ML17214A368

Reactor Containment Bldg Integrated Leakage Rate Test, Final Rept

ML17214A368
Person / Time
Site:	Saint Lucie
Issue date:	04/28/1983
From:	Dillon P, Musto A EBASCO SERVICES, INC.
To:
Shared Package
ML17214A367	List: ML17214A366 ML17214A368
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 8308090525 830803

,PDR

• R ADOCK 05000335 PDR

A~ g C

TABLE OF CONTENTS

~Pa e I'NTRODUCTION ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

II. S UK' ~ ~ ~ ~ o ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~

III. TEST DISCUSSION A. Description of the Containment B. Description of ILRT Test Instrumentation

1. Temperature Instrumentation 6

2. Humidity Instrumentation ..... .... .. ~ -- ~ - ~ ~ ~ ~ ~ ~ ~ ~ ~ 6

~ ~ ~

3. Pressure Instrumentation 7 4~ Flow Instrumentation ......... ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ - ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ 7 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 ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ 19

1. RTD Location and Volume ~ ~ 20

2. RHD Location and Volume 21

3. Flow Diagram for Pressure Sensing & Controlled Leakage .. 22

4. Flow Diagram for Pressurization System ............. .... ~ 23

5. Test Sequence .............................-....... . ~ 24 VI. APPENDICES ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ 25 A. Computer Generated Report Al-A51 1'ontainment Temperature Stabilization ..... Al-A3

2. Integrated Leakage Rate Test (ILRT) ~ ~ ~ ~ ~ ~ A4-A32

.3. Verification Controlled Leakage Rate Test ( CLRT). A33-A51 B. RTD and RHD Volumetric Weighting Factors....-.........

C B and C Test Results .................. ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ . ~ ~ ~ ~ ~ ~ ~ ~ Cl-C9

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 Purif ication 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 6 cubic feet.

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:

(P-Pv) V RT where: 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 0 F. The 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 0 F.

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:

Equivalent SCFM ~Leaka e Accuracy +0. 20 +0.0031X/day Repeatability +0. 05 +0.0008 X/day Sensitivity +0.05 +0.0008 X/day

~

~4

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 failure the'emporary temperature px'inter 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 LIGHT COMPANY 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 LIGHT COMPANY 3 RHD'S AT ELEVATION 171'OLUME 1,049,347 CU FT VOLUME 900,640 CU FT

~

4 RHD'S AT ELEVATION 84" 3 RHD'S AT ELEVATION 40'OLUME 550,013 CU FT FIGURE 2

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

3/8" X 1/2" P QUARTZ 52E EXP.'ONDENSATE BOURDON POT TUBE (TYP.) MANO- TO ATMOS.

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

Fl P 1" X 1/2" RED.

52D (TYP.)

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

FLOVl DlAGRAM ILRT PRESSURIZING & DEPRESSURIZING SYSTEM TO ATMOSPHERE TO UNIT NO. 2 ILRT PENETRATION 8" PIPE F'IPE I

I SEISMIC CLASS I SPECTACLE Pl Pl I

FLANGE ITYPI I I

8~

I BLIND I

REMOVE DRIP FOR ILRT I

POT 6" BLIND I 2" BYPASS I IP'LR I LLR 8r DRAIN I

1 DRAIN OUTDOORS INSIDE OUTSIDE INSIDE I AUXluARV CONTAINMENT CONTAINMENT I BLDG FP8IL ILRT DRYER TRAILER I 1 I F ILTER I WATER OUT WATER IN A/C I I I

REFRIG. 'ATER OUT ERANT MOISTURE I A/C DRYER I / SEPAR-ATOR I AUTO AFTER A/C I DRAIN COOLER I ITYPI I A/C DIES E L DR I YEN POST INDUSTR IAL

/ FII.TER AUTO DRAIN WATER IN A/C OIL FREE I ITYPI WATER OUT AIR COMPRESSORS I {10,000 CFM TOTAL)

I A/C I AFTER I COOLER A/C I

I FILTER MOISTURE I REFRIG- SEPAR. A/C I

ERANT ,

ATOR DRYER WATER IN, I

WATER OUT WATER IN A/C I

ST. LUCIE UNIT NQ. 1.ILRT TEST SEQUENCE 50 45 OB oo 40 35 30 U A PRESSURIZATION 34 PSI PER HOUR

~ 25 OE B CONTAINMENTSTABILIZATIONPERIOD OA C INTERGRATED LEAKAGE RATE TEST (ILRT) 20 D VERIFICATION TEST-CONTROLLED LEAKAGE RATE TEST (CLRT)

E DEPRESSURIZATION 6 PSI PER HOUR 15 10 2045 1130 1600 1600 2100 TUESDAY WEDNESDAY THURSDAY F RIDAY 4-26-83 4-27-83 4-28-83 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 92.562 1 P.OO 91 . 388 1220 90.737 1240 90.240 1300 89.8L9 L3PO 89.509 1340 89.205 1400 88.923 1420 88.666 L440 88.432 1500 88.210

.1$ PO 88.006 1540 87.8L3 L.L87 0.619 0. 568 L 600 87.632 0.939 0.578 0.361 1620 87.457 0.820 0.549 0. P71 L 640 87.287 0.738 0 526 O.PL2 L700 87.131 0.672 0.501 O. 17'1 L 720 86.972 0.634 0.485 0. 149 1740 86.822 0.596 0.~65 0.131 1800 86.679 0.561 0.452 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

/

96.0C I

I 9 ~

TENPERRTURE

'13 STRB

~ '7 ~

IL I 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 ( NIL I 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

A 6 DESCRXPTXGN GF VARXABLES AVG. TEH CQNTAXNHENT HEAN TEHPERATURE CALCULATED FROH VGLUHETRXCALLY WEXGHTED RTD SENSOR XNDICATIONS .

AVE. PRE PRXHARY CQHTAXNHENT PRESSURE XNDXCATIOH.

VAP. PRE CGNTAXNHENT VAPOR PRESSURE CALCULATED FROH VOLUHETRXCAI LY WEIGHTED RI.ID SEHSOR XHDXCATXGNS .

LEAI< 5 XH SXHPLE TOTAL TXHE I EAKAGE RATE.

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

AXR HASS 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 IK C)

CI CC co 687200. 0 W

CQ a

0 CL cC O

686400.

~ Rejected Sample CZ I 68S600.

QJ 684800.

684CQ0 240. 480. 720 ~ 960. 1200 '440. 1680.

1.2000 17 ~ 33 ~

CDNPUTED LERK RRTES

'49 ~ . 65 ~ 81 '7. " 113.

C 04 SIMPLE NRSS POINT LEAK RRTE lo cv e

FITTED HRSS POINT LEAK. RRTE CD CX:

CD CD CC 0.8000 0

!L lal I

CD CC 0-CE n

0-4000 CD O

CL

~ C, CD o.oooo

-O.40OO

~ Rejected Sample

-0 8000 1200. 1440. 168i~

0 ~ 240 ~ 480. 720. ~

C TINE IN MINUTES

l 17 ~ 33 I

COMPUTED LERK RRTES

'9'.

~ ~

I FIT:EC RELRTI VE NRSS PDINT LERK RATE 81 TO

'7 '13.

LIMITS 95% CONF IOENCE LIl'ilT (UCL)

DESIGN BASIS LERKRGE RRTE x x NRC MAXIMUM RLLDNRBLE LERKRGE RATE QJ O.5400 l 0-CQ YYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYYY 0-.

CC C3 0.4400 lrJ CL I

XXXXXXXXXx XXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXX a CZ 0.3400 0-2400 0 1400 240- 480. 720. 9SO. 1200. 1440. 1S80 TlNE lN NINUTE5

1 ~ 17 ~ 33

~ ~

49-

'OLlJNETR I CRLLY WEIGHTED

'7 ~ 113-CONTR INVENT TEMP ERRTURE BC 0000 88.OOOO 86.0000 84.0000 82.0000 1200.

240. 480. 720- 960. 1440. 1680.

TINE IN MINUTES

~6 4"oo 1

1

~

II 17 ~ 33

~ > ~

RVERRBE CONTRINNENT PRESSURE

49. 65. 81 '7 '13. tAl 10 CL 04 C>

V3 CL 56.2000 CC

~ al I

QJ 56.0000 (Q

(Q i@i C7 CS c5 CL CZ EC

55. BOOO Rejected Sample 55.6000 55.4000 240. 480. 720. 960. 1440. 1680 '

TIME IN MINUTES

0.3920

17. 33. 49 '5 ~

VOLUNETRICRLLY NE IBHTED VAPOR PRESSURE 97 ~ 113.

t4 cv CC C)

(Q CL 0.3840 4 I

I C) co 0 3760 Cl Sal C3 CI ch

à CL C) 0.3680 CL CZ 0.3600 0 3520 240. 480. 720- 960. 1200 ~ 1440. 1680.

MINUTES

, 1 A1$

VAAXASLE TABLE

SUMMARY

SAMPLE DELTA AVG TER AVG. PAE VAP. PAE LEAI< S XH LEAI< HAS AXR MASS NINBEA HXNS PSXA PSXA PEA CENT PEA CENT POUNDS 0 BT.632 55.9470 0.3537 0. 000 0.000 685363 2 20 87.457 $ $ .@280 0.$ 541 0.219 0.000 685343 40 87.287 55.9090 0.$ 546 a.246 a.246 685317 60 BT.1$ L 55.8910 a.3549 0.271 O.BT1 685286 5 80 86.%72 ss.ev4a 0.$ 552 0.242 O.P5$ 68527L 6 100 86.8PB 55.8580 0.3556 0.224 O.P$ $ 685r'57 T LBa 86.679 55.8420 0.3560 0.228 685233 8 14a 86.$ 44 b5 BP70 0.$ 564 0. r226 0.224 685213 160 86.414 55.8110 0.3568 0.250 0.236 6851 Ts 1a 180 86.$ 58 55.7980 0.$ 584 a.sso 0. 291 685064 1L 200 86.255 55.7830 a.ss9o 0.382 0 . 33 "7 685000 LP 220 86.066 55.7670 a.ssee a.soT 0.337 6esa41 13 240 $ 5.9$ $ 55."f560 0.3592 a.26o 0.$ 15 685067 L4 P60 8$ .808 GG.T460 0.$ 596 O.r 16 0.284 685096 15 Peo 85.702 55.V340 0.$ 603 0.218 0.263 6850"fB L6 $ 00 55. Tr."20 0.$ 61$ O.r 43 Q.P56 685017 17 $ 2a 85. 514 55.7110 0.362Q 0.2$ 8 0. 24c) 685001 18 $ 40 SAHPLE HAS IBI=EN AEJ ECTED 19 s6a 8$ . $ 16 55.6890 0.$ 631 0.233 0.24P 684965 Ba $ 80 BS.BPB 55.6800 0.3638 O.P26 0.2$ 5 6849bb PL 400 85.138 55.6690 0.$ 644 0.230 0.231 684926 PP 420 85.057 55.6600 0.$ 65l 0.228 0.228 684908 23 440 84.972 ss.6soa 0.3659 0.23l 0.226 684880 24 460 $ 4.891 's.641a 0.$ 665 O.P29 0.224 684862 25 480 84.817 55.6330 0.$ 6TB O.BBT O.BB$ 684846 i 26 500 84.745 55.6P40 0.$ 681 O.P30 Q.BBP 684815 27 520 84.674 55.6160 0.3689 0.229 O.P22 6$ 47c/6 28 540 84.618 55.6080 0.3697 O.P$ 5 O.BBP 684758

'~) s6a 84.5$ 6 $ $ .6000 0.370l 0.228 O.BBP 684756 30 580 84.469 55.8930 0.3707 Q.P24 Q.PP1 684"f46

$1 600 84.4LB 55.5860 0.3713 0.220 684724

$2 620 84.$ 48 GG.GV90 0.$ 718 0.221 0.218 684T11 33 640 ~ 84. 292 55.5730 0.$ 723 O.BLB 0.217 6847a1 34 660 84.233 55.5660 0.37P7 Q.P16 0.215 684684

$5 680 84.180 $ 5.5600 0.$ 73I 0.214 0.213 6$ 46fP 36 voo 84.L28 55.5550 a.svss o.Bae 0.211 6846VP 37 720 84.075 ss.s49a 0.$ 737 0.205 0.208 684659

$8 740 $ 4.023 ss.s44a 0.3739 O.POO O.POS 684660 39 V60 83. 274 55.5380 0.$ 740 0.198 0.20$ 684646 40 780 8"-3 . 930 55.5330 0.$ "f44 O.L96 0.200 684635 41 800 GS.GPBO 0.3747 O.L93 0.197 684627 4P 820 '8$ .845 55.5230 0.$ "f49 O.L93 Q.L9$ 6846LL 4$ e40 8$ .798 55 bLGO 0.375L 0.1PO 0.193 684606 86a 8$ .758 55.5lso a.sfss 0.189 0.190 684591 45 880 8$ .717 $ 5.5090 0.$ 755 a.1$ 4 O.LGB 684592 46 900 8$ . 68$ 55.$ 040 0.$ 759 0.186 O.I86 684567 47 9PO 8$ .644 55.5000 0.3760 O.LBB 0.183 684566 48 940 83.606 55.4950 a.sv62 0. IGP 0. 181 684549 49 960 83.576 55.4910 0.$ 763 a. 181 0.179 684536 50 980 83.53% 55.4880 0.3766 0.176 0.177 68454l

VAAXABLI": TABLE SUHHAAY (COIQTXNUED)

SAHRLE DELTA AVG. TEH AVC~ . PAE VAP. PAE LEAK SXH LEAK HAS AXA HASS IMQHBEA HXNS DEC. F PSXA PSXA PEA CEHT PEIR CENT POUNDS 51 1000 83.511 55.4830 0.3768 O.L79 0. 176 684511 SP '1o2a 83.478 55.4800 0.3770 0.175 0. L74 684515 63 la4o 83.448 55.4760 0.3772 0.175 0.1T2 684499 1o6a 83.422 55.47PO 0.3775 0.175 0.1TO 684478 L

laea 83. 391 55.4690 0.3777 0.172 0.169 6844TB 56 1100 8$ .358 55.4650 0.3779 0.171 0. 167 684468 57 1120 83.$ 37 55.4620 0.3783 O.L71 0. L66 684452 58 1140 83.306 55.4590 0.$ 785 O.L68 O.L64 68445L 5'7 1160 83.288 55.4560 O.STBB a.169 0.163 684432 60 1 180 83.258 55.4520 0.$ 790 0.168 0. 16'2 684419 61 1200 83.232 55.4490 0.3791 0.166 0.160 6844LS 62 1220 83.214 55.4470 0.$ 795 O.L65 0.159 684407 63 124a 83.186 55.4440 0.$ 798 0.163 0. 158 684400 64 1P60 BS.L62 55.4410 0.$ 800 0.162 0. 156 684390 65 1280 83.L42 55.4380 0.3803 0.162 0.155 684374 66 LSOO 83. 1L6 55.4350 0.$ 804 O.L61 O.154 684369 67 132a BS.LOO 55.4330 0.3809 0. 160 0.153 684358 68 1340 8$ .075 55.4300 0.$ 810 0. 159 0.152 684350 69 1360 83.065 55.4280 0.$ 815 O.L59 0. L51 684""3"-3P 70 138a 8$ .036 55.4250 0.3816 0.157 o.1sa 6843$ L L400 83.024 55.4230 0.$ 821 0.157 0.149 6843L5 72 1 4PO'440 8$ .008 55.4POO 0.$ 824 0 158 a.148. 684P9$

TS 82.988 55.4180 0.$ 826 a.156 0.147 684292 END OF TABLE

VAAXAIBLE SURHAAY

8) AMPLE OELTA TEMP TEMP 2 TEHP NLIHBEA RXHS DEG. 13EG . F DEG. DEG DEG 13EG . F 0 81.160 DELETED 81.580 80.940 80.400 DELETED 2 Po 81.080 DI=LI=TED 81.5$ 0 80.'950 80.400 DELETED 40 81.070 DELETED 81.560 80.970 80.420 DELETED 60 SL.170 DELI=TED 81.570 80.970 80.400 DELETED 5 80 81.080 DELETED 81 . 580 80.950 80.4PO DELETED 6 100 SL.LPO DELI"TED 81.540 80.9PO 80.4ao DELI":Tl".:D "f 1PO BL.OSO DELETED 81. >50 80.980 80.480 DELE rED 8 L40 e1.aeo DELETED 81 . $ 60 81.000 80.450 13FI I=TI'"D 9 160 81. neo DELETED 81.600 81.080 80.490 DELETFD 10 :Leo fBL . 180 OEL I:=rEO 81.600 80 . 9fBO 80.480 13ELFTI: D 11 E?00 81.060 DELETED 81.800 ea.44o OEI.ETEO 1P P.PO Sl.n9a DELI."'"TED 81.570 80.970 eo.4sa I:) I=LETI:"'13 18 E?40 81.080 OEL E7EO 81.sea BL.DBO eo.490 OEI...E:TEO r."60 81.n4a OI=LETED BL.GBO 81,080 eo.ssa OEL!-.."I'E:D

1,5 i)80 81.200 DEI F::TED 81.590 81.050 eo.sao DEI I"'"TEO 16 Boa 8:I.. LPO Dl":LIETEI3 8:L . 580 81 . 1PO eo.s; a Dl.".LI":Tl'""l3 17 Spn e1. 1sa DEL ETED SL.610 8:I.. 080 Bo.sea DEI ETEO 18 840 81. 110 Dl=l I.=TED 81 ..'570 e1.aso'1.asa ea.seo 131=LETF" D L9 860 IB1. 1PD DELETED SL.SGO 80.520 DEI ErEO Pn 880 81.120 DELI=TFD 81.$ 90 80.990 ea.sso DELFTEI3 Pl 4no 81.070 DFLETED 81.sso 81.aso eo.ssa DEL.E'rEO 4PD 81.120 OEI I":TFD SL.$ 70 80.990 80.580 131":LF Tl='"D P.S 440 e1. 1oa DEL E'rED 81.$ 80 81.000 80.570 OEI .E:TED 460 8:L . 080 DFLI":TEI3 81.550 81.aso 80.580 13I=LI= TED P.s 480 81.n9o DELF<<TED 81.590 81.080 ea.seo DEL.ETED P6 $ 00 e:L. aeo DELI'""TED 81'.600 BL.070 eo.6no I)ELETED v":)7 GP..O 81 . 0"fo OF I...I":.".'I'ED 81.600 BL.060 80.6LO DELETED i"'8 l )9

!540 81 .:LPO DEL ETEO 81.610 81 . li20 80.680 I:)I.=l I""I'I:""13

$ 60 BL.070 OEI...E:TED 81.580 81 . 080 80.650 OEI .I.=, I EO so 580 Sl Ofo. (3F.I. I'""TFD 81.$ 60 81..0TO 80.680 13EL.I-"'TI:." 13

."-31.

t 3PQ 6() 0 81. ora I:)EI...E I'F::0 81.600 81.070 80.650 OELETI"::.O 680 81. 1oa "

Dl:=L.F;.TEO 8:I.. 590 f31 . 070 80.660 I:)EI..E'I"I:"D 6410 I:)El .I":7'I:":.I:) 8:I.. 680 f31 . 070 80.67n OEI..E IT,:O

3 'I 660 81. 110 I:-"Tl=..D '31=.1..

81.600 81 . Oi""0 80.690 I.') I.=LET!;".".D 85 680 131. DC)0 13E:I...F':Tl:". I:) f31 . 610 e1.:I.no eo.-f1n DEL ETEO

'36 Too 81. 1pa 131.=1... I: TED 81.600 81. 0"fo ea.zoo 131=1 I'"Tl:"13 87 "fr?0 Si .:1.80 f3EI .I:.".TED 81.680 831 . 1ieo BD.690 OEI .E'I'IXO

'38 T40 8:L .:1.10 DEI...IXTED 81 . 6ieo BL.100 SD.TLD 13EI..I.":TI:""D e

3Q) 'f 60 81 . 140 DELETED 81..!590 81.aTn 80. "f10 OEI..ETEO 40 "feo 81 .:1.50 131=LI". TFD 8:I.. 680 8:L .:L40 fBO. fr 0 DI-.-.LI= I I.=D 41 Bnn fB1. 110 OEI E'I'ED 81 . 570 81.070 80.740 DEI E'I'EO epo 8 1..:l. 70 131=.LI:""TEI3 BL. 610 81 . Loo Ba. f4a 13ELETI'- D 48 F340 e1.1no DFL ETED 81.590 BL.OGO 80.740 DELE rED 860 SL.140 Ol'=.L(=TFD 81.680 81.040 80 . "fso DELI-"'TI'""l3 880 81 .:L 00 DI=I...F".TFO 81.590 BL.070 80."f40 OEL ~'TFO 46 900 SL .:I!10 131=..L I'="TFD 81.680 81. n-fa SO.T60 13EI I=TED 47 9PO 81.090 DELETED 81.680 Bl . 070 80. 770 DEI...E:TED 48 940 IB1 . 080 DI=LI=.TED BL.600 81.. 080 80.780 131=.1 I'"'I'ED 49 9y) 0 . A1.100 DELE:rEo 81 . 610 81. 100 en.Teo OE'.LET<<)

sa 980 fB1 . 070 nEI. IX rFO 81.. 6PO BL.OPO 80.780 Ol-:"LE'I E D

A16 VA!,XABLE TABLI.= 8!..NHAAY (CONTXNUEDI SAMPLE OI"., I..TA TEMP 1 TEMP 2 TEMP 8 TEHP TRIP 5 TEI".P 6 iwÃHBEA I~i XNS l3EG . F 13EG . F I3FG . F DFG. F Dl.:G . F l3EG. F 51 1000 e1. o6a OELETEO 81 .630 81 . 100 80.780 DE!. ETED 52 1080 81 . 130 i3FLETI=O 8:I. .590 81.030 80.790 !3EI ETI=D

~8 L040 81.0wa DELETED 81 .600 81.070 BQ.TBQ DELETED 54 1a6a 81.150 OEI r.=-n=O 81 . 620 81.060 80.810 OELETFD i5 1oea 81.150 DEI ETED 81 . 6QO 81 . OPO BQ.T90 DELETED 56 I 1.00 81.LOO oE!..r=-. r Eo 81 , 610 80.990 eo.eaa DFLETED 57 11PO e1.070 OELETEO BL .630 81.11a 80.810 DELETED 58 :I.:I. 40 8:I.. 070 DI:=I. I.".'TFI3 8 :I. .600 8:I., 080 ea.e1a DFI ETED 59 :I.:I. 60 81..:I. 00 DFLETED 81 .6ao 81.120 80.830 DELETED 60 1 LBQ BL.070 DI-'LI'""TED 81 .6ao 81..070 Ba.epa DI=LETED 61 leoa 81.070 DELETED Bl .600 81.080 ea.eoo DELETED 6P 18PO 81.L60 oELErEo 81 .630 81.0TO 80.870 DELETI=D 63 1840 81.120 DELETED BL .600 81.1oa so.eea DELETED 64 1860 81.. 150 DELETED 81 .560 BI.040 80.860 DELETLD 65 LPBO 81.I40 DELETED BL .550 81.0ea 80.850 DELETED 66 1.800 81.110 DELETED 81 .570 81.a1a Bn.e6o DELETED 67 1380 81.130 DELETED BL .560 81.aeo 80.900 DELETED 68 l840 Bt.oea DELI.":TED 81 .560 81.o6a ea.e9o DFLETFD 69 1860 81.140 DELETED BL .580 ,Bl . 070 80.940 DELETED Ta 1380 81 . Loo DELI=TED 81 . 540 81.020 80.920 oELErEo TL 14oa Bl . 150 DELETED 81 .590 BL.OBO 80.990 DELFTED 72 14PO 81.160 DELETED 81 .580 81.070 81.000 DELETFD 73 L440 BI.180 DELETED 81 .55Q 81.040 eo.qeo DELETED Ehlo I3F TABLE

A17 VAAXAIBIE TABLE GlJHHAAY SAMPLE DELTA TEHP TEMP TENP NUHBEA NXNS DEC. DEC 0 81.630 82.$ 90 90.210 90. 1,90 89.9ao 90.280 2 20 BL.630 GP..SGO 89.980 89.930 89.690 90.0PO

~

3 40 81 . 630 82.380 89.TOO 89.670 89.440 89.760 60 81.620 BP.$ 70 89.490 89.450 89.190 89.5$ 0 C'

~) 80 BL.620 82.$ 80 89. 190 89.2oa 88.950 89.aao LOO BP.$ 70 88.960 88..980 ae. r4a 89.080 f 12O 81.630 GP..$ 70 88.750 88.750 88. 'iP.O 88.860 8 140 81.630 BP.$ 50 88.$ 40 88.580 BG.SPO 88.6"fa 9 160 BJ.. 630 82.$ 50 GG.SLO 88.$ 80 88 . 1PQ 88.46a 10 180'00 81. 63a 82.$ 60 88.160 88.180 87.930 GG.HTO 81 . 630 82.$ 40 87.9$ 0 87.990 87.730 88.680 12 PHO 81 . 630 Br2. $ 40 87.740 8"f . BPO 87.$ 50 87.9PO La 240 81.630 82.$ 30 87.620 GT.630 87.$ 80 BT.T40 P60 BP.$ 30 87.410 87.470 8"f .210 BT.$ 60 15 280 81.630 82.$ 30 87. 210 87.290 87.020 87.$ 90 16 $ 00 81.. 620 BP . $ 10 BT.110 87.L40 86.900 87.220 1.7 $ 20 81 . 610 86.920 86.980 86.7$ 0 87.090 te 340 81.610 82.$ 00 86.T60 86.830 86.580 86.9$ 0 L9 '$60 81.61a GH.P90 86.630 86.700 86.430 86.T90

. Ha 380 BL.600 82.290 86.480 86.$ 5a 86.280 86.660 Hl 4aa Gl.600 BH.P70 86.$ 60 86.400 86.160 86.$ 40 HP 420 BL.590 BH.PGO 86.230 86.280 86.020 86.4IO 23 44a 81.600 BH.PGO 86.090 86. 160 85.900 86.270 460 BL.590 BP.PBO 85.990 86.040 85.'780 86.16a 25 480 BL.590 GH.P70 85.830 85.930 85.670 86.aso P6 500 al . 600 GP.P70 85."f50 8$ .eao 85 560 85.920

<<27 SP.O 81.600 GH.P60 85.650 85.700 85.450 85.820

,He 54a 81.600 BrH . PSO 85.510 85.900 8$ .$ 40 GG.TOO 29 $ 60 GL.590 GH.P70 85.450 85.500 85.240 85.600

$0 580 BL.$90 BP.PGO 8$ .$ 00 8$ .410 85.140 85.$ 10

$1 600 81 . 580 82.250 BG.PSO GS.SLO 85.050 85.420

$2 620 Bl.600 BH.P60 85.140 85.PHO 84.9TO 8$ .$ $ 0 33 640 81.600 82.250 85.040 '85.130 '84.880 85.240 660 81.610 BH.PSO 84.9$ 0 8$ .070

• 84.81.0 85.16a

$5 680 Bl . 610 82.240 84.890 84.970 84.740 85.080 36 700 81. 610 BP.P40 84.T90 84.9LO 84.660 84.990

$7 7PO GI.600 BP.HSO 84.700 84.830 84.600 84.920 38 T40 BI.$90 BP.PHO 84.640 84."f60 84.$ ao e4.84a

$9 "f60 BL.600 GH.PPO 84.560 84.700 84.460 84.760 40 780 Bl . 600 BP.PHO 84.480 84.640 84.aea 84.69a 4J. 800 8 J.. 6J.O 82.210 84.450 84. 'iao 84.$ 40 '4.640 4P BPO 81.600 BH.PHO 84.$ $ 0 84.26a 84.570 43 840 GI.600 eH." oa 84.340 84.480 84. P10 84.520 860 81.610 82 . 200 84.PBO 84.4LO 84.160 84.460 45 eea 81.610 82.200 84.220 84.$ 70 84.110 84.400 46 900 Bl . 6IO 82.190 84.1.70 84.$ PO 84.050 84.$ 50 47 920 82.190 e4.1ao 84.2TO 83.990 84.$ 10 48 940 81 . 610 82.180 84. OTO 84.2PO 8$ .9$ 0 84.P60 49 960 81.620 82.170 84.nso 83.890 84.22a 50 980 81.620 BP . 170 8$ .990 84.1$ 0 83.860 84. 1.TO

VAAXABLE TABLE 5UHHAAY (COHTXHUED)

Bi AHPLE DELTA TEMP 7 TEHP 8 TEMP 9 TEHP 10 TEHP II TEMP l2 HLIHBEA MXH5 DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 51 1onn 81.610 82.L60 83.970 84.1QO $ 3.$ 20 84.120 52 1020 81.6'10 82.L50 83.9lo 84.050 83.770 $ 4.09o 53 1O40 81.610 82.I40 83.880 $ 4.O20 83.740 $ 4.06O 106O BL.6lo 82.130 83.820 83.980 83.700 84.010 55 1080 $ 1.61n 82.1IO 83.800 83.950 83.650 83.990 56 1 100 81.610 $ 2.100 83.770 83.900 83.620 83.940 57 1120 81.620 $ 2.0VO BS.T40 83.$ 60 $ 3.590 83.900 58 I 140 81.610 $ 2.090 83.700 83.$ 30 S3.560 83.890 59 1160 81.620 82.070 83.660 $ 3.810 83.550 83.$ 60 60 1 180 Sl.610 $ 2.07O $ 3.610 83.770 83.5QO 83.$ 20 61 1200 $ 1.610 82.060 83.600 83.730 83.480 83.800 62 L220 $ 1.610 $ 2.030 83.560 $ 3.710 83.440 $ 3.760 63 L240 81.610 82.03O 83.520 83.680 S3.420 83.740 1260 81.610 $ 2.O20 $ 3.500 83.650 83.380 83.700 65 1280 $ 1.600 82.020 83.470 83.630 $ 3.360 $ 3.690 66 LSOO 81.610 82.010 83.440 83 590 83.330 $ 3.670 67 L320 81.610 82.010 83.420 83.580 83.310 83.620 68 1340 81.610 $ 2.01O 83.390 83.550 83.280 83.5$ 0 69 1360 81.620 82.0OO $ 3.360 83.520 83.260 $ 3.6LO 70 LSBO 81.630 82.000 83.340 83.510 83.230 83.550 T1 L400 81.630 81.990 83.320 83.480 $ 3.200 83.5LO 72 1420 BL.630 $ 2.000 83.300 83.440 83. 180 83.510 73 L440 $ 1.630 BL.990 83.270 83.430 83.160 83.490 EHD QF TABLE

VAAXAIBLF TABLE SUHHAAY BAHPLE DELTA rEHI TEHP TEHP TEHP TEHP l7 TEHP NCJHBEIR HXNS DEG. DEG. F DEG 0 va. 1-fa )0. $ 80 90.230 BB.STQ DELETED )0. 130 P 20 89.890 90. 1'10 89.970 88.070 DELETED 89.87a 0

3 na 89.64a 89.870 8) . 710 87.850 DELETED 89.620 60 89.400 89.610 89.500 87.580 DELETED 89.390 5 80 8). 160 89.400 8) PSO 87.$ 80 DELFTED 89.160 6 100 88.930 8'2. 160 89.aBa 8"f . 220 DELETED 88.940 f 120 88.730 88.940 Be.ela 86.910 DELETEO 88.720 8 14Q 88.520 88.730 88.600 e6.7aa DELETED Be.saa CP l60 ee.31a 88.520 88.400 86.55a DELETED 88.$ 20 10 180 88.210 88.$ 30 Be.pao 86. Sr"0 oELErED 88.220 11 Baa 87.930 Be.l50 88.610 86.l$ 0 DELETED 87.920 12 220 8-f . 76a 87.970 Bf.esa 85.960 DELFTED 87.740 13 240 87. 5)0 87.810 87.650 85.820 DELETED 87.580 26a BT . 420 87.620 87.4ea 85.750 DELETED BT.420 15 280 BT.BBQ 87.450 87.300 BS.460 DELETED 87.230 16 300 87.080 87.300 87.160 85.550 oELE rEo 87.090 17 SP.O 86. )20 87.150 86. )90 85.360 DELETED 86.940 le $ 40 86. "fea Bf.aaa 86.850 Bb 200 oELE rEo 86.790 19 360 86.640 86.860 86.710 85.070 DELETED 86.640 Ba 380 86.500 86.730 86.580 DELETED 86.5IO Pl 400 86.35a 86.590 86.450 84.800 DELETED 86.370 22 420 86.250 86.460 86.320 84:680 DELETED 86.25a 23 440 86.110 86.$ 50 86.180 84.560 DELFTED 86.120 24 460 86.000 86.230 86.aTa en.380 oELE rEo 86.ala 25 480 85.880 86. 5.5.0 85.950 84.360 DELETED 85.880 i26 500 8'70 86.aaa 85.830 84.240 DELETI=D 85".77Q 27 520 85.66a 85.eva 85."fna 84.140 DELETED 85.660

,28 540 85.560 85.790 85.630 84.030 DELI"=TED 85.570 29 560 85.460 85.69a 85.530 83,.940 DELETED 85.470 30 580 Bb 360 85.590 85.4PO 83.840 DELETED BG.STQ 31 6aa 85.2TQ 85.500 85.$ 20 83.740 DELETED 85.270 32 620 85.170 85.400 85.230 83.650 oELErEo 85.180

'33 640 BG.a90 85.31a 85.lea 83.560 DELETED 85.100 34 . 660 85.a10 85.220, 85.060 83.480 DELETED 85.020 35 680 84. )30 85.l30 84.980 83.370 DELETED 84. 'MO 36 700 Bn.ena 85.070 84.91a BS.PBO DELI=TED 84.8"fa 37 720 84.T60 84.990 84.830 83.POO DELETED 84.790

$8 740 84.690 84.9PO 84.T60 8$ .1$ 0 oELE'rEo 84.720 39 760 84.640 Bn.ena 84.690 83.070 DELETEO 84.660 40 780 84 b60 84. f50 84.630 83.010 OELI='TEO 84.590 800 84.520 84. f1Q e4.56a e3.000 DELETED 84.5PO 42 820 84.460 84.650 84.5la 82.9na oELE rEo 84.4TO 43 840 84.400 84.6ia 84.480 82.860 DELETED 84.420 44 86Q 84.340 84.550 84.420 82.800 oELE rEo 84.$ 60 45 Bea 84.270 84.51a 84.36a 82.760 DELETED 84.300 46 900 84.220 84.460 84.$ 00 BP..710 oELErEo 84.260 47 920 84.1TO 84.4PO 84.250 82.660 DELETED 84.200 48 'Ma Bn.l30 84.$ 60 84.210 82.620 DELETED 84.16a 49 960 84.080 84.330 84. l70 82.570 DELETED 84.120 sa 980 Bn.ana 84.280 e4.5.3a BP..SSO DELETED 84.080

A20 VARXAB1 E TABLE SUHHARY (COhfTXNUED)

SAMPLE DELTA TEMP 1$ TEMP 14 TEMP I5 TEMP 16 TEMP I7 TEMP IS NQXBER 'AXES DEG. F DEG. F DEG. F DEC. F DEG. F BEG. F 5I laoo 84.aoa 84.250 84. 100 82.530 DELETED 84.040 52 l020 83.960 84.POO 84.060 82.5IO DELETED 83.@90 1o4a 83. "ZSO 84. I60 84.0IO 82.460 DELETED 83.960 1060 83.89a 84.130 83.990 BP.440 DFI ETED 83.920 55 1osa 83.860 84.IOO 83.950 82.$ 90 DELETED 83.870 56 l100 83.81a 84.070 8$ .9PO 82.360 OELFTFD 83.840 57 11 a 83.T90 84.030 8$ .880 82.330 DELETED 83.810 58 I 140 83.T50 83.990 83.850 82.290 DELETED 83.TBO 59 I 160 83.740 83.960 83.830 82.260 DELETED Bs.75a 60 I 180 83.700 83.950 83.780 82.230 DELETED 83.700 61 l200 83.670 83.900 83.760 82.POO DELETED 83.680 62 1220 83.640 83.890 83.7oa 82.170 DELETED 83.640 63 l240 Bs.61a 83.850 83.700 82.140 DELETED 83.620 64 126a 8$ .59a 83.820 83.670 82.1aa DFLFTED 83.600 65 1280 83 540 83.810 83.640 82.090 DELETED 83.570 66 1300 83.5$ 0 83.780 83.620 82.050 DELETED 83.52a 67 132a 83. 510 83.760 8$ .6ao 82.030 DELETED 83.510 68 l$ 40 8$ . 480 83.720 83.560 81.%90 DELETFD 83.48a 69 1360 83.450 83.7ao 83.550 81.980 DELETED 83.460 70 1380 8$ .430 83.680 8$ .51a 81.950 DELETED 83.4PO T1 14aa 83.390 83.650 83.500 81.920 DELETED 83.400 72 1420 83.380 83.640 83.490 81.910 DELETED 83.390 Ts 1440 83.370 83.61a 8$ .450 81.890 DELETED 83.360 ENO OF TABLE

A2L TAIPEI E SUHRAAY SAMPLE DELTA 20 TEMP NUHBEA HXNS DEG l3EG DEG I3EG L 0 $ 6.$ ea 87.490 86.640 86.890 87.900 87.650 2 20 86.7$ 0 87.350 86.560 86.790 8"f . 810 87.550 40 86.540 87.260 86.460 86.680 87.690 87.440 60 86.510 BT.150 86.360 86.600 87.600 87.350 5 80 86.440 87.070 86.270 ~ 86. 540 87.500 87.PBO 6 100 $ 6.310 86.9$ 0 $ 6.19Q 86.440 87.430 87.170 T L20 86.230 86.890 86.14a 86.360 87.360 87.090 8 14n 86.230 86.790 86.050 86.3la 87.250 87.0LO 9 L60 86.070 86.7IO es.970 86.L90 87.I90 86.920 1a 180 86.070 86.6la $ 5.910 86.69a BT.690 86.850 L1 2ao es.890 86.540 85.860 e6.63a 87.820 86."f70 1P 220 $ 5.860 86 Rba 85.780 es. <<>60 86.950 86.69a 13 24a es.eRa 86.400 85.680 85.630 86.870 86.630 260 85.700 s6.32a 85.660 85.840 86.810 86.540 L5 P.en $ 5.670 86.pao 85.550 85.T50 86.710 $ 6.460 16 300 85.590 86.160 $ 5.520 85.720 86.660 86.400 17 320 es.saa 86.aeo 85.460 85.650 86.580 86.350 18 340 es.ssa 86.000 85.390 Bb b90 86.530 86.P70 L9 360 es.42a 85.920 85.320 es.s2a 86.470 86.210 20 380 eb.aTO 85.880 .8$ .280 SG.RTO $ 6.410 86.L60 2l 400 85.330 85.810 $ 5.220 $ 5.400 86.350 86.080 2P 420 es.270 85.750 85.180 85.350 86.300 86.0PO 23 440 85.2LO 85:680 SG.LLO 85.290 86. r'30 85. c)60 24 460 85.130 85.610 85. 06'0 85.260 86.L90 85. 910 25 4$ 0 es.1ao 85.550 BS.OOO 85.200 86.120 $ 5.850 P.6 500 BG.LRO 85.500 84.950 85 . 120 86.060 85.790 "c<<7 520 84.9ea 85.450 84.890 85.080 86.020 85.740 28 sRa 84.970 85.390 84.840 85.030 $ 5.960 85.690 29 560 $ 4.900 85.320 84.800 84.980 85.880 85.630 an 580 85.280 84.740 84.930 85.'850 $ 5.580 31 6no SR.esa SS.PRO BR.710 84.900 85.790 $ 5 'ian 32 620 84.760 85.190 84.660 '84.830 85.740 .85,480

'3.. 640 BR.T60 .85.170 84.640 84.800 85.690 85.440 34 66a 84. 7LO es.laa SR.SSO 84.760 '5.640 85.390 35 680 84.680 85.060 84.520 84.7ao 85.590 85.330 36 "f00 84.650 es.020 84.490 84.670 85.560 85.310 37 720 84.570 84.990 84.460 84.630 $ 5.500 85.PSO 38 740 84 540 $ 4.940 84.390 84.5fn $ 5.470 85.2la

%9.-- 760 84.490 84.9'ln 84.360 84.550 85.400 85.160 40 780 84.440 84.890 84.320 84.480 $ 5.340. ss.12a 41 eao 84.380 84.830 84.280 84.4TO 85.3IO 85.080 42 e2a 84.340 84.770 84.270 84.440 es.2sa es.aao 840 84.290 $ 4.730 84.2LO 84.400 85.210 84.990 44 860 BR.PSO $ 4.680 84.170 84.360 85.170 84.'940 45 880 $ 4.190 $ 4.640 84.140 84.320 85.120 84.900 46 900 BR.L70 $ 4.580 BR.LOO" 84. r"90 es.a9a 84. 8"f0 47 920 84.laa 84.530 84.nTa 84.260 85.040 SR.eaa 48 940 sR.nea 84.480 84.040 BR.L90 es.aaa 84."fea 49 960 64.030 84.450 83.990 SR.LTO 84.960 $ 4. -rRa sa 9sa BR.aaa 84.400 sa.96a 84. 140 84.930 84.720

VAAXABLE TABLE SUHHAAY (CONTXNUED)

SAMPLE DELTA TEHP 19 20 TEMP P1 TEHP 22 TEMP 23 TEMP 24 NQVBEn HXNS DEG. F DEG. F DEC. F DEG. F DEG. F DEG. F 51 1OOO 8-3. 970 84 . ""360 Ga.v10 84.1LO $ 4.$ 90 84.670 52 1020 8.".3 . 920 84.$ 10 8$ .890 84.070 84.860 84.640

~ma 1040 83.890 84.290 83.860 84.050 $ 4.830 84.610 54 106O 83.850 84.240 83.810 84.010 84.800 84.570 55 LOBO 83.840 84.'200 83.790 83. 770 84.760 84.550 56 L 100 $ $ .810 84.1$ 0 83.760 83.930 84.730 84.510 57 1 120 83.760 84.1$ 0 83.720 $ 3.8~0 84.TOO 84.480 58 L l40 83.T30 84.L10 83.700 83.860 84.660 84.440 59 L160 83.TOO 84.080 83.670 83.850 84.630 84.420 60 1180 83.670 84.040 8$ .640 83.8PO 84.620 84.380 61 1POO $ 3.64o $ 4.o10 83.610 83.800 84.580 84.360 62 1220 8$ . 660 83.980 8$ .580 83.760 84.560 84.$ $ 0 63 L240 83.580 83.950 83.550 83.720 $ 4.520 84.300 64 1260 83.560 83.900 83.530 83.710 84.500 84.2TO 65 L280 83.550 83.890 83.5LO 83.660 84.480 84.270 66 1300 8$ .510 83.860 83.4TO 8$ .640 84.460 e4.20o 67 L320 83.480 83.820 83.450 83.630 84.430 84.190 68 1340 $ 3.470 83.800 83.420 $ 3.60o 84.400 84. 170 69 1360 83.450 83.TBO 83.4IO 83,.600 84.370 84.140 70 Laeo 8$ .420 83.750 83.$ 80 83.5$ 0 84.$ 50 84.120 71 1400 83.420 83.740 83.$ 50 83.550 84.$ 30 84.090 72 L420 83.$ 90 83. foo 83.330 83.500 84.300 84.080 73 l440 83.370 83.680 83.$ 20 8$ .480 84.290 84.040 END OF rABLE

VARXABLE TABLE SUHHARY 8? AHPLE DELTA TEHP TEHP TEHP 30 NtJHBER HXNS DEG. DEG DEG DEG DEG. F 1 a 87.2TQ 87.650 87.860 87.550 89.990 DELETED P 20 87.160 BT.SPO 87.770 BT.460 89.740 DELETED e

40 87.a7a 87.440 87.670 87.380 89.480 DELETED 60 86 . '??80 87.340 87.570 87.P70 89.210 DELETFD C? 80 86.910 87. r?Ao 87.490 87.190 88.940 DELETED 6 100 86.T90 er. 14a 87.400 8"f . 110 88.730 DFLETI=D 7 120 86.TOO 87.060 87.soa 87.o1a 88.52a DELETED 8 140 86.620 86.940 8"f . 210 86. )?40 se.s1a DELETFD 9 160 86.540 86.870 87.150 86.850 88.100 DELETED 1a 180 86.460 86.800 87.670 86."f60 88.100 DELETED 11 2oa 86.4ao 86.730 86.990 86.670 87. 710 DELETED 12 220 86.710 86.640 86.920 86.640 87.530 DELETED 13 . 24a 86.24a 86.560 86.840 86.550 87.290 DELETED 14 P60 86.180 86.$ 00 86.170 86.450 87.150 DELETED 15 280 86.1ao 86.420 8*.710 86.390 86.990 DELETED 16 saa 86.050 86.350 86.640 86.320 86.840 DELETED 17 32a 85.980 86.280 86.570 86.260 86.69a DELETED 18 340 85.930 86.220 86.520 86.190 86.$ 40 DELETI=D 19 360 85.840 86.150 86.450 86.130 86.400 DELETED 20 380 85 780 86.09o 86.39a 86.050 86.270 DEI E7I=-O 21 4ao 85.730 86.020 86.330 86.010 86.1sa DELETED 2P 42a 85.680 85.970 86.P60 8$ .950 86.000 DELE7'EO 23 440 85.600 85.900 86.210 85.890 85. 860 DELETED 460 8$ .560 85.850 86.150 85.830 85.730 DELETED 25 4ea 85.soa 85.790 86.090 85.780 85.630 DELETED 26 $ 00 8$ .460 85.740 86.050 85."f20 85.500 DELETED 27 52O 85.sea 85.690 85 . '??90 85.670 85.400 DELETED 28 $ 40 8$ .340 85.630 85.950 85.610 85.280 DELETED 29 $ 6a 85.290 85.590 Ss.e9a e$ .$ 6a 85.170 DELETED 30 580 BG.P30 85.530 85.830 85.$ 10 8$ .09o DELETFD Sl 600 85.200 85.490 8$ .7eo 85.460 85.000 DELETED 3P 620 85.140 85.420 85. fsa 8$ .410 84.910 DELETFD 33, 640 85'.10Q 85.4ao BS.680 85.370 84.810 DELETED 34 .66a 85.060 8$ . 330 85.640 8$ .31a e4. -r1a DELETI=O 35 680 85.010 85.310 85.590 85.280 84.630 DELETED 36 700 84.??70 85. 2TO 8$ .540 85.2PO 84.560 DELETED 37 720 84.vsa 85.210 85.500 85 980 84.480 DELETED 740 84.880 85. 170 8$ .460 85.150 84.410 DELETFD 760 84.840 85.120 85. 410 85.090 84.350 DELFTED r 780 84.TBO es.aeo 85.370 Bs.a6o 84.300 DELETED 800 84.740 Bs.a4o sS.s2a 85.000 84.250 DELETED 42 820 84.700 85.000 8$ .280 84.940 84.170 DELETED 43 840 84.660 84.950 85.240 84.920 84. 110 DELETED 860 84.630 84 . 910 85.200 84.860 84.060 DELETED 45 880 84.580 84.860 85.150 84.830 84.a2o DELETED 46 900 e4.54a 84.830 85 . 120 84.7wo 83 . '??60 DELE7'ED 47 92a 84. 4 70 84. 790 85.080 84.740 83. ")10 DELETED 48 940 84. 460 84."f40 8$ .040 84.700 83.870 DI=LLTED v60 84.420 84. 7"10 85.010 84.65a 83.82a DELETED 50 980 84.390 84.6TO 84.970 84.610 83. f70 DFLETED

A24 vAnrABLE TABLC Buiwnv <GDNTxNuED>

BAHPLE DEI TA TEMP 25 TEMP 26 TEMP 27 TENP 28 TEMP 29 TEMP 30 IHJHBEA N Xh!S DEG. F DFG. F DEG. F DEG. F DEG. F DEG . I=

51 1oao $ 4.$ 5a 84.650 8<.9$ 0 84.570 83.7$ 0 DELETED 42 l020 84.290 84.600 84.900 84.540 83.700 DELETED 53 10<0 84.270 84.560 84.860 84.500 $ 3.650 DELETED 54 1060 84.270 84.510 84.830 80.460 83.620 DELETFD 55 1080 84.hoo 84.490 84.790 84.450 83.590 DELETED 56 1100 84 . l70 84.460 84.760 84.400 8$ '.540 DELETED 57 1 '120 8@I. l40 84.~130 84.730 84.390 83.510 DELETED 58 1 140 84. 110 84.$ 90 84.700 84.$ 40 83.080 DELETED 59 l 160 8<.090 84.$ 60 84.670 84.330 83.440 DELETED 60 1 180 84.060 84.$ 10 8<.64a 84.290 83.~00 DELETED 6l 1200 $ 4.aso 84.290 $ <.600 84.260 $ 3.$ 90 DELETED 62 l220 84.000 84.25a 84.580 84.230 83.360 DELETED 63 l240 83.970 84.240 84.550 84.220 83.$ 20 DELETED 64 1260 8$ .94a 84.200 84.5$ 0 84.190 8$ .300 DELETED 65 l280 83.940 84.160 84.510 84.170 83.27a DELETED 66 lsoa 8$ .880 84.110 8<.480 84.130 83.220 DELE'rl.=D 67 1$ 2a Bs.esa 84.110 84.460 84.120 83 . 210 DELETED 68 1340 83.830 84.060 84.430 84.070 Bs.leo DELETED 69 l$ 60 Bs.e2a 84.030 84.400 84.070 83.160 DELETED 70 1380 8$ .800 84.030 80.$ 80 8<.010 83. 1lo DELETED 71 14ao 83.750 83.990 84.$ 60 83.990 83.090 DELETED 72 1420 83.730 8$ .980 84.$ 30 83.990 Ss.aeo DELETED 73 1440 83. 7la Bs.wsa 84.320 83.950 83.060 DELFTED CND Ol= TABI C

VAAXABLE TABLE SUHHAAY SAHPLE DELTA TEMP TEHP HUNBEA HXNS DEG DEG. DEG DEG 0 ev.900 70. 300 90.240 90.590 9o.osa 86.270 2 Po 89.620 90.010 89.960 90 . 310 89.770 85.9$ 0

~

a 40 89.350 89.730 8). 690 90.030 89.560 85.610 60 89.090 $ 8.460 89. 440 $ 9.7$ 0 89.290 85.320 5 80 88.840 $ 9.230 89 . 180 89.sna 89.070 es.ano 6 LOO $ 8.590 88.940 88.950 89.290 88.840 84 Tba 7 I2a 88.360 88.720 89.o6a 88.600 84.510 8 140 88.150 88.520 88. 510 88.840 88.390 84.Pfo CP 160 87.9ao ee.aoa ee.aao ee.6sa 88.190 Sn.oaa 10 iea 8'7 . 740 88.3PO 88.910 88.4PO er.qea Ba.eaa r?00 87. >40 87.900 87.890 88.24a 87.800 83.610 1P r"20 BT.340 8'7 . '750 86.930 Se.aso $ 7.61a Bn.ana 13 240 87.280 87.560 87.540 ST.BBO 87.420 83.200 P60 87. OIO 87.400 87.380 87.710 87.250 Sa.aoa 15 280 86.810 87.2aa 87.180 ST.S2O 87.07Q 82.TSO L6 300 86.670 BT.070 87.ana 87.360 86.940 S2.640 17 32a 86.5LO 86.9ao 86. 8)0 87.230 86. feo 82.460 Le $ 40 86.$ 70 86.750 86.73O er. 070 86.620 82.290 19 a6n 86.230 86.610 86.580 86.920 86.490 82.120 20 380 86.080 86.470 86.440 86.780 86.360 81.980 400 85.950 86.$ 30 86.$ 10 86.650 86.21a $ 1.$ 20 2P 420 85.830 86.2PO 86.180 86.520 86.090 81.680 23 440 85.690 86.o9a 86.050 86. 370 85.960 Sl.530 46a BG.590 8$ .960 8$ .930 86.270 85.820 81.3TO Ps 480 85.470 85.840 85.820 86.150 85. "fIo 81.230

%6 $ 00 '85.340 85. 730 es. rao 86.040 85.6lo Si.o9a 27 520 85.250 85.610 85.600 Sb )$ 0 85.480 80.970 28 sna . 8$ . 130 85.520 $ $ .470 85.820 es.nia 80.850

<29 $ 60 85.0$ 0 85.410 85.380 85.720 85.300 80.750 30 $ 80 $ 4.930 8$ .320 es.2en 85.630 85.POO 80.640 31 600 Sn.enn 85.230 85.190 85.630 85.100 80.550 32 62a $ 4.7so 85.150 Bb 090 Bs.a2o 80.420

~ $ 3. 640 84.660 85.060 85.000 85..$ 40 84.920 80.$ 10 660 84:570 84.970 84.910 85.250 84.8$ 0 80.220 35 680 Bn.neo 84.880 84.830 85.170 84.760 80. 120 36 700 e4.42a 84.820 84.750 8$ .100 84.680 Bo.o2a 37 f20 84.340 84.730 84.680 $ 5.010 Bn.s9a 79.920

$8 "f40 84.270 84.6sa 84.610 84.950 84.530 79.840 39 760 84. 1 )0 84.580 '4.520 84.880 84.470 79.760 40 780 84. 120 84.510 84.470 84.800 84.400 79.680 800 84.060 84.440 84.4LO 84. fso 84.330 79.600 42 820 83.990 84.$ 80 84.350 84.680 $ 4.2$ 0 79.540 43 840 Ba.vaa 84.320 84.2$ 0 84.620 84.2LO 79.480 44 860 8$ .870 84.270 84. r2PO $ 4.570 84.150 79.380 880 83.820 84. 210 84.170 84.510 84.1LO 7). 300 46 9ao ea. rea 84.170 84.130 84.4TO Sn.osa 79.2$ 0 47 920 83. "fI,o 84 9 c'0 84.070 en.noa 84.0LO 79. 190 48 940 83. 680 84.080 84.020 84.350 $ $ .96a 79. 1$ Q r60 83.640 Sn.ano 83.980 84.$ 20 83.920 7c) . 090 50 980 83.600 83.950 84.270 83.870 79.0$ 0

VAAXABLE TABLE BUHHAAY (CONTXNUED3 BiAHPLE DELTA TEHP Bl TEHP $2 TEHP 33 TEHP 34 TEHP 35 TEHP 36 NdHBEA HXHS DEC. F DEG. F DEG. F DFG. F DEG . I= DI=G . F 5 l. xaao 83.$ 50 83. <<)40 $ 3. 8)0 84.220 83.830 78.990 2 x020 $ 3. 5IO 83.900 8."-.3 . 850 84.200 83.790 78 . ">>40

i53 l 040 $ 3.470 $ 3.8$ 0 Bs.exn $ 4.x40 83. "150 78. )00 54 1060 $ 3.430 83.820 83 . "160 $ 4.laa $ $ . -12a 78.87Q 55 J. 080 BB.BBD $ 3.$ 00 83.740 $ 4.aeo 83.680 78.810 56 '>00 $ 3.350 BB.T40 83. 680 84.QSO 83.640 78.800

$7 J. X20 83.$ 2a 83.710 83.670 83.990 83.6la 78.T60 58 1 140 $ 3.280 $ 3. 6$ 0 $ 3.620 $ 3.950 83.570 78. 7l.0 59 Xl60 BB.P50 83.630 $$ .$ 90 83.920 8$ .550 78.660 6a flea $ 3.220 83.610 83.$ 50 8"=3 . 900 'es.$ sa 78.620 6l x200 $ 3.200 es. >$ 0 83.520 83.860 83.480 78.590 62 l220 $ 3.%50 83.550 83.490 83.830 83.440 78.$ 60 63 1240 8<<3.;I.10 83.$ 10 83.460 83.800 83.420 78 . 5P.O 64 x 260 es.a9o $ 3.490 $ 3.430 83 . 170 83.380 78.490 65 1280 BB.D60 83.460 83.400 83.TBO $ 3.36a 78.450 66 1300 $ $ .040 $ 3.4PO $ 3.390 83. 120 83.330 78.420 67 l<<320 83.010 83. 41,0 $ 3.$ 50 83.700 83.300 78.400 68 ls40 82.990 83.3$ 0 BB.BBQ 83.670 83.280 78.370 69 l360 82.960 $ 3.3$ a 83.300 ~

83 640 83.260 78.330 Ta lsea $2 . <<>>30 83.320 BB.P70 83.6la 83.230 78.300 1l 9. 400 82. 710 83.29a 83.250 83.600 83.200 78.270 72 l420 $ 2.890 BB.PBO 83. r'20 8$ .$ 60 83. l70 78.240 73 1440 $ 2.860 83. r?60 BB.POO $ 3.550 83. l60 78.P20 LND DF TABLL

VARXASLE

SUMMARY

S) AMPLE DELTA TEHP 37 TEMP 40 PRES HUH 'I NUMBER MXNS DEG. F DEG PSXA FRACTXON I 0 90.260 9o.osa 89.540 89.970 55.947 DELETED 2 20 89 . '970 89.740 89.370 89.710 55.928 DELETED 40 89.700 89.430 89.090 89.440 ss.9a9 DELETED 60 89.430 89. I60 88.820 89.190 55. 89I DFLETED 5 80 89.200 88.92a 88.550 88.920'8.680 55.874 DELETED 6 100 88.950 88.70Q BB.P90 55.858 DELETED 7 120 Ba.fsa 88 450 Be.aeo 88.4PO 55. 84p DELETED 8 J. 40 88.$ 10 88.230 87.830 BB.POO GG.BP7 DELETI=D 9 I60 88.290 88.020 87.640 87.9'90 55.811 DELETED 10 1aa 88.690 87.810 87.420 Bf.190 55.798 DELETED 200 s7.9ao 87.610 87.220 87.590 55.783 DELETED 1P P20 87.720 87.440 87.620 87.420 55.767 DELETFD ls 24a 87.540 87.260 86.840 87.230 55.756 DELETED I4 P60 87.370 87.090 86.680 87.070 55.746 DELETFD 15 2eo 87.180 86.880 86.490 86.860 55.734 DELETED 16 soa 87.030 86.750 86.370 86.730 55,722 DELETED I7 "-320 86.890 86.590 86.240 86.590 55.7I1 DELETED ia 340 86.730 86.420 86.070 86.450 55.799 DELETED 19 36a 86.590 86.-300 85.890 86.280 55.689 DELETED 2a sea 86.4sa e6.1sa 85.790 86. 160 55.680 DELETED 21 4aa 86.$ 20 86.010 85.650 e6.oso 55.669 DELETED 22 42n 86. I90 85.890 85.510 85.890 ss.66a DELETED 23 44Q 86.o7a 85."fao 85.420 85.780 55.650 DELETED 24 460 8$ .940 8$ .650 85.P90 85.690 oELErEo 25 480 es.esa 85.510 Bsr160 85.570 55.633 DELETED 26 500 85.710 8$ .410 8$ .060 8$ .480 55.6'24 DELETFD r 520 85.600 85.340 84.980 85.$ 90 55.616 DELETED 28 540 85.500 8$ .230 84.'900 8$ .290 55.608 DELETFD 29 560 85.400 BG.I40 84,790 85. 190 55.600 DELETED 30 680 85.310 8$ .030 84.720 85.100 55.593 DELETED

$1 600 86.2IO 84.930 84. 6IO 85.000 55.586 DELETED rsry 6PO BS.I20 84.830 84.530 84.920 55.$ 79 DELETI=D 33 6'40 .85.030 84.750 84.4sa. 84.840 55.573 DELETED 34 660 84.940 84.690 84.$ 80 84.750 55.566 DELFTI=D 35 680 84.86a 84.610 84.280 84.680 55.560 DELETED

$6 -rao 84. rea 84.63a 84.PPO 84.6ao 5 556 DE ErEo

"-37 720 84.7IO 84.450 e4.14a 84.530 55.549 DELETED 38 r4a 84.620 84.$ 80 84.060 84.4sa 55.544 DFLETED 39 760 84.560 84 . "=310 83.990 84.380 55.538 DELETED 40 780 84.500 84.2sa 83.930 84.32n 5$ .633 DELETED 800 84.430 84. I70 83.870 84.260 55.628 DELETED 4P BPO 84.370 s4.12a 83.810 84.200 55,52$ DELETED 43 840 84.290 84.070 83.750 84.I40 55.518 DELETED 860 84.2SO s4.aoo 83.690 84.080 5$ .613 OELETFD 45 880 e4.1ea 83 950 83.640 s4.a4o 55.$ 09 DELETED 46 900 84.140 8+.890 83.600 83.990 55.604 DELETED 47 920 e4.oea 83.850 83.540 83 . 9"-30 55.500 DELETED 48 940 84.a4a 83.800 83.490 BB.BBQ 56.495 OI=LETI" D 49 96o A4.000 83.750 83.430 83.830 55. 49I DELETED 60 980 83.960 83.700 8$ .390 83. rsa 55.488 DEI ETI=D

A28 VAAXABII= TABLE SUANAAY (CQHTXHUED)

SAMPLE DELTA TEMP $7 TEMP $8 TEMP 39 TEHP 40 PAES HUH L HUMBEA HXHS DEG. F DEG. F DEG. F DEG. F PSXA FAACTXOH 51 LOOO 83.910 83 660 83.$ 50 83.750 55.483 DELETED 52 1a2o 83.870 8$ 610 BB.BLO 83.700 55.480 DELETFD

<53 L040 83.830 83 560 83.270 83.660 55.476 DELETED LQ60 83.eoa 83 530 83.23a 83.610 55.47P DELETED 55 LOBO 83.760 83 nba 83.180 83.570 55.469 DELFTED 56 1loo 83."f30 83 440 83 . IBO 8$ . 510 55.465 l3ELETFD 57 1120 8$ ."faa 8$ n20 83.1ao 83.nea 55.462 DELETED 58 l 140 83.660 83 $ 70 83.050 83.440 55 . 4I59 DELETI=D 59 116a 83.62a 83 340 83.040 8$ .n2o 55.456 DELETED 60 1 180 83.600 8$ BPO ee.a1a 83.380 55.452 DELETED 61 12ao 83.570 83 260 82. 760 83.330 55.449 DELETED 62 IP20 83.530 8$ PBO 82.940 83.310 55.447 DELETFD 63 1240 e3.51a 83 190 82.890 83.270 55.444 DELETED 64 1P60 83.470 83 180 82.860 83.250 55.441 DELETED 65 L280 83.440 83 lna 82.840 8$ .21a 55.438 DELETED 66 1300 8$ .420 83 12a 82.820 83.19a 55.435 DELETED 67 1320 83.40o 83 a9o 82.790 BB.L50 55.433 DELETED 68 1340 83.370 83 040 82. f70 83.1$ a 55.4$ a DELETED 69 136a 83.340 83 a~la 82.730 BB.LLO 55.428 DELETED 70 1380 8$ .$ 2a 83 a2o 82.700 BB.a7a 55.425 DELETI=D "f1 1400 83.290 82 970 82.670 83.050 55.423 DELETED T2 1420 BB.P60 8 pQ 950 82.660 83.oea 55.42a DEI FTED TB 14~la 83.250 82 940 82.630 82.990 55.418 DELETED EHD DF TAB( E

VAnXABLE rABL E BUHHAAY SAMPLE DELTA HUH I-IUH 3 HUM I-IUH 5 HUH HUH 7 HUHBEA HXHS FAACTXQH FAACTXDH FAACTXOH FAACTXOH FAACTXDH FAACTXOH 0 0.5$ 0 a. s36 DELETED 0.48l P 20 0.$ 34 0 539 a. 497 DELETED 0.497 0.483 3 40 a.sse 0.$ 4L o.soa DELETED 0.499 0. 485 6a 0.54P a.s44 a.so2 DELETED O.spl 0.487 c> BQ 0.546 0.547 o.saB DELETED o.sas 0.490 6 IOO 0.549 0.549 0.507 DELETED o.snr 0.492 I

V 120 n.ss2 0.552 o . 50"z nELFrEn 0.511 0.495 8 140 0.55$ n.sss 0 . 51r2 DELETED n. 5>14 9 160 0.558 0.557 O. S7.6 DFLETED 0. 57.7 0.503 10 180 0. $ 61 a.s6a a.s2o DEI ETED a.s21 o.sae LI 2ao 0.564 0.56$ 0.522 DELETED 0.5P5 0.512 L2 P20 0. $ 68 a.s66 0 527 DELETED 0.529 O. S16 1$ 24a 0.57l 0.569 0.5$ 2 DELETED 0.533 0 522 L4 260 0.574 0.573 0.$ 36 DELFTED 0.$ $ 8 a.s26 ls 280 0.578 0.578 0.540 DELETED 0.542 0.531 16 300 Q.GBB a.seB a. s44 DELETED 0.$ 47 0.536 17 320 0.587 0.$ 88 0.549 DELETED 0.552 0.541 Le 340 0.59P a.s93 0.553 DEI FTED a.ss7 0. 546 19 $ 60 0.59T a ..>98 0.557 DELETED a.s6o 0.551 20 $ 80 a.6o2 0. 603 0. $ 62 DELETED a.s64 0.555 2L 400 0.607 o.6ae Q.565 DELETED a.:>69 0.559 C' 4PO a. 61'.617 n.613 0. 569 oEI r-.= rr=o 0.$ 74 0. 563 PB 44a 0.6LB 0.575 DELETED a. s-r9 0.$ 67 P4 460 0. 622 0.6PB 0.580 DELETED 0.583 a.sr1 P5 480 0.627 0.628 0 $ 85 DELETED 0.589 0.576 P6 500 0. 632 0.633 0. $90 DELFTED 0.594 0.580

~ QT 520 0.6$ T a.6$ 7 0.595 DELETED 0.598 0.585 28 s4o a.641 0.642 0 . Gr>>8 DELETED 0.603 0.589 29 560 a.646 0.646 0.60$ DELETED 0.607 0.594 30 $ 80 0.650 0.650 0.606 DELETED 0.610 0.598 31 6no 0.655 0.654 0.608 DELETED a.614 0.602 Sr2 620 0.658 a.6se a.61$ DELFTED 0.618 0.60$

33 640 a.663 0.662 0 .'616 DEL'ETED 0. 6P1 0.609 34 66a 0.66T 0.665 0. 619 Dl=l I=TED Q.6P4 '.612 35 680 0.670 a.668 o.62a DELETED 0.627 0.6ls 36 -rao 0.673 0.67L n.622 DELETFD o.63n 0.6LB 37 "120 0. 61T 0.674 0.625 nELETEn 0.632 0.620 38 "140 0. 680 0.676 0. 62"1 OELETEO a.63s 0.6PB 39 160 0.68$ a.6re 0.628 DELFTED 0.636 0.625 40 "180 a.68s 0. 680 0. 6$ 1 DELI=TED Q.638 0.627 41 800 0.687 0.682 0.63$ DELETED 0.640 0. 627 4P BPO a.69o Q.683 0.635 DELETED 0.641 a. 6$ 1 43 840 a.692 0.685 0.636 DELETED 0.643 0. 6$ 2 860 0.694 0.686 0.637 .DELETED 0.645 0.634 eea a.69s a.687 0.6$ 9 DELETED 0.646 0.636 46 9oa a.69r 0.688 0.640 DELETED 0.648 0.638 47 920 0.698 0.689 0.64l DELETFD 0.649 0.639 48 940 a. ron 0.690 0.643 DFLETEO a.6so o.64a 49 960 '0 . 7QI 0. 691. 0.644 DELETED 0.65P 0.64P 50 980 n. 102 a. 692 a.64s DEI I-"'TED a.6sB 0.64$

A30 VAAXABIE TABLE SUHHAAY (CONTXNUED)

BAHPLE DELTA HUH 2 HUH 3 I-IUH I"IUH S I-IUH 6 HUH 7 NUHBEA HXNS FAACTXON FAACTXON FAACTXON FAACTXON FAACTXON FAACTXON SL 1OOO O.TOS 0.693 0.646 DELETED 0.654 0.645

~

Sr2 1030 Q.TQS 0.693 0.647 DELETED 0.656 0.646 53 1040 0.706 0.694 0.649 DELETED 0.657 0.647 54 1060 0.707 n. F>>95 0.651 DEI I= TED 0.658 0. F.49 I.) 5 1OBO 0.708 0.696 0.651 DELE rED 0 659 0.650 56 1100 0.709 0.69r 0.652 DELETLD 0.661 0.65l 57 I 1P.O 0.7LO 0.697 0.654 DELETED 0.662 0.653 58 1140 0.711 0.698 0.655 DELETED 0.663 0.654 59 ll60 0.7L1 0.699 0.656 DELETED 0.664 0.656 60 1180 0. 712 0.700 0.658 DELETED 0.665 0.657 61 1300 0.713 0.7QO 0.657 DELETED 0.666 0.658 6P 1320 0.714 0.701 0. 658 DFLETED 0.66r 0.659 63 1240 0.7L4 O.TOP 0.661 DELETED 0.669 o.660 64 1P6Q 0 . "r15 0.702 0.661 DFI FTED 0.670 0.66'.663 65 1 r'80 0.716 o.703 0.663 DELETED 0.6TL 66 1son 0. r1r 0.703 0.663 DEI ETED 0.67P 0. F64 67 13'>>0 0.717 0.704 0 66'>> DELETED 0.673 0.665 68 1340 0. 718 o. ms a. 665 DI=LLTED 0. 6"f4 0.667 69 1360 0. 71m 0.706 0. 666 DELETED 0.675 0. 66"r 70 L380 0.720 0.706 0. 667 DELFTFD 0.676 0.668 TL 14on O.730 0.707 0,. 668 DELFTED 0.678 0.670 TH 14PO 0. 7P1 0.707 0. DELI=TED 0.679 0.672 73 1440 0.722 0.708 66'.670 DELETED 0.680 0.673 END OF TABLE

VAAXABLI= TAIPEI E SAHPLE DELTA HUH HLW 10 HUHBEA HXHS FAACTXOH Fl)ACTXOH FAACTXOH L 0 0.5'71 0.612 0.5ve

'r 8 2 20 a.596 0.6l7 a.6a4 40 0.601 0.622 0.608 60 a.6o6 0.626 0.613 L) aa 0.6LO 0.629 0.61T 6 100 0. 614 a.633 0.620 7 12n 0.618 Q.686 0.624 8 14n 0.622 0.639 a.627 9 160 0.622 0.642 a.6sa 1a 180 0.628 a.644 a.634 11 2ao 0.681 0.646 0.686 L2 P20 0 . 688 0.648 0.638 18 24a 0.635 0.640 14 26Q 0.68T a.65o 0.641 L5 peo 0.687 a.651 0.648 16 soa a.689 0.652 0.644 17 82a o.64a 0.658 0.645 Le 840 0.641 a.65s a.646 19 860 0. 641 n.654 0.646 2a sea 0.641 0.654 0.647 2l 400 a.642 0.654 0.647 PP 42a 0.642 n.654 0.647 23 44Q 0.642 a.654 0.64T 24 46a 0.642 0.654 0.648 25 480 0.642 0.654 a.648

'26 500 0.642 0.654 0.647 27 520 a.642 0.654 0.647 28 540 0.642 0.654 0.647 29 56a 0.642 0.654 0.647 30 580 0.642 0.654 0.647 81 6oa 0.642 0.654 0.647 8P 620 a.642 a.654 0.647 83 640 0.642 a.658 .0. 647 n.642 n.654 a.647

'4 660 85 680 0.642 Q.654 0.647 86 TOO 0.642 a.654 0.647 87 720 0.642 0.654 0.647 se 740 a.642 a.655 0.648 89 760 0.648 0.655 0.648 40 Tea a.643 0.655 0.649 4l eoa 0.644 0.655 a.*Go 42 820 0.644 0.656 a.65a 43 a4a 0.645 0.657 0.65L e6a 0.646 0.657 0.652 45 aen Q.64T 0.658 0.658 46 900 0.648 0.659 0.654 47 920 0.649 0.660 0.655 48 94a 0.649 0.660 0.656 49 960 '0.650'.651 0.661 0.656 50 sea 0.662 a.658

A32 VAIRXABLE TABLE SUHHAAY (CONTXNUED)

SAHPLE DELTA I-IUH 8 I-IUH 9 I-IUH Lo NUHBEA HXNS FAACTXON FnAC TXON I=AACTX ON xoaa a.653 a.663 0.658 GB Loca 0.653 0.664 0.659

=53 L040 a.65m 0.665 0.660 54 x060 0.655 a.665 0.661 55 lOBO 0.656 0.666 0.66P 56 1 LOO a.657 a.668 a.663 57 s.xpa 0.658 a.668 0.664 58 LL40 0.658 0.669 0.665 59 LL60 a.659 0.670 0.666 6a 1180 0.660 0.67L 0.667 6L 1200 0. 669. 0.672 0.66T 62 l220 a. 66'.663 0.673 0. 669 63 xana 0.675 a.669 64 LP60 0.664 0.675 0.67L 65 1880 0.665 0.676 0.67P 66 'L300 0.666 0.677 0. 6"f3 67 L330 0.66T 0.678 0.674 68 1340 0.668 0.679 0. 6"f5 69 f360 0.670 a.68o 0.6T6 70 .X380 0.670 0.68l 0.677 TL L400 0.67i 0.682 0.678 TP L420 0.673 0.683 0. 6"f9 73 L440 0.674 0.683 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 CQNTAXNMENT HEAN TEMPERATURE CALCULATED FROM VOLUMETRXCALLY MEXGHTED RTD SENSOR XNDXCATZONS.

AVE. PRE PRXMARY CQNTAXNMENT PRE55URE XNDXCATZON.

VAP. PRE CONTAXNMENT VAPOR PRESSURE CALCULATED FROM VQLUHETRXCALLY MEXGHTED RHD SENSOR XNDXCATXONS.

LI=AI< 5 XH SXMPLE TOTAI TXMF LEAKAGE RATE.

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

AXR HASS 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

'I ~

9 ~ 13'. 17 ~ 21- 2S ~ 29-684800. CONTR INMENT R IR MRSSES AIR MASS FITTED AIR NASS- C4 a

684600. 0 CQ I I

C)

C7 5

V3 684400.

CL CO P

O CI 684200.

UJ

'0 684000.

683800

~ 120. 180 ~ 240. 300. 360. 420-,

TINE IN NINUTES

5 ~ 9- 13'- 17- 21 0.5600 COMPUTED LEAK RATES S IttPLE NRSS POINT LEAK RRTE FITTED HRSS POINT LEAK RRTE 0.4800 1 0- CI CP CZ 8 n CI CP O.40OO Cl QJ CL Cl a

CI 0.3200 0-2400 0-1600 240. 300. 360. 420.

60 ~ 120. 180.

TINE IN MINUTES

9 ~

COMPUTED LEAK RRTES w w 13 '7 '1 RELRTI VE TO

~

LIMITS FITTED CLRT MASS POINT LEAKAGE RRTE 2S- 29

'.6400 x x MRXIMVM RCCEPTRBLE v v MINIMUM RCCEPTABLE 5

0. 5600 0 I

I o

EJ C3 CI 0 ~ 4800 IO Cl

't Cl 0.4000 0 3200 0.2400 0 60 ~ 120 180. 240. 300. 360. 420.

TINE IN MINUTES

9- 13 ~ 17 ~ 2S- 29 I

VQLUNETRICRLLY NEIBHTED CONTRINNENT TENPERRTURE '3.>zoo c

~I ID C4 CI CI 8'400 5 I

CJ

~4 5

82.9600 EO la>

Cl lsl Ci O

82.8800 82.8000 82.7200 120- 180 '40. 300- 360- 420-TIME IN MINuTES

~ ~

-I5 ~ 13 ~ 17 ~ 21 ~ 25 ~ 29-

55. 4600 RVERRBE CONTAINMENT PRESSURE CV g

55.4400 0 I4 W

I I

4 Ek QJ 55.4200 (Q

V3 QJ CL 55.4000 55.3800 55.3600 240. 300. 360. 420-0 60 ~ 120. 180.

TIME -IN MINUTES

-I5 ~ 9 ~ 17- 21- 5 ~ 29-0.3920 VOLUNETR I CRLLY WEIGHTED VRPQR PRESSURE CC (Q

0 3900 UJ 40 0.3880 (Q

LLt CL CL a l?'L a

0.3860 CL CC 0.3840 0.3820 240. 300. 360- 420.

60 ~ 120. 180 TINE IN NINUTE5

VAAXABLE TABI E SUHHAAY SAHPLE DELTA AVG. TEH AVC~ . PAE V*P . PAE LEAK SXH LEAK HAS AXA HASS N. HBEA HXNS DEC . I= PSXA PSXA PEA CENT PEA CENT PGUHDS 0 82.909 55.4140 0.$ 834 0.000 a.oao 684282 2 20 82.931 55.4110 a.$ 836 a. 184 O.aaa 684264 40 82.914 ss.4060 0.3840 0.333 0.333 684218 60 82.897 ,55.4010 0.$ 843 0.378 0.389 684174 5 80 82.879 55.3970 0.3846 0.365 0.387 684143 6 100 82.863 55.$ 930 0.$ 850 0.$ 66 0.384 6s41aa 7 120 82.846 55.3890 0.3852 0.. $ 59 0.377 684077 8 140 82.828 55.$ 840 0.3856 0. $ 74 0.$ 81 684033 9 160 82. 817 55.$ 800 0.3859 0.3sa 0.386 683993 10 180 82.802 ss.$ 760 0.$ 862 0.$ 78 0.387 683959 ll r'00 22a 82.783 82.T76 55.3720 55.$ 680 0.3864 0.$ 869 0.370 0.381 0.$ 83 0.385 683930 683884 13 240 82.T60 55.$ 640 0.3811 0.378 0.385 683851 260 82.744 55.3600 0.3875 0.376 a.384 683817 END GF TABLE 1

VAAXABLE TABLE SUHMAAY BANPI E DELTA TEHP l TEHP P. TEHP 3 TEMP TEMP 5 TEMP 6 N'UveEn MXNS DEG. F DEG . I" DEG. r DEG. F DEG. F DI=G . F 1 0 Bl . 170 DELETED Bl.550 Bl 070

. 80.970 DELETED 2 20 81 . 150 DELETED 81.560 81.060 81.03o DELETED 3 40 Sl.160 DELETED Sl.560 81.o70 81.05o DELETED 60 Bl.l40 DELETED 81.5eo 81.10o 81.0eo DELETED 5 80 81.160 DELETED Bl . 560 81.070 81.050 DELETED 6 loo 81 . l70 DELI=TED Sl . 590 ~ 81.070 81.050 DFLETED 7 120 Bl . l90 DELETED 81.560 81.05o'1.aeo Bl.090 DELETED 8 140 81 . l60 DELETED 81.560 81. 100 DFLETI-"D 9 160 81.l60 DELETED Bl . 530 81.0eo Bl . I50 DELETED 10 180 , 81.POO DELI":TED 81.530 81.100 81.150 DFLETrD 1l 200 81.160 DELETED 81.530 Bl.070 81 . l40 DELETED 1 2 220 Bl . 160 DELETED 81 . 570 81.l30 Bl. 160 DELETED 13 240 81.l90 DELETED 81 . 570 81.080 81. 170 DELETED P60 81.130 DELETED 81 . 560 81.070 81 . l60 DELETFD END GF TABLE

A44 VAAXABLE TABLE SLJMMAAY SAMPLE DELTA TEMP 7 TEMP 8 TEMP 9 TEMP 10 TEMP 11 TEMP 12 NQMBEV HXNS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 1 a Bl.640 82.ooa 83.230 83.380 83.l20 83.420 te 2 20 81.640 BL.990 83.200 83.350 83.a9o 83.410 40 Bl.640 81.990 83.180 83.340 BS.OTO 83.390 60 e1.65a 81.@90 83.150 83.320 83.a4o 83.360 5 ea 81.650 e2.aao 83.l40 83.290 83.020 83.350 6 100 e1.65a 81.990 BS.L10 83.270 .83.000 83.320 7 L P.O 81.66a 81. ~>90 83.090 83.250 82.970 83.3LO 8 140 81.660 ep.oia 83.070 83.230 82.960 83.280 9 160 81.660 82.nio 83.050 83.220 82.940 BS.P60 10 180 81.'660 82.aoo 83.040 83.190 BP..920 83.230 11 200 81.680 Bl . 990 83. 010 83.170 82. 'POO 83.240 12 220 81 . 690 82.000 82.990 83.150 82.900 83.190 13 240 81.690 81.990 82.980 83.140 82.860 83.L90 14 260 81.700 BL.990 82.970 83.120 82.8TO 83.170 END OF TABLE

VAAXABLE TABLE SUHHAAY SAHPLE DELTA TEHP 13 TEHP 14 TEHP L5 TEHP 16 TEHP 17 TEHP 18 bAJHBEA HXNS DEG. F DLG. F DEG. F DEG. F DEG. F DI=G . F L 0 83.310 83 560 83.410 81.85a DELETED 83 . SPO 81.810 83.290 "3 20 40 83.300 83.P70 83 83 550 530 83.380 83.350 81.790 DFLETED DELETED 83.P70 60 83.240 83 500 83.330 81.770 DELETED 83.'230 r> 80 83.220 $3 490 83.310 81.750 DELETED 83.230 6 100 83.220 83 460 Bs.sao 81.730 DELETED 83.200 7 120 83.180 83 420 83.2'70 81 . 710 DELETED 83.170 8 140 83.160 83 43a 83.P50 81.650 DELETED 83.L60 CP 160 83.130 83 400 83.240 81.640 DELETED 83.140 1a 180 83.130 83 4ao 83.230 BL.600 DELETED 83.130 L1 200 BS.L20 83 360 83.2ao 81.590 DELETED 83.LOO 12 2PO 83.080 83 370 83.L70 81.570 DELFTED 83.100 LS 240 83.080 83 330 83.16a Bl . 550 DELETED 83.070 L4 260 83.050 83 300 83.150 81.540 DELETFD 83.050 END OF TABLE

VAAXABLE TABLE SUHHAAY SAMPLE DELTA TEHP l9 TEMP 20 TEMP 2'L TEMP 22 TEMP 23 TEMP 24 CJHBEIR AXES DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 0 83.$ 10 83.640 83.270 83.430 84.25a 83.990

'0 ~

2 20 Bs.sea 83.600 BB.P40 83.42a 84.2PO 83.980 40 e3.26a 83.590 83.230 83.400 84.2oa 83.970 60 BB.PBO 83.52a 83.210 83.390 84.LBO 83.950 C) 80 BB.PBO 83.540 83. 9.90 83.340 84.x50 83.930 6 LOO Bs.l90 83.5'lo 83.170 83.360 84.L50 83.890 7 l20 BB.LBO 83.510 83.l.50 BB.BLO 84.sea 83.890 8 'L40 BB.L60 83.470 83.l40 Bs.sao 84.100 83.860 9 160 BB.L50 83.500 83. XLO 83.290 84.090 83.850 aa BS.120 83.430 Bs.a9o BS.P90 84.060 83. 1840 ll L4 LBO 200 220 BB.LOO 83.090 8$ .4PO 83.420 83.080 83.05a 83.2sa BS.PBO 84.o4a 84.aso Bs.eao 8$ .800 ls 240 es.o6a 83.360 Bs.o5a 83.230 84.020 83.770 4260 Bs.a4o 83.350 Bs.asa 83. Pia 84.000 83.770 EHD OF TABLE

VAAXABLE TABLE SUHHAAY SAMPLE DELTA TEMP P5 TEMP 26 TEMP P7 38 TEMP 29 TEMP 30 l4JHIBEA HXNS DEG. F DEG. F DFG. F DEG. F DFG. F DEG. F 1 0 83.660 83.86o 84.270 83.890 83.0PO DELETED r 30 83.660 83.870 84.340 83.890 82.970 DELETI=D 3 4a 83.630 83.840 84.210 83.860 82. 750 DELETED 60 83.610 83.810 84.190 83.860 82.930 DELETED 5 80 83.600 ,83.790 84.l70 83.840 83.900 DELETED 6 100 83.560 83.740 84.150 83.820 82.890 DELETFD 7 130 83.560 83.670 84.180 8$ . Blo 82.860 DELETED 8 140 83.53a 83. 6'r20 84.l10 83.790 SP.830 DELF. TEI3 CP l60 83.520 83.7oa e4.aeo 83.770 BB.BPO DELETED 10 180 83.510 83.630 84.050 83.740 BB.BLO DELETED ll

'1P 200 LPO 83.490 83.460 8$ .550 83.610 e4.o4a 84.030 83.730 83.710 82.790 BP.750 DELETED DELETED l3 240 83.450 83.530 84.010 83.700 82.740 DELETED 14 260 83.430 83.480 83.980 83.680 82.720 DELETED END OF TABLE

VAAXABLE TABLF SUHNAAY SAMPLE DELTA TEMP 31 TEMP 32 TEMP 33 TEMP 34 TEMP 35 TEMP 36 nfuvBEn HXNS DEG. F OEG. F DEG. F DEG. F DFG . F OEG. F L 0 82 820 83.2an 83.150 83.490 83. 1aa 78.L70 P 20 BP 770 83.180 83. 120 83.460 83. Ova 78.120 40 82 760 BS.L50 83.LOO 83.440 83.050 78.LOO 60 S2 730 83.130 83.08a 83.410 83.030 78.080 80 82 720 83.LOO 83.050 83.380 83.ann 78.040 6 100 BP 690 83.aea 83.0PO 83.370 82.980 78.020 7 120 82 670 83.n6a 83.a10 83.350 SP 250 77. 9)0 8 140 Btg 640 83.040 BP.'990 83.340 82.94a 77.950 9 160 82 630 83.01Q 82.960 83.3nn 82. 910 77.920 10 18a 82 590 82.990 82.940 83.P90 82.9aa 77.900 L1 2oa 82 590 82.970 82.920 83.270 82.880 77.870 1P 220 SP 570 82.950 82.920 83.240 82.870 77.850 L3 2<0 82 540 82.940 82.900 83.250 82.850 77.830 260 82 550 82.940 82.890 83. P10 82.830 77.810 END GF TABLE

VARXASI E TABLE SUVVARV SQNPLE DELT~ TEMP $7 TEMP 3S TEMP $9 TED< wa PRES l HUH 1 NUHI3ER RXNS DEG. F DEG. F DEG. F DEG. F PSXA FIQACTXQN 1 a 83. 190 82.870 82 570 82.950 55.414 DELETED p ~

2 20 83.160 82.840 82.560 82.91a 55.4l1 DELETED 3 ga 8$ .1~0 82.810 82.520 82.880 55.406 DELETED 60 83.120 82.790 82.490 82.860 55.401. DELETED 5 80 83.090 82.760 82.470 82.8<0 55.$ 97 DELETED 6 100 8$ .070 82. 750 82.450 82.810 55.$ 93 DELETFD 7 120 83.040 82.730 82.420 82.790 55.389 DELFTED 8 I40 83.030 82.700 82.400 82.770 55. $ 81 DELETFD cp l60 8$ .0la .82.680 ,82.380 82.760 55.$ 80 DELFTED 1a l80 82.990 82.670 82.360 82.740 55.$ 76 DELETI=D l1 2aa 82.970 82.660 82.$ 50 82.720 55.$ 72 DELETED 12 2PO 82.950 82.63a 82.330 82.700 55.$ 68 DELETED l3 2ea 82.940 82.61a 82.$ 20 82.68a 55.$ 64 DELETED 260 82.920 82.590 82.300 82.670 55.$ 60 DELETED END QF TABLE

A5a VARXABLE TABLE

SUMMARY

SAMPLE DELTA I.IUM 2 HUM 3 I-IUM 4 I-IUM 5 HUM 6 HUM 7 HSMBER MXHS FRAc rxoH FRACTXDH FRACTXQH FRAc rxoH FRACTXI3H FRACTXOH 1 a 0.723 0.7a9 0.673 DELFTED 0.683 0.675

'J ~

2 20 a.723 0. 109 0.673 DELETFD 0.683 a.676 40 0.724 0.710 0.674 DELETED 0.685 0.677 60 a.725 0. 711 a.676 DELETED 0.686 0.678 5 80 0.725 0. 711 0.676 DELETED 0.687 0.680 6 1aa a.726 0. 712 a.678 DELFTED 0.688 0.681 7 120 0.7P6 0.712 0.678 DELETED 0.690 0.682 8 140 0.727 a.712 0.680 DELLTED a.690 0.683 9 160 0.728 0.713 a. 681 DELETED 0.691 0.680 1a 180 0.728 0.713 a. 68P oELErEo 0.692 0.685 11 200 0.729 0. 714 0.683 DEI ETED 0.693 a.686 1P 220 0.729 0. 714 a.684 DELE rED 0.694 a.687 13 240 0.730 0.715 0.685 DELETED 0.695 0.688 260 0.730 0.715 a.686 DELETED 0.696 a.689 EHD QF TABLE,,

VAAXABLE TABLE 5UHHAAY 5ANPLE DELTA HUH 8 HUM 9 HUH 10 HUHIBEA XXN5 FAACTXON FAACTXON FAACTXON 0 0.676 0.686 0.682 H a 0.677 0.687 0.683 i~

40 0.678 0.688 0.684 60 0.679 0.689 0.685 5 80 0.6sa 0.690 0.686 6 100 0. 68'I 0.691 0.687 7 J.BO 0.683 . 0.692 0.688 8 L40 0.683 0.693 0.690 C) 160 0.684 0.693 0.690 xa 180 . 0.685 0.694 0.691 r'00 0.686 0.695 0.6vz 12 330 a.687 0.697 0.693 J.3 240 a.688 0. 6)7 0.694 360 a.689 0. 698 0.695 END OF TABLE

APPENDIX B.

RTD AND RHD VOLUMETRIC WEIGHTING FACTORS

ATD VOLUHETAXC MEXGHTXHG FACTOA5 ATD SEVSOA VOLUME NUBBER FAACTXON

'L 0.03561.07 2 DELETED 8 0.08561.07 0.0856107 5 0.0856107 6 DELETED 7 0.0356107 8 0.03561.07 7 0.0267850 1.0 0.0267850 L1. 0.0267850 12 0.0267850 l3 0.0267850 0.02<0870 L5 0.0240870 l6 0.0240870 1.7 0.0240370 L8 0.0240370 l9 0.0240370 20 0.0240370 2L o.o24a87o P2 0.02<0870 28 0.0240370 0.02291.<0 25 DELETED 26 0.02291.~0 27 0.02291.<0 28 0 . 0229140 2P 0.02291.<0 80 0. 0229IWO SL 0.0229x40 82 0.02291.<o 33 o.a2291,4o 84 0.02291.no 35 0.02291.40 36 0.02291.40 87 0.02291.<0 38 0.08227<0 89 0.0822740 40 a.a32274o

e s AHD VQLUHETAXC MEXGIHTXNG FACTQAS nHD SENSQA VQLUNE NUHBEIR FIZACTXQN DELETED 2 0. 1100025 8 0. 1100025 O.IP00858 C'

DELETED 0.1800858 7 0.1200858 8 0.18'ss9180 9 0.189e180 1Q 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 As found As left tion Date SCCH

'escri SCCH Remarks Haintenance Hatch Casket 9-5-79 4.6 4.6 Opened for containment inspec-Interspace tion after Hurricane David.

9-30-79 8.36 8.36 Retest following closure 10"13-79 0.9 0.9 Door opened.

5-5-80 10. 1 10.1 Hatch opened for Reactor Coolant Pump Seal.

6-21-80 8. 8.6 Hatch opened for Reactor Coolant 6'0,1 Pump repair.

6-24-80 10.1 ~ Hatch opened for Reactor Coolant Pump Seal repairs.

5-18-82 100 Hatch opened for Steam Generator inspection prior to Node 4.

5-23-82 100 Opened for Reactor Coolant Pump Seal Repair - retest prior to Hode 4 ~

Personnel Air Lock 11-15-79 1559 1559 Personnel sir lock seals are tested by automatic tester 5-6-80 77688 33 at other than 6~anth intervals.

Alarms on testers are set at 11-4-80 2511 2511 100 sccm per door.

5-26-81 3023 3023 12-7-81 12112 12112 5-27-82 2270 2270 11-16-82 1157 1157

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

REFUELING OUTAGE TYPE B&C TESTING SINCE LAST REPORT As As As As As As Penetration Found Left Found Left Found Left No. Service Valve Test Date SCCH SCCH Date SCCM SCCM Date SCCM SCCH Remarks Main Steam Bellows Tap I I 3-3-83 0 I 9-22-81 0 0 I 3-17-80 77 77 I I I Tap 2 I 3-3-83 0 I 9-22-81 0 0 I 3-17-80 13 13

.I Hain Steam Bellows Tap I I. P-3-83 10 10 9-22-81 0 0 3-17-80 20 20 Tap 2 3"3"83 0 0 9-22-81 0 0 I 3-17-80 15 15 Feedwater Bellows Tap 1 B 3-3"83 10 10 I 9-22-81 0 0 3-17-80 18 18 Tap 2 B ~

3-3-83 0 0 9-22-81 0 0 3-17 "80 17 17 Peedwater Bellows Tap 1 B I 3-3-83 10 10 92281 ~ 0 I 3-17-80 29 29 I I Tap 2 B I 3"3-83 0 0 I 9-22-81 0 I 3-17-80 13 13 I I I 25 Fuel Transfer Tap I B I 3-14-83 100 100 I 11-11-81 0 0 I 3-17-80 10 10 Bellows Tap 2 I See Note below. I 9-22-81 0 0 I 3-18-83 17 17 I I I Maintenance Hatch ' 4-26-83 Gasket Interspace B 0 0 I 11-21-81 50 so I s-s-80 10.1 10.1 I I Fuel Transfer Tube Flange 0 Ring B See Remarks. I 11-11-81 0 I 4-22-80 6.9 6.9 .IWill be tested Iapprox Sept 83.

ISee III-E.

Personnel L'ock Between Doors 4-24-83 42>000 5600 12-7-81 12,000 12>000 5-6-80 77660 4.8 Escape Hatch Between Doors B I 4-24-83 100 100 I 11-17-81 4800 4800 I 5-2-80 8714.61 8714.6 I I I A-1 thru Electrical Penetra- NA B. I 3-2-83 0 . 0 I 9-15-81 0 0 I 3-20-80 0 0 E-IO tions sa>>TYPE TEST 1983 As found 42,220 I 1981 As found 16,850 1980 As found 86>603.61 I ***1983 total I does not 1983 As left 5,820 I 1981 As left 16,850 1980 As left 8>948.41 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.

material its design rating is 16.0 psi. A 'Technical Specification change request is being prepared.

Although of the same

REFUELING OUTAGE TYPE B&C TESTING SINCE LAST REPORT As As As As As As Penetration Found Left Found Left Found Left No. Service Valve Test Date SCCH SCCM Date SCCH SCCH Date SCCH SCCH Renarks Prinary Makeup I-V-15328 C 3-17-83 280 280 9-13-81 250 250 3-19-80 1911 1911 Bypass Leakage Mater 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 & C 2-2j-83 100 100 9-12"81 2400 460 3-14-80 53 53 Bypass Leakage I-V-18796 I-V-18797 2-27-83 200 200 9-12-81 0 0 3-14-80 6 Bypass Leakage I"V-1879 2-27.-83 160 160 9-12-81 0 0 3-14-80 0 Bypass Leakage Instrunent Air I-V-18195 4"7"83 1300 . 1300 9-13-81 510 330 3-19-80 342 . 342 Bypass Leakage I-HV-18-1 & 4-7-83 1606 1606 9-13-81 1100 400 3-19-80 195 195 Bypass Leakage I-V-18193 10 Containnent Purge I-FCV-25-4 & 4-13-83 62)432 29)186 9-21-81 2000 2000 4-17-80 13.7 13.7 I-FCV-25-5 Containnent Purge I-FCV 25-2 & 3-9-83 2 ' x 106

• 400 9-21-81 20 20 4-8-80 8.9 8.9 *Report Follows I-FCV-25-3 14 Nitrogen Supply V&779 3-24i83 9-18-81 12 12 3-18-80 0 Bypass Leakage V-6741 3"24"83 20 20 9-18-81 0 0 3-18-80 0 Bypass Leakage

.23 CCW to RCP I-HCV-14-1 ' 4"1-83

& 7 10 10 11-9-81 300 300 3-26-80 1 Bypass Leakage 24 CCN fron RCP I-HCV-14-2 & 6 C 4"1-83. 190 190 11-9-81 0 0 3-26-80 35 35 Bypass Leakage 26 Letdown Line V-2515 4-5-83 9-17-81 0 0 3"22-80 199 199 Bypass Leakage V-2516 100 100 9-17-81 0 0 3-22-80 116 116 Bypass Leakage 4-5-83'-11-83 Sit Sample Line I-FCV&3-IE 100 100 9-13-81 0 0 3-28-80 6 Bypass Leakage I-FCV&3-IF 3"11"83 100 9-13-81 0 0 3"28-80 3 Bypass Leakage 28B RCS Not Leg Sanple V-5200 C 4-25"83 100 100 9-16-81 0 3-21-80 14 Bypass Leakage V-5203 4-25-83 100 100 9-16"81 0 3-21-80 14 14 Bypass Leakage

REFUELING OUTAGE TYPE B&C 'iESTlNG S1NCE LAST REPORT As As As As As As Penetration Left No. Service Valve Test 'ate Found SCCH SCCH Date Found SCCH Left SCQl Date Found SCCH Lef t SCCH 'emarks 29A Pressuriser Surge V-5201 C 4-25-83 100 100 9-16-81 100 100 3-21-80 1 7.4 Bypass Leakage Line Sample 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 C 4-25-83 100 100 9-16-81 100 100 3.-21-80 401 401 Bypass Leakage Space Sample 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 C 3-12-83 100 100 9-18-81 0 0 3-26-80 24 24 Bypass Leakage Header 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 & C 3-11-83 1300 1300 10-8-81 0 0 4-1-80 144 144 Bypass Leakage V-3463 Rx Cavity Sump Pump I-V-LCV-07-11A & C 3-24-83 1050 1050 10-8-81 100 100 3-28-80 1157 1157 Bypass Leakage Die cha rge I-V-LCV-07-11B 43 Rx Drain Tank Pump V&301 C 4-23-83 550 550 11-15-81 100 3-31-80 100 88 1139 Bypass Leakage Section V&302 C 4-23-83 780 780 11-15-81 1400 1400 3-31-80 3500 1095.3 Bypass Leakage 44 RCP Controlled I-SE-01-1 C 3-14-83 0 0 9-28-81 0 0 3-25-80 17 17 Bleedoff 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 I-VW7189 & C 3-5-83 200 200 10-21-81 100 100 3-24-80 24 24 Bypass Leakage Purification I-VW7206 Refueling Cavity I-V-07188 & C 3-5-83 0 0 10-21-81 300 300 3-24-80 70 70 Bypass Leakage Purification I"V-07170

REFUELINC OUTAGE TYPE B&C TESTING SINCE LAST hLPORT As As As As As As Penetration Found Left Found Left Found Left No. Service Valve 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 I-FSE-27-2 C 3-7-83 0 0 9-14-81 0 0 3-20-80 1 1 Bypass Leakage I-FSE-27-3 C . 3-7-83 0 0 9-14-81 0 0 3-20-80 3 3 Bypass Leakage I-FSE-27-4 C 3-7-83 0 0 9-14-81 0 0 3-20-80 3 3 , Bypass Leakage I-FSE-27-08 C 3-7-83 400 400 9-14-81 0 0 3-20-80 1 1 Bypass Leakage 48C H2 Sample Return I-V-27101 C 3-30-83 890 890 9-14-81 100 100 3-20-80 8736 24.7 Bypass Leakage from Analyzer A 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 C , 3-30-83 3200 1300 9-14-81 100 100 3-20-80 20 20 Bypass Leakage from Analyzer B I-FSE-27-10 C 4-5-83 0 0 9-14-81 0 0 3-20-80 0 0 Bypass Leakage 51C H2 Sampling to I-FSE-27-5 C . 3-7-83 100 100 9-14-81 0 0 3-20-80 0 0 Bypass Leakage Analyzer B I-FSE-27-6 C 3 7 83 100 100 9-14 81 0 0 3-20-80 0 0 Bypass Leakage I-FSE-27-7 C 3-7"83 100 100 9-14-81 0 0 3-20-80 1 1 Bypass Leakage I-FSE-27-9 C 3 7 83 640 640 9-14-81 0 0 3"20-80 3 3 Bypass Leakage 52A Particulate Sample I-FCV-26-1 C 3"12-83 130 130 9-23-81 100 100 3-26-80 88 88 Bypass Leakage to Rad Honitor I-FCV-26-2 C 3-12-83 130 130 9-23-81 150 150 3-26-80 770 770 Bypass Leakage 528 Iodine Sample to I-FCV-26-3 C 3-12-83 100 100 9-23-81 100 100 3-26-80 12 12 Bypass Leakage Rad Monitor 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 As As As As As As Penetration Found Left Found Left Found Left No. Service Valve Test Date SCCH SCCH Date SCCH SCCM Date SCCH SCCM Remarks 52C Radiation Monitor I-FCV-26-5 C 3-17-83 510 510 9-23 81 400 400 3-26-80 114 114 Bypass Leakage Return I-FCV-26-6 C 3-17-83 100 100 9-23-81 3400 100 3-26-80 2364 2364 Bypass Leakage 52D ILRT Controlled I-V-00140 & C 5-.10-83 2300 2300 9-14-81 2500 2500 3-19-80 1 1 Bypass Leakage Leakage I"V-00143 IWT Pressure I-V&0139 & C 5-10-83 0 0 9v14-81 100 100 3-19-80 82 82 Bypass Leakage Sensing Station I-V-00144 54 ILRT Pressurization I-V&0101 C 4-21-83 5700 3500 9-14-81 2800 2800 3-19-80 7142 1500 Bypass Leakage Station 6-9-83 700 700 56 N2 Purge Hakeup I-V-25-11 & C 4-23-83 142 142 9-14-81 280 280 3-25-80 198 198 Bypass Leakage I-V-25-12 I 57 H2 Purge to H2 I-V-25-13 & C 3"10-83 1000 1000 9-14-81 330 330 3-24-80 268 268 Bypass Leakage Purge Filter I-V-25-14 58 H2 Purge Filter I-V-25-15 & C 3-10-83 1000 1000 9-14-81 550 550 3-24-80 465 465 Bypass Leakage Bypass I-V-25-16 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 5 5 I-FCV-25-8 C 4"14-83 1600 1600 10-2-81 340 340 3-24-80 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 (From page C4 and above) 1983 As Left 54,024 1981 As Left 30,952 1980 As Left 22,156.41

• "+BYPASS LEAKAGE TOTALS 1983 As Found 22,818 1981 As found 17,849 1980 As Found 28,707 I

1983 As Left 15,918 1981 As Left 11,903 1980 As Left 13,006.4 NOTES: Total bypass leakage technical specification acceptance criteria is 245,153 sccm.

Total band C leakage technical specification acceptance criteria is 544,786 sccm.

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

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 INITIALLY SYSTEM 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