050 )

=

76.840 deg. F, 0.4568 psia devpoint 4

( 76.840 )

=

77.470 deg. F, 0.4664 psia dewpoint 5

( 77.470 )

=

69.750 deg. F, 0.3598 psia devpcint 6

( 69.750 )

=

1 73.6973 psia pressure 1

( 736973 )

=

73.6978 psia pressure 2

( 736978 )

=

weighted averages, volume and air mass 86.51938 deg. F temperature

=

73.69780 psia

=

. pressure 0.46270 psia vapor pressure

=

274000 cu. ft.

volume

=

99164.1 lba dry air mass

=

l

(

HNP linit 1-1988 ILRT/ Test

, data. set' 30'

. time = 2000 date'='1129 sensor raw data value temperature 1-('

82.210 )

=:

82.210 dog. F temperature 2(

85.170 )

=

85.170 deg. F temperature 3-(

87.530 )

='

87.530 deg. F temperature 4 (.

90.730L) ~ ' ='

90.730 deg. F~

temperature; 5 (-

93.310 )

=

93.310 deg. F.

temperature 6 (, 95.670 )

95.670 deg..F

=

temperature 7.( 100.040 )

.100.040 deg. F

=

temperature

_8.(

105.660')== :105.660 deg. F temperature 9( 112.690 )

,112.690 deg. F

=

temperature 10 (~110.650 )

110.650 deg. F

=

temperature 11 ( 75.530 )

75.530 deg. F

=-

temperature 12 ( 75.990 )

= ' <75.990 deg. F temperature 13 (

75.280 )

75.280 deg..F

=

75.930 deg. F-temperature 14 ( '75.950 )

=

78.620 deg. F, 0.4844 psia

~ dewpoint 1

.(.

78.620 )

=

-dewpoint 2

( -77.700 )

=~

77.700 deg. F, 0.4699 psia dewpoint-3

(-.76.090 ) :=

76.090 deg. F, 0.4455 psia

. dewpoint 4

(

76.840-)

76.840 deg. F, 0.4568 psia

=

77.540 deg. F, 0.4675 psia dewpoint 5

.(

77.540.)

=

dewpoint. 6

('.71.160 l' 71.160 deg.

F',

0.3775 psia.

=

pressure. 1

( 736940 )

=

,73.6940 psia pressure = 2

(

736949 )

=

73.6949 psia weighted averages,-volume and air mass 86.51582 deg. F-temperature

=

73.69490 psia

=

pressure 0.46288 psia vapor pressure

=

volume 274000 cu.. ft,

=

99160.6 lbm dry air mass

HNP Unit 1-1988 ILRT/TOct f

data. set 31

' time = 2015' date = 1129 sensor raw data value 82.250 deg. F temperature -1 ( 82.250 )

=

85.210 deg.,F

' temperature 2 (' 85.210 )

=

87.590 deg. F temperature 3(,87.590 )

=

99.780 deg.'F temperature 4( 90.780 )

=

93.360 deg.' F temperature 5( 93.360 )

=

95.680 deg. F temperature 6(. 95.680 )

=

100.070 deg. F temperature 7( 100.070 )

=

105.700 deg. F temperature 8( 105.700 )

=

temperature 9-( 112.610 )

= 112.610 deg. F 110.480 deg. F temperature 10 ( 110.480 )

=

75.520 deg. F temperature 11 ( 75.520 )

=-

75.970 deg. F temperature 12 ( 75.970 )

=

75.260 deg. F temperature 13 ( 75.260 1

=

75.930 deg. F temperature 14 (.75.930 )

=

78.490 deg. F, 0.4823 psia dewpoint. 1

( 78.490 )

=

77.570 deg. F, 0.4679 psia dewpoint.2

( 77.570 )

=

76.090 deg. F, 0.4455 psia dewpoint 3'

( 76.090 )

=

dewpoint 4

( 76.900 )

=

76.900 deg. F, 0.4577 psia 77.590 deg. F, 0.4682 psia dewpoint 5

( 77.590 )

=

71.950 deg. F,_O.3878 psia dewpoint. 6

( 71.950 )

=

73.6910 psia pressure 1

( 736910 )

=

73.6918 psia pressure 2

( 736918 )

=

weighted averages, volume and air mass 86.51682 deg. F temperature

=

73.69180 psia

=

j pressure 0.46241 psia

=

j vapor pressure 274000 cu. ft.

volume

=

99156.9 lba dry air mass

=

i

\\

l J

\\

l

HNP Unit 1-1988 ILRT/ Test data set 32 time = 2030 date = 1129 sensor raw data value 82.290 deg. F temperature 1( 82.290 )

=

85.260 deg. F temperature 2( 85.260 )

=

87.630 deg. F temperature 3( 87.630 )

=

90.850 deg. F temperature 4( 90.850 )

=

93.410 deg. F temperature 5( 93.410 )

=

05.710 deg. F temperature 6( 95.710 )

=

100.090 (=g. F temperature 7( 100.090 )

=

105.730 deg. F temperature 8( 105.730 )

=

112.570 deg. F temperature 9( 112.570 )

=

110.330 deg. F temperature.10 ( 110.330 )

=

75.500 deg. F temperature 11 ( 75.500 )

=

75.950 deg. F temperature 12 ( 75.950 )

=

75.250 deg. F temperature 13 ( 75.250 ) =

75.920 deg. F temperature 14 ( 75.920 )

=

78.630 deg. F, 0.4846 psia devpoint 1

( 78.630 )

=

77.560 deg. F, 0.4678 psia devpoint 2

( 77.560 )

=

76.030 deg. F, 0.4446 paia devpoint 3

( 76.033 )

=

76.900 deg. F, 0.4577 psia devpoint 4

( 76.900 )

=

77.520 deg. F, 0.4672 paia-devpoint 5

( 77.520 ) =

69.970 deg. F, 0.3626 psia despoint 6

(. 69.970 )

=

13.6881 psia pressure 1

( 736881 )

=

73.6893' psia pressure 2

( 736893 )

=

weighted averages, volume and air mass 86.52242 deg. F temperature

=

73.68930 psia

=

pressure 0.46239 psia

=

vapor pressure 274000 cu. ft.

volume

=

99152.5 lba dry air mass

=

HNP Unit 1-1988 ILRT/ Test data set 33 time = 2045 date =-1129 sensor raw data value 82.320 deg. F temperature 1( 82.320 )

=

85.320 deg. F temperature 2( 85.320 )

=

87.700 deg. F temperature 3( 87.700 )

=

90.910 deg. F temperature 4( 90.910 )

=

93.470 deg. F temperature 5( 93.470 )

=

95.750 deg. F -

temperature 6( 95.750 )

=

100.120 deg. F temperature 7( 100.120 )

=

105.770 deg. F temperature '8 ( 105.770 )

=

112.510 deg. F temperature 9( 112.510 )

=

110.150 deg. F temperature 10 ( 110.150 )

=

75.500 deg. F temperature 11 ( 75.500 )

=

75.950 deg. F temperature 12 ( 75.950 )

=

75.240 deg. F temperature 13 ( 75.240 )

=

75.900 deg. F temperature 14 ( 75.900 )

=

78.800 deg. F, 0.4873 psia devpoint 1

( 78.800 )

=

77.840 deg. F, 0.4721 psia derpoint 2

( 77.840 )

=

76.140 deg. F, 0.4463 psia devpoint 3

( 76.140 )

=.

76.910 deg. F, 0.4578 psia devpoint 4

( 76.910 )

=

77.530 deg. F, 0.4673 psia devpoint 5

( 77.530 ) =

72.570 deg. F, 0.3960 psia devpoint 6

( 72.570 )

=

73.6889 psia prescure' 1

( 736889 )

=

73.6863 psia pressure 2

( 736863 )

=

weighted averages, volume and air mass 86.53297 deg. F temperature

=

73.68630 psia

=

pressure 0.46422 psia

=

vapor pressure 274000 cu. ft.

volume

=

99144.1 lba dry air mass

=

l

BCP Technical Services, Inc.

' Hatch 1988 ILRT Final Report Appendix III VERIFICATION DATA SET i

HNP Unit 1 - 1988 ILRT/ Verification DATA

SUMMARY

REPORT data time date temperature pressure vapor dry air set-deg F psia pressure mass psia lbm 1

2215 1129 86.5382 73.6910 0.4663 99146.6 2

2230 1129 86.5309 73.6781 0.4677 99128.7 3

2245 1129 86.5227 73.6655 0.4672 99113.7 4

2300 1129 86.5232 73.6531 0.4678 99096.1 5

2315 1129 86.5195 73.6407 0.4674 99080.5 6

2330 1129 86.5235 73.6284 0.4675 99062.9 7

2345 1129 86.5214 73.6158 0.4686 99044.7 8

O 1130 86.5262 73.6035 O.4677 99028.4 9

15 1130 86.5322 73.5911 0.4679 99010.3 10 30 1130 86.5327 73.5789 0.4673 98994.5 11 45 1130 86.5212-73.5666 0.4698 98976,6 12 100 1130 86.5202 73.5541 0.4684 98961.7 13 115 1130 86.5239 73.5416 Q.4667 QAQ4Q 7 14 130 1130 86.5190 73.5296 0.4694 98927.4 15 145 1130 86.5191 73.5173 0.4698 98910.2 16 200 1130 86.5215 73.5050 0.4700 98892.8 17 215 1130 86.5230 73.4928 0.4692 98877.2

HNP Unit 1 - 1988 ILRT/ Verification TREND REPORT leakage rates total time maus point data time date elapsed measured leakage uc1 leakage uci

-set time rate rate rate rate rate (hrs)

(%/ day)

(%/ day) 1 2215 1129 0.00 0.0000 0.0000 0.0000 0.0000 0.0000 2 2230 1129 0.25 1.7414 1.7414 1.7414 1.7414 1.7414 3 2245 1129 0.50 1.5946 1.5946 1.5946 1.5946 2.3195 4 2300 1129 0.75 1.6323 1.6016 2.4532 1.6139 1.7300 5 2315 1129 1.00 1.6016 1.5852 1.8933 1.5969 1.6553 6 2330 1129 1.25 1.6212 1.5916 1.8095 1.6067 1.6434 7 2345 1129 1.50 1.6449 1.6084 1.7944 1.6270 1.6610 8

0 1130 1.75 1.6354 1.6143 1.7707 1.6314 1.6564 9

15 1130 2.00 1.6507 1.6247 1.7644 1.6419 1.6639 10 30 1130 2.25 1.6370 1.6266 1.7505 1.6410 1.6583 11 45 1130 2.50 1.6468 1.6314 1.7444 1.6447 1.6592 12 100 1130 2.75 1.6279 1.6289 1.7323 1.6390 1.6524 13 115 1130 3.00 1.6452 1.6322 1.7287 1.6420 1.6536 14 130 1130 3.25 1.6332 1.6315 1.7216 1.6396 1.6497 15 145 1130 3.50 1.6352 1.6315 1.7163 1.6385 1.6473 16 200 1130 3.75 1.6389 1.6324 1.7128 1.6389 1.6466 17 215 1130 4.00 1.6308 1.6313 1.7077 1.6367 1.6438 e

d

HHP Unit 1 - 1988 ILRT/ Verification TOTAL TIME LEAKAGE RATE REPORT VERIFICATION data time date elapsed dry air measured leakage set time mass rate rate (hre)

(1bm)

(%/ day)

(%/ day) 1 2215 1129 0.00 99146.6 0.0000 0.000 2 2230 1129 0.25 99128.7 1.7414 1.741 3 2245 1129 0.50 99113.7 1.5946 1.595 4 2300 1129 0.75 99096.1 1.6323 1.602 5 2315 1129 1.00 99080.5 1.6016 1.585 6 2330 1129 1.25 99062.9 1.6212 1.592 7 2345 1129 1.50 99044.7 1.6449 1.608 8

0 1130 1.75 99028.4 1.6354 1.614 9

15 1130 2.00 99010.3 1.6507 1.625 10 30 1130 2.25 98994.5 1.6370 1.627 11 45 1130 2.50 98976.6 1.6468 1.631 12 100 1130 2.75 98961.7 1.6279 1.629 13 115 1130 3.00 98942.7 1.6452 1.632 14 130 1130 3.25 98927.4 1.6332 1.632 15 145 1130 3.50 98910.2 1.6352 1.631 16 200 1130 3.75 98892.8 1.6389 1.632 17 215 1130 4.00 98877.2 1.6308 1.631 Upper limit on leakage rate =

1.9870 %/ day 1.6313 %/ day Total time leakage rate

=

Lower limit on leakage rate =

1.3870 %/ day i

HNP Unit 1 - 1988 ILRT/ Verification MASS POINT LEAKAGE RATE REPORT VERIFICATION data time date elapsed dry air leakage set time mass rate (hrs)

(1bs)

(%/ day) 1 2215 1129 0.00 99146.6 0.0000 2 2230 1129 0.25 99128.7 1.7414 3 2245 1129 0.50 99113.7 1.5946 4 2300 1129 0.75 99096.1 1.6139 5 2315 1129 1.00 99080.5 1.5969 6 2330 1129 1.25 99062.9 1.6067 7 2345 1129 1.50 99044.7 1.6270 8

0 1130 1.75 99028.4 1.6314 9

15 1130 2.00 99010.3 1.6419 10 30 1130 2.25 98994.5 1.6410 11 45 1130 2.50 98976.6 1.6447 12 100 1130 2.75 98961.7 1.6390 13 115 1130 3.00 98942.7 1.6420 14 130 1130 3.25 98927.4 1.6396 15 145 1130 3.50 98910.2 1.6385 16 200 1130 3.75 98892.8 1.6389 17 215 1130 4.00 98877.2 1.6367 Upper limit on leakage rate =

1.9920 %/ day 1.6367 %/ day Mass point leakage rate

=

Lower limit on leakage rate =

1.3920 %/ day

(

HNP linit 1 - 1988 ILRT/ Verification 73.69 hN

(

P 5

I-I A

\\

~

73.49 i

i i

i 22151129 IIME 2151130 L

HNP Unit 1 - 1988 ILRT/ Verification

^s. w'sN'h,w s

t s

g s

~

L s

~,.

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~

s s

's%

LM s

~,.

g s

S q%

s.,

y 98818 I

I I

l' s 2215 1129 TIME 215 1138 T

HNP Unit 1 - 1988 ILRT/ Verification 2.32 1

\\

y,

) /

D LA V

l 1

)

h 2215 1129 TIME 215 1130

HNP Unit'l - 1988 ILRT/ Verification 2.45 y

t s_

{

=

r

~

f D

}. A a

L 3.

)

i 10.00 I

I I

I 22151129 IIME 2151139 I

(, ( ::

f HNP' Unit 1.-

1988 ILRT/ Verification ip.

data set 1-

- time,='2215-date = 1129 sensor

-raw data.

value

~

~ 1(

82.530'14 82.530 deg. F

' temperature

=

85.580 deg. F temperature 2 (-

85.580 )

=

~87.980 deg. F temperature 3( 87.980

)-

=

91.240 deg. F temperature 4,(

91.240 1

=

93.720 deg. F

- temperature '5 ( 93.720 )

=

95.900 deg..F temperature 6( 95.900 )

=

100.240 deg. F temperature 7't.100.240.)

=

105.890 deg. F temperature 8.( 105.890 )

=

112.080 deg. F temperature 9( 112.080 )

=

109.140 deg. F temperature 10,( 109.140 )

=

75.400 deg. F temperature 11 ( 75.400 )

=

75.850 deg. F

. temperature 12

(,

75.850 )

=

1 75.150 deg. F temperature 13 (

75.150 )

=

75.820 deg. F-

temperature 14 (. 75.820 )

-=

dewpoint 1

(

78.670")

78.670 deg. F, 0.4852. psia

=

77.840 deg. F, 0.4721 psia devpoint 2

( 77.840 )

=

76.470 deg. F, 0.4512 psia

devpoint 3

( 76.470 )

=

77.090 deg. F, 0.4606 psia dewpoint 4

( 77.090 )

=

dewpoint 5

(

77.780

).

77.780 deg. F, 0.4712 psia

=

70.430 deg. F, 0.3683 psia dewpoint 6

( 70.430 )

=

73.6918 psia pressure 1

(

736918 )

=

73.6910 psia pressure 1 2

( 736910 )

=

weighted averagec, volume and air' mass 86.53818 deg. F temperature

=

73.69100 psia

=

pressure 0.46631 psia

=

vapor pressure 274000 cu. ft.

volume

=

99146.6 lba dry air mass

=

L.

l '.

1 l

L_

HNP Unit 1 - 1988 ILRT/ Verification data set

?

l time = 2230 date = 1129

]

sensor raw data value

]

82.560 deg. F

)

temperature-1 (

82.560 )

=

85.610 deg. F temperature 2(

85.610 )

=

temperature 3( 88.030 )

88.030 deg. F

=

temperature 4( 91.280 )

=

91.280 deg. F temperature 5( 93.750 )

93.750 deg. F

=

95.910 deg. F temperature 6( 95.910 )

=

100.260 deg. F temperature 7( 100.260 )

=

temperature 8( 105.890 >

105.890 deg. F

=

111.990 deg. F temperature 9( 111.990.)

=

temperature 10 ( 108.980 )

108.980 deg. F

=

temperature 11 (

75.380 )

75.'380 deg. F

=

temperature 12 (

75.830 )

75.830 deg. F

=

75.130 deg. F temperature 13 (

75.130 )

=

temperature 14 (

75.790 )

75.790 deg. F

=

78.930 deg. F, 0.4894 psia dewpoint 1

(

78.930 )

=

78.030 deg. F, 0.4751 psia dewpoint 2

(

78.030 )

=

76.440 deg. F, 0.4507 psia dewpoint 3

( 76.440 )

=

77.120 deg. F, 0.4610 psia dewpoint 4

(

77.120 )

=

dewpoint 5

( 77.800 )

=

77.800 deg. F, 0.4715 psia dewpoint 6

(

73.050 )

73.050 deg. F, 0.4024 psia

=

73.6787 psia pressure 1

(

736787 )

=

pressure 2

(

736781 )

=

73.6781 psia weighted averages, volume and air mass 86.53095 deg. F temperature

=

73.67810 psia

=

pressure 0.46766 psia vapor pressure =

274000 cu. ft, volume

=

99128.7 lba dry air mass

=

i f

HNPEUnit 1'- 1988 ILRT/ Verification

data set 3L time = 2245 date = 1129 sensor raw data value 82.570 deg. F' temperature'.11(. 82.570 ). =

temperature.2-(

85.650 1.=

85.650 deg. F' temperature 3, (-

88.070 l'

=

88.070 deg. F temperature 4( 91.320 )

=

91.320 deg. F 93.800 deg. F GT temperature 'S (.

93.800 )

=

temperature: 6 (.

95.930 )

=

95.930 deg. F

' temperature 7.( 100.270

)-

100.'270 deg. F

=

temperature 8( 105.900

).

105.900 deg. F-

=

temperature 9-( 111.890 )

' 111.890 deg. F temperature 10 ( 108.820 ) -

108.820 deg. F temperature 11'(

75.370

)-

=

75.370 deg. F temperature 12 ( 75.800 )

=

75.800 deg. F temperature 13 ( 75.090 )

75.090 deg. F

=

temperature 14'(

75.770 )

=

75.770 deg. F

' dewpointl

(-

78.920-)

78.920 deg. F, 0.4892 psia

=

dewpoint' 2

(

77.960 )

77.960 deg. F, 0.4740 psia

=

dewpoint 3

(

76.370 )

76.370 deg. F, 0.4497 psia

=

dewpoint 4

(

77.140-)

77.140 deg. F, 0.4613 psia

=

dewpoint 5

( 77.800 )

=

77.800 deg. F, 0.4715 psia dewpoint 6

( 69.960 )

=

69.960 deg. F, 0.3624 psia pressure-l'

( 736659-)

=

73.6659 psia pressure 2

( 736655 )

=

73.6655 psia weighted averages, volume and air mass 86.52272 deg. F temperature

=

73.66550 psia-pressure

=

0.46720 psia vapor pressure =

volume

=

274000 cu. ft.

99113.7 lba dry air mass

=

-1 l

l

_______.___.___.________.___.______.__m_

< 3%

HNP-Unit 1 - 1988 ILRT/ Verification data set 4

~ time = 2300 'date = 1129 sensor-raw data

'value temperature- 'l(

82.600

).

82.600 deg. F

=

temperature ~2 ( 85.680 )

85.680 deg. F

=

temperature 3(

88.110 )

88.110 deg. F

=

temperature. 4(

91.350 )

91.350 deg. F.

=

. temperature 5(

93.840

)~

93.840 deg. F

=

- temperature 6 (-

95.970

).

=

95.970 deg. F temperature 7( 100.310 )

=

100.310 deg. F temperature 8( 105.910 )

105.910 deg. F-

=

temperature 9( 111.800 )

111.800 deg. F

=

temperature 10 ( 108.640 1 108.640 deg. F

=

- temperature 11 ( -75.350 )

75.350 deg. F

=

temperature 12'('

75.780 )

75.780 deg. F.

=

temperature 13 ( -75.090 )'

75.090 deg. F

=

temperature 14 (

75.760 )

-75.760 deg. F

=

dewpoint -' i.

(

78.940.) -=

78.940 deg..F, 0.4895 psia dewpoint 2

(

78.100 )

78.100 deg. F, 0.4762 paia-

=

dewpoint 3

(

76.380 )

=

.76.380 deg. F, 0.4498 psia dewpoint.4

(.77.170

).

77.170 deg. F, 0.4618 psia

=

dewpoint 5

(.77.780 )

77.780 deg. F, 0.4712 psia

=

dewpoint 6

(.

72.240 )

72.240 deg. F, 0.3916 psia

=

pressure. 1

( 736532 )

73.6532 psia

=

pressure 2

(-

736531 )

73.6531 psia

=

weighted averages, volume and air mass 86.52325 deg. F temperature

=

73.65310 psia pressure

=

0.46776 psia vapor pressure =

volume

=

274000 cu. ft.

99096.1 lbm dry air mass

=

l l

--___m___.

o HNP Unit 1 - 1988 ILRT/ Verification data set 5,

time = 2315 date =-1129 sensor raw data value temperature 1

(-

82.640 )

=

82.640 deg. F temperature 2(

85.720 )

=

85.720 deg. F temperature: 3(

88.140 )

=

88.140 deg. F temperature.4 (

91.430 )

=

91.430 deg. F temperature

_5 (

93.870 )

93.870 deg. F'

=

temperature.

6' (

95.980 )

95.980 deg. F

=

temperature-

'7. ( 100.320 )'

100.320 deg. F

=

temperature 8( 105.920')

105.920 deg. F

=

temperature 9 -(

111.700 ).

=

'111.700 deg. F temperature 10 ( 108.480 )

=- '108.480 deg. F temperature 11'(

75.340 )

,75.340 deg.-F

=

temperature 12.(

75.750 )

=

75.750 deg. F temperature 13

(-

75.080 )

=

75.080 deg. F temperature 14

(.

75.740 ) '=

75.740 deg. F dewpoint 1

( 78.950 )

=

78.950 deg. F, 0.4897 psia dewpoint 2

'(.

78.050 )

=

78.050 deg. F, 0.4754 psia dewpoint 3

('

76.340')

=

76.340 deg. F, 0.4492 psia 77.160 deg. F, 0.4616 psia dewpoint (

77.160 )

=

77.750 deg. F, 0.4707 psia dewpoint 5

.(

77.750 )

=

dewpoint 6

~(

71.310 )

=

71.310 deg. F, 0.3795 psia 73.6406 psia pressure 1

( 736406 )

=

73.6407 psia

. pressure 2

(

736407 )

=

weighted averages, volume and air mass l

86.51949 deg. F temperature _

=

73.64070 psia

=

pressure 0.46738 psia vapor pressure =

volume

=

274000 cu. ft, 99080.5 lbm dry air mass

=

l-

.s l9

I J'

)

HNP Unit 1 - 1988 ILRT/ Verification data set

'6 time = 2330 date = 1129-sensor' raw data value

. temperature' 1 (

82.670')

82.670 deg. F

=

-temperature 2(

85.750 )

85.750 deg. F-

=

temperature 3,(

88.200 )

88.200~deg. F

=

temperature 4(

91.500 )

91.500 deg. F

=

temperature 5(

93.920 )

=1 93.920 deg. F temperature 6(

96.010 )

=

96.010 deg. F temperature ~7 ( 100.340 )

100.340 deg. F'

=

temperature 8 ( 105.930 )

105.930 deg. F

=

temperature 9'( 111.620')

=

111.620 deg. F temperature 10 (.108.310 )

108.310 deg. F

=

temperature 11 (

75.330 )

=

75.330 deg. F temperature 12 ( 75.740 )

75.740 deg.' F

=

temperature 13 ( 75.060 )

=

75.060 deg. F temperature 14 (

75.740 )

75.740 deg. F

=

dewpoint 1

(

78.870 ) ' =

78.870 deg. F, 0.4884 psia dewpoint 2-(

78.130

)-

=.

78.130 deg. F, 0.4767. psia dewpoint 3

(

76.370 l' 76.370 deg. F=,:0.4497 psia

=

dewpoint 4

(

77.180 )

77.180 deg. F, 0.4619 paia

=

dewpoint. 5

(

77.720 )

=

77.720 deg. F, 0.4703 psia dewpoint 6

-(

'70.460 )

70.460 deg. F, 0.3687 psia

=

pressure 1

(

736281

)-

=

73.6281 psia pressure 2

(

736284 >-

73.6284 psia

=

weighted averages, volume and air mass 86.52354 deg. F temperature

=

73.62840 psia presrure

=

0.46750 psia vapor pressure =

volume 274000 cu. ft.

=

99062.9 lba dry air mass

=

u o

i ;M

/

HNP' Unit 1 - 1988 ILR7/ Verification data' set 7'

I

-time = C345.

date = 1129 4

sensor raw data

" value --

. temperature

1. (. ;82.700 ).

82.700 deg. F.

=

- temperature 2

(~

85.780 3.=

85.780'deg. F 88.250 deg. F temperature 3'(

88.250-). =

91.510 deg. F temperature 4 (

91.510 )

=

temperature ~ 5'(

93.~950 )'

=

93.950 deg. F 96.030 deg. F temperature 6(

96.030 )

=

- temperature -7 ( 100.360,).= -100.360 deg. F-105.950 deg. F temperature 8( 105.950 )

s' temperature 9( 111.550 )

111.550 deg. F

=

108.140 deg. F temperature 10 ( 108.140 )

=

75.320'deg.1F temperature 11.(

75.320')

=

75.730 deg. F temperature 12 (

75.730 )

=

75.050 deg. F temperature 13 ( 75.050

)-

=

75.720 deg. F temperature 14 (

75.720 )

=

~78.900 deg. F, 0.4889 psia dewpoint-1

(

78.900 )

=

78.320 deg.

F-,

0.4796 psia.

- dewpoint: 2

(

78.320-)

=

76.450 deg. F, 0.4509 psia dewpoint 3

(

76.450 )

=

77.220 deg.'F, 0.4625 psia dewpoint 4-( 77.220 )

=

77.730 deg. F, 0.4704 psia

- dewpoint 5

(

77.730 )

=

71.020 deg. F, 0.3757 psia-dewpoint 6

( 71.020 )

=

73.6155 psia pressure 1

( 736155 )

=

73.6158 psia pressure 2

( ~736158 )

=

, veighted. averages, volume and air mass 86.52144 deg. F temperature

=

73.61580 psia

=

pressure O.46863 psia

=

vapor pressure 274000 cu. ft.-

volume

=

99044.7 lba dry air mass.

I

(

-l s

ik HNP Unit 1 - 1988 ILRT/ Verification data set 8

i'

[

time =

.0

'date =-1130 1

. raw' data value-j sensor temperature.

1-(

82.720 )

=

82.720 deg. F

? temperature 2(

85.830 )

=

85.830 deg. F L

. 88.290 )

s' temperature 3(

88.290 deg. F temperature L4 ( 91.580 )

91.580 deg. F

=

temperature 5

('--

93.990 )

93.990 deg.'F

=

temperature ~6(

96.060 )

96.060 deg. F

=

' temperature 7( 100.380 )

100.380 deg. F

=

temperature 8-('105.970 )

=

105.970 deg. F temperature-9( 111.490 )

'111.490 deg. F

=

temperature 10 ( 107.960

).

=

107.960 deg. F temperature 11 ( 75.310 )

75.310 deg. F

=

temperature'12 ( 75.730 L) 75.730 deg. F

=

75.040 deg. F temperature 13 ( 75.040 )

=

75.710 deg. F-temperature 14 ( :75.710 )-

=

dewpoint _.1

(

78.860 ).

78.860 deg. F, 0.4882 psia

=

dewpoint ~2

(

78.040~)

=

78.040.deg. F, 0.4752 psia 76.390 deg. F, 0.4500 psia dewpoint 3

(

76.390 )

=

dewpoint 4 st 77.250

)-

77.250 deg. F, 0.4630 psia 77.820 deg. F, 0.4718 psia dewpoint 5

(-

77.820 )

=

i.

dewpo' int 6~

(

72.620 )

72.620 deg.

F, 0.3967. psia

=

~

73.6029 psia pressure 1-(

736029 )

=

pressure 2

(

736035 )

73.6035 psia

=

weighted averages, volume and air mass 86.52623 deg. F temperature.

=

73.60350 psia pressure

=

0.46772 psia

=

vapor pressure 274000 cu. ft.

volume

=

99028.4 lba dry air mass l

l i- _ _ _ _ _ _ _ - _

ex

.HNP Unit 1 - 1988 ILRT/ Verification

.c

-data setc 9 time-s 15'

'date = 1130' sensor raw data value temperature. 1

(-

82.750L)-

82.750 deg. F

=

temperature 2( -85.880 )

85.880 deg. F

=

temperature 3-(.'88.330 )

88.330 deg. F

=

temperature 4

(-

91.630

)~

91.630 deg. F

=

. temperature 5( 94.030 )

=-

94.030 deg. F temperature 6( 96.080 )

's 96.080 deg. F temperature 7 ( 100.410 )

100.410 deg. F

=

temperature? 8.( 105.980-)

.105.980 deg. F

=

temperature 9( 111.400 )

111.400 deg. F

=

temperature 10 ( 107.820 )

=

107.820 deg. F temperature 11 (

75.310 )

=

75.310 deg. F temperature 12 4 75.730 )

75.730 deg. F

=

temperature 13 (.

75.030 )

=

75.030 deg. F-temperature 14 ( 75.710 )

75.710 deg. F

=

dewpoint 1

(-

78.880 )

78.880 deg. F, 0.4886 psia

=

devpoint 2

( 78.070 )

78.070 deg. F, 0.4757 psia

=

deupoint' 3

. ( 76.420 )

m 76.420 deg. F, 0.4504 psia

' dewpoint 4

(.

77.240 )

=

77.240 deg. F, 0.4629 psia dewpoint 5

( 77.810 )

=

77.810 deg. F, 0.4717. psia dewpoint 6

( 69.720 )

=

69.720.deg. F, 0.3595 psia pressure 1

( '735904 )

=

73.5904 psia pressure' 2.

( 735911 )

=

73.5911 pela weighted averages, volume and air mass temperature 86.53217 deg. F

=

73.59110 paia pressure

=

0.46794 psia vapor pressure =

volume 274000 cu. ft.

=

dry air mass 99010.3 lba

=

I

\\

l

_ _ _ a

HNP Unit 1.-

1988 ILRT/ Verification

{

data set 10 time =

30 date = 1130 sensor raw data value

'82.790 deg. F temperature 1 (

82.790 )

=

85.920 deg. F temperature 2(

85.920 )

=

88.370 deg. F temperature 3(

88.370 )

=

91.660 deg. F l

temperature 4(

91.660 )

=

94.060 deg. F temperature-5(.

94.060 )

=

96.130 deg. F temperature 6( 96.130 )

=

100.430 deg. F temperature 7 ( 100.430 )

=

105.990 deg. F temperature 8( 105.990 )

=

111.330 deg. F temperature 9( 111.330 )

=

107.660 deg. F temperature 10 ( 107.660-)

=

75.300 deg. F temperature 11 ( 75.300 )

=

'75.710 deg. F temperature 12 ( 75.710 )

=

75.020 deg. F temperature 13 ( 75.020 )

=

75.690 deg. F temperature 14 (

75.690 )

=

78.670 deg. F, 0.4852 psia dewpoint 1

(

78.670 )

=

77.950 deg. F, 0.4738 psia dewpoint 2

( 77.950 )

=

76.460 deg. F, 0.4510 psia dewpoint 3

(

76.460 )

=

77.260 deg. F, 0.4632 psia dewpoint-4

(

77.260 )

=

77.870 deg. F, 0.4726 psia dewpoint 5

( 77.870 )

=

70.930 deg. F, 0.3746 psia dewpoint 6

(

70.930 )

=

73.5780 paia pressure 1

(

735780 )

=

73.5789 psia pressure 2

( 735789 )

=

weighted averages, volume and air mass 86.53270 deg. F temperature

=

73.57890 psia

=

pressure 0.46732 paia vapor pressure

=

274000 cu. ft.

volume

=

98994.5 lba dry air mass

=

f

mrg.

e 1 :r-Q R

^

b

-i '...

1.

t a

HNPiUnit?1;-<1988 ILRT/ Verification b

.., 1..

8 data: set"'11:

4

time."=.

~45' date s 1130-O sensori

~rav. data ~

value temperature, 1-(f 82.810.)-

=-

82.810 deg.'F; L: '

temperature 52f(' 85.940?.).'

-85.940 deg.).F.

=

Temperature. 3.0 '88.410 ) '=-

88.410 deg.'F-

" temperature.'4;(91.720.')

's-91~.720 deg.-'F

[-

! temperature, 5 (

94.090.)

~

=-

94.090 deg.;F

" temperature 6 (c 96.130")

=.

96.130 deg.:F E

temperature. 7 ( 100.450 )J~=

100.450 deg.'F

temperature. 8-('106.000 > = 106.000 deg.:F

. temperature ' 9-(:111.240 ) - = :- 111.240 deg. F-

'. temperature 10 ( 107.500 )

=

107.500:deg. F:

~ temperature ^ 11 -'(.-

75.270

).

= :- ~75.270 deg. F:

' ~

=

. temperature 12 (.:75.680.')

75.680 deg. F'

. temperature 13-(

74.990;l-' =

74.990 deg. F temperature 14 ( _75.660 )

=

-75.660 deg..F

'N.

> (:. -78.960

),'=

- 78.960 deg. F, O.4898 psia:

~

dewpoint,1

' dewpoint Y2.

..(

78.420') ~=

78.420 deg. F, 0.4812 psia o

'devpoint "3-(,

76.490 );

76.490 deg. F, O.4515 psia

=

dewpoint.4y

.(

77.260 )

77.260 deg. F, 0.4632 psia

=

dewpoint

5.,

-(. 77.900 )

77.900 deg..F, 0.4731 psia'

=

'-dewpoint: 6

(.71.250 )'

=

'71.250 deg. F, O.3787. psia

[

. pressure 1

. ('

735654;)' =

73.5654 psia pressure 2

( 735666')

73.5666 psia

=

weighted averages,Lvolume and air mass 86.52117 deg. F-

temperature

=

73.56660 psia pressure

=

0.46978 psia.

vapor pressure =

volume' 274000 cu. ft.

=

.98976.6 lba dry air mass

=

I.

b

_ _ _ = _ _ _ _.

m.

y

,7 a

H d

F' 1

.HNP. Unit 1 1988'ILRT/ Verification

(

q

? data set-121 m;J.

P time = - 100 : :date1= 1130:

coensor raw data-value

temperature 1-(,:82.830,).

=

82.830 deg. F' temperature 2.(

85.970

)-

85.970 deg.:F:

=

Temperature'13-(

88.450 )-

=

88.450 deg.-F

. temperature';4'(

91.750;)

91.750.deg..F

=

2

,.. temperature :5.( '94.120

).

'=

94.~120 deg.' F temperature >6c(

96.170 )

='

96.170 deg. F temperature 7-( 100.470-)

=

100.470 deg. F temperature 8.( 106.000 )

106.000 deg. F

=-

temperature-9 ('111'120,)-

s' 111.120 deg. F

= temperature 10=(;107.390 ),=- 107.390 deg.. F.

temperature 11_(

75.260 )

=

75.260-deg. F Temperature, 12 (1.75.670 )

75.670 deg. F

=

temperature 13L(

74.980-)

74.980 deg. F

=

temperature.14:( 75.650:;) ~=

75.650 deg..F

dewpoint: 1

-( :78.940 ). ' =-

7

=.

78.940 deg.1F, 0.4895 psia dewpoint 2;

(

78.050 )

?78.050.deg. F, 0.4754. psia 76;450:deg.

F.,

0.4509. psia

, dewpoint -3

( '76.450 )

=

dewpoint 4

( :77.280 )-

77.280 deg. F, 0.4635 psia

=

.dewpointL 5

(

77.850 )

= '

77.850 deg.

F.,

0.4723 psia.

" dewpoint; 6c

(: 70.510-)

70. 510 deg. ' F, : 0. 3693 psia

=

pressure 1

(.735528 )

73.5528 psia-

=

. pressure 2

(-

735541 )

.73.5541 psia

=

weight'ed averages, volume and air mass-temperature 86.52023 deg. F

=

pressure:

73.55410 psia

=

0.46840 psia vapor pressure =

volume

=

274000 cu. ft.

dry air mass 98961.7 lba

=

- " m.

.r;

.HNP Unit 1 - 1988 ILRT/ Verification

' data set 13 time.= <115' date = 1130 D.

~ sensor-raw data value

' temperature 1(. 82.860-)

'82.860 deg. F

=

L temperature. 2 (-

86.030 )

=

L 86.030 deg..F temperature.3.(

88.480 )

=-

88.480 deg. F temperature' 4

(.

91.780'), =

.91.780 deg. F

' temperature-5 ;(

94.170-)

=

94.170 deg. F temperature 6'(.

96.200 l'

=

96.200 deg. F temperature-7,( 100.490 )

=

100.490'deg..F temperature 8( 106.020 ). =

106.020 deg. F temperature 9 ('111.030 ):

111.030 deg. F

=-

temperature 10 ( 107.250 )

2107.250 deg. F

=

temperature 11 ('

75.250 ) ' =

75.250 deg. F temperature 12 ( 75.660;)

. 75.660 deg.'F temperature 13.( '74.980 11

74.980 deg.' F L

temperature 14'(

75.640 )

=

75.640 deg. F

' dewpoint 1

(

78.960-).

78.960 deg..F, 0.4898 psia

=

dewpoint 2

(.

78.340 )

=

78.340 deg. F, 0.4800 psia dewpoint 3

(-

76.510 )'

76.510 deg. F, 0.4518 psia

=

dewpoint -4

( 77.300 )

77.300 deg. F, 0.4638 psia

=

dewpoints 5'

( 77.880 )

=

77.880 deg. F, 0.4727 psia dewpoint 6

( 72.220 )

72.220 deg. F,,0.3913 psia

=

pressure. 1

(,'735404')-

73.5404 psia-

=

pressure.2

( 735419')

73.5419 paia

=

weighted averages, volume and air mass 86.52393 deg. F

. temperature

=

73.54190 psia pressure

=

0.46971. psia vapor pressure

=

volume 274000 cu. ft.

=

dry air mass 98942.7 lbm

=

1 i

i i

7, -, _ __

-l

!HNPLunit 1:- 1988 ILIT/ Verification

.s t

data. set..14' time =.130" ?dateL= 1130:

l $ < : sensor lc raw' data.

value-1 temperature.11('.

82.880 )

=

=82.880 deg..F.'

temperature-2_(l86.050.)

86.050 deg..F

=

temperature :3 ( - 88.530 );. =.

88.530 deg."-F temperature. 4..(

91.800 )

=

91.800 deg.tF temperature 5 (.'94.190 )'

. temperature. 6( 96.220 ) '

'94.190 deg. F

=-

~

96.220 deg; F

=-

temperature. 7-( 100.510.1 )

=

100.510 deg. F temperature.'8 ( 106.030 )

106.030 deg. F.

=

' temperature 9( 110.940 4.

.= 110.940 deg. F

temperature 10.( 107.110

).

~=

107.110 deg.'F temperature 11 ( 75.240 )

75.240 deg. F

=

' temperature 12.(

75.640 ).

r 75.640 deg. F.

' temperature.13'(. 74.960.)-

s' 74.960 deg.-F'

. temperature.14 (-

75.630 )

75.630 deg. F.

=

0 dewpoint 11

'( ~ ' 78.960 )

=.

'78.960.deg. F, 0.4898-psia

' dewpoint 2-( 78.290 )

s' t78.290.deg.

F., O.4792 psia

' dewpoint 3'

. (.76.460 l':=

76.460 deg. F, O.4510 psia dewpoint

'4'

(: 77.340 )'

=~

77.340'deg. F, 0.4644 psia-dewpoint 5 (E 77.860 l'

=-

-dewpoint. 6

(

69.640t)

='

77.860 deg. F, 0.4724 psia.

69.640 deg. F, O.3585 psia

~~

'73.5279 psia pressure 1

(. 735279 ) -=

pressure 2

.(

-735296 ) ~ = - -73.5296 psia

' weighted averages,. volume and air mass 86.51896 deg. F temperature-

.=

73.52960 psia pressure

=

0.46943 psia vapor pressure =

volume

=

274000 cu. ft.

=

98927.4 lba dry air mass g

I 1

-l lf

.HNP Unit 1 - 1988 ILRT/ Verification 1

[.

data set 15 j

, time =

145-date u 1130' i

sensor-raw. data value

{

a temperature- '1? (

82.920 )

=. '82.920 deg. F temperature 2. (-

86.080 )

86.080 deg. F

=

temperature. 3.(-

88.570 )'

=.

88.570 deg. F 91.830 deg. F

'l temperature:

4'(.

91.830 )

=

temperature-5-(

94.230.)

94.'230 deg._F

=

temperature 6 ('

96.230 )

=

96.230 deg. F temperature ' 7 ('100.540 )

100.540 deg. F

=

temperature 8_( 106.040 )

106.040 deg. F

=

temperature 9'( 110.850 )

= :110.850 deg. F temperature-10 ( 106.360 )

106.960 deg. F

=

' temperature'll

(.

75.230

)-

=.

75.230 deg. F temperature 12

(~

75.630 )

75.630 deg.-F

=

temperature 13 (

74.950 ')

74.950 deg. F

=

temperature 14 ( '75.620 )

75.620 deg. F

=

' dewpoint l'

('

78.920

)-

s' 78.920 deg. F, 0.4892 psia dewpoint.'2.

i 78.440 )

78.440 deg. F, 0.4815 psia J

=

dewpoint 3

(

76.460 )

76.460 deg. F, 0.4510 psia

=

dewpoint 4

( 77.340 )

77.340 deg. F, 0.4644 psia

=

. dewpoint 5,

(

77.870 )

77.870 deg.'F, 0.4726 psia

=

dewpoint 6

(

73.070

)-

=

73.070 deg. F, 0.4027 paia

' pressure 1

(

735153 )

73.5153 psia

=

pressure 2

(

735173 )

73.5173 paia

=

weighted averages, volume and air mass 86.51911 deg. F temperature

=

.73.51730 psia,

pressure

=

0.46978 psia vapor pressure

=

volume

=

274000 cu. ft.

98910.2 lbm dry air mass

=

l

1. e L__-

Y 5

HNP Unit 1 - 1988 ILRT/ Verification L

L data.Lset 16-l'

. time =s 200' date = 1130 sensor raw data value-

. temperature l' ( - 82.940 )

82.940 deg. F

=

temperature-2 (

86.120 )

86.120 deg. F-

=

temperature ~.3 ( '88.590 ).

88.590 deg. F

=

temperature 4 (

91.910 )

91.910 deg. F

=

temperature 5

(-

94.260

)-

=

94.260 deg. F temperature.6 (

96.260 )

96.260 deg. F

=

temperature 7( 100.560 )

=

100.560 deg. F temperature 8( 106.040 )

=-

106.040 deg. F temperature 9( 110.760 )

110.760 deg. F

=

temperature 10 ( 106.830-)

106.830 deg. F

=

i temperature'll (

75.220 )

=

75.220 deg. F temperature 12 (l 75.620 )

=

75.620 deg. F

. temperature 13'(

74.940 )

74.940 deg. F

=

temperature 14f(

75.620 )

75.620 deg. F.

=

dewpoint 1

(

79.040^)

79,040 deg.-F, 0.4911 psia

=

dewpoint 2

(

78.240')

=

78.240 deg. F, 0.4784 psia 1-dewpoint 3

(

76.560 )

=

76.560 deg. F, 0.4525 psia dewpoint 4

('

77.340 )

77.340 deg. F, 0.4644 psia

=

dewpoint-5

-(

'77.910 )

77.910 deg. F, 0.4732 psia"

=

dewpoint-6

(

69.'340 )

=

69.340 deg.

F.,

0.3548 psia pressure 1

( -735031

)~

=

73.5031 psia pressure' 2

( '735050 )

73,5050 psia

=

weighted averages, volume-and air mass 86.52148 deg. F temperature

=

73.50500 paia pressure

=

0.47005 psia vapor pressure

=

volume

=

274000 cu. ft.

dry air mass 98892.7 lbm

=

i

y

n pl$

.j y.

I

{

E

~

1 h

.HNP Unit 1 1988 ILRT/ Verification:

J W

Idata set 17I L

?

I

-time"=.

215-date = 1130 cy

,l sensor rawLdata-value o

j

temperature, 1-(

82.970.).L=

82.970.deg. F temperature 2( 186.1601);

-86.160 deg. F

=

temperature : 3-(.:88.640 )-

88.640 deg. F

=

. temperature 4 ( 191.940 )

91.940 deg. F-

=-

temperature 5 (';94.300-)

94.300 deg.;'FJ

=

temperature 6 ( 96.290 )

96.290 deg. F-

=

temperature. 7 ('100.570 )

=

100.570 deg..F

temperature 8 ( 106.050 )

=

106.050 deg. F

. temperature 9'(:110.700 )

=

110.700 deg. F temperature 10 ( 106.70,0 )

= 106.700 deg. F; temperature 11 (: '75.210'); =-

75.210 deg. F i-4 temperature 12L(: 75.610-).

75.610 deg. F

=

temperature 13 (: z74.930

).

74.930 deg. F

=

temperature 14-(- 75.600 )

=

75.600'deg. FJ

. dewpoint 1

-(

78.900 )

78.900 deg. F, 0.4889 psia

=

-dewpoint' 2

(

78.050-)

=

-78.050 deg. F,~0.4754 psia dewpoint 3'

. (

76.550 ).=-

.76.550'deg. F,.O.4524 psia

. dewpoint 4

.- 77.380-)

=~

(

77.380 deg. F, 0.4650 psia Edewpoint-5

(;.77.920 )

=.

77.920'deg. F, 0.4734. psia dewpoint 6.

-(

71;090 )

e 71.090 deg.LF.,~0.3766 psia pressure:.1 -

( -734906 )

!=

73.4906 psia pressure 2.

(-

734928 )

=

73.4928 psia weighted averages, volume and air mass-temperature 86.52297 deg. F

=

pressure L=

73.49280 psia 0.46917 psia vapor pressure-

=

volume

=

274000 cu. ft.

dry air mass.

98877.2 lba

=

o a

k

_

ML20235T193

Contents

Text

SUMMARY

SUMMARY

SUMMARY

References:

SUMMARY

SUMMARY

SUMMARY

SUMMARY

' 111.890 deg. F temperature 10 ( 108.820 ) -

. 75.660 deg.'F temperature 13.( '74.980 11

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ML20235T193

Text

SUMMARY

SUMMARY

SUMMARY

References:

SUMMARY

SUMMARY

SUMMARY

SUMMARY

' 111.890 deg. F temperature 10 ( 108.820 ) -

. 75.660 deg.'F temperature 13.( '74.980 11

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