ML17214A368

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Reactor Containment Bldg Integrated Leakage Rate Test, Final Rept
ML17214A368
Person / Time
Site: Saint Lucie NextEra Energy icon.png
Issue date: 04/28/1983
From: Dillon P, Musto A
EBASCO SERVICES, INC.
To:
Shared Package
ML17214A367 List:
References
NUDOCS 8308090525
Download: ML17214A368 (98)


Text

r 4-ST LUCIE PLANT UNIT NO.

1 NUCLEAR POWER PLANT FT PIERCE, FLORIDA DOCKET NUMBER 50-335 REACTOR CONTAINMENT BUILDING INTEGRATED LEAKAGE RATE TEST FINAL REPORT Prepared for:

FLORIDA POWER 6 LIGHT COMPANY Prepared by:

A J Musto Principal Mechanical Engineer Corporate 6 Consulting Engineering Approved b

F.8.&

P B D lion Manager Plant Start-Up 6 Test Date of Test Completion:

April 28, 1983

  • R 8308090525 830803

,PDR ADOCK 05000335 PDR

A~ g C

TABLE OF CONTENTS I'NTRODUCTION

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III.

TEST DISCUSSION A.

Description of the Containment B.

Description of ILRT Test Instrumentation 1.

2.

3.

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Temperature Instrumentation Humidity Instrumentation.....

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Pressure Instrumentation......................

Flow Instrumentation.........

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C.

Containment Pressurization Equipment D.

Description of the Computer Program E.

Description of the Testing Sequence 1O IV.

ANALYSIS AND INTERPRETATION.................................

14 V.

F IGURES

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19 1.

RTD Location and Volume

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RHD Location and Volume 21 3.

Flow Diagram for Pressure Sensing

& Controlled Leakage..

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Flow Diagram for Pressurization System.............

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Test Sequence.............................-.......

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APPENDICES

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25 A.

Computer Generated Report Al-A51 1'ontainment Temperature Stabilization.....

2.

Integrated Leakage Rate Test (ILRT)

.3.

Verification Controlled Leakage Rate Test

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CLRT).

Al-A3 A4-A32 A33-A51 B.

RTD and RHD Volumetric Weighting Factors....-.........

B and C Test Results..................

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I.

INTRODUCTION A periodic Type "A" Integrated Leakage Rate Test (ILRT) was performed on the primary containment structure of the Florida Power

& Light Company St Lucie Plant Unit No.

1 Pressurized

-Water Reactor.

This ILRT test was performed using the "Absolute Method" of testing in accordance with the Code of Federal Regulations, Title 10, Part 50, Appendix J Primary Reactor Containment Leakage Testing for Water-Cooled Power Reactors; in accordance with ANSI N45.4 1972, American National Standard Leakage-Rate Testing of Containment Structures for Nuclear Reactors and the calculations for leakage rate were performed as recommended in ANSI/ANS 56.8.,

Containment System Leakage Testing Requirements.

The ILRT was performed at a pressure in excess of the calculated peak containment internal pressure related to the design basis accident as specified in the Final Safety Analysis Report (FSAR) and the Technical Specifications.

This report describes and presents the results of this periodic Type "A" leakage rate test, including the supplemental test method utilized for verification.

II.

SUMMARY

To prepare the containment and associated systems penetrating the containment for the Type "A" ILRT, Type "B" Local Penetration leakage rate tests and Type "C" Local Containment Isolation Valve leakage rate tests were performed.

The Fuel Transfer Tube Flange "0" Ring Seal as well as the isolation valves for the Reactor Cavity Purification and Cooling System, the ILRT Pressure Sensing

System, the Controlled Leakage System and the ILRT Pressurizing/Depressurizing System were tested as indicated in Section III-E.

The Type "B" and Type "C" test results are presented in Appendix C.

Prior to pressurization of the containment vessel all containment e

systems and isolation valves were lined up to simulate accident conditions as described in Section 6.2 of the FSAR with the exception of the cavity purification penetrations 46 and 47 and the fuel transfer tube.

Section III-E describes testing of these penetrations.

The containment was pressurized to slightly above 39.6 psig to allow performance of the ILRT.

The containment atmosphere was allowed to stabilize and the accumulation of containment leakage rate data was initiated.

The simple mass point leakage rate was calculated as 0.156%/day.

The fitted mass point leakage rate for the same period was 0.147%/day with an Upper Confidence Limit (UCL) calculated as 0.153%/day.

The acceptance criteria for the ILRT dictates that the measured leakage plus uncertainties must be less than 0.375%/day (.75 times the containment design leakage).

The CLRT results verified the measured leakage within the allowable acceptance band.

P")

Subsequent to the Type "A" test, Local Leakage Rate Test (LLRT) measurements were made on the penetr'ations which were isolated or in use during the ILRT and are discussed later in this report.

The combined ILRT UCL and post-test LLRT leakage rate is 0.154 percent per day.

III.

TEST DISCUSSION A.

Descri tion of the Containment The containment vessel completely encloses the entire reactor and reactor coolant system to ensure no leakage of radioactive materials to the environment in the unlikely event of a loss of coolant accident.

The containment system design incorporates a freestanding containment vessel surrounded by a low leakage concrete shield building.

A four foot annular space is provided between the outer wall of the containment vessel and the inner wall of the shield building to allow filtration of containment vessel leakage during accident conditions to minimize off-site doses.

The freestanding containment vessel is a 1.903 inch thick right circular cylinder with a 0.95 inch thick hemispherical dome and 1.903 inch thick ellipsoidal bottom.

The overall vessel dimensions are 140 foot diameter by 232 foot 4-3/4 inch high.

The vessel is fabricated of ASME-SA 516 Grade 70 pressure vessel quality steel plate.

The net free volume of the containment vessel is 2.5 x 10 cubic feet.

6 The containment vessel structure includes one personnel airlock, one emergency escape lock, one fuel transfer tube, one equipment maintenance hatch and one seal-welded construction hatch.

All process piping and electrical

penetrations are welded directly to the containment vessel nozzles with the exception of the main steam, main feedwater and fuel transfer tube penetrations.

These penetrations are provided with testable multiple ply expansion bellows to allow for thermal growth or building differential motion.

The containment vessel is designed and constructed in accordance with the requirements for Class MC vessels contained in Section III of the ASME code 1971 edition.

The containment vessel is code stamped for a design internal containment pressure of 44 psig at a temperature of 264'F.

The containment vessel and all penetrations are designed to limit leakage to less than 0.5 percent by weight of the contained air per day at the above design conditions.

The calculated peak accident pressure for the design basis accident for the St Lucie Plant Unit No. l is 39.6 psig.

B.

Description of ILRT Test Instrumentation The containment system was equipped with instrumentation to permit leakage rate determination by the "absolute method."

Utilizing this method, the actual mass of dry air within the containment is calculated.

The leakage rate becomes the time rate of change of this value.

The mass of air (Q) is calculated according to the Perfect Gas Law as follows:

where:

(P-Pv)

V RT P

Containment Total Absolute Pressure Pv Containment Water Vapor Pressure V

Containment Net Free Volume R

Gas Constant T

Containment Absolute Temperature

The primary measurement variables required are containment absolute

pressure, containment relative humidity and containment temperature as a

function of time.

During the supplementary verification test, containment bleed-off flow is also recorded.

The Instrument Selection Guide or ISG is used to determine the ability of the instrumentation system to measure the leakage rate.

The calculated ISG for this test met all acceptance cr1teria for all test instrumentation systems.

1.

Temperature Instrumentation Forty precision Resistance Temperature Detectors (RTDs) were located throughout the containment to allow measurement of the volumetrically weighted average air temperature.

The location of the temperature detectors in the containment is depicted in F1gure l.

Each RTD sensor was supplied with a calibrated resistance vs temperature curve accurate to +0.2 F.

The 0

sensit1vity and repeatab1lity of each RTD sensor is less than +0.01 F.

The signal conditioning circuit and readout for the RTD sensors was a Fluke 2180A RTD digital thermometer and a Fluke 2020A printer.

The signal conditioning circuit and readout were calibrated to a loop accuracy of +0.35 F.

0 2.

Humidity Instrumentation Ten Resistance Humidity Detectors (RHDs) were located throughout the containment to allow measurement of the volumetrically weighted average containment vapor pressure.

The location of the RHDs in the containment is depicted in Figure 2.

The calibrated accuracy of the RHDs is +2.5 percent RH,

the repeatability of the RHDs is +0.25 percent RH and the sensitivity of the RHDs is +0.1 percent RH.

The readout device used for the RHDs was a Fluke 2240C datalogger.

3.

Pressure Instrumentation Two precision quartz bourdon tube manometers were used to determine containment absolute pressure.

The arrangement of the tubing connections between the manometers and the containment is shown in Figure 3.

Either manometer could be used as the primary pressure sensor for leakage rate calculations with the remaining sensor being considered as a backup.

The calibrated accuracy of the manometers is +0.015 percent of reading.

The sensitivity, repeatability and resolution of the manometers is +0.001 psi.

4.

Flow Instrumentation 1

A variable area float-type rotameter was used to superimpose a leakage during the supplementary CLRT.

The piping connection between the rotameter and the containment is shown in Figure 3.

The accuracy, repeatability and sensitivity for the rotameter in units of SCFM and converted to equivalent leakage values is given below:

SCFM Equivalent

~Leaka e

Accuracy Repeatability Sensitivity

+0. 20

+0. 05

+0.05

+0.0031X/day

+0.0008 X/day

+0.0008 X/day

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C.

Containment Pressurization Equipment The equipment used to pressurize the containment is shown in Figure 4.

The ten on-line oil-free industrial diesel driven air compressors had a total nominal capacity of 9,000 ACFM.

The compressed air was then routed to the FPSL ILRT dryer trailer for processing prior to enter1ng the containment vessel.

This trailer contained water cooled aftercoolers, moisture separators, deliquescent oil filters, refrigerant a1r dryers and a final post filter.

This equipment assured that clean and dry air was used to pressurize the containment.

D.

Description of the Computer Program The Ebasco ILRT computer program is an interactive Fortran IV program written specif1cally for fast, easy utilization during all phases of the ILRT and CLRT.

Date entry and modifications, if necessary, are readily

, accomplished by the data acquisition team. 'n addition to extensive data P

verif1cation routines, the program calculates, on demand, total time and mass point leak rates as well as the 95 percent Upper Confidence Level for these leakage rate calculations.

Sample refection based upon the Chauvenet criterion may be utilized in the analysis, if required, due to recording errors, power failures, etc.

Input data may be deleted for a given instrument in the case of a sensor malfunction.

This deletion of a given instrument is performed on all samples in the data base.

Volumetric weighting factors, if applicable, are then recalculated for the remaining instrument sensors of that type.

Data evaluations are enhanced by the flexible display of either sensor variables or various computed values in tabular or graphical form on the computer terminal.

Data is recorded on tape to prevent loss during the testing.

All data is stored on the computer systems in use with retrieval capability to any desired data base throughout the testing.

Ancillary portions of the program assist the user in detection of temperature stabilization, perform ISG calculations, perform in-situ Instrument Loop Performance calculations and detect acceptable superimposed CLRT leakage verification.

Temperature, pressure and humidity data are entered interactively via the computer terminal at 20 minute intervals.

Computer verification and checking routines supplement data verification by the data acquisition team.

Modifications are promptly made when errors are detected.

Prior to issuance of this report, further extensive data verification was performed.

E.

Description of the Testing Sequence On April 26, 1983 the final inspection of the containment vessel and internal components was made to prepare the containment for pressurization.

The ILRT instrumentation was checked and the pressurization system was inspected.

The containment reactor cavity water surface was at elevation 60 to cover the reactor and core barrel since the reactor head was removed.

The reactor was defueled because of core barrel thermal shield damage that was

.discovered during this outage.

It was decided to perform the ILRT before the repairs were made and the reactor cavity was left full of water.

A heavy plastic cover was in place over the reactor cavity to prevent the surface water from adding significant amounts of moisture to the containment air.

One temperature sensor (TE-02) and one hunidity sensor (RHD-Ol) were originally designated to be placed inside the reactor cavity, but were not installed because of the water level in the cavity.

The test began with these two sensors deleted.

Sensor volumetric weighting fractions were adjusted for the above-noted conditions.

Due to the water contained in the reactor cavity, three penetrations were not vented to the containment atmosphere during the ILRT without a water seal being present.

The Fuel Transfer Tube penetration and the Reactor Cavity Purification supply and return penetrations were under the Reactor Cavity water level'and therefor'e the containment isolation boundaries were not subjected to containment atmosphere during the ILRT.

Pressurization began at 2045 hours0.0237 days <br />0.568 hours <br />0.00338 weeks <br />7.781225e-4 months <br /> April 26, 1983 utilizing ten oil-free 900 ACFM industrial compressors.

The pressurization rate was approximately 3-1/2 pounds per hour and a target pressure of 56.5 psia was achieved at 1130 hours0.0131 days <br />0.314 hours <br />0.00187 weeks <br />4.29965e-4 months <br /> April 27, 1983.

Data acquisition and analysis was set at'wenty-minute intervals and began at 1140 hours0.0132 days <br />0.317 hours <br />0.00188 weeks <br />4.3377e-4 months <br /> April 27, 1983.

Containment air temperature stabilization criteria was met at 1600 hours0.0185 days <br />0.444 hours <br />0.00265 weeks <br />6.088e-4 months <br /> April 27, 1983.

During the course of this test, additional sensors were determined to be faulty and were deleted from the calculation of volumetric temperature and humidity.

Temperature sensors TE-02, TE-17, TE-30 and humidity sensor RHD-05 were deleted.

All other sensors performed as expected.

At approximately 1930 hours0.0223 days <br />0.536 hours <br />0.00319 weeks <br />7.34365e-4 months <br />, April 27, 1983 the Fluke 2020A printer began malfunctioning when it failed to clearly print the tenths digit on temperature readings.

This necessitated manual acquisition of one data set (2040 hours0.0236 days <br />0.567 hours <br />0.00337 weeks <br />7.7622e-4 months <br /> April 27, 1983) while the printer head was repaired.

Normal automatic data acquisition was established at 2100 hours0.0243 days <br />0.583 hours <br />0.00347 weeks <br />7.9905e-4 months <br /> April 27, 1983.

The last data sample for the ILRT was taken at 1600 hours0.0185 days <br />0.444 hours <br />0.00265 weeks <br />6.088e-4 months <br /> April 28, 1983 with a total number of samples established at 73.

The fitted mass point leakage rate was calculated to be 0.147 percent per day with the upper limit of the 95 percent Confidence Level at 0.153 percent per day.

To verify the results of the ILRT, a verification test or Controlled Leakage Rate Test (CLRT) was conducted.

Using the float-type rotameter described earlier, a superimposed leakage of 17.8 SCFM or 0.270 percent per day was set.

The fitted mass point leakage rate for the CLRT was then calculated to be 0.385 percent per'day which fell within the CLRT acceptance criteria band.

After the test, inspections and repairs were made on the Containment:/Annulus Pressure Differential Transmitter (PDT 25-13A) which exhibited a leak during the test.

This leak was blanked during the ILRT.

An investigation revealed that the low-range differential pressure transmitters had been isolated and equalized to avoid potential calibration read)ustments.

The valve block for PDT 25-lA (which is on the same lines as PDT 25-13A) had been installed upside down.

Opening the equalizing valve resulted in a containment-to-annulus leakage path.

All containment differential transmitters were subsequently local leak rate tested in normal valve lineup.

Total leakage was found to be 16.1 sccm.

A post-LLRT calibration check revealed no calibration problems.

The Fuel Transfer Tube Flange "0" Ring Seal and the Reactor Cavity Purification and Cooling System Isolation Valves (P-46 and P"47) were under water due to continued thermal shield and core barrel work at the time of this report.

The results of the March 5, 1983 LLRT of the reactor cavity purification system were used in lieu of a post-ILRT test.

A review of post-LLRT of the fuel transfer tube revealed a maximum value of 6.9 sccm in 1980.

An arbitrary value of 100 sccm has been assigned for the post-ILRT LLRT results.

FP&L will ensure that leakage is less than this value prior to going to Mode 4.

The ILRT Pressure Sensing and Controlled Leakage System Isolation Valves (P-52E and P-52D) were given post-ILRT Local Leakage Rate Tests (LLRT).

The results of all Type B and C testing (LLRTs) since the last ILRT are presented in Appendix C.

IV.

ANALYSIS AND INTERPRETATION A Periodic Type "A" Integrated Leakage Rate Test (ILRT) for the St Lucie Unit No.

1 Nuclear Power Plant was successfully completed on April 28, 1983.

The final calculated leakage rate was 0.147 percent per day with the upper limit of the 95 percent confidence limit (UCL) calculated to be 0.153 percent per day.

The acceptance'riteria (0.75 La) is 0.375 percent per day.

The verification test or Controlled Leakage Rate Test (CLRT) was conducted immediately after the ILRT with a calculated result of 0.385 percent per day, well within the CLRT acceptance criteria band.

The containment pressurization rate averaged 3.5 pounds per hour utilizing a 9,000 ACFM compressor capacity.

Containment pressurization was stopped at 56.5 psia with a weighted average containment air temperature of 92.5'F.

Data acquisition was set at twenty~inute intervals and containment air temperature stabilization criteria was achieved in four hours and twenty minutes at a containment temperature of 88.1'F.'fter reaching test pressure, temperature stabilization is achieved when the rate of change of the containment air temperature does not deviate by more than 0.5'F/hr from the average rate of change of the containment air temperature over the last four hours.

Refer to Appendix A.l, Temperature Stabilization.

During the pressurization, the leak survey team discovered a leak to I

the annulus via the Containment/Annulus Pressure Pifferential Transmitter (PDT 25-13A) which senses containment pressure through penetration P-45.

The leak, e

O was estimated to be 5

SCFM or approximately 0.08 percent per day.

Attempts to isolate the leak failed.

The transmitter reference leg to the shield building annulus was capped.

The test director decided to perform further investigation and a post-ILRT local leak rate test.

Refer to testing sequence section for details of the investigation.

During the course of the test, six sensors were deleted from the calculation of mean temperature and humidity; Temperature Sensors TE-02, TE-06, TE-17, TE-30, and Humidity Sensors RHD-01 and RHD-05.

Temperature sensor TE-02 and Humidity RHD-Ol were originally designated to be placed in the fuel cavity, but were not installed since the cavity was full.

The four other'deleted sensors either showed signs of eventual failure or had already failed.

The volumetric weighting factors for the remaining adjacent detectors were ad)usted accordingly.

To determine the ability of the instrumentation system to perform during the ILRT, the Instrumentation Selection Guide (ISG) was calculated.

Instrumentation errors were combined using a root-sum-square-formula where the resulting ISG cannot exceed 0.25 La or 0.125 percent per day either prior to or after the test.

Using predicted instrument errors, the pretest ISG was calculated to be 0.00288 percent per day and the post-test ISG was calculated to be 0.00291 percent per day.

This was well below the maximum criteria.

The difference in the pre-and post-test calculations was due to the deleted sensors.

After completion of the test and utilizing the Ebasco Computer Program's instrument error analysis, the actual measured maximum probable 1nstrument error computed with a 95 percent confidence level was 0.00230 percent per day.

This compares favorably w1th the predicted instrument error of the ISG calculation.

During the automatic data acquisition of sample number 18, pressure was printed as 55.799 psia, a 0.088 psi increase from the previous pressure reading.

The pressure readings had been approximately 0.012 psi less than

.each previous pressure reading.

This was a significant deviation from the expected pressure reading.

Further analysis of this pressure jump has shown that the actual pressure was probably 55.699 psia and that the printer failed to sense the tenths digit change due to mechanical hysteresis.

Since this pressure jump was not verified to be incorrect by an immediate visual cross-check with the manometer reading, it is felt that an arbitrary change of this pressure from 55.799 psia to 55.699 is not appropr1ate.

Therefore, 1t has been elected to reject sample 18, entirely. It was not possible to use the backup pressure sensor readings because a simil1ar printing error occurred with the backup sensor at sample number 20.

The ILRT continued until 1600 hours0.0185 days <br />0.444 hours <br />0.00265 weeks <br />6.088e-4 months <br />, April 28, 1983 allowing 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> of data and 73 samples to be used as the bases for leakage rate calculation.

Append1x A.2 shows in tabular and graphic form the pressure, weighted mean temperature, vapor pressure and calculated leakage values in addition to raw data inputs for each sample.

The plot entitled, "Containment Air Masses" shows a smooth trend in conta1nment masses and possessed only one outlying point.

This point is sample number 18 and was'aused by the misprinting of the tenths digit during the data printout.

Sample number 18 was rejected and was not used. in the calculation of leakage rate.

The slope of the mass point regression line expressed in percent per day is the leakage rate.

The plot entitled, "Computed Leakage Rate" displays the fitted mass point calculation of leakage rate and its relationship to simple total time calculations.

It is easy to see that these two calculations came closer together as the test progressed.

The outlying Simple Mass Point, at 340 minutes point, was caused by the bad pressure reading on sample number 18.

The plot entitled, "Computed Leak Rates Relative to Limits" shows the relationship between computed leakage rates and acceptance criteria leakage rates during the test.

The computed leakage rates were notably well below established limits.

The sudden increase shown by both curves which peaked at sample number ll (200 minutes) was caused by the'emporary temperature px'inter failure and the subsequent manual acquisition of temperature data.

This curve digression is also shown on the "Computed Leakage Rate" plot.

Following the ILRT the calculated leakage rate of 0.147 percent per day was verified by conducting a Controlled Leakage Rate Test,(CLRT).

Using the variable area rotameter, a superimposed leakage of 17.8 SCFM or 0.270 pex'cent per day was created and data acquisition began.

The CLRT was conducted between 1640 and 2100 hours0.0243 days <br />0.583 hours <br />0.00347 weeks <br />7.9905e-4 months <br /> on April 28, 1983 with twenty-minute sample intervals and 14 samples.

The calculated leakage rate was determined to be 0.385 percent per day.

Results from this verification test are acceptable provided the difference between the measured CLRT results and the sum of the ILRT results and the superimposed leakage is within 0.25 La.

Appendix A.3 shows clearly that the results fell within this acceptance band.

The post-test Local Leakage Rate Test results are presented in Appendix B of this report.

The results of these tests expressed in percent per day are added to the calculated UCL of 0.153/ per day since they were in use or not vented to containment atmosphere during the ILRT.

The Fuel Transfer Tube Flange "0" Ring, the Reactor Cavity Purification and Cooling

System, the containment differential pressure instruments and the ILRT Pressure Sensing Station post-test LLRT results were insignificant.

The ILRT Controlled Leakage penetration post-test LLRT results each yielded 0.001X per day.

When this is added to the ILRT UCL of 0.153X per day the resulting leakage rate is 0.154X per day.

-FIGURES 1.

RTD Location and Volume 2.

RHD Location and Volume 3.

Flow Diagram For Pressure Sensing and Controlled Leakage 4.

Flow Diagram for Pressurization System 5.

Test Sequence

20 RTD LOCATION/VOLUME ST. LUCIE UNIT NO. 1 FLORIDA POWER 8 LIGHTCOMPANY 3 RTD'S AT EL 194'OLUME 242,055 CU FT 9 RTD'S AT ELEVATION 171'OLUME 458,280 CU FT 10 RTD'S AT ELEVATION 130'OLUME 669,625 CU FT

~

10 RTD'S AT ELEVATION 84'OLUME 600,925 CU FT 8 RTD'S AT ELEVATION 40'OLUME 534,160 CU FT FIGURE 1

RHD LOCATION/VOLUME ST. LUCIE UNIT NO. 1 FLORIDA POWER 8 LIGHTCOMPANY 3 RHD'S AT ELEVATION 171'OLUME 1,049,347 CU FT VOLUME900,640 CU FT

~ 4 RHD'S AT ELEVATION84" 3 RHD'S AT ELEVATION 40'OLUME 550,013 CU FT FIGURE 2

FLOW DIAGRAM ILRTPRESSURE.SENSING 8c CONTROLLED LEAKAGE INST INSIDE CONTAINMENT OUTSIDE CONTAINMENT 3/8" TUBING Pl 1/2" TUBING (TYP.)

P 52E 3/8" X 1/2" EXP.'ONDENSATE POT (TYP.)

QUARTZ BOURDON TUBE MANO-METER TO ATMOS.

LLRTEST 1" PIPE I

1/2" DRAIN& TEST Pl QUARTZ BOURDON TUBE MANO-METER Fl VARIABLEAREA ROTAMETER Fl P

52D 1" X 1/2" RED.

(TYP.)

LLR TEST 1/2" DRAIN&TEST SEISMIC CLASS I

FLOVlDlAGRAM ILRTPRESSURIZING & DEPRESSURIZING SYSTEM TO UNITNO. 2 ILRT PENETRATION 8" PIPE TO ATMOSPHERE F'IPE SPECTACLE FLANGE ITYPI DRIP POT 1

DRAIN OUTDOORS I

I I

I I

I Pl I

I I

I I

INSIDE I AUXluARV I

BLDG 2" BYPASS Pl SEISMIC CLASS I 6" BLIND LLR 8r DRAIN IP'LR I

8

~

BLIND REMOVE FOR ILRT OUTSIDE INSIDE CONTAINMENT CONTAINMENT FP8IL ILRT DRYER TRAILER II WATER OUT I

I I

I I

I I

POST

/

FII.TER I

I I

I I

I I

I I

I WATER OUT I

REFRIG.

ERANT DRYER AUTO DRAIN ITYPI REFRIG-ERANT DRYER F ILTER WATER IN

'ATER OUT MOISTURE

/ SEPAR-ATOR AFTER COOLER AUTO DRAIN ITYPI WATER IN WATER OUT AFTER COOLER WATER IN FILTER MOISTURE

, SEPAR.

ATOR WATER IN, 1

I I

I A/C A/C A/C A/C A/C A/C A/C A/C A/C DIES E L DRI YEN INDUSTR IAL OIL FREE AIR COMPRESSORS

{10,000 CFM TOTAL)

ST. LUCIE UNIT NQ. 1.ILRT TEST SEQUENCE 50 45 OB oo 40 35 30

~ 25 U

20 15 OA A PRESSURIZATION 34 PSI PER HOUR B CONTAINMENTSTABILIZATIONPERIOD C INTERGRATED LEAKAGERATE TEST (ILRT)

D VERIFICATIONTEST-CONTROLLED LEAKAGERATE TEST (CLRT)

E DEPRESSURIZATION 6 PSI PER HOUR OE 10 2045 1130 1600 1600 2100 TUESDAY 4-26-83 WEDNESDAY 4-27-83 THURSDAY 4-28-83 F RIDAY 4-29-83 APPENDICES

APPENDIX A.I COMPUTER GENERATED REPORT TEMPERATURE STABILIZATION

TEHPEIQATUAE STABXLXZATXQN STAATED hT LL40 I-lQUA QN APAXL 27, L983 CQNDUCTED FQA 6.33 I-IQUAS B

C D

1140 1 P.OO 1220 1240 1300 L3PO 1340 1400 1420 L440 1500

.1$ PO 1540 L600 1620 L640 L700 L720 1740 1800 92.562 91. 388 90.737 90.240 89.8L9 89.509 89.205 88.923 88.666 88.432 88.210 88.006 87.8L3 87.632 87.457 87.287 87.131 86.972 86.822 86.679 L.L87 0.939 0.820 0.738 0.672 0.634 0.596 0.561 0.619 0.578 0.549 0 526 0.501 0.485 0.~65 0.452

0. 568 0.361
0. P71 O.PL2 O. 17'1
0. 149 0.131 0.109 A -- TXHE QF DAY XN.HXLXTAAY STANDAAD 8 = AVEAAGE CQNTAXNNENT TEMPERATURE F C = AVFAAGE IJXFFEAENCE XN TI=JfP.

OVER I AST 4 HQLJIZS D = AVErWCE DXFFEnENCE XN TEXP.

QVEn I AST 1

HQUn

/

I 96.0C I

9

~

'13

~ 7

~

TENPERRTURE STRB ILI ZRT ION 94.00 92.00 90.00 88.00 11.40 12.40 13.40 14.40 16.40 17.40 18.40 T INE HOURS

( NILI TRRY STRNDRRD )

APPENDIX A. 2 COMPUTER GENERATED REPORT INTEGRATED LEAKAGE RATE TEST (ILRT)

A 5 FLQRXDA POWER 8

LXGHT COMPANY ST.

LUCXE UNXT J.

CQNTAXNHENT XNTEGRATI=D LI=AI<AGE RATE TEST LEAKAGE RATE MEASURED USXNG TI.IE ABSOLUTE HETI-IQD LEAKAGE RATE COMPUTED USXNG THE HASS PQXNT HETI-IQD TEST PERXQD STARTED AT 1600 HOURS QH APRXL 27, 1988 TEST CONDUCTED FOR 8~.00 I-IOURS FREE SPACE VOLUHE QF CONTAXNNENT XS 2500000 CU FT CQNTAXNHENT WAS PRESSUIQXZED TQ 55.95 PSXA XHXTXAI CONTAXNHENT AXR MEXGI-IT 685868.4 LBS FXNAL CONTAXNHENT AXR MEXGHT 684292.d LBS FXTTED HASS POXHT LEAKAGE RATE XS 0.9.47

'A PER DAY UPPER LXRXT OF 95'/

CQHFXDENCE LEVEL XS 0.l.53 'l PER DAY HRC HAXXNUM ALLOWABLE LEAKAGE RATE XS 0.875 'l PER DAY

'I

DESCRXPTXGN GF VARXABLES A 6 AVG.

TEH AVE.

PRE VAP.

PRE LEAI< 5 XH Lr.=AK HAs AXR HASS CQNTAXNHENT HEAN TEHPERATURE CALCULATED FROH VGLUHETRXCALLY WEXGHTED RTD SENSOR XNDICATIONS.

PRXHARY CQHTAXNHENT PRESSURE XNDXCATIOH.

CGNTAXNHENT VAPOR PRESSURE CALCULATED FROH VOLUHETRXCAILY WEIGHTED RI.ID SEHSOR XHDXCATXGNS.

SXHPLE TOTAL TXHE I EAKAGE RATE.

LEAI<AGF. RATE CQHPUTED FROH FIRST ORDER nr;:Gnr=ssxaN aF Axn HAss DATA.

CQNTAXNHENT AIR HASS.

NOTE FOR TABULAR DATA TABLE VAI UES C)F ZERO 5XGNXFY DATA Xs HGT APPI. XCABI I-.: TQ Tl-IE CALCULATXON.

NOTE FQR CURVES l.

TGP ABSCXSSA SCALE REPRE5ENT5 5AHPLE NUHBERS.

P.

AIR HASS Xs THI= CALCUI ATED COHTAXNHEHT AXR HASS AHD FXTTED AXR HASS I5 Tl-IE LXNEAR LEAST SQUAIRE FXT Ql=

Tl.ll".

AXR HASSFS.

B.

SXHPL@ HASS PQXNT XS THF TOTAL TXHE LEAKAGE RATE AND FXTTED HASS PQXNT XS THE I EAKAGE RATE COHPUTED FRQH FXRST ORDER REGRESSXGH.OF AXR HASS DATA.

IJCL Xs THE IJPPEIR LXHXT OF THE 9G'/

CQHFXDENCE LEVEL QF AIR HASS DATA.

17-33

~

':49.;

66

~

81-97-

'- 113-688000.

CONTAINMENT RIR MASSES AIR MASS FITTEO AIR MASS co 687200.

CQ 686400.

~ Rejected Sample IK C)

CI CC 0

W a

0 CL cC O

CZ 68S600.

I QJ 684800.

684CQ0 240.

480.

720

~

960.

1200 '440.

1680.

17

~

33

~

'49

~.

65

~

81 7.

113.

0-CEn 1.2000 0.8000 0-4000 CDNPUTED LERK RRTES SIMPLE NRSS POINT LEAK RRTE FITTED HRSS POINT LEAK. RRTE C

04lo cve CD CX:

CD CD CC 0

!L lal I

CD CC o.oooo CD O

CL

~C, CD

-O.40OO

~ Rejected Sample

-0 8000 0

~

240

~

480.

720.

1200.

1440.

168i~

~

C TINE IN MINUTES

~

~

17

~

33.

'9'.

I I

81 7'13.

l QJ O.5400 l

0-CQ 0-.

CC C3 0.4400 lrJ CL COMPUTED LERK RRTES RELRTI VE TO LIMITS FIT:EC NRSS PDINT LERK RATE 95%

CONF IOENCE LIl'ilT (UCL)

DESIGN BASIS LERKRGE RRTE x

x NRC MAXIMUM RLLDNRBLE LERKRGE RATE YYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYY 0.3400 XXXXXXXXX I

x XXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXX a

CZ 0-2400 0 1400 240-480.

720.

9SO.

1200.

1440.

1S80 TlNE lN NINUTE5

~

~

49-1

~

17

~

33 1 7

~

113-

'OLlJNETR I CRLLY WEIGHTED CONTR INVENT TEMP ERRTURE BC 0000 88.OOOO 86.0000 84.0000 82.0000 240.

480.

720-960.

1200.

1440.

1680.

TINE IN MINUTES

II

~

~

1

~

17

~

33 49.

65.

~6 4"oo 1

RVERRBE CONTRINNENT PRESSURE CL V3 CL 56.2000 81 7'13.

tAl 10 04 C>

CC

~al I

QJ 56.0000 (Q

(Q CL

55. BOOO Rejected Sample i@i C7 CS c5 CZ EC 55.6000 55.4000 240.

480.

720.

960.

1440.

1680 '

TIME IN MINUTES

17.

33.

49 5

~

97

~

113.

0.3920 CC (Q

CL 0.3840 co 0 3760 CL 0.3680 CL CZ VOLUNETRICRLLY NE IBHTED VAPOR PRESSURE t4 cv C) 4 II C)

Cl Sal C3 CI ch

à C) 0.3600 0 3520 240.

480.

720-960.

1200

~

1440.

1680.

TIME IN MINUTES

, 1

VAAXASLE TABLE

SUMMARY

A1$

SAMPLE NINBEA 2

5 6

T 8

1a 1L LP 13 L4 15 L6 17 18 19 Ba PL PP 23 24 25 i 26 27 28

'~)

30

$ 1

$2 33 34

$5 36 37

$8 39 40 41 4P 4$

45 46 47 48 49 50 DELTA HXNS 0

20 40 60 80 100 LBa 14a 160 180 200 220 240 P60 Peo

$00

$2a

$40 s6a

$80 400 420 440 460 480 500 520 540 s6a 580 600 620 640 660 680 voo 720 740 V60 780 800 820 e40 86a 880 900 9PO 940 960 980 AVG TER BT.632 87.457 87.287 BT.1$ L 86.%72 86.8PB 86.679 86.$ 44 86.414 86.$ 58 86.255 86.066

$5.9$ $

8$.808 85.702

85. 514 8$. $ 16 BS.BPB 85.138 85.057 84.972 AVG.

PAE PSXA 55.9470

$$.@280 55.9090 55.8910 ss.ev4a 55.8580 55.8420 b5 BP70 55.8110 55.7980 55.7830 55.7670 55."f560 GG.T460 55.V340

55. Tr."20 55.7110 55.6890 55.6800 55.6690 55.6600 ss.6soa 84.674 84.618 84.5$ 6 84.469 84.4LB 84.$ 48

~ 84. 292 84.233 84.180 84.L28 84.075

$4.023

83. 274 8"-3. 930

'8$.845 8$.798 8$.758 8$.717 8$. 68$

8$.644 83.606 83.576 83.53%

55.6160 55.6080

$$.6000 55.8930 55.5860 GG.GV90 55.5730 55.5660

$5.5600 55.5550 ss.s49a ss.s44a 55.5380 55.5330 GS.GPBO 55.5230 55 bLGO 55.5lso

$5.5090 55.$ 040 55.5000 55.4950 55.4910 55.4880

$4.891 's.641a 84.817 55.6330 84.745 55.6P40 VAP.

PAE PSXA 0.3537 0.$ 541 0.$ 546 a.3549 0.$ 552 0.3556 0.3560 0.$ 564 0.3568 0.$ 584 a.ss9o a.ssee 0.3592 0.$ 596 0.$ 603 0.$ 61$

0.362Q LEAI< S XH PEA CENT

0. 000 0.219 a.246 0.271 0.242 0.224 0.228
0. r226 0.250 a.sso 0.382 a.soT a.26o O.r 16 0.218 O.r 43 0.2$ 8 LEAI< HAS PEA CENT 0.000 0.000 a.246 O.BT1 O.P5$

O.P$ $

0.224 0.236

0. 291 0. 33 "7 0.337 0.$ 15 0.284 0.263 Q.P56
0. 24c) 0.$ 631 0.3638 0.$ 644 0.$ 65l 0.3659 0.$ 665 0.$ 6TB 0.$ 681 0.3689 0.3697 0.370l 0.3707 0.3713 0.$ 718 0.$ 723 0.37P7 0.$73I a.svss 0.$ 737 0.3739 0.$ 740 0.$ "f44 0.3747 0.$ "f49 0.375L a.sfss 0.$ 755 0.$ 759 0.3760 a.sv62 0.$ 763 0.3766 0.233 O.P26 0.230 0.228 0.23l O.P29 O.BBT O.P30 0.229 O.P$ 5 0.228 Q.P24 0.221 O.BLB Q.P16 0.214 o.Bae 0.205 O.POO 0.198 O.L96 O.L93 O.L93 0.1PO 0.189 a.1$ 4 0.186 O.LBB
0. IGP
a. 181 0.176 0.24P 0.2$ 5 0.231 0.228 0.226 0.224 O.BB$

Q.BBP O.P22 O.BBP O.BBP Q.PP1 0.220 0.218 0.217 0.215 0.213 0.211 0.208 O.POS 0.20$

0.200 0.197 Q.L9$

0.193 0.190 O.LGB O.I86 0.183

0. 181 0.179 0.177 ECTED SAHPLE HAS IBI=EN AEJ AXR MASS POUNDS 685363 685343 685317 685286 68527L 685r'57 685233 685213 6851 Ts 685064 685000 6esa41 685067 685096 6850"fB 685017 685001 684965 6849bb 684926 684908 684880 684862 684846 684815 6$ 47c/6 684758 684756 684"f46 684724 684T11 6847a1 684684 6$46fP 6846VP 684659 684660 684646 684635 684627 6846LL 684606 684591 684592 684567 684566 684549 684536 68454l

VAAXABLI":TABLE SUHHAAY (COIQTXNUED)

SAHRLE IMQHBEA 51 SP 63 L

56 57 58 5'7 60 61 62 63 64 65 66 67 68 69 70 72 TS DELTA HXNS 1000

'1o2a la4o 1o6a laea 1100 1120 1140 1160 1 180 1200 1220 124a 1P60 1280 LSOO 132a 1340 1360 138a L400 1 4PO'440 AVG.

TEH DEC.

F 83.511 83.478 83.448 83.422

83. 391 8$.358 83.$ 37 83.306 83.288 83.258 83.232 83.214 83.186 BS.L62 83.L42
83. 1L6 BS.LOO 8$.075 83.065 8$.036 83.024 8$.008 82.988 AVC~.

PAE PSXA 55.4830 55.4800 55.4760 55.47PO 55.4690 55.4650 55.4620 55.4590 55.4560 55.4520 55.4490 55.4470 55.4440 55.4410 55.4380 55.4350 55.4330 55.4300 55.4280 55.4250 55.4230 55.4POO 55.4180 VAP.

PAE PSXA 0.3768 0.3770 0.3772 0.3775 0.3777 0.3779 0.3783 0.$ 785 O.STBB 0.$ 790 0.3791 0.$ 795 0.$ 798 0.$ 800 0.3803 0.$ 804 0.3809 0.$ 810 0.$ 815 0.3816 0.$ 821 0.$ 824 0.$ 826 LEAK SXH PEA CEHT O.L79 0.175 0.175 0.175 0.172 0.171 O.L71 O.L68 a.169 0.168 0.166 O.L65 0.163 0.162 0.162 O.L61

0. 160
0. 159 O.L59 0.157 0.157 0 158 a.156 LEAK HAS PEIR CENT
0. 176
0. L74 0.1T2 0.1TO 0.169
0. 167
0. L66 O.L64 0.163
0. 16'2 0.160 0.159
0. 158
0. 156 0.155 O.154 0.153 0.152
0. L51 o.1sa 0.149 a.148.

0.147 AXA HASS POUNDS 684511 684515 684499 684478 6844TB 684468 684452 68445L 684432 684419 6844LS 684407 684400 684390 684374 684369 684358 684350 684""3"-3P 6843$ L 6843L5 684P9$

684292 END OF TABLE

VAAXAIBLE SURHAAY 8)AMPLE NLIHBEA 2

5 6

"f 8

9 10 11 1P 18

1,5 16 17 18 L9 Pn Pl P.S P.s P6 v":)7 i"'8 l )9 so

."-31.

t 3PQ

3 'I 85

'36 87

'38 e 3Q) 40 41 48 46 47 48 49 sa OELTA RXHS 0

Po 40 60 80 100 1PO L40 160

Leo E?00 P.PO E?40 r."60 i)80 Boa Spn 840 860 880 4no 4PD 440 460 480

$ 00 GP..O

!540

$60 580 6() 0 680 6410 660 680 Too "fr?0 T40

'f60 "feo Bnn epo F340 860 880 900 9PO 940 9y)0 980 TEMP DEG.

81.160 81.080 81.070 SL.170 81.080 SL.LPO BL.OSO e1.aeo

81. neo fBL. 180 81.060 Sl.n9a 81.080 81.n4a 81.200 8:I.. LPO e1. 1sa
81. 110 IB1. 1PD 81.120 81.070 81.120 e1. 1oa 8:L. 080 81.n9o e:L. aeo 81. 0"fo 81.:LPO BL.070 Sl

. Ofo

81. ora
81. 1oa
81. 110 131. DC)0
81. 1pa Si.:1.80 8:L.:1.10 81. 140 81.:1.50 fB1. 110 8 1..:l. 70 e1.1no SL.140 81.:L 00 SL.:I!10 81.090 IB1. 080

. A1.100 fB1. 070 TEMP 2

13EG.

F DELETED DI=LI=TED DELETED DELI=TED DELETED DELI"TED DELETED DELETED DELETED OEL I:=rEO DELETED DELI."'"TED OEL E7EO OI=LETED DEI F::TED Dl":LIETEI3 DEL ETED Dl=l I.=TED DELETED DELI=TFD DFLETED OEI I":TFD DEL E'rED DFLI":TEI3 DELF<<TED DELI'""TED OF I...I":.".'I'ED DEL ETEO OEI...E:TED (3F.I. I'""TFD I:)EI...E I'F::0

" Dl:=L.F;.TEO I:)El.I":7'I:":.I:)

'31=.1..

I:-"Tl=..D 13E:I...F':Tl:".I:)

131.=1... I: TED f3EI.I:.".TED DEI...IXTED DELETED 131=LI". TFD OEI E'I'ED 131=.LI:""TEI3 DFL ETED Ol'=.L(=TFD DI=I...F".TFO 131=..L I'="TFD DELETED DI=LI=.TED DELE:rEo nEI. IXrFO TEHP DEG.

81.580 81.5$ 0 81.560 81.570 81. 580 81.540 81.

>50 81. $60 81.600 81.600 81.570 81.sea BL.GBO 81.590 8:L. 580 SL.610 81..'570 SL.SGO 81.$ 90 81.sso SL.$ 70 81.$ 80 81.550 81.590 81'.600 81.600 81.610 81.580 81.$ 60 81.600 8:I.. 590 8:I.. 680 81.600 f31. 610 81.600 81.680 81. 6ieo 81..!590 8:I.. 680 81. 570 BL. 610 81.590 81.680 81.590 81.680 81.680 BL.600 81

. 610 81.. 6PO DEG 80.940 80.'950 80.970 80.970 80.950 80.9PO 80.980 81.000 81.080 80

. 9fBO 81.800 80.970 BL.DBO 81,080 81.050 81. 1PO 8:I.. 080 e1.aso'1.asa 80.990 81.aso 80.990 81.000 81.aso 81.080 BL.070 BL.060 81. li20 81. 080 81..0TO 81.070 f31. 070 f31. 070 81. Oi""0 e1.:I.no

81. 0"fo 831. 1ieo BL.100 81.aTn 8:L.:L40 81.070 81. Loo BL.OGO 81.040 BL.070
81. n-fa Bl. 070 81.. 080
81. 100 BL.OPO DEG 80.400 80.400 80.420 80.400 80.4PO 80.4ao 80.480 80.450 80.490 80.480 ea.44o eo.4sa eo.490 eo.ssa eo.sao eo.s; a

Bo.sea ea.seo 80.520 ea.sso eo.ssa 80.580 80.570 80.580 ea.seo eo.6no 80.6LO 80.680 80.650 80.680 80.650 80.660 80.67n 80.690 eo.-f1n ea.zoo BD.690 SD.TLD

80. "f10 fBO. fr 0 80.740 Ba. f4a 80.740 80. "fso 80."f40 SO.T60
80. 770 80.780 en.Teo 80.780 13EG.

F DELETED DELETED DELETED DELETED DELETED DELI":Tl".:D DELE rED 13FI I=TI'"D DELETFD 13ELFTI: D OEI.ETEO I:)I=LETI:"'13 OEI...E:TEO OEL!-.."I'E:D DEI I"'"TEO Dl.".LI":Tl'""l3 DEI ETEO 131=LETF"D DEI ErEO DELFTEI3 DEL.E'rEO 131":LFTl='"D OEI.E:TED 13I=LI= TED DEL.ETED I)ELETED DELETED I:)I.=l I""I'I:""13 OEI.I.=, I EO 13EL.I-"'TI:."13 OELETI"::.O I:)EI..E'I"I:"D OEI..E IT,:O I.')I.=LET!;".".D DEL ETEO 131=1 I'"Tl:"13 OEI.E'I'IXO 13EI..I.":TI:""D OEI..ETEO DI-.-.LI=I I.=D DEI E'I'EO 13ELETI'- D DELE rED DELI-"'TI'""l3 OEL ~'TFO 13EI I=TED DEI...E:TED 131=.1 I'"'I'ED OE'.LET<<)

Ol-:"LE'IE D

VA!,XABLE TABLI.= 8!..NHAAY (CONTXNUEDI A16 SAMPLE iwÃHBEA 51 52

~8 54 i5 56 57 58 59 60 61 6P 63 64 65 66 67 68 69 Ta TL 72 73 OI"., I..TA I~iXNS 1000 1080 L040 1a6a 1oea I1.00 11PO

I.:I.40
I.:I.60 1 LBQ leoa 18PO 1840 1860 LPBO 1.800 1380 l840 1860 1380 14oa 14PO L440 TEMP 1

l3EG.

F e1. o6a 81. 130 81.0wa 81.150 81.150 81.LOO e1.070 8:I.. 070 81..:I. 00 BL.070 81.070 81.L60 81.120 81.. 150 81.I40 81.110 81.130 Bt.oea 81.140 81

. Loo Bl. 150 81.160 BI.180 TEMP 2

13EG.

F OELETEO i3FLETI=O DELETED OEI r.=-n=O DEI ETED oE!..r=-. rEo OELETEO DI:=I. I.".'TFI3 DFLETED DI-'LI'""TED DELETED oELErEo DELETED DELETED DELETED DELETED DELETED DELI.":TED DELETED DELI=TED DELETED DELETED DELETED TEMP I3FG.

81 8:I.

81 81 81 81 BL 8 :I.

81 81 Bl 81 BL 81 BL 81 BL 81 BL 81 81 81 81 8

F

.630

.590

.600

. 620

. 6QO

, 610

.630

.600

.6ao

.6ao

.600

.630

.600

.560

.550

.570

.560

.560

.580

. 540

.590

.580

.55Q TEHP DFG.

F 81. 100 81.030 81.070 81.060 81. OPO 80.990 81.11a 8:I., 080 81.120 81..070 81.080 81.0TO 81.1oa BI.040 81.0ea 81.a1a 81.aeo 81.o6a

,Bl. 070 81.020 BL.OBO 81.070 81.040 TRIP 5

Dl.:G.

F 80.780 80.790 BQ.TBQ 80.810 BQ.T90 eo.eaa 80.810 ea.e1a 80.830 Ba.epa ea.eoo 80.870 so.eea 80.860 80.850 Bn.e6o 80.900 ea.e9o 80.940 80.920 80.990 81.000 eo.qeo TEI".P 6

l3EG.

F DE!. ETED

!3EI ETI=D DELETED OELETFD DELETED DFLETED DELETED DFI ETED DELETED DI=LETED DELETED DELETI=D DELETED DELETLD DELETED DELETED DELETED DFLETFD DELETED oELErEo DELFTED DELETFD DELETED Ehlo I3F TABLE

VAAXAIBIE TABLE GlJHHAAY A17 SAMPLE NUHBEA 2

~ 3

~)

C' f

8 9

10 12 La 15 16 1.7te L9

. Ha Hl HP 23 25 P6

<<27

,He 29

$ 0

$ 1

$2 33

$5 36

$7 38

$9 40 4J.

4P 43 45 46 47 48 49 50 DELTA NXNS 0

20 40 60 80 LOO 12O 140 160 180'00 PHO 240 P60 280

$00

$20 340

'$60 380 4aa 420 44a 460 480 500 SP.O 54a

$60 580 600 620 640 660 680 700 7PO T40 "f60 780 800 BPO 840 860 eea 900 920 940 960 980 81.630 BL.630 81. 630 81.620 BL.620 81.630 81.630 BJ.. 630

81. 63a 81. 630 81

. 630 81.630 81.630 81.. 620 81. 610 81.610 81.61a BL.600 Gl.600 BL.590 81.600 BL.590 BL.590 al. 600 81.600 81.600 GL.590 BL.$90 81. 580 Bl.600 81.600 81.610 Bl. 610

81. 610 GI.600 BI.$90 BL.600 Bl. 600 8 J.. 6J.O 81.600 GI.600 81.610 81.610 Bl. 6IO 81. 610 81.620 81.620 TEHP DEC.82.$ 90 GP..SGO 82.380 BP.$ 70 82.$ 80 BP.$ 70 GP..$ 70 BP.$ 50 82.$ 50 82.$ 60 82.$ 40 Br2. $40 82.$ 30 BP.$ 30 82.$ 30 BP. $ 10 82.$ 00 GH.P90 82.290 BH.P70 BH.PGO BH.PGO BP.PBO GH.P70 GP.P70 GH.P60 BrH. PSO GH.P70 BP.PGO 82.250 BH.P60 82.250 BH.PSO 82.240 BP.P40 BP.HSO BP.PHO GH.PPO BP.PHO 82.210 BH.PHO eH." oa 82. 200 82.200 82.190 82.190 82.180 82.170 BP. 170 TEMP DEC 90.210 89.980 89.TOO 89.490
89. 190 88.960 88.750 88.$ 40 GG.SLO 88.160 87.9$ 0 87.740 87.620 87.410
87. 210 BT.110 86.920 86.T60 86.630 86.480 86.$ 60 86.230 86.090 85.990 85.830 85."f50 85.650 85.510 85.450 8$.$ 00 BG.PSO 85.140 85.040 84.9$ 0 84.890 84.T90 84.700 84.640 84.560 84.480 84.450 84.340 84.PBO 84.220 84.1.70 e4.1ao
84. OTO 84.nso 8$.990 TENP
90. 1,90 89.930 89.670 89.450 89.2oa 88..980 88.750 88.580 88.$ 80 88.180 87.990 8"f. BPO GT.630 87.470 87.290 87.L40 86.980 86.830 86.700 86.$ 5a 86.400 86.280
86. 160 86.040 85.930 8$.eao 85.700 85.900 85.500 8$.410 GS.SLO 85.PHO

'85.130 8$.070 84.970 84.9LO 84.830 84."f60 84.700 84.640

84. 'iao 84.$ $ 0 84.480 84.4LO 84.$ 70 84.$ PO 84.2TO 84.2PO 84.1$ 0 89.9ao 89.690 89.440 89.190 88.950 ae. r4a
88. 'iP.O BG.SPO 88. 1PQ 87.930 87.730 87.$ 50 87.$ 80 8"f.210 87.020 86.900 86.7$ 0 86.580 86.430 86.280 86.160 86.020 85.900 85.'780 85.670 85 560 85.450 8$.$40 85.240 85.140 85.050 84.9TO

'84.880

  • 84.81.0 84.740 84.660 84.600 84.$ ao 84.460 84.aea 84.$ 40 84.26a
84. P10 84.160 84.110 84.050 83.990 8$.9$ 0 83.890 83.860 90.280 90.0PO 89.760 89.5$ 0 89.aao 89.080 88.860 88.6"fa 88.46a GG.HTO 88.680 87.9PO BT.T40 BT.$60 87.$ 90 87.220 87.090 86.9$ 0 86.T90 86.660 86.$ 40 86.4IO 86.270 86.16a 86.aso 85.920 85.820 GG.TOO 85.600 85.$ 10 85.420 8$.$$ 0 85.240 85.16a 85.080 84.990 84.920 e4.84a 84.760 84.69a

'4.640 84.570 84.520 84.460 84.400 84.$ 50 84.$ 10 84.P60 84.22a

84. 1.TO

VAAXABLE TABLE 5UHHAAY (COHTXHUED)

BiAHPLE HLIHBEA 51 52 53 55 56 57 58 59 60 61 62 63 65 66 67 68 69 70 T1 72 73 DELTA MXH5 1onn 1020 1O40 106O 1080 1 100 1120 I140 1160 1 180 1200 L220 L240 1260 1280 LSOO L320 1340 1360 LSBO L400 1420 L440 TEMP 7

DEG.

F 81.610 81.6'10 81.610 BL.6lo

$1.61n 81.610 81.620 81.610 81.620 Sl.610

$1.610

$1.610 81.610 81.610

$1.600 81.610 81.610 81.610 81.620 81.630 81.630 BL.630

$1.630 TEHP 8

DEG.

F 82.L60 82.L50 82.I40 82.130 82.1IO

$2.100

$2.0VO

$2.090 82.070

$2.07O 82.060

$2.030 82.03O

$2.O20 82.020 82.010 82.010

$2.01O 82.0OO 82.000 81.990

$2.000 BL.990 TEMP 9

DEG.

F 83.970 83.9lo 83.880 83.820 83.800 83.770 BS.T40 83.700 83.660

$3.610 83.600 83.560 83.520

$3.500 83.470 83.440 83.420 83.390

$3.360 83.340 83.320 83.300 83.270 TEHP 10 DEG.

F 84.1QO 84.050

$4.O20 83.980 83.950 83.900 83.$ 60 83.$ 30

$3.810 83.770 83.730

$3.710 83.680 83.650 83.630 83 590 83.580 83.550 83.520 83.510 83.480 83.440 83.430 TEHP II DEG.

F

$3.$ 20 83.770 83.740 83.700 83.650 83.620

$3.590 S3.560 83.550 83.5QO 83.480 83.440 S3.420 83.380

$3.360 83.330 83.310 83.280 83.260 83.230

$3.200

83. 180 83.160 TEMP l2 DEG.

F 84.120

$4.09o

$4.06O 84.010 83.990 83.940 83.900 83.890 83.$ 60 83.$ 20 83.800

$3.760 83.740 83.700

$3.690

$3.670 83.620 83.5$ 0

$3.6LO 83.550 83.5LO 83.510 83.490 EHD QF TABLE

VAAXAIBLF TABLE SUHHAAY BAHPLE NCJHBEIR P

0 3 5

6f 8

CP 10 11 12 13 15 16 17le 19 Ba Pl 22 23 24 25 i26 27

,28 29 30 31 32

'33 34 35 36 37

$8 39 40 42 43 44 45 46 47 48 49 sa DELTA HXNS 0

20 na 60 80 100 120 14Q l60 180 Baa 220 240 26a 280 300 SP.O

$40 360 380 400 420 440 460 480 500 520 540 560 580 6aa 620 640

. 660 680 700 720 740 760 780 800 820 840 86Q Bea 900 920

'Ma 960 980 rEHI DEG.

va. 1-fa 89.890 89.64a 89.400 8). 160 88.930 88.730 88.520 ee.31a 88.210 87.930 8-f. 76a

87. 5)0 BT. 420 BT.BBQ 87.080
86. )20
86. "fea 86.640 86.500 86.35a 86.250 86.110 86.000 85.880 8'70 85.66a 85.560 85.460 Bb 360 85.2TQ 85.170 BG.a90 85.a10
84. )30 Bn.ena 84.T60 84.690 84.640 84 b60 84.520 84.460 84.400 84.340 84.270 84.220 84.1TO Bn.l30 84.080 Bn.ana TEHP

)0. $80

90. 1'10 89.870 89.610 89.400 8'2. 160 88.940 88.730 88.520 88.$ 30 Be.l50 87.970 87.810 87.620 87.450 87.300 87.150 Bf.aaa 86.860 86.730 86.590 86.460 86.$ 50 86.230
86. 5.5.0 86.aaa 85.eva 85.790 85.69a 85.590 85.500 85.400 85.31a 85.220, 85.l30 85.070 84.990 84.9PO Bn.ena
84. f50
84. f1Q 84.650 84.6ia 84.550 84.51a 84.460 84.4PO 84.$ 60 84.330 84.280 TEHP 90.230 89.970
8). 710 89.500 8)

PSO 89.aBa Be.ela 88.600 88.400 Be.pao 88.610 Bf.esa 87.650 87.4ea 87.300 87.160

86. )90 86.850 86.710 86.580 86.450 86.320 86.180 86.aTa 85.950 85.830 85."fna 85.630 85.530 85.4PO 85.$ 20 85.230 85.lea 85.060 84.980 84.91a 84.830 84.T60 84.690 84.630 e4.56a 84.5la 84.480 84.420 84.36a 84.$ 00 84.250 84.210
84. l70 e4.5.3a TEHP BB.STQ 88.070 87.850 87.580 87.$ 80 8"f. 220 86.910 e6.7aa 86.55a
86. Sr"0 86.l$ 0 85.960 85.820 85.750 BS.460 85.550 85.360 Bb 200 85.070 84.800 84:680 84.560 en.380 84.360 84.240 84.140 84.030 83,.940 83.840 83.740 83.650 83.560 83.480 83.370 BS.PBO 83.POO 8$.1$ 0 83.070 83.010 e3.000 82.9na 82.860 82.800 82.760 BP..710 82.660 82.620 82.570 BP..SSO TEHP l7 DEG.

F DELETED DELETED DELETED DELETED DELFTED DELETED DELETEO DELETED DELETED oELErED DELETED DELFTED DELETED DELETED DELETED oELE rEo DELETED oELE rEo DELETED DELETED DELETED DELETED DELFTED oELE rEo DELETED DELETI=D DELETED DELI"=TED DELETED DELETED DELETED oELErEo DELETED DELETED DELETED DELI=TED DELETED oELE'rEo DELETEO OELI='TEO DELETED oELE rEo DELETED oELE rEo DELETED oELErEo DELETED DELETED DELETED DELETED TEHP DEG

)0. 130 89.87a 89.620 89.390 89.160 88.940 88.720 Be.saa 88.$ 20 88.220 87.920 87.740 87.580 BT.420 87.230 87.090 86.940 86.790 86.640 86.5IO 86.370 86.25a 86.120 86.ala 85.880 85".77Q 85.660 85.570 85.470 BG.STQ 85.270 85.180 85.100 85.020

84. 'MO 84.8"fa 84.790 84.720 84.660 84.590 84.5PO 84.4TO 84.420 84.$ 60 84.300 84.260 84.200 84.16a 84.120 84.080

VARXAB1 E TABLE SUHHARY (COhfTXNUED)

A20 SAMPLE NQXBER 5I 52 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69 70 T1 72 Ts DELTA

'AXES laoo l020 1o4a 1060 1osa l100 11 a

I140 I160 I180 l200 1220 l240 126a 1280 1300 132a l$40 1360 1380 14aa 1420 1440 TEMP 1$

DEG.

F 84.aoa 83.960

83. "ZSO 83.89a 83.860 83.81a 83.T90 83.T50 83.740 83.700 83.670 83.640 Bs.61a 8$.59a 83 540 83.5$ 0
83. 510 8$. 480 83.450 8$.430 83.390 83.380 83.370 TEMP 14 DEG.

F 84.250 84.POO

84. I60 84.130 84.IOO 84.070 84.030 83.990 83.960 83.950 83.900 83.890 83.850 83.820 83.810 83.780 83.760 83.720 83.7ao 83.680 83.650 83.640 83.61a TEMP I5 DEG.

F

84. 100 84.060 84.0IO 83.990 83.950 8$.9PO 8$.880 83.850 83.830 83.780 83.760 83.7oa 83.700 83.670 83.640 83.620 8$.6ao 83.560 83.550 8$.51a 83.500 83.490 8$.450 TEMP 16 DEC.

F 82.530 82.5IO 82.460 BP.440 82.$ 90 82.360 82.330 82.290 82.260 82.230 82.POO 82.170 82.140 82.1aa 82.090 82.050 82.030 81.%90 81.980 81.950 81.920 81.910 81.890 TEMP I7 DEG.

F DELETED DELETED DELETED DFI ETED DELETED OELFTFD DELETED DELETED DELETED DELETED DELETED DELETED DELETED DFLFTED DELETED DELETED DELETED DELETFD DELETED DELETED DELETED DELETED DELETED TEMP IS BEG.

F 84.040 83.@90 83.960 83.920 83.870 83.840 83.810 83.TBO Bs.75a 83.700 83.680 83.640 83.620 83.600 83.570 83.52a 83.510 83.48a 83.460 83.4PO 83.400 83.390 83.360 ENO OF TABLE

TAIPEI E SUHRAAY A2L SAMPLE NUHBEA L

2 5

6 T

8 9

1a L1 1P 13 L5 16 17 18 L9 202l 2P 23 24 25 P.6 "c<<7 28 29 an 31 32

'3..

34 35 36 37 38

%9.--

40 41 42 44 45 46 47 48 49 sa DELTA HXNS 0

20 40 60 80 100 L20 14n L60 180 2ao 220 24a 260 P.en 300 320 340 360 380 400 420 440 460 4$ 0 500 520 sRa 560 580 6no 620 640 66a 680 "f00 720 740 760 780 eao e2a 840 860 880 900 920 940 960 9sa

$6.$ ea 86.7$ 0 86.540 86.510 86.440

$6.310 86.230 86.230 86.070 86.070 es.890

$5.860 es.eRa 85.700

$5.670 85.590 es.saa es.ssa es.42a eb.aTO 85.330 es.270 85.2LO 85.130 es.1ao BG.LRO 84.9ea 84.970

$4.900 SR.esa 84.760 BR.T60

84. 7LO 84.680 84.650 84.570 84 540 84.490 84.440 84.380 84.340 84.290 BR.PSO

$4.190 BR.L70 84.laa sR.nea 64.030 BR.aaa 20 87.490 87.350 87.260 BT.150 87.070 86.9$ 0 86.890 86.790 86.7IO 86.6la 86.540 86 Rba 86.400 s6.32a 86.pao 86.160 86.aeo 86.000 85.920 85.880 85.810 85.750 85:680 85.610 85.550 85.500 85.450 85.390 85.320 85.280 SS.PRO 85.190

.85.170 es.laa 85.060 es.020 84.990

$4.940 84.9'ln 84.890 84.830 84.770

$4.730

$4.680

$4.640

$4.580 84.530 84.480 84.450 84.400 DEG 86.640 86.560 86.460 86.360 86.270

$6.19Q 86.14a 86.050 es.970

$5.910 85.860 85.780 85.680 85.660 85.550

$5.520 85.460 85.390 85.320

.8$.280

$5.220 85.180 SG.LLO

85. 06'0 BS.OOO 84.950 84.890 84.840 84.800 84.740 BR.710 84.660 84.640 SR.SSO 84.520 84.490 84.460 84.390 84.360 84.320 84.280 84.270 84.2LO 84.170 84.140 BR.LOO" 84.nTa 84.040 83.990 sa.96a l3EG 86.890 86.790 86.680 86.600

~ 86. 540 86.440 86.360 86.3la 86.L90 86.69a e6.63a es. <<>60 85.630 85.840 85.T50 85.720 85.650 Bb b90 es.s2a SG.RTO

$5.400 85.350 85.290 85.260 85.200 85. 120 85.080 85.030 84.980 84.930 84.900

'84.830 84.800 84.760 84.7ao 84.670 84.630 84.5fn 84.550 84.480 84.4TO 84.440 84.400 84.360 84.320

84. r"90 84.260 BR.L90 SR.LTO
84. 140 DEG 87.900 8"f. 810 87.690 87.600 87.500 87.430 87.360 87.250 87.I90 BT.690 87.820 86.950 86.870 86.810 86.710 86.660 86.580 86.530 86.470

$6.410 86.350 86.300

86. r'30 86.L90 86.120 86.060 86.020

$5.960 85.880 85.'850 85.790 85.740 85.690

'5.640 85.590 85.560

$5.500

$5.470 85.400

$5.340.

85.3IO es.2sa 85.210 85.170 85.120 es.a9a 85.040 es.aaa 84.960 84.930 TEMP I3EG 87.650 87.550 87.440 87.350 87.PBO 87.170 87.090 87.0LO 86.920 86.850 86."f70 86.69a 86.630 86.540

$6.460 86.400 86.350 86.P70 86.210 86.L60 86.080 86.0PO

85. c)60
85. 910

$5.850 85.790 85.740 85.690 85.630

$5.580

$5 'ian

.85,480 85.440 85.390 85.330 85.310 85.PSO 85.2la 85.160 ss.12a 85.080 es.aao 84.990 84.'940 84.900

84. 8"f0 SR.eaa 84."fea

$4. -rRa 84.720

VAAXABLE TABLE SUHHAAY (CONTXNUED)

SAMPLE NQVBEn 51 52

~ma 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 DELTA HXNS 1OOO 1020 1040 106O LOBO L100 1 120 L l40 L160 1180 1POO 1220 L240 1260 L280 1300 L320 1340 1360 Laeo 1400 L420 l440 TEHP 19 DEG.

F 8-3. 970 8.".3. 920 83.890 83.850 83.840

$$.810 83.760 83.T30 83.TOO 83.670

$3.64o 8$. 660 83.580 83.560 83.550 8$.510 83.480

$3.470 83.450 8$.420 83.420 83.$ 90 83.370 20 DEG.

F 84. ""360 84.$ 10 84.290 84.240 84.'200 84.1$ 0 84.1$ 0 84.L10 84.080 84.040

$4.o10 83.980 83.950 83.900 83.890 83.860 83.820 83.800 83.TBO 83.750 83.740

83. foo 83.680 TEMP P1 DEC.

F Ga.v10 8$.890 83.860 83.810 83.790 83.760 83.720 83.700 83.670 8$.640 83.610 8$.580 83.550 83.530 83.5LO 83.4TO 83.450 83.420 83.4IO 83.$ 80 83.$ 50 83.330 83.$ 20 TEHP 22 DEG.

F 84.1LO 84.070 84.050 84.010

83. 770 83.930

$3.8~0 83.860 83.850 83.8PO 83.800 83.760 83.720 83.710 83.660 8$.640 83.630

$3.60o 83,.600 83.5$ 0 83.550 83.500 8$.480 TEMP 23 DEG.

F

$4.$ 90 84.860

$4.830 84.800 84.760 84.730 84.TOO 84.660 84.630 84.620 84.580 84.560

$4.520 84.500 84.480 84.460 84.430 84.400 84.370 84.$ 50 84.$ 30 84.300 84.290 TEMP 24 DEG.

F 84.670 84.640 84.610 84.570 84.550 84.510 84.480 84.440 84.420 84.380 84.360 84.$ $ 0 84.300 84.2TO 84.270 e4.20o 84.190

84. 170 84.140 84.120 84.090 84.080 84.040 END OF rABLE

VARXABLE TABLE SUHHARY 8? AHPLE NtJHBER 1

P e

C?

6 7

8 9

1a 11 12 13 14 15 16 17 18 19 20 21 2P 23 25 26 27 28 29 30 Sl

3P33, 34 35 36 r

37 42 43 45 46 47 48 50 DELTA HXNS a

20 40 60 80 100 120 140 160 180 2oa 220 24a P60 280 saa 32a 340 360 380 4ao 42a 440 460 4ea

$00 52O

$40

$ 6a 580 600 620 640

.66a 680 700 720 740 760 780 800 820 840 860 880 900 92a 940 v60 980 TEHP DEG.

87.2TQ 87.160 87.a7a 86. '??80 86.910 86.T90 86.TOO 86.620 86.540 86.460 86.4ao 86.710 86.24a 86.180 86.1ao 86.050 85.980 85.930 85.840 85 780 85.730 85.680 85.600 8$.560 85.soa 8$.460 85.sea 8$.340 85.290 BG.P30 85.200 85.140 85'.10Q 85.060 85.010 84.??70 84.vsa 84.880 84.840 84.TBO 84.740 84.700 84.660 84.630 84.580 e4.54a

84. 4 70
84. 460 84.420 84.390 87.650 BT.SPO 87.440 87.340
87. r?Ao er. 14a 87.060 86.940 86.870 86.800 86.730 86.640 86.560 86.$ 00 86.420 86.350 86.280 86.220 86.150 86.09o 86.020 85.970 85.900 85.850 85.790 85.740 85.690 85.630 85.590 85.530 85.490 85.420 85.4ao 8$

. 330 85.310

85. 2TO 85.210
85. 170 85.120 es.aeo Bs.a4o 85.000 84.950 84

. 910 84.860 84.830

84. 790 84."f40
84. 7"10 84.6TO DEG 87.860 87.770 87.670 87.570 87.490 87.400 87.soa 8"f. 210 87.150 87.670 86.990 86.920 86.840 86.170 8*.710 86.640 86.570 86.520 86.450 86.39a 86.330 86.P60 86.210 86.150 86.090 86.050 85. '??90 85.950 Ss.e9a 85.830 8$.7eo
85. fsa BS.680 85.640 85.590 8$.540 85.500 8$.460
85. 410 85.370 sS.s2a 8$.280 85.240 85.200 85.150 85. 120 85.080 8$.040 85.010 84.970 TEHP DEG 87.550 BT.460 87.380 87.P70 87.190 8"f. 110 87.o1a
86. )?40 86.850 86."f60 86.670 86.640 86.550 86.450 86.390 86.320 86.260 86.190 86.130 86.050 86.010 8$.950 85.890 85.830 85.780 85."f20 85.670 85.610 e$.$ 6a 85.$ 10 85.460 8$.410 85.370 8$.31a 85.280 85.2PO 85 980 85.150 85.090 Bs.a6o 85.000 84.940 84.920 84.860 84.830 84.7wo 84.740 84.700 84.65a 84.610 DEG 89.990 89.740 89.480 89.210 88.940 88.730 88.52a se.s1a 88.100 88.100
87. 710 87.530 87.290 87.150 86.990 86.840 86.69a 86.$ 40 86.400 86.270 86.1sa 86.000
85. 860 85.730 85.630 85.500 85.400 85.280 85.170 8$.09o 85.000 84.910 84.810 e4. -r1a 84.630 84.560 84.480 84.410 84.350 84.300 84.250 84.170
84. 110 84.060 84.a2o 83. '??60
83. ")10 83.870 83.82a
83. f70 TEHP 30 DEG.

F DELETED DELETED DELETED DELETFD DELETED DFLETI=D DELETED DELETFD DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELETI=D DELETED DEI E7I=-O DELETED DELE7'EO DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELETFD DELETED DELETFD DELETED DELETI=O DELETED DELETED DELETED DELETFD DELFTED DELETED DELETED DELETED DELETED DELETED DELETED DELE7'ED DELETED DI=LLTED DELETED DFLETED

vAnrABLE TABLC Buiwnv

<GDNTxNuED>

A24 BAHPLE IHJHBEA 51 42 53 54 55 56 57 58 59 606l 62 63 64 65 66 67 68 69 70 71 72 73 DEI TA N Xh!S 1oao l020 10<0 1060 1080 1100 1 '120 1 140 l160 1 180 1200 l220 l240 1260 l280 lsoa 1$2a 1340 l$60 1380 14ao 1420 1440 TEMP 25 DEG.

F

$4.$ 5a 84.290 84.270 84.270 84.hoo 84. l70 8@I. l40

84. 110 8<.090 84.060

$4.aso 84.000 83.970 8$.94a 83.940 8$.880 Bs.esa 83.830 Bs.e2a 8$.800 83.750 83.730

83. 7la TEMP 26 DFG.

F 84.650 84.600 84.560 84.510 84.490 84.460 84.~130 84.$ 90 84.$ 60 84.$ 10 84.290 84.25a 84.240 84.200 84.160 84.110 84.110 84.060 84.030 84.030 83.990 8$.980 Bs.wsa TEMP 27 DEG.

F 8<.9$ 0 84.900 84.860 84.830 84.790 84.760 84.730 84.700 84.670 8<.64a

$<.600 84.580 84.550 84.5$ 0 84.510 8<.480 84.460 84.430 84.400 80.$ 80 84.$ 60 84.$ 30 84.320 TENP 28 DEG.

F 84.570 84.540 84.500 80.460 84.450 84.400 84.390 84.$ 40 84.330 84.290 84.260 84.230 84.220 84.190 84.170 84.130 84.120 84.070 84.070 8<.010 83.990 83.990 83.950 TEMP 29 DEG.

F 83.7$ 0 83.700

$3.650 83.620 83.590 8$ '.540 83.510 83.080 83.440 83.~00

$3.$ 90 83.360 83.$ 20 8$.300 83.27a 83.220 83. 210 Bs.leo 83.160

83. 1lo 83.090 Ss.aeo 83.060 TEMP 30 DEG.

I=

DELETED DELETED DELETED DELETFD DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELE'rl.=D DELETED DELETED DELETED DELETED DELETED DELETED DELFTED CND Ol= TABI C

VAAXABLE TABLE SUHHAAY SAHPLE HUNBEA 2

~a 5

6 7

8 CP 10 1P 13 15 L6 17 Le 19 20 2P 23 Ps

%6 27 28

<29 30 31 32

~ $3.

35 36 37

$8 39 40 42 43 44 46 47 48 50 DELTA HXNS 0

Po 40 60 80 LOO I2a 140 160 iea r?00 r"20 240 P60 280 300 32a

$40 a6n 380 400 420 440 46a 480

$00 520 sna

$ 60

$80 600 62a 640 660 680 700 f20 "f40 760 780 800 820 840 860 880 9ao 920 940 r60 980 ev.900 89.620 89.350 89.090 88.840

$8.590 88.360 88.150 87.9ao 8'7. 740 87.

>40 BT.340 87.280

87. OIO 86.810 86.670 86.5LO 86.$ 70 86.230 86.080 85.950 85.830 85.690 BG.590 85.470

'85.340 85.250

. 8$. 130 85.0$ 0

$4.930 Sn.enn

$4.7so 84.660 84:570 Bn.neo e4.42a 84.340 84.270

84. 1 )0
84. 120 84.060 83.990 Ba.vaa 8$.870 83.820 ea. rea
83. "fI,o
83. 680 83.640 83.600 TEMP DEG
70. 300 90.010 89.730

$8.460

$9.230 88.940 88.520 ee.aoa 88.3PO 87.900 8'7. '750 87.560 87.400 87.2aa BT.070 86.9ao 86.750 86.610 86.470 86.$ 30 86.2PO 86.o9a 8$.960 85.840

85. 730 85.610 85.520 85.410 8$.320 85.230 85.150 85.060 84.970 84.880 84.820 84.730 84.6sa 84.580 84.510 84.440 84.$ 80 84.320 84.270
84. 210 84.170 84 9 c'0 84.080 Sn.ano DEG.

90.240 89.960 8). 690

89. 440 89. 180 88.950 88.720
88. 510 ee.aao 88.910 87.890 86.930 87.540 87.380 87.180 87.ana
86. 8)0 86.73O 86.580 86.440 86.$ 10 86.180 86.050 8$.930 85.820 es. rao 85.600

$$.470 85.380 es.2en 85.190 Bb 090 85.000 84.910 84.830 84.750 84.680 84.610

'4.520 84.470 84.4LO 84.350 84.2$ 0

84. r2PO 84.170 84.130 84.070 84.020 83.980 83.950 90.590 90. 310 90.030

$9.7$ 0 89.sna 89.290 89.o6a 88.840 ee.6sa 88.4PO 88.24a Se.aso ST.BBO 87.710 ST.S2O 87.360 87.230 er. 070 86.920 86.780 86.650 86.520

86. 370 86.270 86.150 86.040 Sb

)$0 85.820 85.720 85.630 85.630 85..$ 40 85.250 85.170 8$.100

$5.010 84.950 84.880 84.800

84. fso 84.680 84.620

$4.570 84.510 84.4TO en.noa 84.350 84.$ 20 84.270 TEHP DEG9o.osa 89.770 89.560 89.290 89.070 88.840 88.600 88.390 88.190 er.qea 87.800

$7.61a 87.420 87.250 87.07Q 86.940

86. feo 86.620 86.490 86.360 86.21a 86.090 85.960 85.820
85. "fIo 85.6lo 85.480 es.nia 85.300 85.POO 85.100 Bs.a2o 84.920 84.8$ 0 84.760 84.680 Bn.s9a 84.530 84.470 84.400 84.330

$4.2$ 0 84.2LO 84.150 84.1LO Sn.osa 84.0LO

$$.96a 83.920 83.870 DEG 86.270 85.9$ 0 85.610 85.320 es.ano 84 Tba 84.510 84.Pfo Sn.oaa Ba.eaa 83.610 Bn.ana 83.200 Sa.aoa 82.TSO S2.640 82.460 82.290 82.120 81.980

$1.$ 20 81.680 Sl.530 81.3TO 81.230 Si.o9a 80.970 80.850 80.750 80.640 80.550 80.420 80.$ 10 80.220

80. 120 Bo.o2a 79.920 79.840 79.760 79.680 79.600 79.540 79.480 79.380 7). 300 79.2$ 0
79. 190
79. 1$ Q 7c). 090 79.0$ 0

VAAXABLE TABLE BUHHAAY (CONTXNUED3 BiAHPLE NdHBEA 5 l.

2

i53 54 55 56

$7 58 59 6a6l 62 63 64 65 66 67 68 69 Ta 1l 72 73 DELTA HXHS xaao x020 l040 1060 J. 080

'>00 J. X20 1 140 Xl60 flea x200 l220 1240 x260 1280 1300 l<<320 ls40 l360 lsea

9. 400 l420 1440 TEHP Bl DEC.

F 83.$ 50

$3. 5IO

$3.470

$3.430 BB.BBD

$3.350 83.$ 2a

$3.280 BB.P50

$3.220

$3.200

$3.%50 8<<3.;I.10 es.a9o BB.D60

$$.040 83.010 82.990 82.960

$2. <<>>30

82. 710

$2.890

$2.860 TEHP

$2 DEG.

F

83. <<)40 83.900

$3.8$ 0 83.820

$3.$ 00 BB.T40 83.710

$3. 6$ 0 83.630 83.610 es.

>$0 83.550 83.$ 10

$3.490 83.460

$3.4PO

83. 41,0 83.3$ 0

$3.3$ a 83.320 83.29a BB.PBO

83. r?60 TEHP 33 DEG.

F

$3. 8)0 8."-.3. 850 Bs.exn 83. "160 83.740

83. 680 83.670

$3.620

$$.$90 83.$ 50 83.520 83.490 83.460

$3.430 83.400

$3.390

$3.$ 50 BB.BBQ 83.300 BB.P70 83.250

83. r'20 BB.POO TEHP 34 DFG.

F 84.220 84.200

$4.x40

$4.laa

$4.aeo 84.QSO 83.990

$3.950 83.920 8"=3. 900 83.860 83.830 83.800 83. 170 83.TBO

83. 120 83.700 83.670

~ 83 640 83.6la 83.600 8$.$ 60

$3.550 TEHP 35 DEG.

I=

83.830 83.790

83. "150

$$. -12a 83.680 83.640 83.6la 83.570 8$.550

'es.$ sa 83.480 83.440 83.420 83.380

$3.36a 83.330 83.300 83.280 83.260 83.230 83.200

83. l70
83. l60 TEHP 36 DI=G.

F 78.990 78. ">>40

78. )00 78.87Q 78.810 78.800 78.T60
78. 7l.0 78.660 78.620 78.590 78.$ 60 78. 5P.O 78.490 78.450 78.420 78.400 78.370 78.330 78.300 78.270 78.240 78.P20 LND DF TABLL

VARXASLE

SUMMARY

S) AMPLE NUMBER I

2 5

6 7

8 9

10 1PlsI4 15 16I7ia 19 2a 21 22 23 24 25 26 r

28 29 30

$ 1 rsry 33 34 35

$ 6

"-37 38 39 40 4P 43 45 46 47 48 49 60 DELTA MXNS 0

20 40 60 80 100 120 J. 40 I60 1aa 200 P20 24a P60 2eo soa

"-320 340 36a sea 4aa 42n 44Q 460 480 500 520 540 560 680 600 6PO 6'40 660 680

-rao 720 r4a 760 780 800 BPO 840 860 880 900 920 940 96o 980 TEHP DEG.

37 F

90.260 89. '970 89.700 89.430 89.200 88.950 Ba.fsa 88.$ 10 88.290 88.690 s7.9ao 87.720 87.540 87.370 87.180 87.030 86.890 86.730 86.590 86.4sa 86.$ 20

86. I90 86.o7a 8$.940 es.esa 85.710 85.600 85.500 85.400 85.310 86.2IO BS.I20

.85.030 84.940 84.86a

84. rea 84.7IO 84.620 84.560 84.500 84.430 84.370 84.290 84.2SO e4.1ea 84.140 e4.oea 84.a4a A4.000 83.960 DEG 9o.osa 89.740 89.430
89. I60 88.92a 88.70Q 88 450 88.230 88.020 87.810 87.610 87.440 87.260 87.090 86.880 86.750 86.590 86.420 86.-300 e6.1sa 86.010 85.890 85."fao 8$.650 85.510 8$.410 85.340 8$.230 BG.I40 8$.030 84.930 84.830 84.750 84.690 84.610 84.63a 84.450 84.$ 80 84. "=310 84.2sa
84. I70 s4.12a 84.070 s4.aoo 83 950 8+.890 83.850 83.800 83.750 83.700 TEMP 89.540 89.370 89.090 88.820 88.550 BB.P90 Be.aeo 87.830 87.640 87.420 87.220 87.620 86.840 86.680 86.490 86.370 86.240 86.070 85.890 85.790 85.650 85.510 85.420 85.P90 Bsr160 8$.060 84.980 84.'900 84,790 84.720
84. 6IO 84.530 84.4sa.

84.$ 80 84.280 84.PPO e4.14a 84.060 83.990 83.930 83.870 83.810 83.750 83.690 83.640 83.600 83.540 83.490 83.430 8$.390 40 89.970 89.710 89.440 89.190 88.920'8.680 88.4PO BB.POO 87.9'90 Bf.190 87.590 87.420 87.230 87.070 86.860 86.730 86.590 86.450 86.280

86. 160 e6.oso 85.890 85.780 85.690 85.570 8$.480 85.$ 90 8$.290
85. 190 85.100 85.000 84.920 84.840 84.750 84.680 84.6ao 84.530 84.4sa 84.380 84.32n 84.260 84.200 84.I40 84.080 s4.a4o 83.990 83. 9"-30 BB.BBQ 83.830
83. rsa PRES PSXA 55.947 55.928 ss.9a9
55. 89I 55.874 55.858
55. 84p GG.BP7 55.811 55.798 55.783 55.767 55.756 55.746 55.734 55,722 55.7I1 55.799 55.689 55.680 55.669 ss.66a 55.650 55.633 55.6'24 55.616 55.608 55.600 55.593 55.586 55.$ 79 55.573 55.566 55.560 5 556 55.549 55.544 55.538 5$.633 55.628 55,52$

55.518 5$.613 55.$ 09 55.604 55.500 56.495

55. 49I 55.488 HUH

'I FRACTXON DELETED DELETED DELETED DFLETED DELETED DELETED DELETED DELETI=D DELETED DELETED DELETED DELETFD DELETED DELETFD DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELETED oELErEo DELETED DELETFD DELETED DELETFD DELETED DELETED DELETED DELETI=D DELETED DELFTI=D DELETED DE ErEo DELETED DFLETED DELETED DELETED DELETED DELETED DELETED OELETFD DELETED DELETED DELETED OI=LETI"D DELETED DEI ETI=D

VAAXABII=TABLE SUANAAY (CQHTXHUED)

A28 SAMPLE HUMBEA 51 52

<53 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69 70 "f1 T2 TB DELTA HXHS LOOO 1a2o L040 LQ60 LOBO 1loo 1120 l140 116a 1 180 12ao IP20 1240 1P60 L280 1300 1320 1340 136a 1380 1400 1420 14~la TEMP

$7 DEG.

F 83.910 83.870 83.830 83.eoa 83.760 83."f30 8$."faa 83.660 83.62a 83.600 83.570 83.530 e3.51a 83.470 83.440 8$.420 83.40o 83.370 83.340 8$.$2a 83.290 BB.P60 83.250 TEMP DEG.

83 8$

83 83 83 83 8$

83 83 8$

83 8$

83 83 83 83 83 83 83 83 82 8 pQ 82

$8 F

660 610 560 530 nba 440 n20

$70 340 BPO 260 PBO 190 180 lna 12a a9o 040 a~la a2o 970 950 940 TEMP 39 DEG.

F 83.$ 50 BB.BLO 83.270 83.23a 83.180 83

. IBO 83.1ao 83.050 83.040 ee.a1a

82. 760 82.940 82.890 82.860 82.840 82.820 82.790
82. f70 82.730 82.700 82.670 82.660 82.630 TEHP 40 DEG.

F 83.750 83.700 83.660 83.610 83.570 8$. 510 83.nea 83.440 8$.n2o 83.380 83.330 83.310 83.270 83.250 8$.21a 83.19a BB.L50 83.1$ a BB.LLO BB.a7a 83.050 83.oea 82.990 PAES PSXA 55.483 55.480 55.476 55.47P 55.469 55.465 55.462 55. 4I59 55.456 55.452 55.449 55.447 55.444 55.441 55.438 55.435 55.433 55.4$ a 55.428 55.425 55.423 55.42a 55.418 HUH L

FAACTXOH DELETED DELETFD DELETED DELETED DELFTED l3ELETFD DELETED DELETI=D DELETED DELETED DELETED DELETFD DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELETI=D DELETED DEI FTED DELETED EHD DF TAB( E

VAnXABLE rABL E BUHHAAY SAMPLE HUHBEA P

3 c>

6 VI 8

9 10LI L2 1$

L4ls 16 17 Le 19 20 2L C'

PB P4 P5 P6

~QT 28 29 30 31 Sr2 33 34 35 36 37 38 39 40 41 4P 43 46 47 48 49 50 DELTA HXHS 0

20 40 6a BQ IOO 120 140 160 180 2ao P20 24a 260 280 300 320 340

$60

$80 400 4PO 44a 460 480 500 520 s4o 560

$80 6no 620 640 66a 680

-rao "120 "140 160 "180 800 BPO 840 860 eea 9oa 920 940 960 980 HUH I-IUH 3

HUM I-IUH 5

HUH 0.5$ 0 0.$ 34 a.sse 0.54P 0.546 0.549 n.ss2 0.55$

0.558

0. $61 0.564
0. $68 0.57l 0.574 0.578 Q.GBB 0.587 0.59P 0.59T a.6o2 0.607 a.

61'.617

0. 622 0.627
0. 632 0.6$ T a.641 a.646 0.650 0.655 0.658 a.663 0.66T 0.670 0.673
0. 61T
0. 680 0.68$

a.68s 0.687 a.69o a.692 0.694 a.69s a.69r 0.698

a. ron

'0. 7QI

n. 102
a. s36 0 539 0.$ 4L a.s44 0.547 0.549 0.552 n.sss 0.557 a.s6a 0.56$

a.s66 0.569 0.573 0.578 a.seB 0.$ 88 a.s93 a..>98

0. 603 o.6ae n.613 0.6LB 0.6PB 0.628 0.633 a.6$ 7 0.642 0.646 0.650 0.654 a.6se 0.662 0.665 a.668 0.67L 0.674 0.676 a.6re
0. 680 0.682 Q.683 0.685 0.686 a.687 0.688 0.689 0.690
0. 691.
a. 692
a. 497 o.soa a.so2 o.saB 0.507 o. 50"z 0. 51r2 O. S7.6 a.s2o 0.522 0 527 0.5$ 2 0.$ 36 0.540
a. s44 0.549 0.553 0.557
0. $62 Q.565
0. 569 0.575 0.580 0 $85
0. $90 0.595 0. Gr>>8 0.60$

0.606 0.608 a.61$

0.'616

0. 619 o.62a n.622 0.625
0. 62"1 0.628
0. 6$ 1 0.63$

0.635 0.636 0.637 0.6$ 9 0.640 0.64l 0.643 0.644 a.64s DELETED DELETED DELETED DELETED DELETED DELETED nELFrEn DELETED DFLETED DEI ETED DELETED DELETED DELETED DELFTED DELETED DELETED DELETED DEI FTED DELETED DELETED DELETED oEI r-.= rr=o DELETED DELETED DELETED DELFTED DELETED DELETED DELETED DELETED DELETED DELFTED DEL'ETED Dl=l I=TED DELETED DELETFD nELETEn OELETEO DELFTED DELI=TED DELETED DELETED DELETED

.DELETED DELETED DELETED DELETFD DFLETEO DELETED DEI I-"'TED 0.497 0.499 O.spl o.sas o.snr 0.511

n. 5>14
0. 57.7 a.s21 0.5P5 0.529 0.533 0.$ $8 0.542 0.$ 47 0.552 a.ss7 a.s6o a.s64 a.:>69 0.$ 74
a. s-r9 0.583 0.589 0.594 0.598 0.603 0.607 0.610 a.614 0.618
0. 6P1 Q.6P4 0.627 o.63n 0.632 a.63s 0.636 Q.638 0.640 0.641 0.643 0.645 0.646 0.648 0.649 a.6so 0.65P a.6sB FAACTXQH FAACTXDH FAACTXOH FAACTXOH FAACTXDH HUH 7

FAACTXOH 0.48l 0.483

0. 485 0.487 0.490 0.492 0.495 0.503 o.sae 0.512 O. S16 0 522 a.s26 0.531 0.536 0.541
0. 546 0.551 0.555 0.559
0. 563 0.$ 67 a.sr1 0.576 0.580 0.585 0.589 0.594 0.598 0.602 0.60$

0.609

'.612 0.6ls 0.6LB 0.620 0.6PB 0.625 0.627

0. 627
a. 6$ 1
0. 6$2 0.634 0.636 0.638 0.639 o.64a 0.64P 0.64$

VAAXABIE TABLE SUHHAAY (CONTXNUED)

A30 BAHPLE NUHBEA SL

~ Sr2 53 54 I.)5 56 57 58 59 60 61 6P 63 64 65 66 67 68 69 70 TL TH 73 DELTA HXNS 1OOO 1030 1040 1060 1OBO 1100 I1P.O 1140 ll60 1180 1300 1320 1240 1P6Q 1 r'80 1son 13'>>0 1340 1360 L380 14on 14PO 1440 HUH 2

FAACTXON O.TOS Q.TQS 0.706 0.707 0.708 0.709 0.7LO 0.711 0.7L1

0. 712 0.713 0.714 0.7L4 0. "r15 0.716
0. r1r 0.717
0. 718
0. 71m 0.720 O.730
0. 7P1 0.722 HUH 3

FAACTXON 0.693 0.693 0.694

n. F>>95 0.696 0.69r 0.697 0.698 0.699 0.700 0.7QO 0.701 O.TOP 0.702 o.703 0.703 0.704
o. ms 0.706 0.706 0.707 0.707 0.708 I-IUH FAACTXON 0.646 0.647 0.649 0.651 0.651 0.652 0.654 0.655 0.656 0.658 0.657
0. 658 0.661 0.661 0.663 0.663 0 66'>>
a. 665
0. 666
0. 667 0,. 668 0.

66'.670 I"IUH S

FAACTXON DELETED DELETED DELETED DEI I=TED DELE rED DELETLD DELETED DELETED DELETED DELETED DELETED DFLETED DELETED DFI FTED DELETED DEI ETED DELETED DI=LLTED DELETED DELFTFD DELFTED DELI=TED DELETED I-IUH 6

FAACTXON 0.654 0.656 0.657 0.658 0 659 0.661 0.662 0.663 0.664 0.665 0.666 0.66r 0.669 0.670 0.6TL 0.67P 0.673

0. 6"f4 0.675 0.676 0.678 0.679 0.680 HUH 7

FAACTXON 0.645 0.646 0.647

0. F.49 0.650 0.65l 0.653 0.654 0.656 0.657 0.658 0.659 o.660 0.66'.663
0. F64 0.665 0.667
0. 66"r 0.668 0.670 0.672 0.673 END OF TABLE

VAAXABLI= TAIPEI E SAHPLE HUHBEA L

2

'r 8 L) 6 7

8 9

1a 11 L2 18 14 L5 16 17 Le 19 2a2l PP 23 24 25

'26 27 28 29 30 8 1 8P 83

'4 85 86 87 se 89 404l 42 43 45 46 47 48 49 50 DELTA HXHS 0

20 40 60 aa 100 12n 14n 160 180 2ao P20 24a 26Q peo soa 82a 840 860 sea 400 42a 44Q 46a 480 500 520 540 56a 580 6oa 620 640 660 680 TOO 720 740 760 Tea eoa 820 a4a e6a aen 900 920 94a 960 sea HUH HLW 10 0.5'71 a.596 0.601 a.6o6 0.6LO

0. 614 0.618 0.622 0.622 0.628 0.681 0. 688 0.635 0.68T 0.687 a.689 o.64a 0.641
0. 641 0.641 a.642 0.642 0.642 0.642 0.642 0.642 a.642 0.642 0.642 0.642 0.642 a.642 0.642 n.642 0.642 0.642 0.642 a.642 0.648 a.643 0.644 0.644 0.645 0.646 Q.64T 0.648 0.649 0.649

'0.650'.651 0.612 0.6l7 0.622 0.626 0.629 a.633 Q.686 0.639 0.642 a.644 0.646 0.648 a.65o a.651 0.652 0.658 a.65s n.654 0.654 0.654 n.654 a.654 0.654 0.654 0.654 0.654 0.654 0.654 0.654 0.654 a.654 a.658 n.654 Q.654 a.654 0.654 a.655 0.655 0.655 0.655 0.656 0.657 0.657 0.658 0.659 0.660 0.660 0.661 0.662 0.5ve a.6a4 0.608 0.613 0.61T 0.620 0.624 a.627 a.6sa a.634 0.686 0.638 0.640 0.641 0.648 0.644 0.645 a.646 0.646 0.647 0.647 0.647 0.64T 0.648 a.648 0.647 0.647 0.647 0.647 0.647 0.647 0.647

.0. 647 a.647 0.647 0.647 0.647 0.648 0.648 0.649 a.*Go a.65a 0.65L 0.652 0.658 0.654 0.655 0.656 0.656 a.658 FAACTXOH Fl)ACTXOH FAACTXOH

VAIRXABLE TABLE SUHHAAY (CONTXNUED)

A32 SAHPLE NUHBEA GB

=53 54 55 56 57 58 59 6a 6L 62 63 64 65 66 67 68 69 70 TL TP 73 DELTA HXNS xoaa Loca L040 x060 lOBO 1 LOO s.xpa LL40 LL60 1180 1200 l220 xana LP60 1880

'L300 L330 1340 f360

.X380 L400 L420 L440 I-IUH 8

FAACTXON a.653 0.653 a.65m 0.655 0.656 a.657 0.658 0.658 a.659 0.660

0. 669.

a.

66'.663 0.664 0.665 0.666 0.66T 0.668 0.670 0.670 0.67i 0.673 0.674 I-IUH 9

FnACTXON a.663 0.664 0.665 a.665 0.666 a.668 a.668 0.669 0.670 0.67L 0.672 0.673 0.675 0.675 0.676 0.677 0.678 0.679 a.68o 0.68l 0.682 0.683 0.683 I-IUH Lo I=AACTXON 0.658 0.659 0.660 0.661 0.66P a.663 0.664 0.665 0.666 0.667 0.66T

0. 669 a.669 0.67L 0.67P
0. 6"f3 0.674
0. 6"f5 0.6T6 0.677 0.678
0. 6"f9 0.679 END OF TABLE

A 33 APPENDIX A.3 COMPUTER GENERATED REPORT VERIFICATION CONTROLLED LEAKAGE RATE TEST (CLRT)

I=LQRXDA POWER 8

I XGHT COMPANY ST.

LUCXE UHXT CQNTAXNHENT XNTEGRATED LEAKAGE RATE TEST SUPPLEMENTAL VERXFXCATXON TEST LEAKAGE RATF HEASURED USZHG THE ABSOLUTE HETHOD LEAKAGE RATE COMPUTED USZNG THE MASS POXHT NETHOD TEST PERXOD STARTED AT 1640 HOURS QN APRXL 28, 1988 TEST CONDUCTED FOR 4.88 HOURS FREE SPACE VOLUME QF COHTAXNHENT XS P500000 CU I" T CONTAXNNENT 4lAS PRESSURXZED TO 55.41 PSXA XNXTZAL VERXFXCATXQH AXR MEXGHT 684281.9 LBS FXNA'L VERZFZCATZQN AZR WEXGI-IT a88817.1 I eS FXTTED BASS PQXNT LEAKAGE RATE XS 0.880 V, PER DAY LC = 0.384 LAN 0.147 LO = 0.270 LO

+

I AN

.85LA LC LO

+

LAH

+.25LA 0.270

+ 0.147 0.125

< 0.884

< 0.270

+ 0.147

+ 0.125 0.@9'.884 0.54'~

LC

=FXTTED CLRT MASS PQXNT LEAKAGE RATE LAN =FXTTED XLRT MASS PQXNT LEAKAGE RATE LO

~SUPERXNPQSED LEAKAGE DURXNG VERXFXCATXON TEST LA

~CONTAXNHENT DESXGN LEAKAGF RATE

DESCRXPTXON OF VARXABLES AVG.

TEM AVE.

PRE VAP.

PRE LI=AI< 5 XH LEAK MAS AXR HASS CQNTAXNMENT HEAN TEMPERATURE CALCULATED FROM VOLUMETRXCALLYMEXGHTED RTD SENSOR XNDXCATZONS.

PRXMARY CQNTAXNMENT PRE55URE XNDXCATZON.

CONTAXNMENT VAPOR PRESSURE CALCULATED FROM VQLUHETRXCALLY MEXGHTED RHD SENSOR XNDXCATXONS.

SXMPLE TOTAI TXMF LEAKAGE RATE.

LEAKAGE RATE COHPUTED FROM FXRST ORDER RLGRESSZQN QF AXR MASS DATA.

CONTAXNHENT AXR HASS.

NOTE FOR TABUI AR DATA TABLE VALUFS QF ZERO 5XGNXFY DATA XS NQT'I~PI..XCABLE TO TI~E CAI CUI ATXON.

NOTE FOR CURVES TQP ABSCXSSA SCALE REPRESENTS SAMPLE NUMBERS.

2.

AXR MASS XS THE CAI CULATED CONTAXNHENT AXR MASS AND FXTTED AXR MA55 X5 TI-IE LXNEAR LEAST SQUARE FXT OF THE AXR HASSES.

SZMPLE HASS POXNT X5 THE TOTAL TZME LEAKAGE RATE AND FXTTED MASS POZNT XS THE LEAKAGE RATE COMPUTED FROM FXRST ORDER REGRESSXQN OF AXR HASS DATA UCL XS THE UPPER LXMXT QF THE CONFXDENCE LEVEL QF AXR MASS DATA.

e

9

~

'I

~

13'.

17

~

21-2S

~

29-684800.

684600.

CQ V3 684400.

CL 684200.

UJ 684000.

CONTR INMENT R IR MRSSES AIR MASS FITTED AIR NASS-C4 a

0 I

IC)

C7 5

CO P

O CI 683800'0

~

120.

180

~

240.

300.

360.

420-,

TINE IN NINUTES

5

~

9-13'-

17-21-25-0.5600 COMPUTED LEAK RATES S IttPLE NRSS POINT LEAK RRTE FITTED HRSS POINT LEAK RRTE 0.4800 1

0-CZn QJ CL O.40OO 0.3200 CI CP 8

CI CP Cl Cla CI 0-2400 0-1600 60

~

120.

180.

240.

300.

360.

420.

TINE IN MINUTES

9

~

13 7 1

~

2S-29

'.6400

0. 5600 C3 0

~ 4800 0.4000 COMPUTED LEAK RRTES RELRTI VE TO LIMITS w

w FITTED CLRT MASS POINT LEAKAGE RRTE x

x MRXIMVM RCCEPTRBLE v

v MINIMUM RCCEPTABLE 5

0 IIo EJ CI IO Cl

't Cl 0 3200 0.2400 0

60

~

120 180.

240.

300.

360.

420.

TINE IN MINUTES

9-13

~

I 17

~

2S-29

'3.>zoo VQLUNETRICRLLY NEIBHTED CONTRINNENT TENPERRTURE 8'400 82.9600 c~I ID C4 CI CI 5

I CJ

~4 5

EO la>

Cl lsl Ci O

82.8800 82.8000 82.7200 120-180'40.

300-360-420-TIME IN MINuTES

5

~

~

~

13

~

17

~

21

~

25

~

29-

55. 4600 55.4400

-I RVERRBE CONTAINMENT PRESSURE CV g

0 I4 W

II 4

Ek QJ 55.4200 (Q

V3 QJ CL 55.4000 55.3800 55.3600 0

60

~

120.

180.

240.

300.

360.

420-TIME -IN MINUTES

0.3920 17-5

~

29-21-9

~

5

~

-I VOLUNETRI CRLLY WEIGHTED VRPQR PRESSURE CC (Q

0 3900 UJ 40 0.3880 (Q

LLt CL CL 0.3860 CL CC a

l?'La 0.3840 0.3820 60

~

120.

180 240.

300.

360-420.

TINE IN NINUTE5

VAAXABLE TABI E SUHHAAY SAHPLE N. HBEA 2

5 6

7 8

9 10ll 13 DELTA HXNS 0

20 40 60 80 100 120 140 160 180 r'00 22a 240 260 AVG.

TEH DEC.

I=

82.909 82.931 82.914 82.897 82.879 82.863 82.846 82.828

82. 817 82.802 82.783 82.T76 82.T60 82.744 AVC~.

PAE PSXA 55.4140 55.4110 ss.4060

,55.4010 55.3970 55.$ 930 55.3890 55.$ 840 55.$ 800 ss.$ 760 55.3720 55.$ 680 55.$ 640 55.3600 V*P.

PAE PSXA 0.$ 834 a.$ 836 0.3840 0.$ 843 0.3846 0.$ 850 0.3852 0.3856 0.3859 0.$ 862 0.3864 0.$ 869 0.3811 0.3875 LEAK SXH PEA CENT 0.000

a. 184 0.333 0.378 0.365 0.$ 66 0.. $59
0. $74 0.3sa 0.$ 78 0.370 0.381 0.378 0.376 LEAK HAS PEA CENT a.oao O.aaa 0.333 0.389 0.387 0.384 0.377 0.$ 81 0.386 0.387 0.$ 83 0.385 0.385 a.384 AXA HASS PGUHDS 684282 684264 684218 684174 684143 6s41aa 684077 684033 683993 683959 683930 683884 683851 683817 END GF TABLE 1

VAAXABLE TABLE SUHMAAY BANPI E N'UveEn 1

2 3

5 6

7 8

9 101l 1 2 13 DELTA MXNS 0

20 40 60 80 loo 120 140 160 180 200 220 240 P60 TEHP l

DEG.

F Bl. 170 81. 150 Sl.160 Bl.l40 81.160 81. l70 Bl. l90 81. l60 81.l60

, 81.POO 81.160 Bl. 160 81.l90 81.130 TEHP P.

DEG.

I" DELETED DELETED DELETED DELETED DELETED DELI=TED DELETED DELETED DELETED DELI":TED DELETED DELETED DELETED DELETED TEHP 3

DEG.

r Bl.550 81.560 Sl.560 81.5eo Bl. 560 Sl. 590 81.560 81.560 Bl. 530 81.530 81.530 81. 570 81. 570 81. 560 TEMP DEG.

F Bl. 070 81.060 81.o70 81.10o 81.070

~ 81.070 81.05o'1.aeo 81.0eo 81.100 Bl.070 81.l30 81.080 81.070 TEMP 5

DEG.

F 80.970 81.03o 81.05o 81.0eo 81.050 81.050 Bl.090

81. 100 Bl. I50 81.150 81. l40 Bl. 160
81. 170 81. l60 TEMP 6

DI=G.

F DELETED DELETED DELETED DELETED DELETED DFLETED DELETED DFLETI-"D DELETED DFLETrD DELETED DELETED DELETED DELETFD END GF TABLE

VAAXABLE TABLE SLJMMAAY A44 SAMPLE NQMBEV 1

2 te 5

6 7

8 9

10 11 12 13 14 DELTA HXNS a

20 40 60 ea 100 LP.O 140 160 180 200 220 240 260 TEMP 7

DEG.

F Bl.640 81.640 Bl.640 e1.65a 81.650 e1.65a 81.66a 81.660 81.660 81.'660 81.680 81. 690 81.690 81.700 TEMP 8

DEG.

F 82.ooa BL.990 81.990 81.@90 e2.aao 81.990

81. ~>90 ep.oia 82.nio 82.aoo Bl. 990 82.000 81.990 BL.990 TEMP 9

DEG.

F 83.230 83.200 83.180 83.150 83.l40 BS.L10 83.090 83.070 83.050 83.040

83. 010 82.990 82.980 82.970 TEMP 10 DEG.

F 83.380 83.350 83.340 83.320 83.290 83.270 83.250 83.230 83.220 83.190 83.170 83.150 83.140 83.120 TEMP 11 DEG.

F 83.l20 83.a9o BS.OTO 83.a4o 83.020

.83.000 82.970 82.960 82.940 BP..920

82. 'POO 82.900 82.860 82.8TO TEMP 12 DEG.

F 83.420 83.410 83.390 83.360 83.350 83.320 83.3LO 83.280 BS.P60 83.230 83.240 83.190 83.L90 83.170 END OF TABLE

VAAXABLE TABLE SUHHAAY SAHPLE bAJHBEA L

"3 r>

6 7

8 CP 1a L1 12 LS L4 DELTA HXNS 0

20 40 60 80 100 120 140 160 180 200 2PO 240 260 TEHP 13 DEG.

F 83.310 83.300 83.P70 83.240 83.220 83.220 83.180 83.160 83.130 83.130 BS.L20 83.080 83.080 83.050 TEHP DLG.

83 83 83 83

$3 83 83 83 83 83 83 83 83 83 14 F

560 550 530 500 490 460 420 43a 400 4ao 360 370 330 300 TEHP L5 DEG.

F 83.410 83.380 83.350 83.330 83.310 Bs.sao 83.2'70 83.P50 83.240 83.230 83.2ao 83.L70 83.16a 83.150 TEHP 16 DEG.

F 81.85a 81.810 81.790 81.770 81.750 81.730 81. 710 81.650 81.640 BL.600 81.590 81.570 Bl. 550 81.540 TEHP 17 DEG.

F DELETED DFLETED DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELETED DELFTED DELETED DELETFD TEHP 18 DI=G.

F 83. SPO 83.290 83.P70 83.'230 83.230 83.200 83.170 83.L60 83.140 83.130 83.LOO 83.100 83.070 83.050 END OF TABLE

VAAXABLE TABLE SUHHAAY SAMPLE CJHBEIR 2

'0 ~

C) 6 7

8 9

aall L4ls DELTA AXES 0

20 40 60 80 LOO l20

'L40 160 LBO 200 220 240 4260 TEHP l9 DEG.

F 83.$ 10 Bs.sea e3.26a BB.PBO BB.PBO Bs.l90 BB.LBO BB.L60 BB.L50 BS.120 BB.LOO 83.090 es.o6a Bs.a4o TEMP 20 DEG.

F 83.640 83.600 83.590 83.52a 83.540 83.5'lo 83.510 83.470 83.500 83.430 8$.4PO 83.420 83.360 83.350 TEMP 2'L DEG.

F 83.270 BB.P40 83.230 83.210

83. 9.90 83.170 83.l.50 83.l40
83. XLO Bs.a9o 83.080 83.05a Bs.o5a Bs.asa TEMP 22 DEG.

F 83.430 83.42a 83.400 83.390 83.340 83.360 BB.BLO Bs.sao 83.290 BS.P90 83.2sa BS.PBO 83.230

83. Pia TEMP 23 DEG.

F 84.25a 84.2PO 84.2oa 84.LBO 84.x50 84.L50 84.sea 84.100 84.090 84.060 84.o4a 84.aso 84.020 84.000 TEMP 24 DEG.

F 83.990 83.980 83.970 83.950 83.930 83.890 83.890 83.860 83.850

83. 1840 Bs.eao 8$.800 83.770 83.770 EHD OF TABLE

VAAXABLE TABLE SUHHAAY SAMPLE l4JHIBEA 1

r 3

5 6

7 8

CP 10ll

'1Pl3 14 DELTA HXNS 0

30 4a 60 80 100 130 140 l60 180 200 LPO 240 260 TEMP P5 DEG.

F 83.660 83.660 83.630 83.610 83.600 83.560 83.560 83.53a 83.520 83.510 83.490 83.460 83.450 83.430 TEMP 26 DEG.

F 83.86o 83.870 83.840 83.810

,83.790 83.740 83.670

83. 6'r20 83.7oa 83.630 8$.550 83.610 83.530 83.480 TEMP P7 DFG.

F 84.270 84.340 84.210 84.190 84.l70 84.150 84.180 84.l10 e4.aeo 84.050 e4.o4a 84.030 84.010 83.980 38 DEG.

F 83.890 83.890 83.860 83.860 83.840 83.820 8$. Blo 83.790 83.770 83.740 83.730 83.710 83.700 83.680 TEMP 29 DFG.

F 83.0PO 82.970

82. 750 82.930 83.900 82.890 82.860 SP.830 BB.BPO BB.BLO 82.790 BP.750 82.740 82.720 TEMP 30 DEG.

F DELETED DELETI=D DELETED DELETED DELETED DELETFD DELETED DELF.TEI3 DELETED DELETED DELETED DELETED DELETED DELETED END OF TABLE

VAAXABLE TABLF SUHNAAY SAMPLE nfuvBEn L

P 6

7 8

9 10 L1 1P L3 DELTA HXNS 0

20 40 60 80 100 120 140 160 18a 2oa 220 2<0 260 TEMP DEG.

82 BP 82 S2 82 BP 82 Btg 82 82 82 SP 82 82 31 F

820 770 760 730 720 690 670 640 630 590 590 570 540 550 TEMP 32 OEG.

F 83.2an 83.180 BS.L50 83.130 83.LOO 83.aea 83.n6a 83.040 83.01Q 82.990 82.970 82.950 82.940 82.940 TEMP 33 DEG.

F 83.150

83. 120 83.LOO 83.08a 83.050 83.0PO 83.a10 BP.'990 82.960 82.940 82.920 82.920 82.900 82.890 TEMP 34 DEG.

F 83.490 83.460 83.440 83.410 83.380 83.370 83.350 83.340 83.3nn 83.P90 83.270 83.240 83.250

83. P10 TEMP 35 DFG.

F

83. 1aa
83. Ova 83.050 83.030 83.ann 82.980 SP 250 82.94a
82. 910 82.9aa 82.880 82.870 82.850 82.830 TEMP 36 OEG.

F 78.L70 78.120 78.LOO 78.080 78.040 78.020

77. 9)0 77.950 77.920 77.900 77.870 77.850 77.830 77.810 END GF TABLE

VARXASI E TABLE SUVVARV SQNPLE NUHI3ER 1

p ~ 2 3

5 6

7 8

cp 1al1 12l3 DELT~

RXNS a

20 ga 60 80 100 120 I40 l60 l80 2aa 2PO 2ea 260 TEMP

$7 DEG.

F

83. 190 83.160 8$.1~0 83.120 83.090 8$.070 83.040 83.030 8$.0la 82.990 82.970 82.950 82.940 82.920 TEMP 3S DEG.

F 82.870 82.840 82.810 82.790 82.760

82. 750 82.730 82.700

.82.680 82.670 82.660 82.63a 82.61a 82.590 TEMP

$9 DEG.

F 82 570 82.560 82.520 82.490 82.470 82.450 82.420 82.400

,82.380 82.360 82.$ 50 82.330 82.$ 20 82.300 TED<

wa DEG.

F 82.950 82.91a 82.880 82.860 82.8<0 82.810 82.790 82.770 82.760 82.740 82.720 82.700 82.68a 82.670 PRES l

PSXA 55.414 55.4l1 55.406 55.401.

55.$ 97 55.$ 93 55.389

55. $81 55.$ 80 55.$ 76 55.$ 72 55.$ 68 55.$ 64 55.$ 60 HUH 1

FIQACTXQN DELETED DELETED DELETED DELETED DELETED DELETFD DELFTED DELETFD DELFTED DELETI=D DELETED DELETED DELETED DELETED END QF TABLE

VARXABLE TABLE

SUMMARY

A5a SAMPLE HSMBER 1

2

'J ~

5 6

7 8

9 1a 11 1P 13 DELTA MXHS a

20 40 60 80 1aa 120 140 160 180 200 220 240 260 I.IUM 2

FRAc rxoH 0.723 a.723 0.724 a.725 0.725 a.726 0.7P6 0.727 0.728 0.728 0.729 0.729 0.730 0.730 HUM 3

FRACTXDH 0.7a9

0. 109 0.710
0. 711
0. 711
0. 712 0.712 a.712 0.713 0.713
0. 714
0. 714 0.715 0.715 I-IUM 4

FRACTXQH 0.673 0.673 0.674 a.676 0.676 a.678 0.678 0.680

a. 681
a. 68P 0.683 a.684 0.685 a.686 I-IUM 5

FRAc rxoH DELFTED DELETFD DELETED DELETED DELETED DELFTED DELETED DELLTED DELETED oELErEo DEI ETED DELE rED DELETED DELETED HUM 6

FRACTXI3H 0.683 0.683 0.685 0.686 0.687 0.688 0.690 a.690 0.691 0.692 0.693 0.694 0.695 0.696 HUM 7

FRACTXOH 0.675 a.676 0.677 0.678 0.680 0.681 0.682 0.683 0.680 0.685 a.686 a.687 0.688 a.689 EHD QF TABLE,,

VAAXABLE TABLE 5UHHAAY 5ANPLE HUHIBEA H

i~

5 6

7 8

C) xa 12 J.3 DELTA XXN5 0

a 40 60 80 100 J.BO L40 160 180 r'00 330 240 360 HUH 8

FAACTXON 0.676 0.677 0.678 0.679 0.6sa

0. 68'I 0.683 0.683 0.684

. 0.685 0.686 a.687 a.688 a.689 HUM 9

FAACTXON 0.686 0.687 0.688 0.689 0.690 0.691

. 0.692 0.693 0.693 0.694 0.695 0.697

0. 6)7
0. 698 HUH 10 FAACTXON 0.682 0.683 0.684 0.685 0.686 0.687 0.688 0.690 0.690 0.691 0.6vz 0.693 0.694 0.695 END OF TABLE

APPENDIX B.

RTD AND RHD VOLUMETRIC WEIGHTING FACTORS

ATD VOLUHETAXC MEXGHTXHG FACTOA5 ATD SEVSOA NUBBER

'L 2

8 5

6 7

8 7

1.0 L1.

12l3 L5l6 1.7 L8l9 20 2L P2 28 25 26 27 28 2P 80 SL 82 33 84 35 36 87 38 89 40 VOLUME FAACTXON 0.03561.07 DELETED 0.08561.07 0.0856107 0.0856107 DELETED 0.0356107 0.03561.07 0.0267850 0.0267850 0.0267850 0.0267850 0.0267850 0.02<0870 0.0240870 0.0240870 0.0240370 0.0240370 0.0240370 0.0240370 o.o24a87o 0.02<0870 0.0240370 0.02291.<0 DELETED 0.02291.~0 0.02291.<0 0. 0229140 0.02291.<0

0. 0229IWO 0.0229x40 0.02291.<o o.a2291,4o 0.02291.no 0.02291.40 0.02291.40 0.02291.<0 0.08227<0 0.0822740 a.a32274o

AHD VQLUHETAXC MEXGIHTXNG FACTQAS e s nHD SENSQA NUHBEIR VQLUNE FIZACTXQN 2

8 C'

7 8

9 1Q DELETED

0. 1100025
0. 1100025 O.IP00858 DELETED 0.1800858 0.1200858 0.18'ss9180 0.189e180 0.1899180

APPENDIX C.

TYPE B 6 C TEST RESULTS SINCE LAST ILRT (LLRT)

~i ji

TYPE B TESTING BETWEEN RbFUELINC OUTAGES SINCE LAST ILRT

'escri tion Date As found As left SCCH SCCH Remarks Haintenance Hatch Casket 9-5-79 Interspace 9-30-79 10"13-79 5-5-80 6-21-80 6-24-80 5-18-82 5-23-82 4.6 8.36 0.9

10. 1 8.

6'0,1 4.6 8.36 0.9 10.1 8.6 10.1

~

100 100 Opened for containment inspec-tion after Hurricane David.

Retest following closure Door opened.

Hatch opened for Reactor Coolant Pump Seal.

Hatch opened for Reactor Coolant Pump repair.

Hatch opened for Reactor Coolant Pump Seal repairs.

Hatch opened for Steam Generator inspection prior to Node 4.

Opened for Reactor Coolant Pump Seal Repair - retest prior to Hode 4 ~

Personnel Air Lock 11-15-79 1559 5-6-80 77688 11-4-80 2511 5-26-81 3023 12-7-81 12112 5-27-82 2270 11-16-82 1157 1559 33 2511 3023 12112 2270 1157 Personnel sir lock seals are tested by automatic tester at other than 6~anth intervals.

Alarms on testers are set at 100 sccm per door.

TYPE B TESTING BETWEEN REFUELING OUTAGES SINCE LAST ILRT Description Date As found As left SCCM SCCM Remarks Emergency Escape Natch 11 16-79 5-2-80 11-3-80 5"27-81 11-17-81 5-27-82 11-17"82 12 8724 100 5200 950 1050 12 8724 100 100 5200 950 1050 TYPE C TESTING BETNEEN REFUELING OUTAGES SINCE LAST ILRT Penetration As found As left Service Valve Date SCCM SCCM R

28A SIT Sample I-FCV&3"IF 9-28-79 4.3 4.3 Initial Test After Line I-FCV-03"IF 9-28-79 5.6 5.6 Plant Modification

Penetration No.

Service Valve REFUELING OUTAGE TYPE B&C TESTING SINCE LAST REPORT As As As As As As Found Left Found Left Found Left Test Date SCCH SCCH Date SCCM SCCM Date SCCM SCCH Remarks Main Steam Bellows Tap I Tap 2

Hain Steam Bellows Tap I Tap 2

Feedwater Bellows Peedwater Bellows 25 Fuel Transfer Bellows Maintenance Hatch Tap 1 Tap 2

Tap 1 Tap 2

Tap I Tap 2

Gasket Interspace Fuel Transfer Tube Flange 0 Ring I 3-3-83 I

I 3-3-83

.I I. P-3-83 0

I I

0 I

9-22-81 9-22-81 10 10 9-22-81 B

3"3"83 0

3-3"83 10 0

9-22-81 10 I 9-22-81 B

See Remarks.

0 9-22-81 10 92281 0

I I

100 I

I I

0 I

I I

9-22-81 11-11-81 9-22-81 11-21-81 11-11-81 B

~ 3-3-83 0

10 B

I 3-3-83 I

B I 3"3-83 0

I B

I 3-14-83 100 I See Note below.

I B

4-26-83 0

0 0

I 3-17-80 I

0 0

I 3-17-80 77 77 13 13 0

0 50

~

0 I 3-17-80 I

0 I 3-17-80 I

0 I 3-17-80 0

I 3-18-83 I

so I s-s-80 I

0 I 4-22-80 29 29 13 13 10 10 17 17 10.1 10.1 6.9 6.9

.IWill be tested Iapprox Sept 83.

ISee III-E.

0 0

3-17-80 20 20 0

0 I 3-17-80 15 15 0

0 3-17-80 18 18 0

0 3-17 "80 17 17 A-1 thru E-IO Personnel L'ock Escape Hatch Between Doors Between Doors Electrical Penetra-NA tions 4-24-83 42>000 5600 B

I 4-24-83 100 100 I

B.

I 3-2-83 0

0 12-7-81 12,000 12>000 5-6-80 77660 4.8 I 11-17-81 4800 I

I 9-15-81 0

4800 I 5-2-80 8714.61 8714.6 I

0 I 3-20-80 0

0 sa>>TYPE TEST 1983 As found 42,220 1983 As left 5,820 I 1981 As found 16,850 I

I 1981 As left 16,850 1980 As found 86>603.61 1980 As left 8>948.41 I ***1983 total does not include fuel transfer tube.

See III-E.

NOTE:

P-25 During a design review of Units 1 and 2 it was found that Tap 2 of P-25 is not a primary containment boundary.

Although of the same material its design rating is 16.0 psi.

A 'Technical Specification change request is being prepared.

REFUELING OUTAGE TYPE B&C TESTING SINCE LAST REPORT Penetration No.

Service Valve As As As As Found Left Found Left Test Date SCCH SCCM Date SCCH SCCH As As Found Left Date SCCH SCCH Renarks Prinary Makeup I-V-15328 Mater C

3-17-83 280 280 9-13-81 250 250 3-19-80 1911 1911 Bypass Leakage IWV-15-1 C

3-17-83 0

9-13-81 0

0 3-19-80 73 73 Bypass Leakage Station Air I-V-18794 &

I-V-18796 C

2-2j-83 100 100 9-12"81 2400 460 3-14-80 53 53 Bypass Leakage Instrunent Air I-V-18797 I"V-1879 I-V-18195 I-HV-18-1 &

I-V-18193 2-27-83 2-27.-83 4"7"83 4-7-83 200 160 200 160 1606 1606 1300 1300 9-12-81 0

9-12-81 0

0 3-14-80 6

0 3-14-80 0

9-13-81 510 330 3-19-80 342 342 9-13-81 1100 400 3-19-80 195 195 Bypass Leakage Bypass Leakage Bypass Leakage Bypass Leakage 10 Containnent Purge I-FCV-25-4 I-FCV-25-5 4-13-83 62)432 29)186 9-21-81 2000 2000 4-17-80 13.7 13.7 Containnent Purge I-FCV 25-2 I-FCV-25-3 3-9-83 2'

x 106

  • 400 9-21-81 20 20 4-8-80 8.9 8.9
  • Report Follows 14

.23 24 26 28B Nitrogen Supply V&779 V-6741 CCW to RCP CCN fron RCP Letdown Line I-HCV-14-1 & 7 I-HCV-14-2 & 6 C

V-2515 V-2516 C

Sit Sample Line I-FCV&3-IE I-FCV&3-IF RCS Not Leg Sanple V-5200 V-5203 3-24i83 3"24"83 4"1-83 4"1-83.

4-5-83 4-5-83'-11-83 3"11"83 4-25"83 4-25-83 20 10 190 100 100 100 100 20 9-18-81 12 9-18-81 0

12 3-18-80 0

0 3-18-80 0

10 190 100 11-9-81 0

9-17-81 0

9-17-81 0

0 3-26-80 35 35 0

3"22-80 199 199 0

3-22-80 116 116 100 9-13-81 0

100 9-13-81 100 9-16-81 100 9-16"81 0

0 3-28-80 6

0 3"28-80 3

0 3-21-80 14 0

3-21-80 14 14 11-9-81 300 300 3-26-80 1

Bypass Leakage Bypass Leakage Bypass Leakage Bypass Leakage Bypass Leakage Bypass Leakage Bypass Leakage Bypass Leakage Bypass Leakage Bypass Leakage

REFUELING OUTAGE TYPE B&C 'iESTlNG S1NCE LAST REPORT Penetration No.

Service Valve As As As As Found Left Found Left Test 'ate SCCH SCCH Date SCCH SCQl Date As As Found Left SCCH SCCH

'emarks 29A Pressuriser Surge V-5201 Line Sample C

4-25-83 100 100 9-16-81 100 100 3-21-80 1

7.4 Bypass Leakage V-5204 C

4-25-83 100 100 9-16 81 0

0 3-21-80 8

8 Bypass Leakage 29B Pressuriser Steam V-5202 Space Sample C

4-25-83 100 100 9-16-81 100 100 3.-21-80 401 401 Bypass Leakage V-5205 C

4-25-83 100 100 9-16-81 100 100 3=21-80 7

7 Bypass Leakage 31 Containment Vent V-6554 Header C

3-12-83 100 100 9-18-81 0

0 3-26-80 24 24 Bypass Leakage V-6555 C

3-12-83 100 100 9-18-81 0

0 3-26-80 4

4 Bypass Leakage 41 SIT Test Line I-V-07009 &

V-3463 C

3-11-83 1300 1300 10-8-81 0

0 4-1-80 144 144 Bypass Leakage Rx Cavity Sump Pump Diecha rge I-V-LCV-07-11A &

C 3-24-83 1050 1050 10-8-81 100 100 3-28-80 1157 1157 Bypass Leakage I-V-LCV-07-11B 43 Rx Drain Tank Pump Section V&301 V&302 C

4-23-83 550 550 11-15-81 100 100 3-31-80 88 1139 Bypass Leakage C

4-23-83 780 780 11-15-81 1400 1400 3-31-80 3500 1095.3 Bypass Leakage 44 RCP Controlled Bleedoff I-SE-01-1 C

3-14-83 0

0 9-28-81 0

0 3-25-80 17 17 Bypass Leakage V-2505 C

3-14-83 0

0 9-28-81 0

0 3-25-80 0

0 Bypass Leakage 46 Refueling Cavity Purification Refueling Cavity Purification I-VW7189 &

I-VW7206 I-V-07188 &

I"V-07170 C

3-5-83 200 200 10-21-81 100 100 3-24-80 24 24 Bypass Leakage C

3-5-83 0

0 10-21-81 300 300 3-24-80 70 70 Bypass Leakage

REFUELINC OUTAGE TYPE B&C TESTING SINCE LAST hLPORT Penetration No.

Service Valve As As As As As As Found Left Found Left Found Left Test Date SCCH SCCH Date SCCH SCCH Date SCCH SCCH Remarks 48A H2 Sampling to Analyzer A I-PSE"27-1 C,

3"7-83 0

0 9-14-81 0

0 3"20-80 i

1 Bypass Leakage 48C H2 Sample Return from Analyzer A I-FSE-27-2 I-FSE-27-3 I-FSE-27-4 I-FSE-27-08 I-V-27101 C

3-7-83 C.

3-7-83 C

3-7-83 C

3-7-83 0

0 9-14-81 0

0 9-14-81 0

0 9-14-81 9-14-81 9-14-81 400 400 C

3-30-83 890 890 0

0 3-20-80 1

1 Bypass Leakage 0

0 3-20-80 3

3 Bypass Leakage 0

0 3-20-80 3

3 Bypass Leakage 0

0 3-20-80 1

1 Bypass Leakage 100 100 3-20-80 8736 24.7 Bypass Leakage I"FSE-27-11 C

3-7-83 600

~

600 9-14-81 0

0 3-20-80 I

1 Bypass Leakage 51A H2 Sample Return I-V-27102 from Analyzer B

C 3-30-83 3200 1300 9-14-81 100 100 3-20-80 20 20 Bypass Leakage 51C H2 Sampling to Analyzer B

I-FSE-27-10 I-FSE-27-5 C

4-5-83 C

3-7-83 0

0 9-14-81 0

0 3-20-80 0

0 Bypass Leakage 100 100 9-14-81 0

0 3-20-80 0

0 Bypass Leakage I-FSE-27-6 I-FSE-27-7 I-FSE-27-9 52A Particulate Sample I-FCV-26-1 to Rad Honitor C

3 7 83 100 100 9-14 81 0

0 C

3-7"83 100 100 9-14-81 0

0 3-20-80 3-20-80 C

3"12-83 130 130 9-23-81 100 100 3-26-80 C

3 7 83 640 640 9-14-81 0

0 3"20-80 0

0 Bypass Leakage 1

1 Bypass Leakage 3

3 Bypass Leakage 88 88 Bypass Leakage I-FCV-26-2 528 Iodine Sample to I-FCV-26-3 Rad Monitor C

3-12-83 130 130 9-23-81 150 150 3-26-80 770 770 Bypass Leakage C

3-12-83 100 100 9-23-81 100 100 3-26-80 12 12 Bypass Leakage I-FCV-26-4 C

3-12"83 570 570 9-23"81 500 500 3-26-80 714 714 Bypass Leakage

REFUELINC OUTAGE TYPE B&C 'IESTING SINCE LAST RLPORT Penetration No.

Service Valve Test Date As As Found Left SCCH SCCH Date As As Found Left SCCH SCCM Date As As Found Left SCCH SCCM Remarks 52C 52D ILRT Controlled Leakage I-V-00140 &

I"V-00143 C

5-.10-83 Radiation Monitor I-FCV-26-5 C

3-17-83 Return I-FCV-26-6 C

3-17-83 510 510 9-23 81 400 400 3-26-80 114 114 Bypass Leakage 100 100 9-23-81 3400 100 3-26-80 2364 2364 Bypass Leakage 2300 2300 9-14-81 2500 2500 3-19-80 1

1 Bypass Leakage IWT Pressure Sensing Station I-V&0139 &

I-V-00144 C

5-10-83 0

0 9v14-81 100 100 3-19-80 82 82 Bypass Leakage 54 ILRT Pressurization I-V&0101 Station C

4-21-83 5700 3500 9-14-81 6-9-83 700 700 2800 2800 3-19-80 7142 1500 Bypass Leakage 56 N2 Purge Hakeup I-V-25-11 &

C 4-23-83 142 142 9-14-81 I-V-25-12 I

280 280 3-25-80 198 198 Bypass Leakage 57 H2 Purge to H2 Purge Filter I-V-25-13 &

C 3"10-83 1000 1000 9-14-81 I-V-25-14 330 330 3-24-80 268 268 Bypass Leakage 58 H2 Purge Filter Bypass I-V-25-15 &

I-V-25-16 C

3-10-83 1000 1000 9-14-81 550 550 3-24-80 465 465 Bypass Leakage 67 Cont Vacuum Relief I-V-25-20 &

C 4-14-83 220 220 10-1-81 100 100 3-21-80 5

5 I-FCV-25-7

. C 4-14-83 1100 1100 10-1-81 800 800 3-21-80 172 172 68 Cont Vacuum Relief I-V-25-21 C

4-14"83 250 250 10-2-81 0

0 3-24-80 I-FCV-25-8 C

4"14-83 1600 1600 10-2-81 340 340 3-24-80 5

5 7

7

    • +TYPE C TEST TOTALS 1983 As Found 2 y 987'50 1981 As Found 20'42 1980 As Pound 28'08 6

1983 As Left 48,204 1981 As Left 14,102 1980 As Left 13,208

++"TYPE B and C

TEST TOTALS 1983 As Found 30,301,70 1981 As Found 36,892 1980 As Found 115,512.21 NOTES:

  • "+BYPASS LEAKAGE TOTALS 1983 As Found 22,818 1981 As 1983 As Left 15,918 1981 As technical specification acceptance criteria is 245,153 sccm.

technical specification acceptance criteria is 544,786 sccm.

Total bypass leakage Total band C leakage found 17,849 I

Left 11,903 Summation based upon leakage which would occur if best boundary value(s) failed.

(From page C4 and above) 1983 As Left 54,024 1981 As Left 30,952 1980 As Left 22,156.41 1980 As Found 28,707 1980 As Left 13,006.4

LOCAL LEAKAGE RATE TEST PROBLEMS SINCE LAST ILRT The plant did not meet the acceptance criteria for Local Leakage Rate Testing during the 1983 refueling outage.

All problems were reported on License Event Report (LER) 335"83-18.

The problems were as follows:

1.

On March 9, 1983 containment purge isolation valve I-FCV-25-3 was found to be leaking at 2,900,000 sccm.

The seat of I-FCV-25-3 was adjusted.

No cause was determined.

A retest in conjunction with the outboard isolation valve I-FCV-25-2 indicated a combined leakage of 400 sccm.

All other containment isolation valves of this type and size were tested satisfactorily during this refueling outage.

2.

On March 9, 1983 containment H2 sampling return line check valves I-V-27101 and I-V-27102 were found to be leaking excessively during setup for testing.

The valves were tapped and promptly closed.

No leakage measurement was obtained before closure.

I-V-27101 and I-V-27102 were disassembled and found to contain dirt.

The valves were cleaned>

reassembled, and satisfactorily retested.

The redundant isolation valves were satisfactorily tested.

3.

On April 1, 1983 RCP component cooling water isolation valve I-HCV-14-6 was found to be slightly off its seat while test personnel were attempting to partially drain the component cooling water system to perform the local leakage rate test.

The jacking screw was found to be engaged and was promptly adjusted.

The valve was then successfully tested.

The plant was in either cold shutdown or refueling modes throughout the period of misadjustment and met Technical Specification requirement for containment isolation in these modes.

I-HCV-14-6 limit switches had been adjusted on March 9 whi.le the plant was in cold shutdown.

The valve was returned to service with the jacking screw engaged sufficiently to keep the valve just off its seat.

The screw was adjusted immediately upon discovery.

The maintenance personnel involved have been instructed regarding returning equipment to service in the operating configuration.

The test of this valve in conjunction with the other isolation valve indicated a combined leakage of 190 sccm.

t H

J

o WIRE STRAND AND BAR SYSTEMS o

INITIALLYSYSTEM CAPACITIES WERE IN THE ORDER OF 4,45 MN (500 TONS),

o LATER. LARGE SYSTEMS UP TO 11 MN (1200 TONS)

DEVELOPED REDUCTION IN NUf"jBER OF ANCHORAGES R DUCTS -

If)CREASED SPACING o

PRINCIPAL PRESTRESSING SYSTEMS BBRV AND VSL