ML19270H248
| ML19270H248 | |
| Person / Time | |
|---|---|
| Site: | Turkey Point  |
| Issue date: | 03/20/1979 |
| From: | FLORIDA POWER & LIGHT CO. |
| To: | |
| Shared Package | |
| ML17338A781 | List: |
| References | |
| NUDOCS 7906250350 | |
| Download: ML19270H248 (176) | |
Text
/
Florida Power and Light Ceapany Turkey Point Plant Unit No. 3 Docket Number 50-250 REACTOR CONTAIhTENT BUILDING IhTEGRATED LEAKAGE RATE TEST MARCH 20, 1979 f
Submitted to The United States Nuclear Regulatory Commission Pursuant to Facility Operating License No. DPR-31 2310 002 E
s qc % 250350
f(
TABLE OF CONTENTS I.
INTRODUCTION II.
TEST SYNOPSIS III. TEST DATA SUMFfARY A.
Plant Info rma tion B.
Technical Data C.
Test Results - Type A Test D.
Test Results - Type B and C Tests E.
Integrated Leakage Rate Measurement System F.
Permanent Plant Instrumentation Ised during Test G.
Information Retained at Plant IV.
ANALYSIS AND INTERPRETATION AP P END IX A.
Failed Test Report - Type A Test V.
OPERATING PROCEDURE 13100.1 #3 ILRT MASTER COPY 2340 003
I.
INTRODUCTION The reactor containment building Integrated Leakage Rate, Type A, Test, is performed to demonstrate that leakage through the primary reactor contain-ment and systems and components penetrating primary containment does not exceed the allowable leakage rate specified in the Plant Technical Specifi-c a t io ns.
The successful periodic Type A and supplemental verification tests were performed according to the requirements of the Turkey Point Plant, Unit 3, Technical Specifications and 10CFR50, Appendix J.
The Turkey Point Plant Type A test method is the absolute method described in ANSI N45.4-1972,
" Leakage Rate Testing of Containment Structures for Nuclent Reactors" and ANSI N274, " Containment System Leakage Testing Requirements", Draf t No. 2, Rev. 3 - November 15, 1978.
The leakage rate was calculated using formulas f rom ANSI N45.4-1972 and BN-TOP-1, Rev. 1.
" Testing Criteria for Integrated Leakage Rate Testing of Primary Containment Structures f or Nuclear Power Plants" (Total-Time) and ANSI N274 (Mass-Point). Type A and verification tes t durations were according to the criteria of BN-TOP-1.
The test results are reported in accordance with the requirements of 10CFR50, Appendix J,Section V.B.3.
II.
TEST SYNOPSIS After initial pressurization to test pressure, a leak was discovered through the 3A Steam Generator steam line vent valve.
The containment was depres-surized to repair the valve, then the containment was repressurized to test pressure. A leak was discovered at the Personnel Airlock equalizing valve shaf t seal (inner door). This leak was repaired, and no other leak paths were discovered.
The Type A test was started at 2245 on 3/19/79. At 1045 on 3/20/79, the Type A test was terminated with a calculated leakage rate of 0.034% per day, with an upper 95% confidence limit of 0.060% per day (Total-Time Method) and 0.031% per day, with an upper 95% confidence limit of 0.033%
per day (Mass-Point Method).
At 1245 on 3/20/79 a verification flow rate of 0.103% per day was established. The verification test was successfully completed at 1815 on 3/20/79.
2Ti]
004 1
III. TEST DATA
SUMMARY
A.
Plant In f o rma tion Owner Florida Power and Light Company Plant Turkey Point Plant, Unit 3 Location Homestead, Florida Containment Type Prestressed, post-tensioned concrete NSSS Supplier, Type Westinghouse, PWR Date Test Completed March 20, 1979 B.
Technical Data 1.
Containment Net Free Air Volume 1,5 50,000 cu. ft.
2.
Design Pressure 50 psig 3.
Design Temperature 276*F 4
Calculated Peak Accident Pressure, Pa 50 psig 5.
Cont ainment ILRT Average Temperature Limits 80 - 90
- F 6.
Calculated Peak Accident Temperature 283*F C.
Test Results - Type A Test 1.
Test Method Absolute 2.
Data Analysis Techniques Mass Point (per ANSI N274) and Total-Time (per BN-TOP-1) 3.
Test Pressure 25 psig 4.
Maximum Allowable Leakage Rate, L
0.1029% / day t
5.
75% of L 0.0772%/ day t
6.
Integrated Leakage Rate Test Leakage Rate, %/dav Results From Regres-At Upper 95%
sion Line Conf idence (Ltm)
Limit a.
Mass point analysis 0.031 0.033 b.
Total-Time analysis 0.034 0.060 7.
Verification Test Imposed Leakage Rate, L, %/ day 0.10 3 g
9,r c)aJ, 003 e
2
8.
Verification Test Results Leakage Rate, % /dav a.
Mass Point Analysis 0.117 b.
Total-Time Analysis 0.1 18 9.
Verification Test Limits Test Limits, %/ day a.
Mass Point Analysis 1)
Upper Limit (L +L
+0.25L,)
0.160 g
2)
Lower Limit (L +L
-0.25L )
0.108 o tm a
b.
Total-fine Analysis 1)
Upper Limit (L +L
+0.25L )
0.163 g
tm a
2)
Lower Limit (L +L
-0.25L )
0.111 g
a 10.
Report Printouts The Report Printouts of the Type A and verification test calculations are provided for the Mass Point and Total-Time Analyses.
(Tables 2 through 7) Stabilization data is also provided.
(Table 9)
D.
Test Results - Type B and C Tests Test results for local leak rate tests performed since the previous 1976 Integrated Leak Rate Test are provided.
(Table 9)
E.
Integrated Leakage Rate Measurement System 1.
Absolute Pressure (1 channel)
Range:
0-100,000 counts Accuracy:
0.015% of reading Resolution:
0.001% F.S.
Range:
0-49 psi Texas Instrument Model 145-02 Precision Pressure Instrument No. 1940 Bourdon Capsule #4433 Calibration Date:
12-15-78 Texas Instrument Model 145-02 Precision Pressure Instrument No. 1941 Bourdon Capsule #4434 Calibration Date:
12-15-78 2340 006 3
2.
Drybulb Temperature (22 sensors)
Resistance Temperature Detectors - Leeds and Northrup Thermohn Model 818 7-10-S, 3-lead, 100-ohm coppe r and Numatron numeric display model 900-9999-9999-1-5.
Limit of error:
0.2*F S tatic resistance:
100 ohms Read out - Leeds & Northrup Numatron Calibration Date:
2-14-79 Calibration Standard Thermometer -
Taylor Total Immersion Thermometers IS*F to 89'F
.20*F D ivisions S/N 63F3484 Calibration Date:
12-18-78 S/N 63F3640 calibration Date:
12-18-78 RTD - Leeds & Northrup 100 ohn copper thermohms Catalog 8187-10-S Catalog No. 300-9999-9999-1-S Calibration Date:
3-10-79 3.
Dewpoint Temperature (4 sensors)
Dewpoint Temperature Sys tems - EG& i Inc. Dewpoint Hygrometer with 4 sensors.
Accuracy:
0.54*F Sens itivity :
0.18'F Read out - Keithley Model 173 Auto Range DVM Calibration Date:
3-16-79 System Model 660-C1 Sensor Model 660-S2 Calibration Date S/N 391 S/N 423 12-14-78 S/N 400 S/N 378 12-14-78 S/N 405 S/N 406 12-20-78 S/N 397 S/N 484 3-14 -7 9 4.
Verification Flow (1 channel)
Flowmeter-Brooks Hi-accuracy full view rotameter, Model 1110.
Range:
1.24 - 12.4 scfm Accuracy:
+0.1 scfm Repeatab ility :
0.01 scfm Calibration date:
1-12-79 j ;q q 007 e
o 4
5.
Gauge Pressure (1 channel) - Not used directly in calculations.
9 Wallace & Tiernan Model 61A-1A-0100 Range:
0-100 psig Accuracy:
0.1% F.S.
Sensitivity:
0.01% F.S.
Calibration Date:
3-13-79 6.
Overall Instrumentation Selection Guideline (ISG) Value (from ANSI N274) based on ILRT instrumentation and an eleven hour minimum test duration:
+0.0257%/ day 7.
Drybulb and Dewpoint Temperature Sensor Volume Fractions -
See Table 1.
F.
Permanent Plant Instrumentation Used During Test None.
G.
Information Retained at Plant The following information shall be retained by the owner and shall be made available for review at the Facility:
c(
l.
Access Procedure Included in test procedure Section V.
2.
Containment Penetrations A listing of all containment pene'. rations, including the total number of like penetrations, penetration size and function.
3.
Operating Instrument Status No nornal operating instrumentation was used for the leakage rate test.
4.
Systems Status (at time of test)
A system line-up, showing required valve positions and status of piping systems, is contained in Section V, OP 13100.1.
5.
Event Log A continuous, sequential log of events from initial survey of containment to the Post Containment ILRT Final Inspection.
2343 008 5
6.
Instrwnentation Validation ci Documentation o'f instrumentation calibrations and standards.
Included with the doeur.wntation is an error analysis of instrumentation.
7.
Temperature Stabilization Data to verify temperature stabilization criteria as estab-lished by test procedure is contained in Table 8.
8.
Test Procedure The working copy of test procedure including
(
signature sign-off of procedural steps, is contained in Section V OP 13100.1.
9.
Local Leak Rate Tests The procedure and all data that verifies completion.of penetrations and valve testing (B&C type tests) including as found leak rates - corrective action taken, and final leak rate.
10.
Integrated Leak Rate Data r
[,
Computer printouts, manual data accumulation along with
^
summary description of computer program, 11.
Quality Assurance The Quality Assurance audit plan and checklist that was used to monitor ILRT with proper sign-of fs.is contained in Section V, OP 13100.1.
12.
Test Exceptions A listing of all test exceptions including changes in con-tainment system boundaries instituted by licensee to con-clude successful testing.is contained in Section V, OP 13100.1.
13.
Instrumentation Malfunctions There was no sensor raalfunction, repairs, or methods used to redistribute volume fractions to operating instru-mentation.
14.
Confidence Limits A review of confidence limits of test results with accom-panying computer printouts where applicable.
2340 009 6
[
15.
Verification Leak Rates Descriptions of methods used, superimposed leakage,.ith calibration information on totalizers and flowmeters along with calculations that were used to measure the verification leakage rate is contained in Section V, OP 13100.1 16.
Graohs Plots presenting data obtained during the test.
17.
P&ID's TheP&ID'sofsystemsreadilyavailable.
IV.
ANALYSIS AND INTERPRETATION The Integrated Leakage Rate Test results at the upper 95% confidence level, L
, 0.033%/ day (Mass Point analysis) and 0.060 (Total Time analysis), satisfy tne acceptance criteria. The acceptance criterion is L
< 0.75L = 0.0772%/
day @ P > 25 psig.
t.
234]
010 k
7
TABLE 1 Dewpoint #
Volume Fraction 1.
0.268 2.
0.267 3.
0.267 4.
0.198 1.000 RTD #
1.
0.1600 2.
0.3620 3.
0.0200 4.
0.0200 5.
0.0200 6.
0.0200 7.
0.0200 8.
0.0200 9.
0.0165 10.
0.0165 11.
0.0165 12.
0.0165 13.
0.0165 14.
0.0165 15.
0.0165 16.
0.0165 17.
0.0165 18.
0.0165 19.
0.0165 20.
0.0165 21.
0.1600 1.0000 2 ;hh b
TABLE 2
- UMMAGY DATA TUCt EY POIr4T Ur4 T T 3 ILPT 1556000.6o 0.102 VOL
=
9LMAK
=
4
+
TIME DATE TEr1P PPE350PE 2245 319 538.888 41.3656 2300 319 538.877 41.9e47 2315 319 538.868 41.9646 2330 319 538.851 41.9635 2345 319 538.848 41.9625 0
320 538.948 41.9619 15 320 538.8?9 41.9618 30 320 539.928 41.9665 45
?20 538.823 41.9602 100 320 535.814 41.9592 115 320 538.806 41.9584 130 020 538.901 41.9578 145 320 5?8.796 41.G569 200 320 538.785 41.9568 215 320 538.787 41.9558 230 326 538.781 41.9553 245 320 538.776 41.9555 300 320 538.??O 41.9544 315 320 578.764 41.9532 330 320 538.758 41.9528 345 320 538.748 41.9524 400 320 538.746 41.9517 415 320 538.737 41.3510 430 320 538.738 41.9510 445 320 538.731 41.9507 500 320 530.730 41.9495 515 320 538.723 41.9492 53n 320 538.716 41.9490 545 320 538.707 41.9483 600 320 538.707 41.9474 615 320 538.704 41.9475 630 320 538.695 41.9467 645 320 528.695 41.9462 700 320 538.690 41.9458 715 320 538.687 41.9456 730
?20 538.679 41.9450 745 320 338.679 41.9444 900 320
~i38. 675 41.9446 815 320 138.667 41.9436 830 320 538.665 41.9433 845 320 538.660 41.9429 900 320 538.658 41.9431 915 320 538.656 41.4417 930 320 538.651 41.9420 9'4f) 012 945 320 538.650 41.9419 1000 320 538.645 41.9415 1015 320 538.650 41.9407 1030 320 538.649 41.9412 1045 320 538.651 41.9408 q
O O
- 0. 0
- 0. 0 i
1 t
TABLE 3 TUPVEY POlr4T Ur41 T 3 ILPT TPEriD PEPOPT LEAKAGE PATE: ibiEIGHT PEPCEr4T DAY' T O T A L - T I M E At4 A L'.*: I I TIME Ar4D DATE AT ITAET OF TECT:
2245 0319 ELAPIED TIME:
12.00 HOUR':
tt0. DATA ELAo5ED t1EAf4 MEAIUPED CALCULATED CHG Its CALC LP UFCEP o S *.
P O I r-4 T.
ilME LE6kAGE DATE LEAFAGE PATE FPOM LA:T PCIt4T C Ct.F LEVEL 10 2.25 O.017 0.013 0.09?
11 2.50 0.017 0.016 0.001 0.05L 12 2.75 0.018
- 0. 019 n.003
- 0. ni-13
- 3. On 0.019 0.023 n.004
- 0. OH 14
- 3..: 5 n.019 0.022
-0,001
- 0. Oi!
15 3.50 0.020 0.026 o.092 0.692 16 3.75 0.021 0.028
- n. Oni 0.691 17 4.00 0.021 0.028
-0.nel
- 0. 079 18
- 4. 29 n.022 i.
'29 6.001 n.077 19 4.50 0,02?
0.031 0,nno n.n75 20 4.75
- 0. 02 3 0.033 0.001 0.077 21 5.00 0.U23 0.033 0.00n 0.076 22 5.25 0.024 0.034 0.001 0.OTE 23 5.50 0.024
- 0. 034 0.000 0.075 24 5.75 0.025 n.034 0.090 v.074 25 6.00 0.025 0.034
-0.000
- 0. 072 26 6.25 0.025
- 0. 035 O. 001 0.072 27 6.50 0.025 O. 036 0.000 0.072 23 6.75 n.026 0.035
-0,000 6.071 29 7.00 0.026 0.035
-0.000 v.070
?O 7.25 0.026 0.035 0.000 0.070 31 7.50 0.U26 0.035
-0.000 0.06L 32 7.75 0.026
- 0. A35
-0.000
- 0. 0.3 33 8.00 0.026 0.035 O.000 0.068 34 6.25 0.027
- 0. 036 0.One n.067 35
?.50 0,027 0.036
-0.000 0.067 36 3.75 0.027 0.035
-0.000 0.066 37 9.00 0.027 0.036 0.000 6.066 38 9.25 0.027 0.035
-0.000 0.065 39 9.50 0.027 0.035
-0.000 0.064 40 9.75 0.027 0.035
-0.000 0.064 41 10.00 0.027 0.035
-0.On0
- 0. 06 ?
42 10.25 0.027 0.034
-0.000
- 0. 0d ?
43 10.50 0.027 0.035 0.000 0.063 44 10.75 0.027 0.034
-0.000 0.061 45 11.00 0.027 0.034
-0.000 0.061 46 11.25 0.027 0.034
-0.000 0.061 47 11.50 0.027 0.034 0.000 0.061 48 11.75 0.028 0.034
-0.On0 0.060 49 12.00 0.028 0.034 0.000
- 0. 06o 0.034 THE CALCULATED LEAvAGE PATE
=
J
TABLE 4 TUPNEY POIriT Ur IT 3 ILPT LEAKAGE PATE (blEIGHT PEPCEf4T/ DAY 4 TOT AL-TIME A'4ALYS I 3 TIME 4r4D DATE AT TTAPT 05-TEIT:
2245 0319 ELAP5ED TIME:
12.00 HOUS:
TIME TEMR.
PPE!!UPE MEA 5UPED (P)
(PSIA)
LEAFAGE PATE 2245 538.988 41.9658 2300 5?9.877 41.9647 0.056 2315 538.868 41.9640 0.028 2330 534.851 41.9635
-0.044 2345 5?S.848 41.9625 O.011 0
538.848 41.9619 n.036 15 539.839 41.9618 0.007 30 538.828 41.9605 0.021 45 538.823 41.?602 0.015 100 533.814 41.9592 n.021 115 538.806 41.9584 0.023 130 535.801 41.9578 0.025 145 538.796 41.9569 0.033 200 538.785 41.9568 0.017 215 538.787 41.9558 0.035 230 538.781 41.955?
0.03S 245 538.776 41.9555 0.023 300 538.770 41.9544 0.030 315 538.764 41.9532 0.037 330 5?8.758 41.9529 0.035 345 538.748 41.9524 0.029 400 538.746 41.9517 0.033 415 538.737 41.9510 0.032 430 538.738 41.9510 0.031 445 538.731 41.9507 0.027 500 538.730 41.9495 0.037 515 538.723 41.9492 0.0?3 530 538.716 41.9490 0.029 545 538.707 41.9483 0.028 600 5?8.707 41.9474 0.034 615 538.704 41.9475 0.030 630 538.695 41.9467 0.030 77 o
n 1 j, 645 538.695 41.9462 0.033 CJ4d Ul4 700 538.690 41.9458 0.032 715 539.687 41.9456 0.031 730 538.679 41.9450 0.030 745 538.679 41.9444 0.033 TNO ibhNd f dIJn Uiliidisb i
TABLE 4 (cont. )
TUC 6:EY EOlt4T O'4IT 3 ILPT LEA 6: AGE PATE (MEIGHT PEPCENT< DAYS TOTAL-TIME ANALYII."
TIME Ar4D DATE AT ITAPT OF TEIT:
2245 0319 ELAP5ED TIME:
12.00 HOUP?
TIME TEMP.
PPEEIUPE MEASURED (P)
(P!IA)
LEAKAGE PATE 800 538.675 41.9446 0.029 815 538.667 41.9436 0.030 830 538.665 41.9433 0.030 945 538.660 41.9429 0.029 900 538.656 41.9431 0.027 915 538.656 41.9417 0.033 930 538.651 41.9420 0.028 945 538.650 41.9419 n.028 1000 539.645 41.9415 0.027 1015 539.650 41.9407 0.0??
1030 538.648 41.9412 0.029 1045 538.651 41.9408
- 0. 031 MEAN OP MEASUPED LEALAGE PATE
=
0,028 ITD. DEVIATION OP MEA:UPED LEAK: AGE PATE!
0.013
=
MAXIMUM ALLCuRELE LEAL: AGE PATE 0.103
=
75 "< OP MAXIMUM ALLCuaFLE LEAVAGE PATE 0.077
=
THE UPPEP 95*. COriFIDEt4CE LIMIT
=
0.060 THE CALCULATED LEALAGE PATE
=
0.034 z-015 P00!! ORlFdliM;
TABLE 5 TURKEY POIr4T UttIT 3 ILPT LEAFAGE FATE ddE IGHT PEE C Er4T /D AY'.
MA33-COINT ANALY31[
TIME Ar*D DATE AT STAPT OF TE T:
2245 0319 ELAPIED TIME:
- 12. 00 WOUP5 TIME TEr'P PPE05UPF FTMT. AIP MA:: LGI:
TGT. AVG. rm::
< c :.
.:P 31 W.
MA!!.:L E M i (LEM)
LO:':.LFM hPi 2245 538.888 41.9658 325804 2300 538.577 41.9647 325802 1.9 7.5 2315 538.869 41.9640 315802
-0.0
- 3. 8 2330 539.851 41.9635 325?O9
-6.4
-6.0 2345 538.84?
41.9625 32590?
5.9 1.4 0
538.848 41.9619 325798 4.7 4.9 15 538.P39 41.9618 325?03
-4.7 1.0 30 538.828 41.9605 325759
- 3. 4 E.2 45 539.323 41.9602 325800
-0.7 2.1 100 539.814 41.9592 325798 2.3 2.9 115 538.80e 41.9584 325796 1.4 3.2 130 538.801 41.9578 325795 1.6 3. "-
145 538.796 41.9569 325791 4.0 4.5 800 538.785 41.9568 325797
-5.9 E. :-
215 538.787 41.9558 325788
- 9. 0 4.7 230 535.781 41.9553 325787 0.2 4.5 245 538.776 41.9555 325792
-4.6 3.1 300 53?.770 41.9544 325787 4.9 4.0 315 538.764 41.9532 325781 5.7 5.*
330 538.758 41.9528 325782
-0.5 4.7 345 538.748 41.9524 325785
-2.9 3.9 400 538.746 41.9517 325791 4.2 4.5 415 538.737 41.9510 325781
-0.0 4.3 430 5?8.738 41.9510 325780
- 0. 6 4.2 445 538.731 41.9507 325782
-1.9 3.7 500 539.730 41.9495 325773 8.7 5.0 515 538.723 41.9492 325775
-1.9 4.5 5?O 538.716 41.9490 325778
-2.7 3.9 545 538.707 41.9483 325778
-0.0 3.8 600 538.707 41.9474 325771 7.0 4.6 615 538.704 41.9475 325773
-2.6 4.1 630 538.695 41.9467 325773
- 0. 8 4.1 645 538.695 41.9462 325769 3.9 4.4 700 538.690 41.9458 325769 0.1 4.2 715 538.687 41.9456 325769
-0.3 4.2 730 538.679 41.9450 325769
-0.2 4.0 745 538.679 41.9444 325764 4.7 4.4 234~
0l6 P00R DitBIML
TABLE 5 (cont. )
TUr.+ gy POIt4T Util T 3 ILET LEerAGE PATE U.'E I G w T PEPC Er0 I' A'.
MA
-POIrdT At4ALY: I:
TIME Ar40 t@TE AT TAPT OF TE:T:
2245 n310 ELAPIED TIME:
12.66 WOUL:
TIME TEMP PPE!!UPE CTMT. AIE MA LO:
TOT.Av6. MA :
( c '.
. p I A ')
M A;; etrMs
. lpm.
LO:7
.LFM<wc.
300 538.675 41.9446
?i5768
-4.0
'.9 815 538.667 41.9436 325.'66 2.9 4.1 830 538.665 41.9433 325764 1.1 4.1 845 538.660 41.9429 325764 6.1 4.n 900 538.656 41.9431 325767
-2,6 3.6 915 539.656 41.9417
?25757 9.7 4.5 930 538.651 41.9420 325763
-5.4
- 3. 9 945 538.650 41.9419 325763 v.2
- .6 1000 538.645 41.9415 32576I 0.1.
- 3. 7 1015 538.650 41.9407 325753 9.2 4.4 1030 539.648 41.9412 325758
-5.1
- 3. 9 1045 538.651 41.9409 325753 4.9 4.2 FPEE AIP VOLUME 0:ED < M IL L I Oti: OP CU.
FT.>
1.55i.
=
PEGPESOIOti LIriE INTERCEPT ( L E M')
325?os
=
SLOPE (LEM *P')
-4.2
=
MAXIMUM ALLOI.lAELE LEArAGE PATE 0.10i
=
75 % GF MAXIMUM ALLDI.lAFLE LEAFAGE PATE 0.077
=
THE UPPEP 95?. CONPIDEr4CE LIMIT 0.033
=
THE CALCULATED LEAVAGE PATE 0.031
=
d 9J 0 i,/
n,rn 1
P00RORl3Na
TABLE 6 TU;tEY PDIr4T Ur4IT 3 VEPIFICATICr*
LEAL AGE r ATE NEIGHT P EP C Er 4 T / D A'.' 4 TOTAL-TIME At4ALYEI TIME At4D DATE AT STAFT OF TE:T:
124*- 0:-20 ELAP3ED TIME:
- 5. 5 fi HOUP:
TIME TEMP.
PPE:IUPE MEAIUPED
.: P.
<P IA' LEAtAGE PATE 1245 538.638 41.9358 1?00 538.640 41.9355 0.104 1915 538.642 41.9353 0.092 1930 538.626 41.9346
- 0. 0:: 0 1345 539.633 41.93?'
n.121 140n 538.628 41.9326 0.111 1415 5?8.630 41.9321 0.117 1430 536.619 41.9312 0.102 1445 538.614 41.93n9 0.087 1500 538.615 41.9301
- 0. n99 1515 538.616 41.9298 0.121 1530 538.611 41.9282 0.114 1545 538.61?
41.9277 0.117 "3?.610 41.9269 0.112 le00 1615 538.606 41.9261 n.118 1630 538.600 41.9259 0.106 1645 538.600 41.9252 0.109 17nn 538.599 41.9247 0.109 1715 538.598 41.9236 0.116 1730 538.595 41.9230 0.114 1745 5?8.595 41.9221 0.119 1800 538.589 41.9213 0.116 1815 538.586 41.9207 0.115 0.109 MEAri OF MEA 30 PED LEAKAGE PATES
=
=
0.011 STD. DEVIATIOtt OF MERSUPED LEAVAGE PATEI VEPIFICATION TEST LEAKAGE PATE UPFEP LIMIT =
0.163 VEPIFICATIOri TECT LEA 6: AGE PATE LOWEP LIMIT =
0.111 0.118 THE CALCULATED LEAKAGE PATE
=
2H J 018 MROR]W-
TABLE 7 TUCtEY POIt4T Ur* I T 3 '/EPIFIC ATIGt4 LEAKAGE DATE ': h!E I GHT PEPCEr.T DA.".
M A.: E-PD I f 4T Ar.ALY!I!
TIME Ar4D DATE AT !TAPT OF TEIT:
1245 0?20 ELAREED TIME:
5.50 HOUP:
TIME TEME PPEISUPE CTMT. AIP M AI-: LOI:
TDT. AVG. MA:-
_________________________________-LEro____________'__________'LEM.+0'_______
< cr.
.; p 3 I A >
MA: 3.-
.LFM LO:: ~
1245 5 3:E. e 38 41.9358 325722 1300 538.640 41.9355 325719 3.5 14.2 1315 538.642 41.9353
?25716 2.8
- 12. ':
1390 539.636 41.9346
?25714 1.8 10.8 1345 536.63?
41.93??
325706 8.3 16.4 140n 539.625 41.9326 325704 2.4 15.0 1415 538.6?u 41.9321 325699 5.1 15.9 1430 538.619 41.9312 32569:::
0,3 13.9 1445 538.614 41.930:'
325699
- 0. 7 11.8 1500 538.615 41.9301 325652 6.5 13.5 1515 53A.61e 41.9288
?256::.1 10.7 16.4 1530 539.611 41.9262
?25680 1.6 15.5 1545 R:- 5:. 613 41.9277 325675 5.1 15.5 1600 538.610 41.9269 325670 4.4 16.1 1615 538.606 41.9261 325666
- 3. 8 16.0 1630 539.600 41.9259 325669
-2.1 14.4 1645 57:8.600 41.9252 325663 5.4 14.?
1700 539.590 41.9247 325660
- 3. 3 14.7 1715 53?.598 41.92?6 325652 7.9 15.7 1730 5?S.595 41.9230 325649 2.9 15.5 1745 538.595 41.9221 325642
- 7. 0 16.1 18n0 538.589 41.9213 325639 2.6 15.5 1815 538.586 41.9207 325637 2.9 15.6 FPEE AIP VOLUME U3ED (MILLIOri! CF CU. F T. ')
=
1.550 PEGPESS IDri LINE IriTEPCEPT (LEM) 325724
=
! LOPE (LEM/HP)
-15.9
=
VEPIFICATIOr4 TEST LEAKAGE PATE UPPEP LIMIT =
0.160 VEPIFICATION TEST LEAKAGE PATE LOhiEF LIMIT
=
0.10?
THE CALCULATED LEAKAGE PATE 0.117
=
m an g
[} t j c. rr, bJ H
/
( n : @m y_ ri r wrs 3jttQ $pt e M ' n.. l s.f a e t^~
k o w.
ny
TABLE 8 TUD'EY POIr4T UrtIT 3 ITABILIZATIOr4 DATA TIME DATE TEMP PPE5!UPE 1845 319 5?9.062 41.9828 1900 319 539.056 41.9813 1915 319 539.040 41.979::
1930 319 S39.026 41.9788 1945 319 539. O l e.
41.9771
?.t 0 0 319 539.012 41.9765 c015 319 539.n01 41.9753 3030 319 538.987 41.9742 2045 319 53:::.971 41.9734 2100 319 53:. 9e.4 41.9721 E115 319 538.952 41.9710 2130 319 5??.934 41.9701 214 c-319 528.910 41.9686 2200 319 53:.918 41.9683 2215 319 538.909 41.9685 2230 319 538.905 41.9661 n, o n
n e
'c i
I %)
% G rJun uaiaa.
TABLE 9 CONTAINMENT LEAK RATE TESTS (TYPE B AND C IESTS)
The following routine local leak rate tests were performed during the reporting period on Unit 3; i.e., since the Unit 3, 1976 operational ILRT (Type A test).
The following procedures were used:
Operating Procedure 13404.1 - Containment Boundary Isolation Valves Local Leak Rate Test Operating Procedure 13514.1 - Personnel / Emergency Air Locks Operating Procedure 13531.1 - Equipment Access Hatches Operating Procedure 13104.1 - Containment Purge Valves Operating Procedure 13404.2 - Electrical Penetration Canisters Operating Procedure 13404.1 - Containment Isolation Valves Operating Procedure 16004.1 - Fuel Transfer Tube Flange
, Penetration Tested 1.
Personnel Air Lock (entire air lock test)
"AS LEFT" "AS LEFT" TEST DATE LEAK RATE (cc/ min)
TEST DATE LEAK RATE (ce/nin) 12/19/75 0
7/27/77 10 3/17/76 0
12/15/77 15 7/13/76 0
1/29/78 30 11/08/76 0
5/17/78 0
3/30/77 0
8/31/78 5
3/02/79 40 2.
Emergency Air Lock (entire air lock test) 12/08/75 0
12/05/77 0
3/18/76 10 1/23/78 0
7/14/76 19.0 5/05/;8 0
11/09/76 0
8/29/78 20 3/31/77 40 2/21/79 20 7/25/77 0
3.
Fuel Transfer Flange 11/27/75 78.9 3/03/79 335 1/10/77 80 3/07/79 100 1/27/78 40 4.
Equipment Hatch 12/11/75 0
2/06/78 0
12/16/76 0
2/10/78 0
1/13/77 20 8/05/73 0
11/09/77 0
2/09/79 0
1/03/78 60 3/13/79 0
1/29/78 0
3/25/79 0
2?40 021
FLORIDA P0h'ER & LIGHT COMPANY TURKEY POINT UNIT i'3 November 1976 to January 1977
CC/ MIN P.S.I.A.
CC/ MIN 1
Mov-750/751 12/28/76 66 2,500 2,500 2
MOV-744A & B, 12/28/76 65.2 160 160 MOV-734 3
MOV-716A 11/24/76 65.5 75.46 75.46 MOV-716B 11/24/76 65.7 51.45 51.45 CV-717 11/25/76 70 330 330 4
MOV-730/732 11/25/76 68 13.72 13.72 5
CV-516/552 11/19/76 72.3 0
0 6
550 11/19/76 71.6 0
0 518 11/19/76 69.5 0
0 7
CV-519A 12/02/76 75.5 0
0 CV-522A, B, C 8
CV-951/956A 12/30/76 66 140 140 989A 12/30/76 66 220 220 9
9S9B 11/17/76 71 0
0 CV-933, CV-956B 11/17/76 71 0
0 10 CV-4650A, B 11/20/76 72.7 0
0 CV-4657 66 110 110 11 MOV-872 11/22/76 70.9 0
0 12 737A 11/25/76 70 0
0 738 11/25/76 70 0
0 13 737B 11/25/76 70 0
0 739 11/25/76 70 0
0 14 CV-200A, B, C 11/30/76 66 8,000 12/29/76 67.7 100 CV-204 11/27/79 74.8 0
0 15 HCV-121/333 11/27/76 74.75 10.29 10.29 CV-312C 11/27/76 75.2 0
0 16 HV-3-1/2 11/15/76 67.1 0
0 17 895V 11/16/76 67.6 37.33 37.33 18 MOV-866A, B 11/16/76 64.8 102.9 102.9 CV-869 19A CV-890A 11/16/76 69.9 34.30 34.30 MOV-880A, 891A 11/16/76 70.0 0
0 883M 19B CV-8903 11/16/76 68.0 68.6 68.6 880B. 891B, 11/16/76 70.0 0
0 883N 2340 022
Page 2
- 3 REFUELING, PTP UNIT #3 November 1976 to Januarv 1977 AS FOUND AS LEFT DATE PRESSURE LEAK RATE PRESSURE LEAK RATE PEN VALVE TESTED P.S.I.A.
CC/ MIN P.S.I.A.
CC/ MIN 20 989C 11/23/76 77.7 0
0 CV-955A, B 11/23/76 73.9 20 20 CV-956C 21/22 MOV-1417 11/24/76 65.5 264 264 MOV-1418 23 CV-2821, 2822 11/26/76 72.7 34.3 34.3 24A 297A 11/15/76 71.2 0
0 298A 11/17/76 70 0
0 24B 297B 11/18/76 72.8 0
0 298B 11/17/76 66 0
0 24C 297C 11/18/76 70.7 0
0 298C 11/17/76 69.0 17.2 17.2 25 MOV-3817, CV-307 11/17/76 72.9 0
0 28A MOV-1410 11/19/76 66 12,000 12/17/76 72.0 0
280 MOV-1411 11/19/76 66 21,000 12/17/76 69.6 50 28C MOV-1412 11/19/76 66 31,000 12/17/76 71.5 35 29 CV-2S03 1/03/77 69 30 30 CV-336 1/03/77 68.1 30 30 31 CV-4659A, B 11/20/76 71.7 0
0 32 Cv "s" 11/19/76 70 0
0 SV-2912 11/20/76 71 0
0 33 SV-2913 11/20/76 72 0
0 SV-2911 11/20/76 71.5 0
0 34 203, 205 11/26/76 68.9 51.45 51.45 35 2600, 2601 11/24/76 69.3 50 50 36 POV-2602, 2603 12/23/76 68.5 400 400 39 Trans Tub Flange 1/10/77 69.3 80 80 40 Equip Hatch 1/13/77 67.3 20 20 12/16/76 75 0
0 41 Pers Air Lock 11/08/76 67.0 0
0 (out) 3/30/77 65.9 0
0 (in) 11/08/76 70 0
0 3/30/77 71.8 0
0 42 CV-S55 11/21/76 67.6 400 400 43 MOV-626 11/24/76 67.4 20.58 20.5S 736 11/24/76 63.0 6.86 6.86 47 CV "A" 12/02/76 66.4 110 110 23:iJ 023
Page 3
- 3 REFUELINC, FTP UNIT #3 Nover.ber 1976 to January 1977 AS FOUND AS LETT DATE PRESSURE LEAK RATE PRESSURE 1.EAK RATE PEN VALVE TESTED P.S.I.A.
CC/MIM P.S.I.A.
CC/ MIN 49 Emerg Air Lock 11/09/76 70 0
0 Inner 3/31/77 69.2 0
0 Out 11/09/76 68 0
0 3/31/77 66 0
0 52 CV-4668A, B 11/23/76
>40,000 1/11/77 71.7 0
53 H-V-3-3, 3-4 11/15/76 70 0
0 54A 860A, 861A 11/20/76 70 0
0 54B MOV-860B, 861B 11/18/76 71.6 0
0 55 CV-955C, D, E
12/30/76 70 5
5 CV-956 58 CV-873A 11/22/76 70 0
0 59 CV-873B 11/22/76 68 65 65 60 CV-873C 11/22/76 68 150 150 58/59/60 MOV-843A, B 11/22/76 75.7 0
0 61 Valve "C" 12/08/76 70 0
0 63 CV-2819/2326 11/21/76 66 6,000 1/11/77 66 8,000 64A MOV-1425 12/08/76 70.4 30 30 64D MOV-1426 12/07/76 71.5 30 30 64C MOV-1427 12/07/76 67.8 50 50 63A Valve "E" 11/20/76 67.5 0
0 65B Valve "F" 1/11/76 66.9 1,000 1,000 65C Valve "G" 11/22/76 68 0
0 TOTAL
>l24,718.44 14,903 All electrical canisters were tested and the "as found" leakage was "0" cc/ min.
U c 9;1 7
97 4J
FLORIDA POUER & LIG!!T CO.'!PANY TURl'EY POI::T UNIT ! 3 November 1976 to February 1978
CC/!IN P.S.I.A.
CC/ MIN 1
MOV-750/751 1/15/78 66.1 730 730 2
MOV-744A, B 1/15/78 67.4 55 55 HCV-3-758 FCV-3-605 3
CV-717 12/09/77 70.81 0
0 MOV-716B 12/C5/77 74.4 0
0 MOV-716A 12/05/77 74 58.8 58.8 4
MOV-730, 732 12/06/77 69.5 0
0 5
CV-516, 552 11/30/77 70.1 0
0 6
CV-518 12/13/77 73.8 75 75 7
CV-519A, n 12/01/77 69.9 5
5 CV-552, A, B, C 8
CV-951, 956A 11/30/77 69.7 0
0 989A 12/01/77 70.4 0
0 9
CV-953, 956A 12/01/77 70 0
0 989B 12/01/77 69.2 0
0 10 CV-4658A, B 12/13/77 70 50 50 CV-4657 12/13/77 71.3 71 71 11 MOV-872 12/05/77 70.1 0
0 12 737A, CV-739 12/07/77 69.8 0
0 13 737B, CV-738 12/07/77 68.4 0
0 14 CV-200A, B, C 1/16/78 66 13,500 2/03/78 69.9 359 CV-204 12/08/77 65.9 1,900 1/16/78 69.0 0
15 CV-312C 12/07/77 69.62 15 15 HCV-121, 333 12/07/77 71.08 28 28 16 HV-3-1 & 2 11/29/77 69.5 0
0 17 895V 12/02/77
/0.1 0
0 18 MOV-866A, B 12/01/77 69.5 0
0 CV-369 19A 891A, CV-890A 11/30/77 67.6 60 60 MOV-880A 11/30/77 69.7 0
0 2340 025
Page 2 f4 REFUELING, PTP UMIT #3 November 1976 to February 197S AS FOUND AS LEFT DATE PRESSURE LEAK RATE PRESSURE LEAK RATE PEN VALVE TESTED P.S.I.A.
CC/ MIN P.S.I.A.
CC/ MIN 19B 891B, CV-3903 11/30/77 69.7 0
0 MOV-880B 11/?0/77 69.9 0
0 20 955A, B, 956C 11/30/77 69.95 0
0 989C 11/30/77 69.7 0
0 21/22 MOV-1417, 1418 12/06/77 68.7 56 56 23 CV-2S21, 2822 12/18/77 72.6 0
0 24A 298A 12/05/77 70.1 0
0 24B 29S8 12/05/77 69.52 10 (0
24C 298C 12/05/77 69.7 0
0 25 MOV-381 12/01/77 70.2 0
0 28A MOV-1410, 127 12/05/77 67.3 4,800 MOV-1410, 127 12/29/77 65.9 14 28B MOV-1411, 327 12/05/77 67.6 0
0 28C MOV-1412, 327 12/13/77 68.2 0
0 29 CV-336 1/24/77 68 30 30 CV-2803 1/24/77 76.8 30 30 31 CV-4659A, B 11/30/77 69.8 0
0 32 SV-2912 12/13/77 66.1 2,000 SV-2912 1/27/77 66.2 98 CV "D" 12/09/77 68.64 2'S 28 33 SV-29tl, 2913 11/29/77 65.3S 126 126 SV-2913 & Iso Va 11/28/77 65.21 14 8 148 34 203, 205 12/22/77 69.5 85 85 35 PV-2600, 2601 12/12/77 67 210 210 36 PV-2602, 2603 1/24/78 66.1 9,423 9,423 42 PCV-846 12/14/77 66.9 779 779 CV-855 12/14/77 66.4 3,500 CV-855 1/26/78 66 1,000 43 MOV-626, 736 12/07/77 70.3 0
0 47 CV "A" 12/01/77 67.9 59 59 52 CV-466SA, B 11/30/77 70.2 0
0 53 HV-3-3 & 4 11/29/77 69.1 23 23 54A MOV-860A 12/09/77 70.7 0
0 861A SSB MOV-860B 12/09/77 70.5 0
0 361B 55 CV-955C, D,
E 12/08/77 70.4 0
0 CV-956D 2340 026
Page 3
- 4 REFUELING, PTP UNIT #3 November 1976 to Febru, v 1978 AS FOL~ND AS LIFT DATE PRESSURE LEAK RATE PRESSURE LEAK RATE PEN VALVE TESTED P.S.I.A.
CC/ MIN P.S.I.A.
CC/ MIN 53 CV-873A 12/06/77 69.05 0
0 59 CV-873B 12/06/77 65 190 190 60 CV-873C 12/05/77 64.91 210 210 58/59/60 MOV-843A, B 12/02/77 66.4 2,100 MOV-843A, B 1/26/78 66 1,600 61B Test Valve "C" 11/28/77 66 0
0 64A MOV-1425 12/02/77 68.8 10 64B MOV-1426 12/02/77 70.5 0
0 64C MOV-1427 12/02/77 69.2 6
6 65A Valve "E" 1/27/78 69.6 0
0 65B Valve "F" 1/04/78 69.5 0
0 65C Valve "G" 1/04/78 69.7 0
0 63 CV-2319/2826 1/24/78 66.7 6,200 CV-2819/2826 1/27/78 66.2 3,538 29 Blind Flange 1/27/73 70.7 40 40 40 Inner Annulus 1/29/78 69.0 0
0 2/10/78 67.2 0
0 41 Inner Annulus 1/29/78 69.9 0
0 Entire Air Lock 1/29/73 66.1 30 30 49 Inner Annulus 1/23/73 67.6 0
0 Entire Air Lock 1/23/7S 68.0 0
0 TOTAL 46,580.3 19,249.8 All electrical canisters were leak rate tested all had "0" leakage excect for
- 1) South SKV "A" RCP electrical canister had a cracked insulator.
"As found" leak rate was >30,000 cc/nin.
The insulator was replaced and the electrical canister was retested, the leakage was "0" cc/ min.
- 2) North SKV "A" RCP electrical canister had a leaking seal and a crack in it.
"As found" leakage was 510 cc/ min.
The insulator was replaced and the electrical canister was retested, the leak rate was "0" cc/nin.
2340 027
FLORIDA PO', ER & LIGHT CO:'PANY TURKEY POINT UNIT f3 1979
CC/ MIN P.S.I.A.
CC/ MIN 1
MOV-3-751 2/15/79 66.5 2,500 2,500 5
CV-3-516 1/05/79 68.4 0
0 6
Check Valve 518 1/24/79 66.5 820 2/15/79 66.5 620 7
CV-3-519A, B 1/9/79 63.7 0
0 CV-3-522A, B, C 8
CV-3-951 2/26/79 65.8 30 30 CV-3-956A 1/05/79 68.6 0
0 989A 1/05/79 66.7 600 1/09/79 67.5 9
CV-3-953 2/26/79 67.0 0
0 CV-3-956B 1/05/79 68.9 0
0 989B 1/05/79 68.6 0
0 10 CV-3-4653B 1/16/79 70.4 0
0 PCV-3-1014 1/16/79 69.9 0
0 11 MOV-3-872 2/21/79 68.6 0
0 14 CV-3-200A, B, C 1/17/79 66.3 20,000 2/16/79 68.7 0
CV-3-204 1/17/79 66.9 70 70 15 Check Valve 312C 2/12/79 68.7 0
0 HCV-3-121, 333 2/08/79 68.8 0
0 16 HV-3-2 1/10/79 66.4 85 85 17 895V 1/11/79 70.2 0
0 19A MOV-3-8SOA 1/03/79 69.2 15 15 Check Valve 890A 1/03/79 67.7 220 220 19B
!!OV-3-8SO B 1/03/79 70.7 0
0 Check Valve 890B 1/03/79 72.5 0
0 20 CV-3-955A 2/26/79 67.9 30 30 CV-3-955B 2/26/79 67.0 0
0 CV-3-956C 1/11/79 70.7 0
0 23 CV-3-2821 1/15/79 66.2 8,000 8,000 CV-3-2322 1/12/79 72.0 0
0 3/07/79 66.0 51,000 3/09/79 66.5 0
24A Check Valve 298A 1/11/79 69.0 0
0 2 10 028
Page 2
- 5 REFUELING, FTP UNIT #3 1979 AS FOUND AS LEFT DATE PRESSURE LEAK RATE PRESSURE LEAK RATE PEi VALVE TESTED P.S.I.A.
CC/ MIN P.S.I.A.
CC/MIT 24B Check Valve 298B 1/11/79 69.5 0
0 24C Check Valve 298C 1/11/79 69.2 0
0 25 MOV-3-381 1/11/79 69.9 0
0 29 Check Valve 336 1/04/79 67.2 90 90 CV-3-2803 1/04/79 68.6 0
0 31 CV-3-4695B 1/12/79 69.4 0
0 32 Check Valve 11-003 1/19/79 69.0
>50,000 2/27/79 68.8 0
SV-2912 1/18/79 66.0
>50,000 2/26/79 66.7 1,700 2/26/79 66.7 580 3/11/7; 66.1 560 33 SV-2911 1/18/79 66.5 195 195 SV-2913 1/18/79 66.4 140 140 34 Check Valve 205 1/04/79 66.0
>50,000 1/05/79 66.0 16,000 1/08/79 66.3 11,000 3/02/79 66.1 10,000 204 1/04/79 67.6 0
0 35 PV-2601, PV-2600 1/10/79 68.6 35 PV-2601, PV-2600 1/10/79 69.6 10 36 PV-2602, PV-2603 1/10/79 67.8 30 3/12/79 66.5 50 39 Fuel Trans Flange 3/03/79 67.0 335 3/07/79 67.2 100 40 Equip Hatch 2/09/79 84.8 0
3/13/79 81.8 0
0 41 Personnel Air Lock 3/02/79 66.3/71.7 40/0 40/0 42 CV-3-855 1/16/79 66.5
>50,000 2/09/79 65.8 3,000 47 Check Valve 10-567 1/09/79 67.9 85 85 52 CV-3-4668B 1/12/79 69.8 0
0 53 HV-3-4 1/10/79 69.1 60 60 54A MOV-3-861A 1/15/79 69.4 0
0 54B MOV-3-861B 1/12/79 69.9 0
0 55 CV-3-955c 2/27/79 69.0 0
0 CV-3-955D 2/27/79 68.0 0
0 CV-3-955E 2/27/79 67.0 0
0 CV-3-956D 1/12/79 69.7 0
0 61B valve "C" 1/19/79 69.2 0
0 23^0 029
Page 3
- 5 REFUELING, PTP UNIT #3 1979 AS FOUND AS LEFT DATE PRESSURE LEAK RATE PRESSUPI LEAK RATE PEN VALVE TESTED P.S.I.A.
CC/ MIN P.S.I.A.
CC/ MIN 63 CV-3-2819 1/17/79 66.2 820 2/27/79 66.9 50 CV-3-2826 1/17/79 66.0
>50,000 2/28/79 6,.7 4,000 3/06/79 65.9 460 65A Flange "E" 3/25/79 68.5 0
0 65B Valve "F" 2/20/79 66.7 0
3/05/79 66.6 0
3/25/79 66.2 3,400 3/26/79 65.9 150 65C Valve "C" 2/20/79 66.6 0
3/25/79 66.2 4,000 3/26/79 67.2 0
TOTAL
>342,600 26,560 All electrical canisters were leak rate tested the as found leakage was "0" cc/ min.
J 40 030
APPENDIX A FAILED TEST REPORT - TYPE A TEST
INTRODUCTION Section V.B.3. of 10CFR50, Appendix J requires a summary report of Type A test leakage rate results that failed to meet test acceptance criteria, which includes an analysis and interpretation of test data, the instrumen-tation system error analysis and a description of containment conditions causing test failure. The following information is reported in response to this requirement.
DISCUSSION The initial Type A test failed because of excessive leakage at the Personnel Airlock equalizing valve shaf t seal (inner door). This leak was repaired, and the Containment Leakage Rate Test was successfully conducted.
Prior to beginning the ILRT, the airlock had been local leakage rate tested and the leakage rate found to be essentially zero, i.e., approximately 0.0006%/ day.
After reaching ILRT test pressure, several hours of data yielded a leakage rate that was out of acceptable limits and was stable as indicated by the Trend Report (see attached Reports).
Leak search teams found a leak at the airlock inner door equalizing valve shaft seal. The cavity in the shaft seal was then filled with grease and the leak stopped.
A successful 'LRT was then performed.
New components for the shaf t seal have been ordered from the Pittsburgh-Des Moines Steel Co. (the airlock manuf acturer) to ef fect pe rmanent repairs.
Appropriate local leakage rate tests will be performed.
The Type A test data and data analysis showing the excessive leakage rate prior to finding and stopping the leak follow.
The instrumentation system error analysis is based on the Instrumentation Selection Guide (ISG) formula from ANSI N274, Draf t No. 2, Revision 3 -
November 15, 1978 " Containment System Leakage Testing Requirement s".
The formula is ISG = +_
2(
)
+ 2(
)
+ 2( p )
The symbols are defined in Appendix C of ANSI N274.
Based on the following test conditions:
Test duration:
8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> Containment total pressure:
42 psia Containment water vapor pressure:
0.239 psia Containment temperature:
538*R The error associated with the instrumentation system, ISG, is +0.035% per day.
2
- ]
032
ANSI N274 requires that the ISG shall not exceed 0.25 Lt, or 0.25 (0.1029),
or 0.0257.
While the ISC is greater than this value, the unacceptable Icakage rate can be considered to be accurate based on the stability of the leakage rate as shown by the accompanying Trend Report. The ISC is d epe ndent on test duration. Had the test been continued for three more hours as the final successful ILRT was, the ISC would have been satisfactory.
However, this vould have been strictly a data gathering exercise and would have served no useful purpose.
As stated in ANSI N274 the ISG formula is not based on a statistical analysis of the actual leakage rate data and is not added to the leakage rate value. The ISC value is used only for instrument selection and loss of sensor criteria.
It is reported per the specific requirements of 10CFR50, Appendix J,Section V.B.3.
.JJ D 33 h"
PB ?R 0-aL.:dmiss3 y 9
l t
3U*f190Y DATA TUckEY COIriT UtiIT 3 ILCT ALMAX = 0.102 VOL = 1550000.00
+
+
TIME DATE TEMo ocE! UCE 1300 319 539.463 42.0219 1315 319 539.443 42.0196 1330 319 53?.420 42.0175 1345 319 5 ~;9. 396 42.0157 1400 319 539.377 42.0130 1415
'319 539.347 42.0115 1430 319 539.334 42.009s 1445 319 539.315 42.0079 1500 319 539.292 42.0061 1515 319 539.273 42.0039 1530 319 539.257 42.0023 1545 319 539.239 42.0005 1600 319 539.226 41.9990 1615 319 539.213 41.9974 1630 319 539.203 41.9959 1645 319 539.190 41.9942 1700 319 539.160 41.9923 1715 319 539.153 41.9906 1730 319 539.140 41.9996 1745 319 539.131 41.9979 1900 319 539.110 41.996s 1915 319 539.09-;
41.9951 1930 319 539.093 41.9940 1945 319 539.062 41.9929 1900 319 539.050 41.9913 l
1915 319 539.040 41.9799 1930 319 539.029 41.9799 1945 319 539.Ols 41.9771 2000 319 539.012 41.9765 2015 319 539.001 41.9753 2030 319 539.997 41.9742 2045 319 539.971 41.9734 21 10 319 539.9s4 41.9721 0
0
- 0. 0
- 0. 0 g.;.
034 1
a
n TUoKEY POIriT UNIT 3 ILPT TPEriD PEPOPT LEAF: AGE CATES 0.iEIGHT PERCENT /DAYN TOTAL-TIME AriALYSI TIME AND DATE AT STACT OF TEST:
1300 0319 ELAD5ED TIME:
9.00 HOURS t iG. DATA ELA IED MEAN MEASUFED CALCULATED
- HG Ir4 ULC L o Vo?EF 95's COINTT TIME LEAKAGE CATE LERKAGE CATE FCOM LAST POIriT CONF LEVEL 10 2.25 0.099 0.065 0.*41 11 2.50 0.096 0.065 O.000 0.I to 5 ~5 0.095 0.066 0.001 0.183 13 3.00 0.094 0.067 0.001 0.132 14
?.25 0.094 0.070 0.002 0.132 15 3.50 0.094 0.073 0.003 0.134 16 3.75 0.093 0.074 0.001 9.133 17 4.00 0.093 0.074 0.001 0.131 19 4.25 O.093 0.077 0.003 0.133 19 4.50 9.093 0.079 0.001 9.132 20 4.75 0.093 0.091
- 0. 002 0.134 21 5.00 0.093 0.091 0.000 0.133 22 5.25 0.093 0.092 0.000 0.131 23 5.50 9.092 0.091
-0.000 9.130 24 5,75 v.092 0.090
-0.001 0.127 25 6.00 0.091 0.079
-0.001 0.125 26 6.25 0.091 9.079
-0.000 0.123 27 6.50 0.091 0.079
-0.001 0.121 9.75 0.090 0.079 0.000 9.121 is 29 7.00 0.090 0.079
-0.000 0.120 30 7.25 0.090 0.079
-0.000 0.119 31 7.50 0.090 0.079
-0.000 0.117 32
'.75 0.099 0.077
-0.001 0.116 33 3.00 0.099
- 0. 076
-0.001 0.114 0.076 THE CALCULATED LEAVAGE FATE
=
[l " b 1717 v3 Lasd i.
t
8 '! : s p ry' 13ft p
' } pl3 NW f
q Uz vi y
TUOkEY FOINT UNIT 3 ILPT LEAK A'3E P ATE GtEIGHT PEPCENT'DAYT TOTAL-TIME ANALYSIS TIME AND DATE AT 3 TART OC TEST:
1300 0319 ELAPSED TIME:
9.00 HOUo!
TIME TEMP.
PPE5500E MEA 5UCED (04 i:PS I AT LEARAGE CATE 1300 539.463 42.0219 1315 539.443 42.0196 0.170 1330 539.420 42.0175 O.120 1945 539.396 42.0157 0.075 1400 539.377 42.013J 0.126 1415 539.347 42.0115 O.062 1430 539.334 42.G096 0.096 1445 539.315 42.0079 0.094 1500 539.292 J2.0061 0.071 1515 539.273 42.0036 0.099 1530 539.257 42.0023 0.091 1545 539.239 42.0005 0.0?2 1600 539.226 41.9990 0.095 1615 539.213 41.9974 0.099 1630 539.203 41.9959 0.094 1645 539.190 41.9942 0.096 1700 539.160 41.9923 0.096 1715 539.153 41.9906 0.096 1730 539.140 41.9996 0.091 1745 539.131 41.9979 0.099 1900 539.110 41.9966 0.099 1915 539.096 41.9951 9.099 1930 539.093 41.9940 0.096 1945 539.062 41.9329 0.079 1900 539.050 41.9913 0.090 1915 539.040 41.9799 0.094 1930 539.026 41.9799 0.090 1945 539.016 41.9771 0.095 2000 539.012 41.9765 0.094 2015 539. M1 41.9753 0.094 2030 539.997 41.9742 0.091 2045 539.971 41.9734 i.075 2100 539.964 41.9721 s.079 MER*i DC MEASURED LERKAGE CATE3 0.099
=
- TD. DEYIATION OF MERIUCED LEAKAGE PATES 0.019
=
M AX I M' :M ALLO'aASLE LEAKAGE cATE 0.102
=
75 "; GF MAXIMUM ALLO *lABLE LEAKAGE CATE 0.077
=
0.114 THE UooCP 95*. CONCIDENCE LIMIT
=
0.076 THE CALCULATED LEAKAGE CATE
=
2340 036
)
[
T'JOK EY ODINT 'JN I T 3 ILPT LEALAGE CATE dEIGHT oECCENT 'DAYT MAII COINT ANALY;I TIME AMD DATE AT ! TACT QC TEST:
1300 0319 ELAoSED TIME:
9.00 HOURS TIME TEMo coE!5UCC
T M T. AIP MASS LD3s TOT.AV9. M955 (CT i: o S I A.
MASE (LBMT (L E M
LOSS (LEM' HOT 1300 539.463 42.0219 32599E 1315 539.443 42.0196 325996 5.9 23.0 1330 539.420 42.0175 325994 2.4 16.3 1345 539.396 42.0157 325994
-0.5 10.2 1400 539.377 42.0130 325975 9.5 17.1 1415 539.347 42.0115 325991
-s.5 9.5 1430 539.334 42.0096 32!B75 6.9 11.6 1445 539.315 42.0079 325972 2.5 11.4 1500 539.292 42.0061 325973
-0.7 9.6 1515 539.273 42.0036 325965 7.9 12.1 1530 539.257 42.0023 325964 0.4 11.0 1545 539,239 42.0005 325961 3.1 11.1 1400 539.226 41.9990 325959 3.9 11.5 1615 539.213 41.9974 325953 4.6 12.0 1630 539.203 41.9959 325947 5.6 12.7 1s 45 539.190 41.9942 325949
-0.7 11.'
1700 539.160 41.9933 325946 2.7 11.6 1715 539.153 41.9906 325937 9.0 13.1 1730 539.140 41.9996 325937
-0.1 12.3 1745 539.131 41.9979 325929 7.9 13.3 1900 539.110 41.9966 325932
-2.s 12.1 1915 539.096 41.9951 325329 3.2 12.1 1930 539.093 41.9940 325929 0.7 11.7 1945 539.062 41.9929 325931
-3.4 10.6 1900 539.050 41.9913 325927 4.4 10.9 1915 53i.040 41.9799 325921 5.6 11.4 1930 539.026 41.9799 325922
-0.7 10.9 1945 539.Ols 41.9771 325915 7.1 11.5 2000 539.012 41.9765 325912 2.2 11.4 2015 539.001 41.9753 325310 2.7 11.4 2030 539.997 41.9742 325910 0.1 11.0 2045 539.971 41.9734 325913
-3.5 10.2 1100 539.964 41.9721 325907 5.9 10.s eccg.;Io VOLUME USED (MILLIONS OF CU. CT.T 1.55
=
SE95E!! ION LIME INTEPCEPT (LEMT 325990
=
ELOPE (LBM' HOT
-10.9
=
MANIMUM ALLO'dAELE LEAKAGE RATE 0.102
=
75 *. OF MAXIMUM ALLO'JAELE LEAKAGE CATE 0.077
=
THE UooEC 95's CONCIDENCE LIMIT 0.094
=
THE CALCULATED LEAVA'3E CATE 0.090
=
230 037
V Operating Procedure 13,100.1
//3 Integrated Leak Rate Test Master Copy s
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- I
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, 7I
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Fl'.rida Power & Lignt Company Turkey Point Units 3 & 4 REQUEST FOR PROCEDURE CHAtJGE/ PERIODIC PROCEDURE REVIEW /OTSC lZ 70 OTSO NO.
8 f 6 E INSTRUCTrO.'.S ON REVERSE StoE.
I Request for Perio 0 e,oc.dic l 1 Reaan fcr Request:
h OTSC Proc. Change Rev,ew i
L i
I i ?. r'rccedure Number Ob 13lCo.I Date of procedure I
l Procedure Titfe:
J L R T' t
- 3. Ocsaibe Details of Change: (if no changes are recommended as a result of a periodic review, write none)
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- 1. H. nan for Change C.:*cribed Above:
i
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(SRO) Date H. '?.uu?J this charge in a chantje in the procedures descriL*1d in the FSAR? Yes., _ _ No._ ___
, j.j If yes. a r'rocedure Chuge Safety Evaluation such as in Admemstratwe Procedure 0109.1 is required to be corroteted.
i i
H l 5
- 3. Comoteted by Date Ct I,j !
iO
.1 '. cwed bY Date l ~ l1 *. Cnar.ge Reviewed by PNSC on or PNSC ri; view not required w_
t
- 12. Charge Approved b/
Plant Supt. Date
Florida Power & Light Ccmp::ny Turkey Point Units 3 & 4 REQUEST FOR PROCEDURE CHANGE / PERIODIC PROCEDURE REVIEW /OTSC OOJ
/f C o rsc no wf E SEE INSTRUCTIONS ON REVERSE 310E.
Periodic Request for O Proc. Review
- 1. Reason for Raquest:
TSC Proc. Change MhM
!b I)
- 2. Procedure Number f3fOOe1 Date of procedure y
k NYa. D
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Tk We Uk&,t/
/H f l
- 3. Describe Details of Cnange: (if no changes are recommended as a result of a periodic review, write nonel
~
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- 4. Reasen for Change Described Above:
I
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64 Oi /G/N/HLy wStY73st / s /^t
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- 5. Submitted by
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b L/. (ll, i L'i d&gs!M,
3-lf Y J. / y., y y (SRO) Date
- 7. Approved by 1
S. Would this change be a change in the procedures described in the FSAR? Yes No
!! yts. 4 Procedure Change Safety Evaluation such as in Administrative Procedure 0109.1 is required to oc compierea.
!j f.
Date
- 9. Cornpleted by O
l d
D4te j
- 10. Reviewed by
- 11. Chaye Reviewed by PNSC on or PNSC review not reuuired U I2. Change Approved by Plant Supt. Date
~
F O R A S r l e u t. 't. 2. :4
Florida Power & Light Company Turkey Point Units 3 & 4 REQUEST FOR PROCEDURE CHANGE / PERIODIC PROCEDURE REVIEW /OTSC f {,]
OTSO NO.
NO.
JEE INSTRUCTIONS ON REVERSE SIDE.
Requ Periodic O eroc.est for
1. Reason for Request
SC chance eroc. Review M AMif-9. /17 7
- 2. Procedure Number OP I31 EO,,1 Date of procedure Procedure
Title:
[ Af y-5 gyp L. E g,. g g 7 g 3 T -- D'M ~y h/W WfT-3
- 3. Describe Details of Change: (If no changes are recommended as a result of a periodic review, write none)
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ADD "'rC1m*, n av c.caset non,sicu-OFF L ME, b ET=
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- 4. Reason for Change Described Above:
l3.. Vgg J. ~ SGPM AS-/S ~ &nMLcowitn, WC<w Wm1 ciruusm,
(;Py2A PSHl ~
Ei* LOOI 'ISS~ Ib ' OCW'^'A'UUllCIl-l 9 p g g h fLt=tL7 '0S~lS 0<*N f/5P M PL'A-2 1: /, 0 0 1 1 l
t h
G. Submitted by J-/g -yr Date
~
Approved by Date
- )
/[O
- 7. Approved by (SRO) Date
-Yn
,(. t2%x-
- 8. Would this change be a chanh in the proceduhs described in the FSAR? Yes No if yes, a Procedure Change Safety Evaluation such as in Administrative Procedure 0109.1 is required to be completed.
H
- 9. Completed by Date Q
d l
' Reviewed by Date l
- 11. Change Reviewed by PNSC on or PNSC review not required
- 12. Change Approved by Plant Supt. Date annu%7:4 AF v.ti/n
Florida Power & Light Company Turkey Point Units 3 & 4 REQUEST FOR PROCEDURE CHANGE / PERIODIC PROCEDURE REVIEW /OTSC A /_*1 oTse no. ' P u /
A SEE INSTRUCTIONS ON REVERSE Sloe.
Request for Periodic
1. Reason for Request
O oTSC O Proc. Change 0 e,0c. Review
- 2. Procedure Number Date of procedure Procedure
Title:
- 3. Describe Details of Change: (if no changes are recommended as a result of a periodic review, write none)
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- 4. Reason for Change Described Above:
g p3 n Pen a - er anweiute
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- 5. Submitted by Date O
A yi f
I Approved by
/
Date j
'/. Approved by (SRO) Date
- 8. Would th s change be a change in the procedures described in the FSAR? 'Yes No if yes, a Procedure Change Safety Evaluation such as in Administrative Procedure 0103.1 is required to be completed.
h b
- 9. Completed by Date Q
d d
- 10. Reviewed by Date
.J
- 11. Change Reviewed by PNSC on or PNSC review nct ecquired
- 12. Change Approved by Plant Supt, Date FORM $7t4 RCV.1/7A
Florida Power & Light Company Turkey Point Units 3 & 4 REQUEST FOR PROCEDURE CHANGE / PERIODIC PROCEDURE REVIEW /OTSC A / '7 oTSc No. "t b, /
SEE INSTRUCTIONS oN REVERSE SiOE.
Request for Periodic
1. Reason for Request
O oTsc proc. Change Proc. aeview
- 2. Procedure Numbe, Date of procedure Procedure
Title:
- 3. Describe Details of Change: (If no changes are recommended as a result of a per. odic review, write none)
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- 4. Reason for Change Descr: bed Above; b P 3k'Peu 3 ; -
c_e. mew yypo b
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- 5. Submitted by Date
/ Q l
. Approved by j,
Date v
- 7. Approved by (SRO) Date
- 8. Would this change be a change in the procedures described in the FSAR7 Yes No If yes, a Procedure Chr.nge Safety Evaluation such as in Administrative Procedure 0109.1 is required to be completed.
Oi
- 9. Completed b'/
Date O
'O. Reviewed by Date
- 11. Change, siewed by PNSC on or PNSC review not required j
- 12. Change Approved by Plant Supt, Dato FORM 5714 HCV.1/78
Florida Power & Light Company Turkey Point Units 3 & 4 REQUEST FOR PROCEDURE CHANGE / PERIODIC PROCEDURE REVIEW /OTSC
/y7 OTSC NO.
SEE INSTRUCTIONS ON REVERSE SIDE.
Request for Periodic
1. Reason for Request
OTSC Proc. Change Proc. Review
- 2. Procedure Number Date of procedure Procedure Titfe:
- 3. Describe Details of Change: (if no changes are recommended as a result of a periodic review, write none) 2_ I b n (d B - b.hfid4 C Pf/dE7F/YDCM EMIO b~ ! b T#'
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'1 ADD DESCC1PTW2 SK6 Tert PCC H71ttciM C'M SV T. -.
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- 4. Reason for Change Described Above:
$ ?g 2.1 1%M V 18 - CE FLc.c.r "As - ts ' ccafice;:~anen f3 hsAklPF S E i L E C "t] S -IS Cct]F-oQUCr'\\7/CM b 97 2-2. P 'N L-5 B - 2 E FL E-CT 'MS-/S GMA4PMM77DN Q ppz. w at,sc - hmzar v7s-is'ecmcccm/cu 2:40 044
- 5. Submitted by n
Date f'
(
Approved by Date
- 7. Approved by (SRO) Date
- 8. Would this change be a change in the procedures described in the FSAR? Yes No if yes, a Procedure Change Safety Evaiustion such as in Administrative Procedure 0109.1 is required to be completed.
S
- 9. Completed by Date Q
0 I
(
'O. Reviewed by Date
- 11. Change Reviewed by PNSC on or PNSC review not required
- 12. Change Approved by Plant Supt, Date FORM 5714 nCV.1/78
Florida Power & Light Company Turkey Point Units 3 & 4 REQUEST FOR PROCEDURE CHANGE / PERIODIC PROCEDURE REVIEW /OTSCOTSC
~
SEE INSTRUCTIONS ON REVERSE SiOE.
/h F / D0 Request for Periodic
1. Reason for Request
OTSC Proc. Change Proc. Review
- 2. Procedure Number Date of procedure Procedure
Title:
- 3. Describe Details of Change: (If no changes are recommended as a result of a periodic review, write none) hA-PCg, k5B -
D E L C 7 E-y ALVE *] Li:T A", ADD WCCM'F LrWg E'A ( crO; f
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- 4. Feason for Change Described Above:
- 4 [ PEM. (c 5 Ga_,_,
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S. Submitted by Date l
A f
Approved by Date
_/g_{Q
- 7. Approved by (SRO) Date
- 8. Would this change be a change in the procedures described in the FSAR? Yes No f
if yes, a Procedure Change Safety Evaluation such as in Administrative Procedure 0109.1 is required to be completed.
H'
- 9. Completed by Date d
i d 10. Peviewed by Date f
- 11. Change Reviewed by PNSC on or PNSC review not required l
- 12. Change Approved by Plant Supt. Date FORM 5714 RcV. 2/78
Florida Power & Light Company Turkey Point Units 3 & 4 REQUEST FOR PROCEDURE CHANGE / PERIOD!C PROCEDURE REVIEW /OTSC OTSC NO __ ' I J,,.[C,_
' y, "l vf *. /' / c -. 4 Y
s E INSTRUCTIONS ON REVEHSE Sinr.
Ni Her;uest for l
- 1. Heason for Heetoest:
[~d O TSC U Proc. Change
- b. Peno fic Proc. Review f
///)f_"('/r 9 / 9 <79
- 2. Procedure Numtm / '//f.]
Date of procedure
/
Procedure Title.
/191 r i, a j y g f) g,,, g g j p 37_
- 3. Describe Deta:Is of Change: (If no changes are recommended as a result of a periodic review, write none) 0' i';). 2 G ~ Tl H (;' ~ b2 t r 7 r L'L V, n T' T C BJ /)Db Hble TC"WW6 NLU'e ?
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- 7. Approvad by s
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- 8. Would this change befaMge in the proceddes descritwd in the FSAR ? Yes No if yes. a Procedure Chaqqe Safety Fvaluation such.is in Administrativ.= Procedure 0109.1 is requ; red to tw come! r'ed.
i
- 9. Completed by Date o
O a,
cj.
Reviewed by Date
- 11. Chang. H.*viewad by PNSC on os PNSC evi w not required 0 I
- 12. Change Approved by Plan! Sons, Date
.d e'ORM $ 714 H F V.1/75
Florida Power & I iqht Companv T :st..~ Po t i be 3 & 1
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- 5. Submitted by Date poroved by Date
- 7. Aromv d by (SRO) Date 3 Vi ni!J th.s ch uv;" be a change in tha procedures describ.d in the FSM" Yas___.*lo_
3 ?"n.edva Ch try G.ifety Ev suar on such a m Adm,mstr.itvr hoo due 01091 i. re.u nrad ta !. completed
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12 Ch any Approved by Plant Supt. Date fronM SM4 Mt:v.1/75
Florida Power & Light Company TurP / Po:nt Umt'. 'l '. 4 REQUEST FOR PROCEDURE CHANGEiPEntCCIC PP.0CEDURE REV:E'A.OT SC
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[_r,/j OTSC C Proc. Change bPioc.Re.,ew Rcquost for Per. odic
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Date of procedure B"
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- 7. Aparo.sd by (SRO) Date f.,,,y.,
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- 8. Would tu change be a change in the proced.es descritx.d in the FSAR7 Yes No l' yes, a Wocedure Chate Safety Evaluar on such as in Administratae Procedure 0100.1 is rec.:; red 's be comp'eted.
W I
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Turkey Point Units 3 & 4 7
/p REQUEST FOR PROCEDURE CHANGE / PERIODIC PROCEDURE REVIEW /OTSC k
t/g OTSC NO.
TE: SEE INSTRUCTIONS ON REVERSE SIDE.
Request for Periodic
1. Reason for Request
%OTSD p,oc. Change Proc. F.eview
- 2. Procedure Number
(([ h!
Date of procedure _ /
LprEGAMEb lEM bG $S7
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Procedure
Title:
- 3. Describe Details of Change: (l'.io changes are recommended as a result of a periodic review, write none)
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- 5. Saumitted by 4
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Date
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- 6. Approved by I
Date
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- 7. Approved by
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(SRO) Date a
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- 8. Would this change be a change (in the procedures described in the FSAR7 Yes No
/
if yes, a Procccure Change Safety Evaluation such as in Administrative Procedure 010f).1 is required to be completed.
G,
- 9. Cr:rnpleted by Date O
d
- 10. Rcsiewed by Date
.. q
- 11. Change R: viewed by PNSC on or PNSC review net required
- 12. Changa Approved by Plant Supt. Date F GH M ill4 h t. t. 1/16
~
Florida Power & Light Company Turkey Point Units 3 & 4 REQUEST FOR PROCEDURE CHANGE / PERIODIC PROCEDURE REVIEW /OTSC
%u a OTSC NO.
SEE INSTHUCT10NS ON AEVFn!E S10E.
Request for Periodic
1. Reason for Request
@ OTSC C Proc. Change Proc. Review 3/9/79
- 2. Procedure Number _ / 3 /oo. /
Date of proceeure 312, k[
Procedure Titte:
- 3. Descrite Details of Change: (if no changes are recommended as a result of a periodic review, write r*one) 0
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- 7. Approved bv (SRO) Date 4_,n ^ + f-g e
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3
- 8. Would this change De a change in thirprJeedures describ n the FSAR? Yes No if yes, a Procedure Change Safety Evafuation such as in Administrative Proccdure 0109.1 is required to be comp!etM.
H'
) ' J' "9 ]-}l
- 9. Completed by Date 0
0 e
d 10. Reviewed by Date i
i.. Chan ;e Reviewed by PNSC on or PNSC review not required
- 12. Change Approved by Plant Supt Date FORM 3 714 REY. trf e
FOR COCI:U:.uT CONTROL USE ONLY FLORIDA P0'a'ER & LICflT COMPANY TURKEY POINT UNIT 3
</
OPERATING PROCEDURE 13100.1 T DATE MARCII 16, 1979 7 yy T DEPT T 1)OCT
1.0 Title
f. /
t T DOCN INTECRATED LEAK RATE TEST T SYS T COMP 2.0 Approval and List of Ef fective Pages:
T ITM
2.1 Approval
TM Change dated 3/16/79 Re iewed by PNSC Ma. ch 16, 1979 Approved by N S Plant Supt.,
Mbe
/dI.
1979 V
7/
2.2 List of Ef fective Pare'(:
Page Date Page Date Page Date Page Date 1
3 /16/79 17 2 /15/79 33 2/15/79 49 3/16/79 2
2/15/79 18 2/15/79 34 2/15/79 50 3/16/79 3
3/16/79 19 2 /15/79 35 2 /15/79 51 3/16/79 4
2/15/79 20 2/15/79 36 2/15/79 52 3/16/79
~
5 2/15/79 21 2/15/79 37 2/15/79 53 3/16/79 6
3/16/79 22 2/15/79 38 2/15/79 54 3/16/79 7
2/15/79 23 2/15/79 39 2 /15/79 55 3/16/79 8
3/9/79 24 2/15/79 40 2/15/79 56 3/16/79 9
2/15/79 25 2/15/79 41 2 /15/79 57 3/16/79 10 3/16/79 26 2/15/79 42 2/15/79 58
' 3/16/79 11 2/15/79 27 2 /15/79 43 2/15/79 59 3/16/79 12 2/15/79 28 2/15/79 44 2/'5/79 60 3/16/79 13 2/15/79 29 2/15/79 45 2/15/79 61 3/16/79 14 3/9/79 30 2/15/79 46 2/15/79 62 3/16/79 15 2 /15 /79 31 2 /15 /79 47 3 /16/19 63 3/16/79 16 2/15/79 32 2/15/79 48 3/16/79 64 3/16/79 65 3/16/79 66 3/16/79 67 3/16/79 68 3/16/79 69 3/16/79 30
Purpose:
The purpose of this test is to assure that leakage through the primary reactor containment, and systems and components penetrating the pric:ary containment does not exceed the allowable leakage rate values as specified in Technical Specification, section 4.4.1 and 10CFR50, Appendix J.
27 3 05,2 3.1 Method and Disciission of Test Techniques The Integrated Leak Rate Test shall be performed by the absolute ecthod by vt.ich the actual mass of contained air is calculated as a function of time.
2/15/79 OPERATING MOCEDURE 13100.1, PACE 2 INTir.ft ATED LCAK R ATE TEST I
3 1.1 Corroboration of Mensurement Provisions shall be made within this test whereby the icok rate measurement.s shall be validated independently by the use of a Controlled Leakage Rate Test (CLRT).
This validation shall be pe rf o rmed for a sufficient duration to accurately establish validation following the ceas urements at the test pressure.
At the end of the overall test, a statistical analysis of the total time Icak rate shall be performed.
3.1 2 Test computations The equations used in this test procedure may be found in ORNL - NSIC 26, " Testing of Containment Sys t ems used with Ligh t-Wa te r-Coole d Power Reactors"' (Frank C. Zapp) as well as in the "i reposed Standard for Leakage Rate Testing of Containment Structures,"
ANS Standards Committee, October 1970.
Basically the leak race of a volume may be computed by watching the test pressure decay, while at the same time, compensating for any changes in temperature and humidity.
Thus the leak-rate (L) becomes:
(1 - Tg [P2 - W 1)
(100). W ere L% = 24 2
Delta t
(
T2 (Pt - W ] ).
g Tg = Tc=perature (Rankine) at t0, weighted c.verage, T2 = Temperature (Rankine) at t, weighted average, Pg = Pressure, psia, at t '
0 Pp = Pressure, psia, at.tg, Wg = Water vapor partial pressure at t0 Psia V2 = Water. vapor partial pressure at tt, psia and Delta t = (tg-t0) hours of test duration L (%) = Percent mass leak rate coeputed over the duration of the test A sample sheet earked,FOR INFORMATION ONLY may be used for c:anual calculations and is attached to this procedure.
Refer to Appendix E.
Discrete temperature and humidity, eletents shall be placed throughout the contairnent, cach placed spatially within a calculated fractional volume.
The temperature, T. therefore, will be weighted average:
I =]n V
T where D D 053 3
1, g,f g-V total Vg = Incre: ental volume at T, an'd
- ~ j"y og - Total containment volume g
4
3/16/79 OPERATINC PROCEDURE 13100.1, PAGE 3 INTFI;R ATED LEAK RATE TEST In practice it is usual to represent Vi as a fraction'. so that Vtot
=
V ot in net cubic feet 1,550,000 Water vapor 1.000, though
=
t pressures shall be handled similarly.
The tabulated volume fractions for these sensors shall be as follows:
T1 and T21 = 0.1600 each, where Vr1
+
Vr21 = 495,800 = 0.320 V otT 1,550,000 V otT t
t T2 and T22 = 0.1810 each, where Vr2
+
Vr22 559,786 = 0.362
=
VentT VeotT 1,550,000 T3 thru T8 - 0,0200 each, where Vr3 thru V8 187,553 = 0.120
=
T 1,550,000 V ot t
T9 thru T20 = 0.0165 each, where VI9 thru Vr20 306,861 = 0.198
=
V otT 1,550,000 t
VTotal
= 1.0000 VP1
= 0.268, where Vvp1 415,400 = 0.268
=
V T
1,550,000 tot 827,739 - 0.534 VP2 and VP3 = 0.26 7 each, where Vvp2 + Vvp3
=
V T
1,550,000 tot VP4
= 0.198, where Vvp4 306,861 = 0.198
=
VtotT 1,550,000 YTotal
= 1.0000 313 Statistical Handling of Test Data Least squares analysis of the leak rate calculations will provide the best linear regression fit to the data for the duration of the test
(
period.
The effect of instrument error on total-time leak rate and statistical leak rat.e shall be computed such that the resultant leak rate including this possible error shall have a confidence level of 95%.
4.0 Precautions and Limits:
/4.1 The primary containment must be pressurized with air of such quality (oil and humidity) that it can be done safely with the least negative influence on the progress of the test.
The air should be oil-free and should be cooled with an aftercooler to approximately 800 F to 850 F.
2~
0 054
2/15/79
~
OPERATING PROCEDURE 13100.1 PAGE 4 INTFER ATED LEAR, RATE TEST 4.2 the air in the contalment should be circulated such that the presence of absolutely stagnant air can be prevented.
Here it is impo r tan t that the energy given to the circulating air is minimal.
A few horsepowe r are all that are required, no more than three horsepower shall suf fice.
The reason for this is to caintain a nearly adiabatic condition of the containment environment once the test is started. The less energy introduced, therefore, the smaller the uncertainty in the resulting measurements.
An uncontrolled increase in te=perature (such as could be produced by large fans) masks the leak rate.
NOTE: Any fan placed in the contaiment must pump air of density up to approximately three times greater than standard conditions; modifications, either in supply voltage or bicde size / pitch may be required.
!4.3 Once the test pressure is achieved, approximately four (4) hours should be allotted for stabili:stion of temperature.
Conditions would normally be conside red stable when the ave rage temperature does not va ry by mere than 1.0 F per hour for the last two (2) horts.
4.4 Access around the periphery of the contaiment should be li=1ted to approxicately 100 feet during periods of pressuri:stion.
Th'ese areas should
, be posted during these periods and limited to authorized personnel only as determined by the Lead Test Engineer.
These areas do not. include the Fuel Handling
- Euilding, Reactor Auxiliary Building (excep t electrical and rechanical penetration roocs), and any elevation above ground level.
- W.~ W shp e.
/4.5 If a contain=ent entry is required pncr te 14 3 psig, competent medical personnel shall be available.
No personnel shall be allowed to enter the contaiment above 14.3 psig without conforming to U. S.
Navy Diving Manual, NAVS!!IPS 250-538, January 1959, stipulations.
/4.6 All syste::s associated with the contaiment must be aligned as required by the Containment Isolation Signal (CIS).
All boundary valves shall be closed.
.\\ny block valve which could prevent a contaiment isolation valve from being subjected to containment air. pressure shall be left open.
The position of the valves shall be per Appendix A.
Closure of containment isolation valves shall be accomplished by norcul operation and without any preliminary exercising or adjustments (e.g.,
no tightening of valves after
(
closure by valve motor).
d.' 7 All pressure - damageable equipment should be removed from the contaiment or vented.
NOT included is any ins t rumenta tion associated with containment isolation or monitoring of accident conditions.
Removed equipment shall be properly stored.
Included would be the following:
EQUIPMENT PROTECTION Reactor Vent to Ccntainment Pressurizer Vent to Contaiment Refer to Pressurizer Relief Tank Vent. to Containment Appendix A Reactor Coolant Drain Tank Vent to Contaiment Accumulators Vent to Ca tainment 2;.iJ 055
2/IS/n OPERATING ITt0CEDURE 13100.1, PACE 5 INTFl:R ATr.D LEAX R ATE TEST EQUITNENT PROTECTION Stean Generator Snubber Vent to Containment Oil Reservoir (if required)
Polar Crane Hydraulic Reservoir Vent to Containment and Cear Boxes (if required)
Manipulator Crane Cear Boxes Vent to Containment (if requirrd)
Remove from Containment Acetylene, (etc) Bottles Fire Ext'inguishers Remove from Contaidnent Wooden Scaf folding Remove from Containment Refuelinc Machine Eaufbment TV Monitor Remove frem Contairraent (if required)
Position Readout Units Remove from Containment (if required)
Dillon Load Meters and Remove from Containment Powar Supply (if required)
- .71 All instruments located inside the containment should be checked and 4
properly vented, if necessary, in order to prevent damage.
Refer to Appendix F.
2.8 All wood platforms and wood scaffoldirt should be removed. The porous nature 4
of wood will complicate the test and may abort it.
49 Any water standing on floors, in low spots, in open piping and in tankage should be removed as required and the areas left dry.
The success of the test depends also on the changes la humidity during the test.
These efforts vill tend to stabilice the relative humidity.
/.10 Open vents or drains as shown in Appendix B to simulate those conditions that 4
would be expected during a LOCA.
All vented syerems shall be drained of water to assure exposure of the contain=ent isolation valves to containment air pressure.
/4.11 Check proper installation of pressurizing system and blowdown piping without
(
opening inlet valve at penetration.
1..
4.12 Check that the oil and coisture content of the air downstream of the filters and temperature are satisfactory.
Air quality may be checked by discharging a quantity of air on a piece of white cloth or paper at a convenient veut or drain connection.
./4.13 Check that installation and calibration of instrumentation for the ILRT is completed and properly documented.
4.14 Inspect, close, and seal personnel and emergency air lock innce and outer doors.
...:/
2"4] 056 4
3/16/79 OPERATING PROCEDURE 13100.1, PACE 6 INTFrR ATED LEAR P ATE TEST 4.15 All electrical equipment should be de-energized within the containment except for those services required and power requirements for circulating fans.
Refer to Appendix G.
/4.16 A general inspection of the accessible interior and exterior surf aces of the containment structures and components has been satisfactorily performed with no evidence of s truc tural deterioration that may affect containment structural integrity or leak-tightness.
/4.17 A desk calculator or equivalent instrument shall be avaliable in the unlikely event that the computers, phone connections or terminals are inoperable. Us e the data sheet in Appendix E.
&4W
)4.18 Ihe Local Leak Rate Tgsts should be completed. gg #4 4.19 RCS leakage evaluation per Operatica cedure 020t. 2, Schedule of Periodic Tests, Checks, Calibratic perating Evolutions, Appendix B, cannot be performed during t s T.
In lieu of this, the contain: rant sump level shall be used to uste RCS leakage and this shall be so noted on the daily calcu on sheet.
5.0 Related System Status:
5.1 The following instrumentation or equivalent are required for the Integrated Leak Rate Test and are recently calibrated and properly documented:
/3.1.1 Temperature Monitoring & Indicatina System Consisting of 22 sensors, selector switches, constant current supply and digital indicator system accuracy of 0.20 F.
Leeds & Northrup instrumentation utilizing 100 ohm copper t he r= ohms, Catalog 8187 S.
Catalog No. 900-9999-9999-1-S numatron numeric display.,
/.1.2 Flow Meter 5
Brooks Hi-accuracy full view rotameter, Model 1110.
RANGE:
0-12.4 scfm at 25 psig, 700 F OR 0-28 scfm at 5 psig, 700 F d.1 3 Dew Point E G & G Inc. Dew Point Hygrometers Model 660Cl-S2, (4 each)
RANGE:
-500 C to + 1000 C, accuracy 4 0.30 C, repeatability + 0.10 C.
/.1.4 A 5 Precision Pressure Cauce 1.
Readout
- unit, calibration accuracy of 0.015%
of
- reading, resolution 0.001% full scale, readout 100,000 counts full
=
scale.
1N O 057
2/15/79 OPERATINC mOCEDURE 13100.1, PACE 7 INTEC!! ATED LEAK RATE TEST d.
Absolute pressure capsule -
2
+
(1) Range 0-49 psi (2) Range 0-100 psi Texas Instrumnt Model 145 l5.1.5 Pressure cauge Range 0-100 psia, graduation -0.1 psia, accuracy 0.1% full scale, sensitivity 0.01% full scale.
Wallace & Tiernan Model #61A-IA-0100.
Vd.2 The data for this test shall be manually acquired from the ILRT cabinet containing the ins trucentation listed above.
These data shall be entered into the ILRT co=puter program utilizing a Texas Instrument 700 terminal or equivalent.
The cocpute r generated report and associated data shall be appended to and form a part of this procedure.
- .3 Throughout the
- test, te=peratures, pressure and vapor pressure are 5
monitored.
These data are used to compute the leak rate from the perfect gas
- law, PV=nRT, using either the poin t-t o-poin t method or the total-ti=e method.
Leak rate predictions and estimates of error are provided by first order linear regression over the test duration nominally of 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />.
Further, the sensitivity to sensor inaccuracy is cocputed and the final NRC report should demonstrate that the test has met the minimum allowable NRC leakage rates within statistical error bounds.
l5.4 Containment HVAC system should be available to maintain a temperature of nor higher than 90 F or lower than 80 F within the contain=ent.
This temperature range should be cuintained, if possible, for a matter of days before the beginning of the ILRT.
A purge period may be performed whereby the initial voluce of "cois t" containmen t air is replaced with " drier" air prior to actual ILRT pressurization.
5.5 Shortly before the ILRT, the Contain=ent' HVAC systes is to be shutdown and isolated frem its electrical and cooling water supply.
/5.6 The reactor shall be in a cold shutdown condition.
/.7 5
The following pressuri=ation and support equipment or equivalent are required for tihe Integrated Leak Rate Test:
_ Equipment Quantity Ca pa city Model No.
Aftercooler 2
5000 SCFM/ca.
GT A200 (American Std)
Centrifugal Moisture Separator 2
5000' SCFM/ca.
Type T (Wrigh t-Aus tin)
Centrifugal - Coalescent 2
6500 SCFM/ca.
S10 A30 Oil Separator (Ceneral/Zurn)
E t; 0 0 5 3... _
OPERATING PROCEDURE 13100.1, PACE 8 INTECR ATED IIAK RATE TEST Equipment
_ Quantity Capn eity Model No.
Refrigerated Air Drier 1
3200 SCFM WC-3200 A. E. C. (Cencral/Zurn) 1 4800 SCFM R-960W Air Filter (General /Zurn) 1 11,000 SCFM 77111 Air Compressors (Atlas-Copco) 8 900 SCFM/an.
PIS-900 Blove:cs (Coppus) 6 1500.SCFM/ca.
HIT-3050-18
/.8 5
Valve line-up, as delineated in Appendix A, shall be completed.
)5.9 Steam generators a re' closed to the containment atmosphere; i.e.,
manways installed, vents and drains closed, level and flow instruments installed and/or root valves closed.
Install Pressure gauge on steam side of each stcam generator outside of contain=ent.
/.0
References:
6 The principal guides for the preparation of this test' procedure were the 10 CFR part 50 and the American National Standard document outlining the cethods for leak-rate testing. Others were consulted, in addition:
61 Leakage Rate Testing of Containcent Structures for Nuclear Reactors, American National Standard ANSI N45.4 - 19 72.
6.2 Primary Reactor Containment Leakage Testing for Water-Cooled Power Reactors, Appendix J.
Title 10, CFR Part 50.
6.3 Testing Containment Sys tems used with Ligh t-Wa ter-Cooled Power Rea c to rs,
Frank Zapp, et al, ORNL - NSIC - 26 UC - 80 Reactor Technology.
6.4 hrkey Point Plant Technical Specifications.
6.5 Bechtel Corporation preoperational
- test procedure and final report for Initial Integrated Leak Rate Test of the Reactor Containment Building.
6.6 Bechtel Corporation Testing Criteria BN-TOP-1, Revision 1, 11/1/72 70 Records Required:
!.1 Current I & C calibration sheets fo'r all instrumentation listed in Section 7
5.1.
Y.2 A dated log of events and pertinent observations shall be maintained during 7
the test.
d.3 Completed ILRT procedure, test log and data sheets constitute quality 7
assurance records and, therefore, shall be routed to the Technical Supervisor for review and rou ting to the Quality Control Su rveillance Technician in accordance with Administrative Procedurc 0190.16, Scheduling and Surveillance of Periodic Tests and Checks Required by Technical Sepcifications, and shall be retained in accordance with Administrative Procedurc 0190.14, Document Control and Quality Assurancu Records.
2 40 059
2/15/79 OPERATING MOCEDURE 13100.1, PAGE 9 INTECR ATED LEAK R ATE TEST 1
0 Instructions:
8.1 Precautions and Limits and Related Systen Status (sections 4.0 and 5.0, respectively) have been satisf actorily completed.
N' S 3/MM Date Verified by M.
Date
/
Q. C. Accepted by a
e %
yg 8.2 rt pressurization and continue to pressuri e entil containment air pre ure reaches 25.0 psig + 3 psig, -0 psig (alternately the test may be condu ced at peak test pressure (Pp) of 50 psig + 5 psig, -0 pisg).
Monitor hour phy51 cal parameters as outlined in "ILRT Data Sheet".
klf every Maximum pr ssurization rate should be 4 to 6 psi /hr. During pressurization:
821 Mai tain'coi (ure and oil content as low as possible.
p\\
D congi nt temperature above 60 F and below 120 E.
8.2.2 Main 8.2.3 Check f o ea
%c pressure should not fall belcw 25.0 psig (50 NO In c
fo alte:rdRe test) for the duration of this test.
NM Verified by
/
\\ s/>
Date the pressurization phase of the test.
83 The following shall e
u Centain:ent indai 8.3.1 p at Verified by
\\
O Date
/
N /
3, achievgd, J4hlate coptainment pressurizing system 8.4 When desired pressure is and leak check the pressurizin
'stemjaptes v \\
\\
Verified by A
Date t
8.5 Usingultrasonicicakdetectorsandotgop lu r,io k the condition of each suspect local exterior leak area.
form glbcalda(test measurement for suspect leaks if required aitd record./
(J
~~
Da Verified by
' /
d$te Q. C. Accepted by
__ n
~/
O every one (1) 8.6 Record data as outlined belcw in Appendix D a min. um of *b a
hour.
No repairs are allowed once the ILRT commences wit ut/ returning to this point.
8.6.1 Sample. number 4 () 0 <> (;
~
6_
8.6.2 Date and time J
f' '\\9C N
8.6.3 Data Logger's name O
3/16/79 OPERATING PROCEDLTtE 13100.1, PAGE 10 INTEGR ATED LEAR R ATE TEST 8.6.4 Containment temperature - 22 8.6.5 Containment dewpoint temperature - 4.
8.6.6 Containment pressure - 1 8.6.7 Outside atmospheric temperature - 1 8.6.8 Outside atmospheric pressure - 1 8.7 From the data gathered on at least an hourly basis, determine that:
8.7.1 The containment conditions are stablized and trends are predictable.
Stabilization should take approximately four hours.
Verified by Date Time 8.7.2 Forecasted leak rate is significantly better than allowable limits.
Perform local leak survey.
[
Verified by Date Time 8.8 Continue ILRT measurements until interpreted data indicates that the ILRT criterion is met for a minimum period of eight (8) hours in accordance with Appendix C.
Verified by Date Time Q. C. Accepted by Date Time Y
8.9 Once predictable and allowable trends have been established, verify the test results by superimposing a leakage approximately equivalent to Lt -(La for the alternate test).
Test duration shall be approximately four (4) hours in length to verify the ability to measure the leak.
[
Verified by Date Time The following additional data shall be recorded during this phase of the test.
8.9.1 Containment air flow (totameter), SCFM.
8.10 Compare the ILRT leak rate and verification leak races.
If the comparison above indicated that the ILRT leak rate is not substantiated by the verification tes t (dif ference within 0.25 L, alternately 0.25 L ),
e ntinue t
a the ILRT leak rate and recheck.
At the end of the extended test period, repeat the verification test, if required.
d" Verified by Date Time
)
Q. C. Accepted by Date Time II
.2340 001 9o ow..
OPERATING PROCEDURE 13100.1, PAGE 11 INTEGRATED LEAK RATE TEST J
8.11 Sample containment atmosphere prior to blowdown.
Upon permission f rom Lead Test Engineer, open blowdown valve and release air from containment utilizing a maximum depressurization rate of approximately 4 to 6 pai/hr.
Date}/N frime /7; MO Verified by /.
/ u.,,.c 8.12 When atmospheric pressure is achieved, containment atmosphere shall be sampled followed b containment entry and inspection.
Verified by aI2 Dated '2/9 Time /66 Date 3-2 I ~7) Time _/_i (Sh Q. C. Accepted by
,O 4 'C-
/
8.13 Inform Nuclear Plant Supervisor that ILRT is complete and affected aystems and equipment are ned-over o Operations Department.
Verified by
(.
_46 Datq8-4"/- W Time /0/6 Date d-2/ - 7 9 8.14 Procedure com ed by 2
i
/
8.15 Procedure reviewed by
, /, //j -r ef'dd -
Date //~t/ 79 Technical Department Supv.
/
b7 4
7 b #i d 9
O
2/15/79
~
OPERATING EROCEDURE 13100.1, PAGE 9 INTECR ATED LEAK RATE TEST
.0.
Instructions:
8.1 Precautions and Limits and Related System Status (sections 4.0 and 5.0, respectively) have been satisfactorily completed.
Verified by
///7 Date O W
. e s,,
3 "/ 8 ~ b M.!
Date Q. C. Accepted by
/
8.2 Start pressurization and continue to pressurize until containment air pressure reaches 25.0 psig + 3 psig, -0 psig (alternately the test may be conducted at peak test pressure (Pp) of 50 psig + 5 psig. -0 pisg).
Monitor every half hour physical parameters as outlined in "ILRT Data Sheet".
Maximum pressurization rate should be 4 to 6 psi /hr. During pressurization:
8.2.1 K2intain moisture and oil content as low as possible.
8.2.2 Maintain contair=ent temperature above 60 F and below 120 F.
8.2.3 Check for leaks.
NOTE:
In any case, the pressure should not f all below 25.0 psig (50 psig for 'he alternate test) for the duration of this test.
f Verified by h ' / erfC('
Date O '/ 'f ~ 79
/
8.3 The following shall be monitored during the pressurization phase of the test.
8.3.1 Containment inlet air temperature.
Verified by d
Date f- /9 - 79
/
8.4 When desired pressure is achieve d, isolate contairnent pressurizing system and leak check the pressuriz.ing system valves.
if Date 8-/8-79 Verified by 8.5 Using ultrasonic leak detectors and/or soap solution, check the condition of i
cach suspect local exterior, leak area.
Perform local leak test measurement for s.uspect leaks if required and record.
Verified by
[
Date.8- /9 - 74
~
i
/
3 ' / f-f k Q. C. Accepted by
/
Date
/
8.6 Record data as outlined below in Appendix D a minimum of once every one (1) hour.
No repairs are allowed once the ILRT comennees without returning to this point.
8.6.1 Sample number 8.6.2 Date and ti=e 7
8 6.3 Data Logger's name
3/16/79 OPERATING PROCEDURE 13100.1, PAGE 10 INTECit ATED l.EAK t< ATE TEST 8.6.4 Containment temperature - 22 8.6.5 Containment dewpoint temperature - 4.
8.6.6 Containment pressure - 1 8.6.7 Outside at=cspheric temperature - 1 8.6.8 Outside atmospheric pressure - 1 8.7 From the data gathered on at least an. hourly basis, determine that:
8.7.1 The containment conditions are stab 11 zed and trends are predictable.
Stabilization s}.ould take approximately four hours.
Date 8-<9 '79 Time /6CO Verificd by w.me 8.7 2 Forecasted leak rate is significantly better than allowable limits.
Perform local leak survey.
Verified by.l D A w m s n r,
Da tc 3-f} -79 Time 2A 00 8.8 Continue ILRT measurements until interpreted data indicates that the ILRT criterion is met for a minimum period of eight (8) hours in accordance with Appendix C.
Verified by
- trw..wA Date 7 'U i Time
-*#'C Q. C. Accepted by U/
W<. "
Date 3 ~ M Ti::.e //0 k
8.9 once predictable and allowable trends have been established, verify tha test results by superimposing a leakage approximately equivalent to Lt ILa f r the alternate test).
Test duration shall be approximately four (4) hcurs in length to verify,the ability to measure the leak.
n b, \\
+
-, ' ' '. S l!! Time Verified by Date
'?
/
/
The following additional data shall be recorded during this phase of the test.
7
~
E.9.1 Containment air flow (rotameter), SCnt.
~
8.10 Compare the ILRT leak rate and verification Icak rates.
If the comparison above indicated that the ILRT leak rate is not substantiated by the verification test (dif ference within 0.25 L. alternately 0.25 L,),
continue t
the ILRT leak rate and recheck.
At the end of the extended test period, repeat the verification tes t, if required.
Verified by
_, n. vt e w n vL -
Date l, %G $ Time /O5
'ITime / b 3 5 Q. C. Accepted by er K C+ m Date c/
2:!;3 064
~
2/15/79 OPERATING FROCEDURE 13100.1, PAGE 11 INTEGRATED LEAK RATE TEST 8.11 Sample containment atmosphere prior to blowdown.
Upon permission from Lead Test Engineer, open blowdown valve and release air from containment utill:1ng a maximum depressurization rate of approximately 4 to 6 psi /hr.
Date W N O Iki=c /S M Verified by
/e.-
4 8.12 When atmospheric pressure is achieved, containment atmosphere shall be sampled followed b contain=ent atry and inspection.
rfM Dated P W Time /6 6 Verified'by e
Q. C. Accepted by
.O s's c-Date 3 - 2_l -79 Time /o:ISe
/
8.13 Inform Nuclear Plant Supervisor that ILRT is complete and affected syste=s and equipment are ened-over o Operations Department.
U Verified by f' -
46 Data 8-2/-
Time /C/6" Date d '/-/ - 7,9 8.14 Procedure com d by o.e:r 8.15 Procedure reviewed by Tectaical Department Supv.
Date 2340 0u5 O
=
O we e
_e___
m 2/15/79 OPERATING MOCEDUP.E 13100.1, PACE 12 INTFER ATED LEAK RATE TEST g
/
APPENDIX A VALVE LINE-UP s.
r
=
me..-
2/15/79 OPERATING Itt0Cr. DURE 13100.1, PACE 13 TNTFER ATED LEAK RATE TEST INTECRATED LEAX RATE TEST APPENDLT A PEN. #
E13fCTION VALVE NO.
POSITION RDfARKS VERIFIED BY/DATE o tsc. Q v' k r "l4I C C ~' M T H t'>
A-'b-
~1 'l 1
To RHR MCV-750 NA System in MOV-751 NA servicc C The-4 L-7
-750A---
- Olesed-~
during ILRT
-75 03----
Closed TdlCO
(' LB$ED J>% 3-15-%
s t
c h % L- _33Lb ciosa0
~
- 1) ? p s,
- 1. > s - i<i 2
From RHR MOV-744A NA ~~
System 1n MOV-744B NA service FCV-605 NA during ILRT HVC-758 NA 734 Closed (wAl 3 79 734A Closed
/N/r*
3 -/ 5 75r 3
CCW to RCP's 716E Closed Not to be OHb $ ~16 '7I MOV-716A Closed vented and/
PAf4 3.)67'l MOV-716B Closed or drained NO 3 -
'7'1 716D Closed 1/<do 3-15
'7't 718A Closed h// 9-ic-%
718B Closed
/h D 9-l' Fr 718C Closed 2hD 8 -le-H
/
4 CCW from H0h-730 Closed Not to be P ff b 3'I b '77 RCP's 730A Closed vented and/
LE)N R-16-' 9 730B Closed or drained
/r W h-t 5 N 727A Closed
'd/>
"-1 727B Closed fin /t 5 -lT 'N 727C Closed (2th
-is /N
'/
b'17 /i-C N t<
cK W*
M 5
PRT to C<.
CV-51'6 Closed
- 1('/I MNi3. A'l6~19.-
9 /6'79 552 Open F4 /$ 3 - /n - / i 517B Open
\\hh W/6 '79 TC-2 Closed W H n '3 - i ~ - 't TC-80 Open
+M D 3 - M - N SV-4600M Closed f4d 5it hl
'Il']
6T;L1>.i,- ; i N.y) t%.. e o
. r s..
ey 7 rq Q
7
(_., t L)
UUi
3/9/79 OPERATING PROCEDintE 13100.1, PACE 14 INTFCR ATED f.EAK RATE TEST INTECRATED LEAK RATE TEST APPENDIX A PEN. J FUNCTION VALVE NO.
POSITION RDfARKS VERIFIED BY/DATE to PRT 550 Closed Os6 3 -/ # '7'7 6
N2 518 NA Check Valve
'N - -;J/.
TC-3 Open i
.J 4 TC,#8 O
31 i' Q,,,,,,,,,v, 3 gen y,,, _,,,,,,,,,,,_nne a..
y i
' ?
a'
- rs e 4 u I, 3C,) 3 - t 's - fl0 Open
,,,,r-
'/
7 PW to CV-519A Closed M
3-#5'77 Standpipes CV-519B Closed GB ' 1 -l P '/'-/
M 3 -I5 rjo CV-522A Closed CV-5523 Closed Cro;'
9 P/
CV-552C Clo:< d
%tf) 2 Ih -T!10-532 Closed
/P46
~5-1 3 N 10-531 Open P eith
-.ss7r 10-543 Closed F rt h A - / Y-M 10-563 Closed K P A
~3 -t b 'l 9 Nth 9-/ I'-M 8
Prz. Sts.
CV-951 Closed Sample CV-956A Closed fid h
'4 - i S
~) l 989A Closed M /s 9-I e - W New TC Open f//t(v '
s o - '< "
991 Closed W4b
'4 - l 5 -7's 1
TC 5
% n Y4h
' 6 15 - 7 */
New Iso.V1v.
C1osed LM)
- -l5 -'N
/
9 Prz. Liquid CV-953 Closed -
/> O O - I < 'N/
Sample CV-956B Closed
,/Pitis
'h-13 -7'l 989B Closed s/o r. L i4 en New TC Open
%A 9-I N-'#/
992 Closed WuA 3. / 6 -7 'i TC-6 Open
? Flh 3-8 3 - 7'l New Iso.Viv.
Closed M 15'-l E 'M
/
10 RCDT & PRT 4608 Closed fd34-F FH B 3 /5 71 Vent; N CV-4658A nnonCJG%
CTS ( Lj']
-r'H Y>
7, -,,. /.;*f -I 5 7'l 2
to RCDT CV-465SB Closed 7;', n 4666A Closed l'G 3 1 3 7a TC-8 Closed v;4 3 S. / < 7/
4653 Open
/bA 3- / T f j, 7 4656 Open
/ n.m
+i.7 0?SC
-w-87 -,
_ m sed u n ?
4657 Bonnet Removed
)'it L3
> - I.5 o
'I b I-ef,p l 2,, a y,
2340 Ou8
2/15/79 OPERATINC PROCEDURE 13100.1 PACE 15 INTFT.R ATED LEAY, RATE TEST INTECRATED LEAK RATE TEST APPENDIX A PEN. #
RINCTION VALVE NO.
POSITION REMARKS VERIFIED BY/DATE
- ,- s ;,. f M.
11 Alt. Lohead 887 PM ^d-A s is 72 fe-Ne t'^ 4 " 3
~
/ U'> ~3-// '79 SIS MOV-863A Closed
/
MOV-8633 Closed
?!A /> 4 - /(- 'FI
(
MOV-8 72, Closcd M'46 ; # > 7't 046
's - l ') - 7</
940N Closed T - - --,f',f 940L
-Open cr- "
y4e-e ta p;g
- ,,,,.,. p ;
12 CCW to Excess 737A Closed Not to be MN P>
'3 14-79 LTDN. HX.
73 7G Closed vented and/
DWB l 5 -7 9 or drained 13 CCW from CV-379 Closed Not to be h5 ) 3 16-7#/
Execss vented and/
LTDN. HX.
drained 14 Letdown to 309D Closed
~5-lT-09 Regen EX LCV-460 Open O/n/) 3 - /S /M CV-200A Closed
(/N> ':; -l ' - W CV,200B Closed
'PM) '2.-lei-H CV-200C Closed
&A 0'C-N CV-204 Closed I/Ju6 d- / s - 7</
201A Open (W) 9-I 5-W 201C Closed QhM 3 - K ru 201 Closed (h,4ib
- -tS-7, L' T '> L
'l 201[E Open 9H n
- - W-7/
205A Closed
[U#S/ 3 -/6 -79 205B Closed 34B 3 i 5 -/'/
15 CVCS to 290 closed -
Check Valve 4)fM 7-/6-M Regen.
289 closed With Fuel in
/s)W/
-t-/'.-7f HX 286 Closed the vessel, 4)#3/
3-/4 19 120B Closed 121 should be
' e !;
2 - ' ' -
't 312C NA closed, but 11CV-121 Closed
.Mi>
3 -/6-7f 333 Closed 120A should M/# 3-/4 - 7/
c> TsG "- A 4-
-l-20P-i Nd Closed.
be closed, U2/3 'R - 1 K
'T-1
." +
202A Opcn one Ch.
'!L' U/
3-/'- 7C 120A Open pp Dir.ch.
202B Open (290,289,or l ' '.</
6- / '. /
-y CV-310A Open
.~#
286) should C(hu b3L - ;< i C ib C;dm '~ i" #' 'M bc open.
'; * ~,
ch
.,- i -
/
C y-p / /
cLgstw T"'"
+-
( M /> 1 - t a' M 2340(lo9
2/15/79 OPERATINC MOCEDtJRE 13100.1. PACE 16 INTFER ATED LEAK R ATE TEST INTEURATED LEAK RATE TEST APPENDIX A PEN. #
RINCTION VALVE NO.
POSITION REMARKS VERIFIED BY/DATE 16 PACVS HV-3-1 Closed M
S-/5 77 HV-3-2 Closed
.M b 3 -l s. W HV-3-8 Closed TW h
'.4 - 1, 7 1 HV-1 Closed
/d#d 7-/4-79 HV-2 Open
!1)$3,1 3-/C-79 3
HV-7 Open h)#3 3 -/6 -A
? "r^~. c e-=~"
''T"
?
& ", y
..ue,-
r,.
17 SIS Test 850A Closed
$-13-i L-79 Line 8503 Closed 61 -*, - / e -
850C Closed 6 - ' ', -
~
85CD Closed c n + c -... n 850E Closed Chl)
~;' ! 5- ? Y 850F Closed 3A
'# - 1 K ^ 7 837 Closed l'/d/ffl 7 N-79 8950 C1osea h)MS1 3 !f.-79
'dff:Al 2-/4-74 89SK C1osed
/
895P Closed
/d//j/
3- /4 -7/
849A Closed Ov) o-,r-t;q 895V Closed lN)RS) f N-79 940M open Om
~
94N:
Closed
/Qd 'W S-/4-7/
942F Open IA>H3l 5-/S -7i' 18 SIS MOV-866A Closed Not to be CT'S
.?-- //. -7 N MOV-866B Closed vented and/
=-
L'-r-MOV-869 Closed or drained sHD
-/5-a g
942C Closed W&
'4 - / 6 - W 883R Closed
( h/)
'2.- J N - W
/
19A cont't.
890A NA Check Valve Spray A MOV-680A Closed 3 -//-M 942W Closed
/WA 3 - I G -TP 896C Closed
/ /(b A 4 - t(a -71 883M Closed MM
'3 - 10 Mt 883K Closed KlM 3 - l G - PT 844A Closed
/C,4
'C-/G-W 891A Open Wh4
- )- ( G ~. 2 940U Open X C.4 n-tr Y
r L. J 't J V! U
2/15/79 OPERATINC PROCEDURE 13100.1, PACE 17 INTFI;R ATF.D LEAK H ATE TEST INTECRATED LEAK RATE TEST APPENDIX A PEN. #
FUNCTION VALVE NO.
POSITION RDfARKS VERIFIED BY/DATE 19B Cont't.
8903 NA Check Val.ve Spray B MOV-880B Closed
(
?-16-9 9 942V Closed
///)//S/ 7-/6 -79
/ J//J,/
3-/4-79 8960 Closed
/t 883N Closed
/////J/
3 -/d -7 4 883L Closed 4)FJ/
3-/' -79 e
844B Closed
/d//?/
3 -/4 ~19 891B Open
/4,47J/
3 -/4 -W 940T Open
/////#
3-/4-79 20 A&B Hot CV-955A Closed b 9-T-M Leg Sample CV-955B Closed
'TM1>
6 - K - ':<t CV-956C Closed T/ h 6 's - / 6 /< /
989C Closed
' G/ / - l / t79 New TC A Open M />
'C'- 18s-Er New TC B open fh/)
'R - I R ' M
/
993 Closed (ir si r>
M 13 - i'r 20 Open
"/15
-7'/
New Iso Vlv A Closed "Jt>>
9 - /6 '/'/
New Iso Vlv B Closed
/p/
0' W Il
<h 3-k,- N 21 CCW to MOV-1417 Closed Not to be
_/"ilH 3 -t 6 '/4 Coolees 10- 871 Closed vented and/
or drained
/
22 CCW from MOV-1418 Closed Not to be
?// b 3 -/5-77 Coolers10-872 Closed vented and/
t-F lh 5 / 4 / </
or drained 23 Cont't Sump 4671 Closed
//
3-//,~/9 CV-2821 Closed M l')
% 'i - N CV-2822 Closed 0,. ri
..f,-
TC-22 Closed
,,,1 10 %, <, 1 -
IC-102 Open
- 46 3 / 5-7'!
4693A Open 4.~
/
4693B Open v ?. / r < -/.. -7 f f
0~/1 o'?O 0"'d O
2/15/79 OERATING PROCEDlRE 13100.1, PACE 18 INTmR ATED LEAK RATE TEST INTERATED LEAK RATE TEST APPENDIX A PEN. #
DJ!CTION VALVE NO.
POSITION RDIARKS VERIFIED BY/DATE 24A Seal Water 297A Closed hfiD 3-15'79 te RCP-A 298C Closed ova %ie-OW 298A NA Check Valve
'/
285D open OM 1-lT-M 285A Open
/Mtf b S - /1 ~/4 24B Seal Water 297B Closed h N b D'I #~ M to RCP-B 298H Closed OtB 3 - 16 '7-?
2983 NA Check Valve
/
285E Open
$19 4l6-M 285B Open I h n *:> - I S - Ti g
24C Seal Water 297C Closed Oth 3-M 7'l to RCP-C 4961-I C ->
Closed 01/>
"5-/s-'N 298C NA Cheek Valve
/
y"b d48 3 W N
Open 285F 285C Open
(/11F>
3 - r 6 7-/
25 RCP S.W.
318 Closed (d/d 7 -/f,W Return 380 Closed
//)]/j/
~3-/4-71 CV-307 Closed C -,,
HCV-137 Closed Ltto ' ; - 1.
v 304B Closed
- 62 /:
-fr u r 304F Closed G v />
$7-it.
'f/
304K Closed Mhh ^ - i c
'e 'r
\\.
306A Closed
//rrA
'7, - f r to 306B Closed dho 9-fr en CV-389 Normal
// < ' ~
}!0V-381
- Closed, FO 5 - / >.7 f 384A Closed..
(1+ h
.^ - / w P, 384B Open Vfli M - in 7/
306C open
&n
- 6. - I - / ' t
/_ -
p _ 3 -/f> 'jy
- r x.w j u t-M-e n
"'~~ ~ -~ ~ -
29 Inst. Air 336 NA Check Valve 1
Supply CV-2803 Closed See Note on 8/ 3-i['N TC-53 Open App. 3,
'/- -
f^' -
TC-59 Closed' PaSe 36 TC-107 Open fU-
>,- -, jl,-
337A Closed Vhr
-U-H y.
+,,..e.
290 072
2/15/79 OPERATING PROCEDURE 13100.1, PACE 19 INTFER ATED I.EAK RATE TEST INTFAR ATED I.EAK RATE TEST r
APPENDIX A PEN. #
RJNCTION VALVE NO.
MSITION RDfARKS VERIFIED BY/DATE 31 RCDT to CA CV-4659A Open
.M M 1/4-74 CV-4659B Closed
- AD
~3
/ 5 -79 4654 Open Cof?
9-H-'N 4667A,
Closed
/P4h 3-la - h 4667B Open
/DA 3-19 '77 SV-4600E Closed I_.h> ' * - /l - V-f 4655A Open
[bM
- I - 'N 4655B open
- rs 3
,t.. W 32 Cont't. Air TC-30 Open NO 8-15-79 Sample Return 11-003 NA Check Valve
- ~
11-002 Open
[
l
?>- S ' N TC-31 Closed
/on 916
'N SV-2912 Closed A'n
?- /A - 7 9 TC-109 Open jo/)
o-l/-97 SV-3 713 Closed gg th' b
$ - l l. 'N c.-r t-, i ;-
e
-., o e*
fi e. n
-//
33 Cont't. Air 11-001 Open hM T'l/ - N Sample SV-2913 Closed 6A/ >
3 I/. '/9 SV-2911 Closed (7/)#
4- / I,
'7'/
TC'32 Closed
d 1/,
F-it e --
TC-33 Closed t />TA %//.
'N TC-110 Open fih6
~;'- I/
'F-t SV-3 709 Closed
~[7 h A 1 - l'
'Y
'.//
34 Service Air 204 Closed
/~7%
O I'i - 7 Cf 205 NA Check Valve 203 Closed
-8/A A- /6 -77 TC-34A Closed
-C4 2, - n-77 TC-34 Open fDi
-s -,, - 7 f 216 Open 07 %' *,! g. J Clo_9 c, -, F f 1: t e u c aa y,,., ;
35 Cont't. Purge PV-2601 Closed
@S C- < L N PV-2600 Closed 5-" ' ' '
e T'E # b,# 1-004-Closed
.. ;me, a o e r > ( fth E - l -s 'N
- .asq
,r.n a,,~..,ou>~*',..
g, 36 Cont't. Purge PV-2603 Closed h/ C !' M PV-2602 Closed Sh r.
R,
,. ; w a 't c 6 14-005- / ' -' J 'i Closed lA > ~ "-
,s,.....,.
'/
"Y g. 7 i
/
- i > --
y y n
-f. },9 c J *t d Gi 3
2/15/79 OPERATINC GCCEDURE 13100. I, PACE 20 INTEGR ATED f,EAK R ATE TEST INTECR ATED I.EAK RATE TEST APPENDIX A PEN. #
EU!CTION VALVE NO.
POSITION RDiARKS VERIFIED BY/DATE oftx.
It-r
.pj ef 4 egago XD4 3 i-+ f 42 N to 4618 V Closed O_'2O D- //. -N 2
Accum.
4618 X Closed 7/Vr/>
'R- /6 - W
'/Y1)')
R - I/ 'hY 847C Closed HCV-936-Closed d220 S-r i-W e
CV-853A Closed "6h />
9-l'-99 CV-853B Closed f/bo 4-t6-9Y CV-853C Closed C/@ 5
,A
'N g,g CV-855 Closed
/#M w - m T-f 940R Closed
- D4 A - (6 T/
0,W?. r.:-., r. ;0.*,*'
an;u 9
A.n 4$19M Open..
un n-4 L*' M ' "~ " --
r' # *
- t'7%
26 - IS P/
E
- r,s d t. 7 -
f.tbM%
creu c:r_,o,. o, -2,., s. o 43
'CCW from FCV-626 Closed Not to be
/;'d R-4 7/
RCP Ihermal 626A Closed vented and/
rN 3 - h - 7'/
72SA Closed Cn/>
^ 1 '; '? /
7283 Closed WVD
% II 'N 728C Closed d6f)
S - I S- 'N 7
47 Pric:ary Water 10-006 Open 7c0 3-t 6-W to Wash TC-40 Closed FM
-$ - # 6 Pl Header 10-567 NA Check Valve TC-ll3 Open dl_')/8-/4-D
'52 From RCDT 4669 Closed
/d/I2/ /-//-2f Pu=ps 4671 Closed
/df/S/
f-N-79 1101 Closed
/d4'S,/
3 -/4 -W I
CV-4668A Open s2 %
,-5-ic.- n CV-4668B Closed
- -i,'4 -P - &N 4663A Open CSf>
-tK 'N 4663B Open ykt) L 66 'P!
4668C Closed A C-i
- - c4 - ? r 4668D Open rDie B. n TI 53 PACVS HV-3-3 Closed Refer to d4 AWP
!!V-3-4 Closed Pen #16
/N R r%<<
HV-3-7 Closed uN\\
R ro 74
?7l?
-)7d i
L cs J
S..' I.
OPERATINC PROCEDURE 13100.1, PACE 21 INTECR ATED f.FAM P ATE TEST INTEZ: RATED LEAK RATE TEST APPENDIX A PEN. #
FUNCTION VALVE NO.
POSITION EDiARKS VERIFIED BY/DATE 54A Recire.
HOV-860A Open Not to be.
[) N-I/. -N Sump HOV-861A Closed vented and/
fr2n #-/6 'N 899C closed or drained
,7h I
54B Hov-860B open W.
- W
(
H0V-861B Closed
[2B 9-6 /M 899E Closed 7T) 899D Closcd Y/.2, 899F Closed
'/-/4 898P Closed
'l %
898N Closed
.',, 3
\\,/
M 55 Accumulator New TC A Open
/4 #
3 -i - 7 'i New TC B Open
- w"
> -c:
9 Ncv TC C Open Fu t+
2
- -?Y CV-955C Closed fla N 3-e3-?9 CV-955D Closed
/'a> N 3,3-7/
CV-955E Closed p ro <*
~4-e>
19 CV-956D Closed
/AM T- / /,- 09 994 Closed
//6 A -.s. r'/
989E Open f#ff.
-, /. N P
. TC-117 Open
/h)fJ/ 3-/(,-7f' 9 70A Closed (12/>
9- //, 'd Valve E Closed j',(ivN M
$ -t/.- 9-r New Iso Vlv A Closed f
3-/5-19 New Iso Viv B Closed
' u,*/
2-<;
/
New Iso Viv C Closed f ee,r ' -/ 5 -/7
/7Cb 3-//- M 58 SIS HOV-84M Closed Not to be 59 HOV-843B Closed vented and/
/ M /,
'2-I / ' N
,^
60 941E Closed or drained f/ Y, 3 -b - / 7 94IF
' Closed
'N 5 -r T-7 /
~
941C closed r N, 3 -/5-7 9 895T Closed Chr)
% I /- - W
' M -830
-Closed -
e<
//gjjg 3,$
n~
....v
(
77 Deadweight Valve C Closed r,
,r y..,.' - f/ T-l/,-@
g Tester Val cc P Open-.-- @
/_ /
.. t,c TC-51 Closed C.ri/>
+ -- I r. </ 9 v(ut TC-120 Open
'vh.n
- -ii - C, l
7 M40 075 ee e
4
2/15/79 OPERATING ITIOCEDLHE 13100.1, PACE 22 INTFER ATED trak RATE TEST INTECRATED LEAK RATE TEST APPENDIX A PEN. #
FUNCTION VALVE NO.
POSITION RDfARKS VERIFIED BY/DATE 65A From ILRT Valve E As Required Compressor TC-55 Closed b> 3-M #)9
/
s s
< cm W 65B ILRT Press.
-ILRTP
-Ope n-In service Sensor Line Valve F Open during
' h/ '
S-//-Vf TC-56 Closed ILRT & CLRT
'OR
'# l.'
'A f i.
?r-FLnustrf5' CVe =m
- i t' I'! '
f
- 1. - o 5
- 9 65C CLRT Flow kLRT-B--
Open--- 0nc 5 lIn service Line TC-57 Closed during C h r '>
.'3 - /4 - 71
'l ?> > 5 - l /. ' M Valve G Open CLRT i
~r A.*: L
- j..,i re,,~<o g-
- c., w.,
63 Ins trument CV-2819 Closed 87'E 3'/6 O Air Bleed 11-006 Closed
/cm 7.,%
CV-2826 Closed D1 M - i s F/
NA Reactor 500 Open 3 - /d-U Vessel Vent
/
h.S. 5-M -79 NA Pressurizer 545 Open
.b.3-/d-M Vents 546 Open
'll. S. 1-/4 ??
547 open
/J, S. 5-/6-79
/l. S.
3- /4 - 7 C NA Accumulators 883A Open
.b. 3-/[-27 Vents 883D Open
/.f.
S. /(- 7 )
883G Open
)/.S. 3- /t - 7 7 u,
eu ea e
.es e
2/15/79 OPERATING PROCEDURE 13100.1, PACE 23 INTFr.R ATF.D LEAK RATE TCST APPENDIX B VALVE DRAWINGS 22:0 077 e
9 e
~
O eoe e
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2/15/79 OPERATING PROCEDURE 13100.1, PACE 24 INTECR ATED LEAK R ATE TEST APPENDIX B I
DISIDE CONTAINMENT OITISIDE CONTAIMMENT I
verc r
'D;uTi_
M-WE M
c* */ -
R
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3 TS cdL-7
I PUtM PUMT p.i s u
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2/15/79 OPERATING PROCEDURE 13100.1. PACE 25 INTEGRATED LEAK RATE TEST APPENDIX B
)
INSIDE CONTAU!ME'IT OUISIDE CO!:TAEIMENT I
f IP7tbE
^
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M 71L,6 716 A -
Tl],
P k/
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[
A A B
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B C
,i 2: 4 0 0 ~/ 9 I
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7
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y7.3o V727 TJ727 U72'l 41 6 4A /A B A C.
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B C
g
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2/15/79 t r'
~
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O PERATII'G PROCEDURE 13100.1 PAGE 26 4.
INTFER ATED f.EAK RATE TEST N
APPENDIX B INSIDE CONTAINMENT OITTSIDE CONTAINME'IT PRT l
M 517B 4
s s $aN.. 3 SS2 g
Sgs
(
)
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m -4ac y,my 54 9 TC %'
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2/15/79 OPERATING DiOCEDURE 13100.1, PAGE 2 7 INTECR ATED LE/.K RATE TEST APPENDIX B INSIDE CONTAINMENT OITISIDE CONTAIl: MENT n
i SISS WA A
I PW orne/z p 922.A PbMS UN T 10- 593 (0-363 m
q 9ftu em.wm VI N'
( c.VCS)
A l
+ >.<./ 522 8
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fo-532.
1o-531 O
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+
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- = mm 0
ww, h
>IPLE SPACE NEY 56A SA 1
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"::: ac<
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space NEW 95 3 7 4 3,gpLg I
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OPERATING tit 0CEDURE 13100.1, PACE 28 INTECH ATI:D I.EAK R ATE TEST i : '/
APP. :3IX B
.p'g'$
_OUTSIDE CONTAIINENT
- ^
_DISIDE CONTAE.MNT 486-Tr 87 j
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$"dl 4
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,1.
PACC 29 INTECR ATED LEAR 7 *.TE TEST OtfrSIDE CONTAI!.EIT i
APPENDIX B INSIDE CONTATl:ME'IT 737G
~N
@ X ccw 738 757A Y
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2/15/79 OPERATING FROCEDL'RE 13100.1, PAGE 30 INTECH ATED LEAK RATE TEST APPENDIX B INSIDE CONTAD; MENT OITISIDE CONTAI? MENT g / f *??"A cl' 4 ?^,-
I Nica I
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2/15/79 OPERATI!!G IROCEDURE 13100.1, PACE 31 INTEGR ATED LEAK R ATE TEST APPDIDIX E
,DISIDE CCiTAIP.EtiT OUTSIDE C0!iTAU NE!!T I
850 s
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2/15/79 OPERATING FROCEDURE 13100.1, PACE 32 INTECR ATED LEAK RATE TEST APPENDIX B INSIDE CONTAINMENT OUTSIDE CONTAINMENT 1
I I
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2/15/79 OPERATING FROCEDURE 13100.1. PACE 33 INTECRATED LEAK RATE TEST APPENDIX B O[JTSIDECONTAUMENT INSIDE CONTAU MENT I
i I
ILt.e gn'
- ( R0011 TO SA>!PLE FROM A&B itTXR I
~
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2/15/79 OPE"ATING PROCEDL"tE 13100.1, PACE 34 INTECR ATED LEAK RATE TEST APPENDIX E U; SIDE CONTAU: MENT OUTSIDE CONTAniME'rr 4M3A
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2/15/79 OPERATING PROCEDURE 13100.1, PACE 35 INTECR ATED LEAK R ATE TEST APPENDIX B INSIDE COtiTATliMEtiT OUTSIDE CO:iTAINME'iT 3048 i
SfAL. Wilt [O.
FILTER BYPASS h307
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2/15/79 OPERATING TROCEDURE 13100.1, PACE 36 I NTFER ATET) 1.EAK R ATE TEST APPENDIX B r3
]
_INSIDE CONTAU.EIT OtrTSIDE CONTAUiMENT f'
I To cos.rraiu M E W 364
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2/15/79 OPERATING FROCEDURE 13100.1, PAGE 3 7 INTECRATED LEAK RATE TEST APPENDIX 3 INSIDE CONTAE.*MEIT OUTSIDE CONTAILYENT 4
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2/15/79 OPERATING PROCEDURE 13100.1, PACE 38 INTFER ATED LEAK R ATE TEST APPCfDIX B DISIDE CONTArtMENT OITISIDE CO!!TArtMENT I
216 2.04-EC3 206 203 M
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2/15/79 OPERATIrlG iMOCT. DURE 13!00.1 PAGE 39 ItiTFT.R ATED LEAK R ATE TEST APPEflDIX B INSIDE CO:ITAILHE:IT
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2/15/79 OPERATING FROCEDURE 13100.1, PAGE 40 INTEGR ATED LEAK RATE TEST APPENDIX B
_INSIDE CONTAD! MENT OITISIDE CCNTAI!: MENT i
X 728A M
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2/15/79 OPERATING FROCEDURE 13100.1, PAGE 41 INTECR ATED LEAK RATE TEST APPENDIX B
'DISIDE CONTAriMENT OITISIDE CONTADDTiT I
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/15/ 19 OPERATING FR0t RE, PACE 45 INTECR ATED LEAK RATE TEST OUTSIDE CONTAI!NENT VIEW
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3/16/79 OPERATING PROCEDlIRE 13100.1, PACE 48 INTECRATED f EAK RATE TEST O
APPENDIX C DEFINITIONS AND ACCEPTANCE CRITERIA 2XJ 102
3/16/79 OPEPATING PROCEDURE 13100.1. PACE 49 INTEGR ATED LEAK RATE TEST APPENDIX C Definitions and Accentance Criteria:
P, (50 psig)
The calculated peak containment internal pressure related to the design basis accident and specified in the Technical Specifications.
P (2 25 psig)
The containment vessel reduced test pressure selected to t
measure the integrated leakage rate during periodic Type A tests.
L,,/L, (%/24 hrs. )
The total measured containment leakage rates by weight at P g
a and P,
respectively, obtained from testing the containment t
with components and systems in the state as close as practical to that which would exist under design basis accident conditions (e.g., vented, drained, flooded or pressurized).
L, (0.25 / day)
The maximum allowable leakage rate by weight at t$e(50 psig)
P as specified fo r preoperational tests in Technical Specificatin and as specified for periodic tests in the operating license.
L
(%/24 hrs.)
Maximum allowable test leakage rate by weight at P (25 psig) t t
derived from the preoperational test data as follows:
btm Lg5L L,,
a where.
L,
= 0.2500 2'l0 103 L
= 0.0667 tm L,,
= 0.162 therefore, L
5 0.2500 0.0667 t
0.162
$ 0.2500 (0.4117)
L L
1 0.1029 t
, L
- periodic test - For periodic Type A tests tm at P ' b shall be less than 0. 75 L t
tm t
Ltm 5 0 75 (0.1029)
Ltm 5 0.0772 %/ day by weight @ 25 psig L,, - periodic test - For periodic Type A tests at P,, L,, shall be less than 0. 75 L a
L,, < 0 75 (O.25)
L,, < 0.1875:/ day by weight @ 50 psig
3/16/79 OPERATING PROCEDURE 13100.1, PACE 50 INTECRATED LEAR RATE TEST The criteria listed below for either the short duration test or the twenty-four hour hour or longer duration test shall be met.
SHORT DURATION TEST ACCEPTANCE CRITERTA:
The Trend Report (BN-T0p-1 Total Time Calculations) based on total-time calculations indicates that the magnitude of the calculated Icakage rate is tending to stabiliae at a value less than 75% of the maximum allowable leakage rate.
_ Note:
The magnitude of the calculated leakage rate may be increasing slightly as it tends to stabiliac.
In this case, the ave rage rate of increase of the calculated leakage rate shall be de te rmined from the accumulated data over the last 5 hours5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> or last 20 data points, whichever provides more points.
Using this average rate, the calculated leakage rate is then linearly extrapolated to the 24th hour data point.
This extrapolated value of the calculated leakage rate must be less than 75% of the maximum allowable leakage rate.
The calculated leakage rate based on total-time calculations is less than 75% of the maximum allowable leakage rate.
The end-of-tes t upper 95% confidence limit for the calculated leakage rate, based on total-time calculations is less than the maximum allowable leakage rate.
The mean of the measured leakage rates, based on total-time calculations over the last 5 hours5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> of test or last 20 data points the maximum allowable leakage rate.
(whichever provides more data), is less than The calculated leakage rate at the 95% confidence level, based on ma ss-point calculations is less than 75% of the maximum allowable Icakage rate.
Data has been recorded at approximately equal intervals and in no case at, intervals greater.than one hour.
At least 20 data points are provided for proper statistical analysis.
The minimum test for duration is 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br />.
At least two-thirds of the drybulb temperature sensors and the dewpoint temperature sensors, and one absolute pressure gauge are fully operational. Additionally, the ISG (See ANSI N274) shall not exceed 0.25 La.
TWENTY-FOUR-HOUR OR LONCER DURATION TEST ACCEPTANCE CRITERTA:
The calculated leakage rate and the end-of -test upper 95% confidence icvel, based on mass-point calculations (ANSI N274) is less than 75% of the maximum allowable Icakage rate.
Data has been recorded at approximately equal intervals and in no case at in te rvals greater than one hour.
At Icast 20 data points are provided for proper statistical analysis.
.he ISG (ANSI N274) does not exceed 0.25 La.
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3/16/79 OPERATING PROCEDURE 13100.1, PACE 51 II.*TEGR ATED LEAR R ATE TEST VERIFICATION TEST ACCEPTANCE CRITERIA Imposed Leakage Rate Method (Lo + Ltm - 0.25 lt) < Lc < (Lo + Ltm + 0.25 Lt) where:
Lam = containment leakage rate calculated during presure ILRT.
Lt = maximum allowable leakage rate for reduced pressure ILRT.
i Lc= containment Icahage rate calculated during verification test.
Lo = Icakage rate imposed on containment using flow measuring device.
Lo = (1 4 0.25) Lt The verification test duration is at least four hours and at least 10 data points are used.
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3/16/79 OPERATIllC PROCEDURE 13100.1, PACE 52 INTECRATED LEAK RATE TEST APPENDIX -D Data Sheets
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3/9/79 OPERATING FROCEDLTE 13100.1, PACE 52 4
INTECo ATED LEAX UTE T:CT 4-O\\b APPENDIX D AMBIENT TDf?ERATL2E HOL2 NO.
BAROMETRIC FRESSL2E MTE ROTA. lTER FLC'.1 VERIFIED BY Y
t ILRT DATA SHEET TIME / SAMPLE NO.
/
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3/16/79 OPERATING PROCEDURE 13100.1 PACE 53 INTITR ATi D !.r.AV. M ATE TEST APPENDIX D AMBIE!;T TDiPERATURE ff b HOUR NO.
3 0, l @
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BARO'IETRIC PRESSURE DATE F.OTA:iCTER FLOW VERIFIED BY
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h 3/16/79 OPERATING I?OCEDURE 13100.I, PAGE 53 INT!:CR ATI.D l.f:AK R ATE ~"ST APPENDTX D AMBIENT TalPERATURE Il0UR NO.
3 DATE 3 /8 77 BARO *fETRIC PRESSURE ROTAMETER FL0il VERIFIED BY hn ILRT DATA SHEET LIME /S AMPLE NO.
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3/16/79 OPERATING PROCEDt?'tc 13100. ],
PACE 53 INTEC!l ATED I.EAK It ATE TEST APPENDIX D AMBIENT TEMPERATURE
!!OUR NO.
BAR0!!ETRIC PRESSURE
- (. /.6 DATE d
'7C ROTAMETER FLO'.1 VERIFIED BY Y C PrYik W
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3/16/79 OPEPdTI:C P"0CEDC'r 13100.1, PACE 53 IllTI:CR ATI:D f.!W PATE Ti?.9T APPEfDIX D
/ q0 AMBIENT TCiPEPATURE (n /
HOUR NO.
BARO'iETRIC PRESSURE O'/ O 8//+2 7k DATE
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1 VERIFIED BY;P(<M Usr(
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.6
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Pressure 0 1
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5 9 3 r_ r-Pressurc # 2 (S PARE )
CddO S (/ b 'll 6 '/ 6
".1, >
D. Pt. - Dew Point RllD - Relative Humidity Deccctor, 9'eq
- j,l
- Pressure,
.U l l c-Terminal Operator
3/16/79 OPERATI!!C PROCrDUltn 13100.1. PAGE 53 f t1Tirit ATI:D l.I:AK RATE TI:ST APPP.t: DIX D
/.}:BIE!!T TR!PERATURE
((
HOUR liO.
i AbObG BAROMETRIC PnESSURE 30,/3 DATc ROTAMETER TLOW VcRITIED BY M tt 1
ILRT DATA SIIEET O I.' i W Til1E/SAMPl.E MO.
occo/ 8 m.%e/
7 ced / /0 e # &/ //
RTD 0 1
'/ t*.2 3
-/ c*, '/ 2 Y J
(- 3
(/r'. 6 4 RTD 0 2 M1 2X K '7 Y4^'
39 23 XX lA' RTD #
3
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/ '7. -4 3
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l RTD # 4 R 2
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\\' J 'i l 1.TD 0 5
- P 2, I L~
W.3, 10
? ?. l'1 E 2. D1'"<2 'l.Y RTD G 6 C;.7 f. 3
- 22. f. A
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- .3 2.1:1 RTD 0 7
R.2. 6 /
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) ). X ()
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87.3.2 d
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'72150
'7 [f ','S Pressure #! 2 (S PARE )
(. J b'70 67V7T 724 M
'7e 23V D. Pt. - Deu Point
.a ;,6 0 1.1 2 RllD - Relative Humidity Detector, c
- Pressure, Terminal Operator 9
3 N 79 OPERATINO PROCEDUltC 13!00. 2, par:E 53 INTIElt ATED 1.EAK P ATE TEST APPENDIX D AMBIEliT TDIPERATURE S9 Il0UR NO.
BAROMETRIC PRESSURE 30' //
DATE
/INY ROTAMETER FLCU VERIFIED BY,,
k_MN /,,
I ILRT DATA SHEET TIME /SAMPl.E NO.
O.200 / /2 CQ 3:) /
/3 0 ? c -' /
6 -f-d3M eI RTD #
1 C/ / -(f~
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7 9.L.T]
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7; 44
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RTD II 9 9 9. 7T t" r. C
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t RTD # 10 R l. 44-3i s~/
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/
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I RTD # 13
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J RTD # 19 9'J. J 2
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i ItTD # 21 (SPARE)
Q/. 0 7 g j. )q l
RTD # 22 (S PARE )
.ty. /5' gy,4 '/
l
/
/
D. Pt. #
1
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! Pressurc # 1
'7(1F/76 T/ P ? 4 4-Pressure f! 2 (S PARC) x,t 4 2 /.
.A --t-D. Pt. - Dew Point q,,
Elb - Relative ilumidity Detcetor, 9~lO}
- Pressure, Terminal Operator 6
3/16/79 OPERATIric IT,0CCDUlt!'. 13100.1, PACE 53 I!1717:l! AT!:D l.!:AK ltATE TEST APPE!! DIX D AMBIE!!T TRIPCRATURE S3 110UR NO. BARO!iETRIC PRESSURE 3 6. /? 9 $ DATE N /d !N s'1 l I Y)! U N 8lA ROT /JiETER F1.0W VERIFIED BY t STAB).L J2A 7/O Ai .3 TA R Y ILRT DATA SilCET i TDfE/SA!!PLE No. 01-(' / / C3/ 5 / 2 0 330/ 3 C215 / -/ RTD 0 1 W, (' 4 ,~)3. 1 5 77 R. Ed.. / !. \\ RTD 0 2 .70' 3 l-S'/. 4 (7 '. ' * ~.73 S -f.( 'i RTD # 3 9 2.) ? c J. 3 :s 5,. c f S c. rj f RTD # 4 7>.57 5 p. /. '/ S r. 7 (, 9/. OE RTD 0 5 ?2.23
- 71. 5 A-
'?l. 2 9 Co.o 4 RTD 11 6 3 2, '$,y
- 9). TA 8 p. I I y i <.i RTD 0 7-97.25 R J. 2 c}
Sr.til RC. Tir RTD 0 8 8.2. C 5' =Lt. 2 '1 SC. 93 x.C 7$ RTD f 9 5 s. ;/ 3 S O. (, O S c. <M vo. F> RTD 0 10 Kl.14 K.: 4-G St '.72 -1 ll RTD o 11 VO. 3.'s"~ YO. i i 7 t'. G 4 7? '? RTD o 12 de. l l 9:. c s me; c.7 7.i. 7 i RTD 0 13 ?o..M <7 7. V ; 7444
- 79. ("I RTD 0 14
?n. L1 7.b //) 7 <i. /. 7 7</. cl RTD # 15 SJ.72 yt. i 3 $., cc 7 -,. y 'f RTD # 16 Cn. 3I') 71.92 79 7 T 7 '.,,'. 5 RTD # 17 J J. Cf 7 'l. I'/ 79.4-6 '79. 1 J-RTD # 18 's i, e.6 V* 2S 5(, / 4, N'? C U RTD 0 19 7 4. 9 M 77 41 79 47 7'i -77 RTD # 20 V'o. D f-7 9. ' ( X S7 7cJ. ?c. RTD F 21 (S PA R Z ) t r '/, ) 2. y W. 2 f(. v ', ' ',' y / s RTD 0 22 (S PARE ) ,4 7, f 7 N /,. / f y4. 4 7 R (.<4 D. Pt. 0 1 f, 5~C / j. sf.(. ) l, al Tf
- f. ep S j D. Pt. 81 2
/. 4 4-i
- , ? > ~2
/, 3 f 2 /, -;',1 D. Pt. i-3 . i 57 . <; 4 4 n e. q . <j r.$ k, D. Pt. 0 4 9 f7 , j 76 9V7 i Off ( Pressure 4 1 8 7C? 6 $ ,T(-Jc'<) R'. [- C / f.' CE'7 Pressure e 2 (S PARE ) 97773 17fcq .< 7 37 0 m-- s7'C7 D. Pt. - Dow Point R11D - Relative llumidity Dctccror, 7f j q,,
- Pressure, I I Terminal Operator
3/16/79 OPERAT7 tic Pn0CrDUitE 13100.1, PACE 53 IllTII:R AT!:D !.1:AR lt ATE Tr.ST APPEllDIX D AMDIEliT TDIPERATURE 62 110UR 110. BAR0!1ETRIC PRESSURE 30'6 7 DATE /9 I'74 / ROTAliETER F1.0tl VERIFIED BY IQ o wn A - i ILRT DATA S!!EET TTHE/S124P1.? 110. [4'C6 / C (:415 / (_, 0 43C / 7 r~44 (f 9 / RTD # 1 9 f,. -3 7 .W.S 3 V4 4 I $ 'l, /, f N RTD # 2 + '2. 7 ~7 C' 2, 77
- 91. M CM t.
RTD # 3 W. /-t A c. (- 9 Y:.c. 23 L 4 7-RTD # 4 O'(, ( / 5 ei /. 'a f .h 7 )
- - e '- '.
t RTD # 5 <'/ ?C. / 'i .W. (- ( 5 c, /- C RTD ii 6 i, :4 'f067 'ro. TI M.aA RTD # 7 M7, *k$'
- 90. 5 4 M', 24-
- 90. f f' RTD # 8
~49 / J. '" A 9'.2 / A kC. 4 3 .N '., 5 4-RTD # 9 P .2 3 <">. i 0' (.f i7 % /. / 2. RTD # 10 U?. /7 5 7 *). '/ 7 7y, YY 79.Ay RTD # 11
- 77. T7 74.7/
7 4 f-6 70,6/ RTD l' 12
- 79. f,2 7 Q.nc,
~71.~,7) ~7G 4 *
- RTD # 13 7:,77 77.AG 79 33 7017 RTD # 14
' ';.r.s 9-
- 74. <F 7
/9 45' 7 4.4 2. / RTD # 1$ 79. '7 7 t; %.i 7G. /6 7A 76 RTD # 16 7-<. 6 (/
- 74. f ?
74 5/ 79, <17 RTD # 17 7 9 2 't-7 </. 26 7G. / 3 7%6U RTD # 18 Tu. si 2 7G, la 7 c,. s -f 7e, jy RTD # 19 7V. 5 4
- 71. 2 <
- 74. ? =f
-76. 2 2. RTD # 20 79.V2 7d.17 70 1/ 70, / '/ RTD u 21 (S PA R E ) l 15,./ /c-V4,73 W p. 7 //
- 4 ca.
RTD # 22 (S PARE ) ,V 3. /.2 '(.2,(, f ,$ j,,2 2. 9 l,(/ 7, D. Pt. # 1 /. <"/ 5' / /, "} T3 /, 4 't I /. -f f f D. Pt. # 2 I 43 'l I.340 i 3 7X r -~2 i 7 D. Yt. F 3 , S ci l I.nof
- ,a. ] <t-o ;-f
( .D. Pt. # 4 f, t*LI i. n.f.1 g, o fs f.- I. O -} 4*~ Prennurc 4 1 J'/,4 6 / M M #44?I S.'. 3 7. 3 66 3 S.1 Pressurc #! 2 (S PA R C ) R' 7 / ','/ V 7 l.2.,2 .V 7 0 7 T E 7t' 3 i D. Pt. - Dow Point RllD - Relative Humidity Detector, o Io r , J l*IJ.
- Pressure, Teminal Operator
3/16/79 OPERAT7!iC PRDCrDURE 13100.1 PACE 53 I NTIT.I' ATI{l) I.CAK MATE TT.ST APPEllDTX D AMBIE!!T TDIPERATURE d/ HOUR NO. 3 !/ I f BAR0!iETRIC PRESSURE 36, 67 I DATE ROT /JfETER FLON VERIFIED BY ILRT DATA SilEET cSvi<*
- .1 OEl>'I
/0 CS*k / // L& / /L-Tine /Stairl.R 1:0. D'2'O / RTD # 1 V 4: 77 E' 3, -i'2 M.,,2 '/ S3. e 3 RTD # 2 4'/. 7 ( .Y /, 5 7 &/, 3 ? s'/ 2 9 RTD # 3 v_- 32 ,y /'. J ef- " v.
- 2. '/
'<<',9 RTD # 4
- w. '. C 'r
.? C 4 3' C. 't 3 3 RTD C 5 ' f. 5 -; Sr. 4 /s 9C.'ti W.A5 RTD 11 6 5 (. 3 >> GO..:t ej & f. 2 4. G-c 'c p.5 RTD 0 7 %*. 0 47 90 0 '] Ss'G. 00 '7'i. 9 '/ RTD # 8 7 t'
- / j W'. 2 4-
.F,, / ? I M'. / y 5 c. r.'o RTU I! 9 .7f r) <l WC, C I ' ' a'el. RTD # 10
- 79. [5 7 9. f 3
- 79. 7'/
7 <; 7 /. RTD # 11 <71, f7 7'/. ff 7</. s/ 7 9 4 RTD Il 12 7 <; 4 4 7 9 yo /?, 3(,- 77 3/ p'r.)
- 13 7/.24 7 (f. / 9 79./y 79,/ 4 RTD # 14 79,.7 /
79 3 Y '7 4. ? E / '/. D RTD # 13 7 ci. 7 7 '79 7u 70 (f 7'? 2. (. RTD # 16 7'i A i 76 'F2 7 G. 4 l ~7 i.1 / ~ RTD # 17 / f, (J~ 7 7. O f 7 P. 41 7 ? 9 /., RTD G 18 7 c. 7 6-7073 ~7 9. 7 ) 7., {. ) RTD # 19 7</, /6 79 / ~7 79f4 7 </ / / RTD # 20 77 if qq. j 2. 7f j C J <~. ; ' RTD re 21 (S PA R C ) 5' L / 5 g.->. ro N 7 7/ q.; c t > RTD # 22 (S PARE) b' /. 6 6-Q /. 4-f V/ J d, . /. (;'/ D. Pt. 0 1 ), 9 4 C l 't 3 l2 l. 4 3 Cs /. A 2 'l D. Pt. # 2 /, R iel /. 3F5 /. 3.2 f: /. ? j G* D. Pt. v 3 i. c 59 o.C&O r r <,' r7 p.jl2 \\ D. Pt. # 4 /. ( 9 (/ /. / / 'Y / / 3f /, i S.2 Pressurc # 1 .%.'3 Y '7 fe'6> A 6'l R624l .$b.2/2 Pressure v 2 (S PAR E ) J77.5
- .8 6 4 'I '/
Y(> '/ 6 5 %'/38 &'/ / 3 D. Pt. - Dow Point RllD - Relative llumidity Detector, .s. ,4 n je J ,9 7-
- Pressure, Terminal Operator 4
3/16/79 Ol' ERAT 7!1G PROCEDURE 13100.1, PAGE 53 IllTIT.R ATED f.!:AK R ATE TEST APPEllDIX D AMBIENT TDIPERATURE d;/ !!OUR NO. BAROMETRIC PRESSURE 30.// DATE /I
- [
/ ROTAMETER FLOW VERIFIED BY ILRT DATA SilCET TIME /SAMP1.E No. 06#8 / s3 (6/ T / /4 ('d 3 0 / if et/1$~/ / /o RTD 0 1 .T). S'l 3 2. /.1 T.) % 9 *2. 'f 2 RTD 0 2 S*/. d 7 &#.95~ 80..h~~ 8't. 7e RTD # 3 Ve. > 0
- -M / 7 Po. /.3 5c //
RTD # 4 .W.43 +M 2 \\' t' *- :' 4-J~' J. C RTD 0 5 RO. 50 .Y0. A S' ?A J O ko. I 7 RTD fi 6 ye. / / .Go.d'7 V-o. r') 2. 7 9 G '/ RTD 0 7
- 99. 9 5~
'7 ti, 9 0 79.99
- 79. fd 7 RTD # 8
- 4't. O 'l
,VO. 0 2~ C(. C 'Z 7 9. '/ i' RTD 0 9 Rn. 0 4 +n. O l AC.O }
- *r
(' 2-- RTD # 10
- 77. 74 79.7 2
~7'J. 7 0 7 </ 76 RTD # 11
- 70. 9 /e 7 9.<4 2.
7 7. M 7'l. *] 6 RTD I' 12 79.3 0 74.20' 74 _3 7 77 24 RTD 0 13 99 (O l'1. C 'l 7G 663 "'7 9. C 4 RTD 0 14 76.32 74 30 74).3 0 7 9.2 </ RTD 0 15 7 9. f.>.3 7 9, r,2 7e; (. O
- 79. g !
RTD # 16 7 9. 3 7
- 77. %
7t; 33 7 6. 4 <} RTD C 17 7 S. 'l3 7?*92 7 9. 9 U 7 T. S'/ RTD u 18 7 9 /- 6~
- 71. c. 4 -
7'). l 2 9 'i <- C RTD 0 1t)
- 79. O 'l 7407 7// o 7 79 Cd>
RTD # 20 79.C I ~7 h t' 4 77 / 2 7 7. c~ A RTD se 21 (S PARE ) Y). 'l O 9). 7 -1 V). Tf V2. V 3 RTD # 22 (S PARE) S'd, (/ 6 80, V f .90.77 W.70 D. Pt. 0 1 /, 4 2'l / - 425- /.42R /. 9-2 2 U. Pt. 0 2 i, 3 r in
- i. 21A-
) ~> c:(, ) ~} l.1' D. Pt. e-3 I.I3I / 14'7 I. I c q-
- t. t7?
Y.. D. Pt. 0 4 1, I 7.2. l,l.Tfx I, 192 (, a c 't Pressure a 1 S6/95- .f6 / 7S &, / 57 R6/41 Pressure e 2 (SPARE) .W. s*/ l .C c;. 5/ 7 / $b f 53 p-(_,7 3 7 D. Pt. - Dew Point RilD - Relative IIunidity Detector, ] }'.] ] }}[
- Pressure, Terminal Operator 4
3/16/79 OPERATII:C PROCEDUnn 13100.1 PACE 53 IllTI:CR ATI:D I.l:AK lt ATE TI:ST APPE!!DTX D AMBIENT TDIPERATURE d/ HOUR NO. 5 i DAR0 METRIC P:1 ESSURE 38- )/ 3 DATE / / / / #79 ROTAMETER FLOW VERIFIED BY ILRT DATA SHEET TIl!E/SAMP1.E NO. d 7t'd / /7 6/i5' / /g 0730/ / // CW5 / 2 0 RTD 0 l E' L 2,3 8'). J A 82.0-3 2'). 9 2. y RTD # 2 ' n. f. ';:. .V..',,
- 7 TC, 9 ')
...AR RTD C 3 W. O <7 L:0.09 '<C 04 'w, e c RTD # 4 ': ' i '7 t. I 2-W '- /u .i J i ' ^' RTD # 5 9 0. / 2-- b'C O 'l 3D
- O 5~
4*D. 0 3 RTD # 6 7 7. </ 4-7 9 c/ )
- 79. ? 7 7';, '> S' RTD #
7 7 G C'4- "7 t/. 7 3 79, V ~) H. PO RTD # 8 7 9. 9cl ) 9. 9 () 7'i. W '7'j. ?(- RTD V 9 R-C. C'.2 70 () V 5'.; t') 7 c; t, i RTD # 10
- 79. /t)
~79. 6 d, 7'),(.) 7 <i. t.<j-RTD a 11 7'. 3 7 7 9. 3 Ge 7'J. 3 4 77 '3 I / RTD o 12 7 9. 2.2 ~74 21
- 70. 2-l i?. 2 t>
RTD # 13 79 /"' 3 7<7 e J 79.c b 7s. 'j ) RTD f 14 7 9. 2 6 7936 7'/. 7 /, 7 9 16~ RTD # 1$ 7 </. 5~7 79..i7 7 ri 5~$~ MN RTD # 16 ~7T 3 3 79 3i 7 'j. 2'l 71. r RTD P 17 '70. 9 ~7 7 c, C' 5 7S'P4
- ?O 5l RTD C 18 90.5 7
- 79. 5 4 10.5 3 7 <), s )
RTD # 19 ~7<f. C 4 7']. 0 2
- 94. E 2.
7 Q. C / RTD # 20 7 7. L' 6 7 i. (i -/ 7 's c/ / 7 p, ej 7 RTD # 21 (S PA RE ) 5-).2'f S ), ro .yp.0 g-P f. 9 <,' o RTD # 22 (S PARE ) .i'O. (. 7) kv,53 90.43 9ts i c/ D. .t.
- 1 l.410 1.4/9'
/. 4 / _S- /. 4 /4 D. Pt. # 2 l,.) C h' I.207 ). 2 / *7 (..).M D. Pt. i; 3 1, i + $- /.7c/ J,2/O
- 1. ),c-
, D. Pt. # 4 f. 12 / [, p,) @ l,2 3G /. 2 4 _'t Pressure a ! Th / 2 6' f'6 / / /). 5'6 /C 7 .f t, C ST Prensure t' 2 (SPARE) 949)O 3/,Por .f( / 'l 2 7 (~, 760 D. Pt. - Dow Point
- m. ? f n 4 4 n RllD - Relative llumidity Dctcetor, G
'< U lld \\
- Pressure, Terminal Operator e
3/16/79 OPERATING PROCEDURC 13100.1, PACE S3 It! TIER ATI:n I.!:AK 1: ATE TEST APPEllDIX D AMBIEliT Tf2!PERATURE [,'i IIOUR liO. [, 3 ['i ! 7 7 BAROMETRIC PRESSURE 38./i DATE / ROTAMETER TI.CW VERIFIED BY II.RT DATA SilEET Tusc/SAMP1.E no. M:e /.21 CS/S / .3 2-Mw/
- n 3 cHr/ 2 9-(
RTD # 1 8' /. Y / ,Y/. ? / Mi fel Bl.53 RTD # 2 .P6' 3 6 TO. 2'/ F(V 2 5 PO 2.0 RTD # 3 7 ',, r/ s' 7 ;. 9 7 N 'M- / v u -? RTD # 4 96.06 70.r ? I 74 99 /') '> t - RTD # 5 .W.OO '7'f. '/ 5 7 9.')4- /99/ RTD fi 6
- 79. fr.2 7.). 7 y 70 7 -f 7 9 y/_
RTD # 7 7tJ, 7'I 7/77 79 75 79 74-RTD # 8 7'J '#' 3 7'J. M 79 7e 79 7v RTD 0 9 '7:j. fi.3 7:). cj 3 7 9. y+ yo q ), RTD # 10 7'). l>.2 7 4. L / 7'9 U D 79(:o RTD # 11 1 79 31 '7r/ 2 c/ / 9.7A / 9. d te RTD 11 12 7 'i. / <' 1.i. ) A 79.frfa.- yy i r. RTD # 13 7 e 4 *) 7.; rj 7 7g cry 7p.g RTD # 14 7 "). 2 3 7 ').1 2 7y ii 2 4. L t RTD # 15 ^] ') 54 _7 'l. il 7 sj 5I 79 20 RTD # 16 77 2 g '79, 2 7 79 ?4-70 ET RTD # 17
- ) Y.Y.}
7 W.93 ic' b i - ?r.bf RTD # 18 79.n. ,, 4-3 / >. 4 / 7,ae RTD # 19 7?. '/ '/ 7?.'/ 7 7 S.CNe 7 h '/O RTD # 20 7 7. '/5 7.Y, (if 79 94-75 c1 RTD 21 (:> PA RE ) ' 51. e~4 y/ 7/- F-t Ic 5 vi % RTD # 22 (S PARE) VO, 3 '4
- 96. 2 6 f C. 2.(
r-C. I Is D. Pt. # 1 f. 4-1.3 }. 41 3 I M *7 l.4 C') D. Pt. # 2 1 32.3 f.223 r n'M l.ZW D. Pt. I 3 '). 2 2 /~) /. 2 2 C I J ie I 219 ,D. Pt. # 4 I. 1 A '4-
- 1. ] $,8 f LSI l253 Prescurc # 1
- 4. O 7 3 W.663
.50052-NOO4L Pressure <! 2 (SPARE) l ,Y (, */ (.4 64.*/ci~7 r L / 4 (,- P fr 7 2,4-D. Pt. - Dow Point RilD - Relative !!u:.idity Detcetor, ,.,_.'.n )39 i.m 'i d
- Pressure, Teminal Operator e'
aA 3/16/79 OPER ATI!:G PROCFDURE 13100.1, PAGE 53 INTECR ATED I.CAK RATE TEST APPEfDIX D AMBIE!.'T TC1PERATURE 70 HOUR NO. BAROMETRIC PRESSURE 3D I h DATE /M // # W ROT / DIETER FLOW VERIFIED BY ILRT DATA SHEET T D1E /S AMPl.t' !!O. O9CO/ 2..~') C9I3 / 2 C, c996/ 2 '7 CN -7/ ?_. & RTD # 1 6;s40 D l. ;, 7 8/ 30 P l. ?_ t_ RTD (8 2 F e f Ic N'. ! 7 "- C r :- "c / t-RTD # 3 74 '/s j 79 So 10 Fr / v.s 7 RTD 4 4 79 94-l 79 9L 7' '/ RTD # 5 79 86 79 EG-N n>
- 79. ss e
RTD # 6 79 ?O 79 L-P-7 9 t-L-79 te 3 RTD # 7 79./4 79 72_ 79,7/ 74 7c RTD # 8 79,7) ?9 77. ? 'i 7/ 7-) 7 0 RTD # 9
- 7094, 79 4r N 2 0 74 NF RTD # 10 7 + -ib 79 56 7 (-). % "/
7" S fc RTD d 11 79ZT 79 24-79 74-
- hi72, RTD v 12 79 14-77 f3 7 ': i; N
'Z. RTD # 13 7M 96 /6 96 JM 'n 7 9 ') r RTD # 14 /9 2./ 79 2 L / 4. 7 c. 70.?I RTD 0 !$ 7 9. SO ry.4 9
- 79. J >
7,4[ RTD # 16 7 9 2. T 79 14-74 > 7 -923 RTD P 17 ?b bl 7L.YO }& P/ 7 %.70 RTD # lb 7 't..J -i 7').15 7 :- .1 /. .1 9 RTD # 19 7F.9 5 7X 94 7,4 9V > w < d. RTD I' 2D 7 9 <> 3 7F-O? 7" o? ^' RTD r. 21 (.3 PAR E ) M /.4 8 F/ di '- /. $ 4 As
- 2. 7 RTD # 22 (S PARE )
PO.12. - Fo c9 ecc6 Fo Oa D. Pt. # 1 'l 40/ l.405 I.dC:3 /. 4 Q :i D. Pt. u 2 1 2.33 I.13'? I 7.39 !- Zd 2. D. Pt. i 3 1
- 7. 334-t 2.46 I>,5 1 2 4 '.-
D. Pt. # 4 f. 2 '3 ') l 233 i. 2 5 '-)
- 1. Z ic 2 -
Pressure # 1 f%-0 3 3 8007 S'
- /cC17 P ce il Pressure e 2 (S PARE) t 7 2 (c h 7/l-t(c 7/ A t /c L D. Pt. - Dew Point RllD - Relative Humidity Detector, q.,,,
3gg csiJ itv
- Pressure, Terminal Operator
3/16/79 OPERATINC PROCEDURC 13100.1, PAGE S3 1NTIT; RATED 1.EAK R ATE TEST APPEND 7X D AMBIENT TDIPERATURE 72 HOUR NO. BAROMETRIC PRESSURE il DATE /&2 W ROTAMETER FLOW VERIFIED BY ILRT DATA SIIEET TIME /SA'iPLE NO. /CCO / D / 01 5 / 3C 1030/ 3I Ic4T/ 37__ RTD # 1 P. I I L~ ?I C '7 Y'l. 03 ? {' Hle \\. RTD # 2 F r3, O 3 74.40 /9 07 7'-L ':4-RTD # 3 70 F, T "' c RTD # 4 ~7 9..v 7 In c3 ' f-JT 7-9 ' d-RTD # 5 7 /. . D -, 77 J '; 7 L-5 RTD i; 6 7 9 v. I 7 c.. -i 9 74. % 79 wa-RTD # 7 79.70 70 70 74 (ch ~7 9 f.-te RTD # P 79.!S .^) ! 7 7 4 G 5^ U 7+. RTD I! 9 79.97 70 .u 7 70 s c.. c, 1 RTD & 10 '/ % '3 5- 'O % 7s '56 7 -) r> RTD # 11 79 23 74 2L /9 E' 7a zu RTD I' 12 7 9. # 2__ '7 0. / 2_._ /4.ti 7'i li RTD # 13 78.9'i ' M 9 -J 7h 9 ? 7 N.') 4 RTD # 14 P). 2 8 lb Eu i'*.I'r RTD # 15
- 74. 4 r, 7447
/ca a 7 79 : t. RTD # 16 79 2.3 79 _7 3 e 4 73 79 ) e RTD f 17 7 Y. t-l 76 y < ii. c : / h. /'9 RTD # 18 7 ".1 ? -~ -7 41 2-V -e l_ RTD # 19 78 94-7H 9 -7 /.w.9 -3 /r~ 0 2_ RTD # 20 7 0. ') $ /u 4L /A 92.- /M 4L RTD i. 21 (.s i>A R E ) F i
- 7. 0
-f./a-e i c +. .% i. f.. i RTD # 22 (S PARE ) 79 99 79 9 tg /993 799 C D. Pt. # 1 t.406 /4CC i 34 2 J. i t3 / D. Pt. /! 2 1246 / 2d 7 1 2.19 .752, D. Pt. i: 3 I L4 7 I ' -t te 1 1 4.'_ i i Sf' k D. Pt. # 4 f.Z S9 l. ' I-h 1.763 i / ic h i Pressure M 1 S(c CO 2.-- PS 9 C)3 c 59P T-P 7).C C..- Pressure i! 2 (SPARE) F, t - (c 9 4 - ,.: te T. - . ec L 'e e c e-(c /a D. Pt. - Dew Point RilD - Relative llumidity Detector, 9 " * ') 19 .v il
- Pressure, ferminal Operator
.e
3/16/79 OPERATI!;C PROCEDur9 13100.1, PACE 53 I f3 TIT.R ATI:n i.!:AK H ATE TI'.ST API'E!! DIX D o AMBIE!!T TDIPERATURE '7 2._ HOUR NO. BAROiETRIC PRFSSURE 3 C). / 7 DATE / /M W ROTA!iETER FLON VERIFIED BY ILRT DATA SHEET ' ~ - TIME /SAMPl.E ??O. / /00 / 3:5 f)ff / E,4 l l 30 / 2' T l 121F/ >_,4 RTD # 1 T-- O. 9(* M C1.,5 4 l'2 D, '7 9 ucs.7-T t RTD # 2 79 91 79. P F. 7 7 9,Fc./'4 7 9 P -ii RTD e 3 7-) 79 7c3 76 ~7 V' /, 7 7 79 77 RTD # 4 2 9."- > 1HH? 7 P'i l~' l V ^ '9 N. L. RTD U S /9 7_7-7C) 70 7 %. fc 4 ?Q U9 RTD U 6 79.*57-79 SO 79.47
- 7) a7 RTD #
7 7 C). 6+ 79 Ic 5 7 9. (c 4-7 9 G4-RTD # 8 '7C../c M 74 .'c t 7 4 Ic i 7 -) cc RTD # 9 7 9. ! ;, 74 76 7 -) -b + N " (.- RTD # 10 79 9) 79 49 79.49 74 2.0 RTD # 11 70 I P-7 ') l b 74.I7 79 I 7 RTD u 12 /g 09 14.#o 79 fi 74 O RTD # 13 7A. O 5 7X c1L. 78. 9 F, 7 8 w r.- RTD # 14 7 '9. /.5 7 9. f c-79. l ?> /9/r RTD 0 lb 7'). A G-7H % 7 H-4 7 7 9..lv RTD # 16 79 20 79 ?_t 7 9 2.f ~' o it RTD # 17 /F.MO 7,M.X I 78,60 7F E 7_, RTD v 18 ^> 4<- 79t-A> 4 2 - / '> RTD # 19 7M. 9 2 78 MO 78.9/ 7 r -9
- RTD # 20 7 8 C).7 7.% 9 8 7V 97 7M
'2> RTD i. 21 (S i>ARE ) PV '. 4 /., FL 90 ue /.5 u(- ct MTD # 22 (S PARE) 7C). F G.- 79 84-7 C). 8 2-. J9 i ; ~ D. Pt. # 1 l 390 J. 3F. 7 f. 3 F3 i '5f-S D. Pt. # 2 I..: 5 'i / ' b C-I. Z ic 2. - f 7 L => D. Pt. i-3 i c tc4-e, > tc o i Z. / /. / vc; 't. D. Pt. # 4 l. 7_7 Z i. 2 7d l. Z. 7 7 l /_. / 9 Pressurc # 1 A T4 7d E. 59 Ic 9 F '3L) (? 5 i '. 5 9 '5 b Pressure v 2 (SPARE) 5. If /0 /r 7 A e rc /c f P Ic/c 5'5 Abeic D. Pt. - Dew Point. EllD - Relative Huctidity Detcetor, },' ].] l l. u) q'
- Pressure, Terminal Operator
3/16/79 OPERAT7!ic PROCEDURE 13100.1, PAGE 53 I NTVCH AT!:!) I.1:AK lt ATE TI:ST APPENDIX D AMBIE!1T TRIPERATURE 7 2-HOUR NO. A? #Ad 7 BAR0!iETRIC PRESSURE DATE ROTA!!ETER FLOW VERIFIED BY ILRT DATA SilEET TntE/sA!irl.E !:0. l? 00 / 37 f 115/ Ba LEY -3 9 1245~/ 40 RTD # I b'Q 7 O DC- (c 's
- 20.5 7
'$O 35 RTD # 2 ? ') P.2 ~7 9 c' O W 7'T - ci 70 RTD C 3 i -> - 7 G> 7 k* 75 7cf ' tH ~7'n ~7 c.:- RTD # 4 7 0 T' / 79 ?^ I r Ci. 7'- 4 -') RTD # 5 7 C) I.: 7 7 % - U (.: 'T9, W '7'4 'A RTD (/ 6 79 415 74 43
- 76. 4-I
-<-e d/ RTD # 7 7 0. /c - 7 9.(c4 - ' 7<-/ /_, '3 ~b ra2 o RTD # 8 7 '/ (c 0 7 9 -5 F '7C/ M 7 7c' Ko RTD 0 4 7H ML. 74. FA-jc1, % *7, 7 '. G 2 RTD # 10 794h 79 49 W. 4-H W ':- 7 RTD # 11 79 17 ~74.I7 '~7 C, t5 - ' - <.. fi / RTD v 12 79 /o 7 c) /o M cf, c c7 -0
- cs RTD # 13 7F
(,' fc 7F 0 - ,o pet 'i G.: 5 RTD # 14 /9. / 5) 79#9 74 rF9 - ce r4 RTD # l$ / c) 4 / 7 9.c v w m3 7G u; RTD # 16 79 2C 79 70 75/ 7a 7C RTD l' 17 Jh. H I 7P. bl ~1 Q O/ mO- % 2_ RTi> Il 18 /4 4 _d 70 43 m<f.% -a M RTD # 19 7M. 9 7_, 7A 91 78.Q/ ~7%' 9C RTD # 20 7 l-9L '7 5-e' 7 '~' 5 7 7I RTD r, 21 (S P.\\R E ) P-c'. 71 wa.y/ Go, o 7 go of RTD # 22 (S PARE) 79,79 79.75-7/.74 Fy. 7 7_ 0 D. Pt. # 1 t. 3 ?.~5 1 378.- /. 3EC / A 7c4 D. Pt. # 2 I ?_ L:T. I Z.7C'
- f.,T '74 1.
7_-,T D. Pt. F 3 l. ~/_. LW l ?71 /. 2 -7e_. "'O' . D. Pt. # 4 1 2 V4 - I ? W7 I, 2f C ~790 Pres r:ure # 1 4 5C2 5 3 P T-/d F. .:25944-
- 'es q
- o Pressure v 2 (S PAR E )
'. - (c Ica <- P L-fcGo 8 (, /'. -a:5 Ouro 'a. I D. Pt. - Dew Point RllD - Relative Humidity Detector, ~1 ' '. I 'l ! ') J 7 -- io ec
- Pressure, Terminal Operator
3/16/79 Ol'ERATING PROCEDURE 13100.1, PACE 53 INTirR ATI:D I.!:AK R ATE TEST APPENDIX D AMBIENT TDIPERATURE 7Z HOUR NO. BAROMETRIC PRESSURE 5 O. t 7_ DATE / MM 7f ROTAMETER FLCW VERIFIED BY ILRT DATA S11EET TIME /S AMPl.E "O. t ; I) / di i3 iei / 42 / SOC / 43 /346/44 RTD # 1 96,So 6C,47 C;O 42-SO 29 RTD # 2 7C1 7/t %. 72 79. 70 ' c' RTD 0 3 ict. 9]_ 7 c.y 7p 7:1 7? mcs rc RTD # 4 7'1 T'.s ?C' T7 7=.' 7 1:, T: RTD # 5 ~19 (s 2. ' 7 ? W/ '9Ct t, r '74.6N C RTD # 6 ~79,--p, 7c/, % 7 7cf. 2j=5 79, u;. RTD 0 7 '7c7 Q2_ ' + r( ~ ~Ff. /c f
- -7Q '_ -C s
RTD # 8 W,W6 74,W- %/, T3 l '7". Q RTU # 9 79 *7f-). Y 9C ' T i 7:-) '!~ u RTD # 10 W,4-9 ~7'-r. 4 /s W.4 3 --f ;'. M RTD # 11 7G.fes 7:r i3 7-/. I a- %' IO RTD 11 12 '7 1 Tf '-rci r o '7ay LA' T1 rp RTD # 13 7> C/5 -'O C?:- 7' L (,a -o% RTD # 14 ~l'f. / 7 7 'l. i '.) ~Y). I?_'. ~7G ' 's~ RTD # 15 '7cy zud ~F-1 G;
- 39.t45
~7=f :-6 n~ RTD # 16 - 7< r, sQ 74 ?_(_> '7c/ f9 '7' f a RTD l' 17 ~ 70. Pn 70 C/ 3 ? %'O -7G B C RTD # 18 C - / r, a ci 7Cr 46 W.4e 7 <-r. W RTD # 19 71:23. 9 0 ~7R C-9 l% %4 7 ' *, '~.9 RTD l' 20 7 'i Cf/ M, ;f 2 T.; J-r p 7 'A c C r RTD (< 21 (5 i'A R E ) Ws, c-i7 4o,62 M C,ep-r ya y RTD # 22 (S PARE ) 7CL lO 7;7,(g9 T -/ ( 6 7(-r, /g D. Pt. # 1 /, 9 '7 4 i, 'A'7 2 /,3/sM t. 7 q /-r D. Pt. # 2
- p. 2 '. O i 2( A r,
2_c;'O I_ -' P a D. Pt. ii 3 /, 2 7 "; _N S r,.Lct 1 i T ' .1 (. D. Pt. # 4 / 2.94 t,294 /, >$1cf i, -2c/ Pressure # 1 C,9 'A 5 icf '> i <'4 c/ 2-r G ~~; '/ '_ 4 Pressure <! 2 (SPARE) l R'/g/p 2 7 M /;/j
- 7. 2 g /_, (, / 9 9, o /J j :5 D. Pt. - Dow Point RilD - Relative Humidity Detector, 2X J 124-
- Pressure, Tcminal Operator e e 1..
- 3/16/79 OPERATI!;G PROCEDURE 13100.1 PACE 53 1!!TI:CR ATI:D !.!:AK R ATE TEST APPENDTX D AM31EllT TDIPERATURE 7 2.
HOUR NO. BAROMETRIC PRESSURE TC,/0-DATE M/ - ~[h / ROTA!!ETER FLOW VERIFIED BY ILRT DATA SilEET TIlf t:/S AMP!.E !:0. ST / /- E O 4(4 / /zl- / 4 4~///@a 2fF / 445 g RTD # 1 ,C(f. :t4 C(5. 7_9/ 80,ZG
- 90. Z 7_ _.
RTD # 2 -'79. /. : /. 7G./A 7C/ /. 2, 7 f/. /_ 7_ t RTD # 3 - 7cf. t Cf mq, C :'7 7:/ r 4 o _ ^7 RTD # 4 Tf-f I% 7'i. *T ~- 7=!, 7 I 7c' '7 : RTD # 5 7'4.57 /4. % W,65 ~7c/ e 5 RTD (/ 6 7 ry, 22f $ 7c1, 31 -7 9, 'E.> % 2G RTD # 7 ~7Cf. '30 3C],C-f1 79. '-Ff '7Ci.' ~ RTD # 8 -7Cr.+s'7_ -~l 9 A t - Ic;. 47/ 79.ci'r RTD I' 9 7 'r. G -- -74/ 'M 7-t. 5 O ~7'r, ?rr RTD # 10 ' 7Cr. 4+-5 -~l9 4.'A fFW 2e.&L 7/.4 :s r RTD # 11 '7"f, / Z %,// ' J 4, / 2 P // RTD (/ 12 ~7 cv (/;2 72) e-(,,, - 7e-r e.c _, wG RTD # 13 ~7CJ e/ - H 92 N;. -I 3 '7' x-2 RTD l' 14 W /f, 7Cr 0 ~7Cf. f 5 TJ / 4" RTU # 15 7'? 4s3 ?'/ f43 ' 7ct,t.us
- 91. f.4'A RTD # 16 7'r,/9 77 jf' 7ci, /G 4
7 7. /(,, RTD l' 17 T T/ % GC ' 7 77 -.'<.^7 RT D l' 18 <t:r.4 7 - P/, c.1.~/ 7c./ 4./J/ 7:r C4 RTD # 19 7 9. %Ci - 7R F-54 ~79'. MS 7A WR i RTD # 20 7 8,C// "B CJy > 7 w,cfi -7'T C g / RTD // 21 ( h PARF. ) R 0.41 1 e ':7 5 -s o c.g 3 p /- a c/ RTD # 22 (S PARE ) 7CF, e-.'/_ -'7Cf,6c1 - /C/ q7 7",.~, /, l D. Pt. # I /. 2/ 4 t. ~3 f, l /, MQ / x 4.a t D. Pt. # 2 /, 2c. f f /, 9c/ / /. -',c/ 7 / ~__ c7 P D. Yt. i: 3
- i..2. %t t, 7-.cits
/
- a.
~% i = o.7. D. Pt. # 4 s. ~:RA
- t. 9/Y7
/, % i0 / 5// Prent:urc # 1 ('54 19 FW~l t 6 th 221I5 Di',4 lN Pressure t' 2 (S PAR E) p fa /0 CFf M G D CJ s C' r, /~.,,fA n:'-5Mr D. Pt. - Dew Point _ RilD - Relative Humidity Detcetor,
- IYessure, Terminal Operator
3/16/79 Ol'ERATING PROCEDU:tn 13100.1, PAGE 53 INTIT.II ATI:n f.EAK P ATI: TEST APPENDIX D AMBIEliT TDiPERATURE 110UR 110. BAROIiETRIC PRESSURE OO, dk$ DATE /k MA/2 ROTAliETER FLON VERIFIED BY ILRT DATA SilEET TI!1E/S AMPl.E No. /4C0 / 49 / ^5 /M/ O /6M 51 /@$/ M2. RTD 0 1 TG * /$ $U* /[ 20 /l f%.0% RTD C 2 i/ /. n ?/ p/ ~/ c,. c y m r. ry p RTD # 3 7'/ /./. 7-/ '. i' 74/ (44 7 9.'s_3 RTD 0 4 ~ % i '/ T' ./
- l
,.V 3 -1 .; ?* / '*}. 58 'Y'l -52.- '?? -5/
- 79. SC)
RTD 0 5 / RTD # 6 7/, J V 7'/,ffy -/%j/, 7c-t. M RTD 0 7 7// i T 7/ -3 7 79-f 7 M C 6(., / ~ RTD 0 8 1'l 4' 7/.47 l 'i 4 )
- 71.. />
RTD V 9 '/'I 'N/ ~2/ ?) lu #9') 3 c-r ~r-1 RTD 0 10 ')*/ J A 'N cJ2 - 1'7 *J 'L W?.'4 2 RTD 0 l1 N 10 7'i-V/ 7-1 &~/ 1 9.c.J4' RTD ti 12 1 11 (> ~~ -7't. :os ' 9 '/. /; r ~c;< 95 RTD # 13 Ci' c/ 't 7 (.' d 8 V/, / / ,e ii RTD 0 14 'Y/-) V ]? !V 7 ti / V 1u ta RTD 0 15 'J'/ 4 6 'it/. 4 J-2!/. 4 f '"iq,4.~7_ RTD # 16 //-/ / /. 7 /f' '/ y. / f 7'- t5 RTD l' 17 M' '7'/ ~7 9. M' ~' C '!' ~7 c' "' RTD # 16 e/ y. /</ /2/. 49 7'/..fo 1 cy.5 C RTD 0 19 '/f. ! y
- 79. Q /,,
7P, f 7 78 R7 RTD 0 20 '+ Yv / :, 6) /3,3 '; TW RTD ie 21 (S PARE ) 5 i, ff 5r./I en. / g' N c). f'3 / MTD # 22 (S PARE) ?'/,C3 7/ f/ 79.C/ -,)cf ef T i D. Pt. O I / :/(V /e 3(3 /. Jf/ 1 2 '= 0 D. Pt. 0 2 /&/ /- dC Y /- 3 0fr /.: ~ :$- D. Pt. i; 3 /- %' < t/- / it o :, / fG 'i 1 A t n' b. D. Pt. 0 4 /, 9 /_f /-i/T /_:4/.f /, O'm/ Pressure 4 I R'C#/89 76762 T f M96/ 3 9 i- "1 ;., / Pressure (? 2 (S PARC ) '(/s fv/.-- Q' /, ('/' t s'/3 _Cyc/ 0 /_ 3 -5 J '_., D. Pt. - Dew Point RllD - Relative ilumidity Detector, 3,.i q tq/ c_)tU ltO
- Pressure, Terminal Operator
3/16/79 Ol'ERATING PRDCEDUltn 13100.1. PAGE 53 I f1TEGR ATI:D f.!:AV. R ATE TI:ST APPEND 7X D AMBIE!IT TRIPERATURE ~T / !!OUR NO. BAROMETRIC PRESSURE N C8 DATE /4 Mao ~79 ROTAMETER TLOW VERIFIED BY ILRT DATA SilEET TIME /SAMPl.E NO. /6(C/ M /6/9 / Mll- /dM/ 65 //Ar/ % (' RTD # 1 5' O. C 6 $O.CQ Rv 60
- 79. V D RTD # 2
~79 $5 7C1 Cil '7't CU 7'l FI RTD # 3 79.03 7er. /. j_ 7~/. 'l 7:/ /. O RTD # 4 7c7. L,0 1 < i. /. l. 7</ ' i '/</. e. C RTD # 5 M SC 7-f. 4e1 7 (/, NK' '7't a P RTD v 6 7 c-t.1, 7';. ] d 71.2 5 7'/, 2 / RTD # 7 ~7 <=1,5<o T 'i. 5 G 7'l sh 'iQ 57 RTD # 8 7 c.; a9
- 3., A (~
}/.itc
- 79..; j RTD # 9
- 7e9 7Q -7c't. 7 ; 7 t. 7 :- 7 '/. 1/ RTD # 10 ~T-1. 4-I X) G t ~7ti L I 21 JD RTD # 11 %. C8' Fi. O P ?'t A '/'/ e / RTD te 12 7<-t.Cc. 70
- r. c 1
?q.. > c- /v. c y RTD # 13 '7 8,cy g 7 e f), n,e f 2,_ y e,qo RTD # 14 ' H. tw 7(/, t'l..ja ~74.IC 'i~/. s s RTD # 1$ %. '* t ?/.4i 7's. 4 ( 7 v. 40 RTD # 16 ~79,t6 ~7't 1 (. 74.I 3 7(/ /9 RTD # 17 '78, '7-f / 4' 7 V 79, JV 7t.77 RTD (! l8 7 c1. 2,( , - / c., > 7. <- e i 7 <.* :/ RTD # 19 %, 93 7 7V, Q7 77.i7 ? % G /, MTD # 20 %. 'rff ~X. csn T<. ?9 K i'? RTD r. 21 (., P.4 R E ) l pg o eA er. <v, i n n,- M,.L RTD # 22 (S PARE ) l '7:5',4 7 7ri, a ; 79 4/_ 7 y.,lf D. Pt. # 1 /.2cQ /. 3r/f' /.333 /, y3' P D. Pt. '? 2 1, _% Ia / 4C.O J. n / /.e /. 2 :: o D. Pt. i; 3 f, 93 /. a / g_ f. 4,9
- f. ga/
-. D. Pt. # 4 1, 3 16
- j. *dDd>
/. 3 *i9 /. 3s () Prescurc # 1 42%'V 3 Rfr G r C4-( / (' fqN c Prennure e 2 (S PARE ) 8,AR 9 N'(o s \\f/ N /,,s 7 / 3 (. C N D. Pt. - Dew Point RllD - Relative Humidity Dctcetor, 3,? 9 , 9.y
- Pressure,
<a9o IL/ Terminal Operator e d. --
3/16/79 Ol'ERATI!ic Pn0CCDUnn 13!00.1. PACE 53 I fiTECit ATED I.CAK ItATE TEST APPENDTX D AMBIE!iT TI21PERATURE 7/ !!OUR NO. 3b075~ DATE / [//9/d 7k BAROMETRIC I?. ESSURE ROTA!!ETER FLOW VERIFIED BY ILRT DATA SilEET Tn!E/SAMP1.E NO. /7BB / ['2 /7/$~/ Sr /750/.f9 / 7~/d 6d RTD 0 1 ')'). 'j3 9[]. '}/)
- 19. Yf
'7d. W ( / RTD 0 2 1') f/ ' 7 'I 'Ej 7'). c/ ') 'st..J 7 RTD P 3 9'1 d,0 1c/.y :/ 54.sv 'ir;. :[ PTD 0 4 7'/. l, d 'r; .d ' ' -i RTD 0 5 7'/../ '7 ') cf JJ, l'/ J/f ')-/ U C RTD C 6 ']'). J / T/ *)n 1'l- / () '7:7 / 't RTD 0 7 '7'/, ff 7'/. CC 7'/. -id '75/ OZ RTD 0 8 7'/ Jii 7'/. d2 1'/. J/ " T:s J / RTD V 9 '?'/ /'/ '2's
- 4
^ /, :') 'i RTD 0 10 T/ J/ 2 ~j JO "2: .$ 'I'i, ili) RTD 0 11 'Id R', G'/. C.?> ], (?. n't. o G RTD l' 12 '}').C.i/ '):/. n,i C:t. o b '/:1. c. '), RTD 0 13 '] ?. 'M '7 Y H/ 'I C C
- X
'l RTD l' 14 'Xi. /d ')'l / b ') 4,':; ').'), " RTD 0 lb 'isf J i ~7cy. a ) <;+/. agi -py,an ~. RTD # 16 'l'/ 6'/ 7(/ i.; O ' ' if 9 RTD 0 17 '79.77 77 71 O P, '7'? 4:2 70 RTD C 18 i-) t12 7'l. J 7 ')-/ ti / ' c;4 7 i RTD 0 19 J ?, W, '/ ?. V L ' N. fd 'i P,3 / RTD 0 20 ' t, '< ' / 7 k J */ 'r,
- '/
'." A / RTD (. 21 (5 PARE) /'/ '/'/ 7'r. '/ 7 ' / /. W/ q'/.'/ / RTD 0 22 (S PARE ) 7-/ dt/ 7/ /'4 '/ '/, 44'2 'Y/ d '2._- D. Pt. 0 ) /, 6-39 /. 3 ff /,.3 c/f) /. 5 q ? D. Pt. 0 2 /-J"2n /f2[ /.. 5..; t, / - k -l D. Vt. F 3 /. 9 'd 5' }._4st' / a27 / 'a x o D. Pt. 0 4 / -i3L / 3-3 /z, /. 4 3/., /. 3.3V Pressurc 0 1 65 V/ ~f7C C f Y'7/- C'D'73 Prensure (! 2 (S PAR E ) ? 6 f7.l4 % f/N $ ra (f rf., $ (,- q d i D. Pt. - Dow Point RilD - Relative liumidity Detector, 'q 1qn J l.O
- Pressure, Terminal Operator
-s -.~ 3/16/79 OPERATING PROCEDURE 13100.1 PACE 53 J NTirR ATI:D f.I:AK R ATE TEST APPEllDTX D AMBIENT TD1PERATURE !!OUR NO. hO. d[ DATE N AR 7f BAROMETRIC PRESSURE ROTAMETER FLC11 VERIFIED BY ILRT DATA SilEET TInR/sAuPl.E no. L??/) / ?/ if/f/ d2 // fat 63 /F(.N] /d ( RTD & 1 '74 P1 79.7T 7 M. ~7 0- ~7 (/ ~7 3 RTD # 2 7 (-i.G 0, ~l' I, LA 5 ~~7 (f f.4 u 7ef, u 1 RTD # 3 ~/ C. 5 \\ L 7'/, 5 7 ~70 4'/ - 7 <1 ee f RTD # 4 '7's. V i
- i 's b L 7'l. bG
~7'1 f-.C RTD # 5 7':). $ l 7ef. # 3 ~7 C. # ')' ~7<1. 4 / t RTD 11 6 2C1. f '7 ~7 ei. / 2 ~7 Cf. / /s ~7CI, I 5 RTD # 7 7#.C f 74,6 % '79. 6G 7 4, f G-1 RTD # 8 1 (1 A f 7 'i. ',/ t ' ~7 (1, 29 -7 6. 3 7 RTD # 9 "r-f 7 <' - ~7 ' t 77 -7ei. 7 A 7 <7. 7 3 RTD # 10 '/ci.'3Crctra 7 'i. 3'/ ~7 C. S F 7</. 2. 7 f RTD # 11 ~F1. O t, 7C1 c.,6 ~7t/. CU '1 ti. 6 -)- RTD t/ 12 ~7C.r.;L 7(i ,.~"J. 7 9. &J., 7G e c. t RTD # 13 ~7s.s ( ~J y a / 7r e 7 y f> Pc. RTD # 14 79.I 2_ 7 tJ, / 1. 7 <f, i t 7 <j, t g RTD # 15 '79. S<l 7 cf. A G' 7 '), 2 9 7 c/ gy RTD # 16 7'),e( 79 // -T cf, C L/ 7C/. c(/ RTD # 17 7 7.'7 (-, '7 P 7 C. 'l F 7 6 7F 7
- P.TD # IS 7'f. $18 70, $,/ ~3
~7 (i. 44) 7 ), 'N 6 RTD # 19 ~/4.V;l 7 F. P 2 7F. P % "? 9. F *1 RTD # 20 7G.R '/ f. F '/ 7 C(. MS' ~7f. f 7 RTD si 21 (SPARE) ~71 'i
- c) - B f 79. P 's 7ti. F b RTD # 22 (S PARE )
- 71. d.O 7 <G, g ej q q, -ef;
-7c/, p/ D. Pt. # 1 1,537 1, ~3'3 6 l, 736 i, 7% D. Pt. G 2 f. R '5 *7 ) 334 1, 3 ~A L.s I. TU D. Pt. i: 3 I. 2 R 'L I b h *) r ~2,'2.') I 4 2 ** D. Pt. # 4
- 1. %d.%
i* 3J V I 7_ J 9 r, ~362 psm&& Pressurc # 1 '2 C'2 ~/ f $686A O& ' ' ' - r til [-- 6 #6 L./ Pressure r! 2 (S PARE) C' / : C / - 7_ /m-L, 6 5 9 F8 9 67 ' 9/;_4 C d c D. Pt. - Dew Point RilD - Relative lluctidity Detector, 1 1 110 ~
- 2.. ; i U l.L 7
- Pressure, Terminal Operator aP
e 3/16/79 OPERATINC PROCEDUnr. 13100.1, PACE S3 llrr!T.R ATI:D I.1:AK !! ATE TI:ST APPENDTX D AMBIENT TI21PERATURE bb 110UR NO. BAR0!iETRIC PRESSURE 80 p37E /q7q ROTAliETER FLO!! VERIFIED BY ILRT DATA ':llEET TI11E/ SAMPLE NO. /Oro /[6 /4/5 /66 /e7 A- / /.7 / 4 d 6 / /.'a 8 RTD # 1 7 9,"7 / 7'7, (-(/ 7 (i, /., 6 7'/.6c! RTD # 2 "74, u n 7 C) i L4 0 79,3Q -79 '4 5 RTD # 3 ~7(/, 6 6 '7'/..o d. 7cf. 6 d. 7(i Ad RTD # 4 '7e t. ei a f ~79.'59 29 @ ~7"/ ^ RTD # 5 74/. O o ~7e/, u o Wf. 8t/ 7e/ 2 r' RTD # 6 "7(f, i L.4 7(/. 1 '6 7 c). /'J-RTD # 7 ~1Tr. 5 i 79 6/ Tr.51 74c Si RTD # 8 7C, ~% -?"/. 2 G 7cf, 4 u 79, 3Q f RTD F 9 7(i.76 7 't. 7 7 7C. '7 6 "/ct.1 % f RTD # 10 ~7 '/. 3 7 7/.'67 7 4. '$ $ ? </, % RTD # 11 7(/. O 3 '7 4, c 1 79 M1 ~6 c 'A RTD u 12 7C. ro 7C (Ic/
- o (;9 79 r/ r/
f RTD # 13 -78 9 9 7 A' R d 7 F. F3 "/ O F4 RTD # 14 "'14, I # 7(( lO one 7'/. 0 9 79. 6c/ RTD # 1$ '7 (I. '4 F ~7C4 6 ~/ / ;2j; 79_ g 6 7t), "4 L, RTD # 16 7 9. O ~7 '7(f. 09 -7 r; 6(l '7c7 c3 RTD # 17 7K, 7 V ~79. '7 y-7 9 ~7 '5 -!E. 7 '5 RTD # 18 ~1 G, ~4 c7 --e f, "v( 1O_77 -7'/. 4 C, RTD # It) - 1 P. 5. I ~7 /1' Ro 7f. 7 6 7R )?/ RTD # 20 ~7 E. W 7 ~1P C"7 9P S' 7 7 C.'& RTD F 21 (SPARE) 7 '). 7 7 7' f. 7 6 7 9.~1 V 7 ci, 71 RTD # 22 (S PARE) '/c/, 3 G ~7(7, 3 (, ~1 c). '3 L.,/ 7 9. 'd a' D. Pt. # 1 1 'd 3 6 l _3 2,y ), g -26
- i. 335 D.
Pt. # 2 / 2,9 (( ) ~A 4 C
- l. 6UG i. 3 4 LJ D.
Pt. F 3 I. M f 'f o, ^AujtJ t. ~2> 'N 7 s.%44 k_..D. Pt. # 4 l. 369 i, ~2, S t.J i. % S L/ ). 356 Pressurc # 1 85 60t 8 5 e 6ct M6 e57 _6' 5 Rea'. Pressure v 2 (S PARE ) 66 55-) 8635'O E-(~ S u.ds 66,546 D. Pt. - Dew Point RllD - Relative !!unidity Detector, 7 na J
- Pressure, Teminal Operator eo *
-m.
3/16/79 OPERATING PROCEDURE 13100.1, PAGE 53 I NTII;R ATI:D I.EAK H ATE TEST g ENDIX D /f AlfBIENT TDiPERATURE te-w Il0UR NO. DAR0 METRIC PRESSURE 3bsOkO DATE I /t7 9 / ' ROTAMETER FLOW VERIFIED BY ILRT DATA SHEET TIME /SAMPl.E NO. @/r0 / Sk TJ6 / 7# MO7c/ 7/ 1'd S/ 7 S. ( RTD # 1 74/.6-3 ~ 7 C/ M 7(/,66 7'l 6d RTD # 2 7 c/, 'A Q 7 </, T '1 -79 R L-, "7ti '4 5 RTD # 3 7t/, 4 d '7 <i 4 u 7 ri, 5 3 7 <i 6a RTD # 4 7(f. 69 ~7 (/. 5 2 7 c7 46 ni r6 RTD # 5 7cj, g g 79,29 7 9, p(., -7cf % RTD v 6 753, o, 7'/.I'L 7(f. It o i. C 'T c RTD # 7' '79 % ~7 6, 6'J-7c7 5 i '79. S o _ RTD # 8 ~7G. 3 4 '7/, 3 '.% "/4/ 3 1 '7 l. W # E RTD # 9 9 c). ~7 'A M n, "J J ~7'i 7 ! ~10 ~1 l RTD # 10 74. W.,, 79, Ele 7(i, 36 7/i '2 A RTD # 11 74/. c '2. 7 0. c 'A 79, C / 7/ (o RTD o 12
- 79. On m c/, to
~]R 4 't 9,^ ff F RTD # 13 79,8 3 7Q P') ~19 C*n ~7C' S o RTD # 14 79,09 7(i. e4 7C1 6 / 7c;, cP C RTD # 15 79.'57 7(/. 4'/ 79 -3 7 7 (f, R, RTD # 16 ~77. # 7 7'/, C/2 7/ N, 77 67 RTD P 17 7C 74 1R 7W 7 R 'I *b ~9 0 70-nTD v 18 va, 74.. '7t/ 4 -7G :7d 7</ 3E RTD # 19 7P 56 7F. f'O 92, Er' 7 ?, *7 9 RTD # 20 7# c'7 7CF7 7X F(. 7 ' ' 6 x RTu u al (SPARE) 7'/, d.#/ 7 (/, (.7 7 ci, A 6 ?c/,6 'A RTD # 22 (S PARE) 79 3d 7I. 3 (./ 7(/, 23 7(f. S fl. D. Pt. # 1 1 3'37 r. % '3 B /. 'No I -3 + u D. Pt. # 2 i,347 1, 350 /. 35/ L%3 D. Pt. F 3 \\ '% u Lt 1. S u ;> /. Mau l. A S -) . D. Pt. # 4 l. -2) 5(o I. 3 5c/ /. E SS
- 1. 3 9'd,.
Pressurc # 1 85P53 65A6/ e5 F :4(/ /MP47 Prer:sure e 2 (S PARE) J/.o 5 u u AA54& 8/o 6 a o 9 6 5 % C' D. Pt. - Dew Point EllD - Relative !!umidity Dctcetor,
- Pressure,
_)' A G 1)'1 l i ( s 't v Terminal Operator
3/16179 OPEnArznc rnocEDunE 13100.1, Pace 53 IfiTIT:R ATI:n I.I:AK N ATE TI:ST APPEllD7X D l AMBIENT T121PERATURE /O !!OUR NO. 3', 6 3//q / 7q BAROMETRIC PRESSURE 33TE ROTA!iETER FLOW VERIFIED BY 2h/,, ILRT DATA S!!EET yl 4 (.o
- '"6 TIME /S/JfPl.E NO.
J/co / 73 7//5 / 7M J / 3.' / 75 'M/7S ( RTD # 1 747, 9 1 7e/.60 7474 t, 7'/. W RTD # 2 "Wi 7' MO "4 % 9:l, 9 '). '7 G. k RTD # 3 1:1 52 Kl 5t 9t, So m<t, R o RTD # 4 '74 A.- ~/ t/ 9 7 c: 53 7ri 7, i' RTD # 5 ~7tl. % 7'l, 3 6 7'/. 9d 76 33 RTD ti 6
- 74. 6(-f 7cf oc/
'/c/, M/ 7 ef, c -7 RTD # 7 ~J'i U C] qcy Gl '7c{.LJ C) -syr 5 o RTD # 8 lCt. 9o C 9/,90 79 9A 7 c/, '1c/ RTD P 9 7cl. 9 'd - I ri, ' / J-7cf, f 7 9 <j_ ! -y RTD # 10 ~7'/, 3 5 -7 (/. 36 ~7"j. 3 '5 7 e). ?4 RTD 3 11 7 '/, cec' 7f/ CO 7 M (/ Q 7 4 (f o RTD is 12 7 /d (/ (( 74 (/ n '7 ;< 9 '7 7 fi (f>: RTD # 13 7 C' !.'i ~7 C' i'l 7 F I' f 7 9 . RTD # 14 7e?. 01 ~74,6(f '7(1.C'S -7</,0-7 RTD # 15 7Ci 7 tf. :(4-, 7 (/ ~3 '> '7 '/, 34./ RTD # 16 70, C6 7rl (6 -7c/, Ed ? <?, c 6 RTD # 17 ~7#, ~7 G 74~7/ ~79 7"7 7 C "? / P.TD # 18 -~ </ '4 c.J
- 74. 6 3 7*'t, 3 ~.2.
r c), 8# RTD # 19 -7,C', 7 f/ 7f.C'o 78, 7e '
- S. 7 y c
RTD l' 20 7 . F(. ~7 c', C '7 7?. FC, > F t:(- RTD (e 21 (S PARE ) 7 G, d. / / cf, gg /rf q, 7cj, c;. RTD # 22 (S PARE ) 7 Q, 3 C. 7(J,30 7ef, sc/ -;c/, ~24 D. Pt. # 1 l o 'S 3 9 l 3 UG l. 3 L/ '-l I, R S '). D. Pt. # 2 /, "$ 61 / 3 6 'l /, 3 T(., / 34 7 D. Yt. i 3 6 ';$ U G i ~56;D r 9 KC i "-7 F '.1. C D.~ Pt. # 4 l, S 5 6 / 'A /o O /. A 6 3. /. 4 6 3 Prcncurc # 1 ? 5.Ou 6 2DPUU d55 CU'l- <=' S ? V C Pressure v 2 (S PARE) 8 6, $ 2. 7 84,5S') CO $ 3 '1 2 6.5 N 9 D. Pt. - Dew Point RilD - Relative !!umidity Detect'r, [, u', ' ') j Qt
- Pressure, Teminal Operator
3/16/79 OPERAT71 C PRDCEDURE 1310D.1 PACE 53 IfrilT.R ATED I.!:AK 1( ATE TEST APPEllDTX D AMBIE!iT TDtPERATURE !!OUR NO. M//1/71 DAR0 METRIC PP. ESSURE '30. C95 oATE ROTAlfETER FLOW VERIFIED BY e 14RT AT;9/eT ILRT DATA SilEET TIME /SAMPl.E NO. .2766/ 77 2f/S7 7 b' 2N/ W 12dN \\ RTD 0 1 'l't'.d / 70 33 'N 5% '7'i. S'L \\ RTD 0 2 '?'1 3 / ~7 l 3 / 'W 5/ 'l!I. h ' '> ~ E' RTD e 3 'h/. >~/ /C).50 'I'l-O O GU nr Y} RTD e 4 ^'l ~th ~~ C 1. "I *i2- ' i 0' RTD 0 5 7'? 5'/ 79 5; 'i 'l *4.'i -- 'l /. *d 3 p RTD il 6 J')./M/ '2'y.0 f?' 9'/. O'? '/'/. O (> RTD 0 7 7/. fD 'M. i/ ~19 ~iO '/4 Y'1 RTD 0 8 }'/ J'i ?/. }'1 2 'l. *) 4 i'/# 4 ~7 N RTU V 9 ')'l. /. /. ')') s.1
- 10 - l s
- 7')
- / /
RTD 0 10 'i'l. is' 74 44 29 E'S '70. 3 ' \\ RTD n 11 7 T ')? 79.ri ? ?? -l'l 7 Y* G '1 ) RTD re 12 7f. '1 (' -7 V 'f V 6(. 0 ( < ;/ / / RTD 0 13 ~)?. if) '7 G 50 Ge'.Fil M.Yi RTD 0 14 ~7'7. e / 7') - 0 V Gri.07 7't O 7 RTD 0 15 7/.;'r., 7 o. 2 s'- -7ef. 4,
- q M n
RTD 0 16 7/1 O 7 11.08/ 'If". N 7'-1. *' 6 RTD 0 17 ?f,7 / '7(~ 'V 44'0/ ~/ V ~71 77.77 RTD # 18 9</. / / 7/ - 3 2 - 7er. 4 / ' ;t. % > RTD 0 19 7 F.79 7 9 ~7 '/ '7.Y. 7'? '73.7'i RTD 0 20 '?f.P(. 7'r - -i (, , c.:1.2. - '/ '/ ?, 's7 /.1 RTD v 21 (SPARE) O'/. a,"~2_. 7 9 3'a e. .pf 7'147 RTD # 22 (S PARE) 9'/. "Y/ 7 e/.)c; '/ '/. _/9 74.2-i D. Pt. 0 1 /. '84 /. ]</ s / '2a/ R l *3i14 D. Pt. # 2 /.359 /. *; / / / h,o / d e,, / D. Pt. i: 3
- j. -f ff f
.] S~_.3 !. -:/..; i -w.', .. D. Pt. 0 4 /.3(.</ / - Bg, 5'" / 4 t.f /. -5/. rp Prensurc 0 1 S'.9 ? S'/ WE869 ?y~'/ "A' /. R <'~ Q 3 i ^~ Pressure i! 2 (S PARE) .M:' $ R/) f/o f f '/ Q-r Q << $d,c 2 /,. o D. Pt. - Dew Point RilD - Relative Humidity Dctcetor, "; ? A n 177 4 s 'r LJ lJJ
- Pressure, "I.IA IW
Terminal Operator ..L....
3/16/79 OPERATI :C PRDCEDU tB 13100.1, PACE 53 IllTV. Cit ATI:D I.!!AK 1( ATE TEST APPE!1 DIX D AMBIE!!T TD1PERATURE HOUR NO. 2 A M//d 7h BAROiETRIC PRESSURE 36./06 DATE // (// VERIFIED BY ('/ //. p/r/; ROTMiETER TLOW 'r. / / JLRT DATA S!!EET, A A TmEIS Atirl.E 1:0. 036/)/ ? 23/ s'/ 9 2890/ 2MS? RTD 0 1 ~~l ej,.y; j' f.,', '] y ) G../ 9_
- )q. 9 /
RTD # 2 74 f2 c J 74.Oc1 ' ; </ ') - 7C RTD l: 3 10, att it-s. 4 *v 7'/ J V 7 ' /.J 1 RTD C 4 1(l A ~1 '.'!? tb i ' l. -f / 7<!. S / RTD 0 5 1'( 7i ~1 G.*3 I 7 '}. 3 / 9'1 -3n RTD G 6 -7 cf, 0 5 ~70 O c, 7'/. 03 7 cy. py RTD # 7 it/ n.4Q 79. 4 C1 7(/. M'/ 7'/. E RTD # 8 -7'T, 2 1 7C. 2 7 7"/. A 7 7t/. J 7 3 RTD e 9 ~7 '1. /_. S -7 t ',. '. 3 7/ /. ( _ ~7'/.' ;2_ RTD # 10 ~7G, 'R Q '7 C. %L 7'/ s3 7'/. 63 1 RTD # 11 ~/G,C/~7 '7 R J 1 '7 R 'R 7%t/7 RTD is 12 -; (*. c/ 7 7 << ci 1 7'c '//,4 %. 4/ 7 RTD 0 13 %'. ~/ (( m. ~1 9 ? ? 7'/ 7 '. ',, RTD f 14 ~79, 0 7 ~7G c 7 7'/. 0 7 7'/ tM RTD # 15 7c/, 3 3 70. $q ftf. V.l - '7 'f. y 1 RTD # 16 "J // O 3 ' 74. O )_ "; e 2, 7/ C/ RTD # 17 1/' 7 '2-79.~/ 8 'IF. 7 / 778 RTD # 18 7'/, 30 78 T.. ? ' V.1/ P 7'1. 2 Y / RTD # !9 7 F. 7t? '7 '<. % 7?.77 77 M' RTD # 20 7#.b 6 74. i t.. ' i'. i f M ',4 / RTD r. 21 (S PARE ) ~/ci, u.4 -7el.u 2, 7e/. V / ~74 4 n RTD 0 22 (S PARE) 1 ~/(/, 'J/7 ~7(f. -) /o /4. !/f '79.75 D. Pt. 3 I l.36'2. /, 3(,3 / "u / /. 8/. / D. Pt. 0 2 )o A L-.(o l. W2- - f. R (d /.it,'/ D. Pt. i; 3 'A tz, '). f.q/.j j 6 -j V /.359 L, D. Pt. # 4
- 1. 5 'l I, 3 7 l
/. -i'77 /. 6 7 '.L ~ Presnitre # 1 8'5 8 'ilL 'r A V C9 3 3 T5?31 G2 20 , Prenstire !! 2 (S PARE ) 8 0 5'A 6 M S'fC 2 t/,.' n/ 5/,24 ',1 3 Rs 5 -) 1 D. Pt. - Dew Point RllD - Relative !!umidity Detector, 9,.,, hOk c.:.J
- Pressure, OIM Terminal Operator d
3/16/79 O!'ERATI: C PROCEDt!!:E !3100.1, PACE 53 I NTIT.R AT ED l.1:AR H ATF. TI:ST APPEllD7X D o AMBIENT TRIPERATURE !!OUR NO. 3 BAROMETRIC PRESSURE DATE -86 M42 D ROTAMETER TL0t1 MA /' '!d*- VERIFIED BY I f.H.RT DATA SHEEL ~ TIME /SAMPl.E No. Of06 / 8 00/r / S 0030/ 5 oc4 Q ( RTD # 1 ~76 74 77.2 0 '7'/. / '7 '77e / 7 RTD 0 2 7Cl 2 7
- 79. 17
% 27 'T lb RTD # 3 79.4 7 7997 7y 9 L 7 <7. 6 RTD # 4 79, JC 7'I FO 7 ',' eT. 71, d RTD 0 5 79 30 7<i. 30 '79. 2 X 79 2 Y RTD 11 6 pi. t' 3 79 0 A 76.02 79 0 J. RTD # 7 79-41 7<7. fp 75,4 7 7') 'i f RTD J B 7'). ] 6 79.)7 77J/, h 77 25' RTD # 9 7 'T t, 5~ 7 L). L4 7:e L2 7y T.i RTD F 10 '/ '). L7 7 9 7 ~2 '7'T. 7 3 75 32 RTD # 11 75'.9 7 74',9 7 / ^. <i 5' 7E 'i d - RTD u 12 77*)7 7 Y. 9 7 7 '+. '/ / 7 '. 'I / RTD 0 13 79.7'l 77-7 '1 7 7? 1 *: 5 _RTD C 14 ~7 9 t~ '7 '7 9.c 7 79 t'b ) <j 57 RTD 0 lb 7935 7'). 3 % 79 35 79.J 4 RTD ll 16 79 0/ / 9. c' l 7. (- l 7~,i19 RTD f 17 777/ 7.5'. 7 / 7 0. 7L) 7R 7 / RTD # 18 7 9, J y'
- 79. y /
7<. ; 5-7 ;.2 4-f _ RTD # 19 7? 7F' 7.9, 7g 77 7'/ 7 Q. 7 7 RTD # 20 '75'. 5 i, 7.S,Y (,, J y..-f f,, 7 v,. g - RTD G 21 (S?ARE) 7 ').<//, 7 /. ]S yc). 3 L. p <p. 15 RTD # 22 (S PARE ) -79,J <[ J924 79.2 4 /cJ ) <} D. Pt. 1 l.369-I.36b
- 1. 3L: I i M.6 D.
Pt. # 2
- 1. 35 5 I 4 G '7 i. 3 '7 I i'3 70 D.
Pt. F 3 1, 378 f.34A Ir 3L 5 1 4.> A D. Pt. # 4 /.374 I 7 77 /<T7Y l 3 7'T Prennurc A 1 STd 2 'l 85$0 $ $ 5 3.2 7 @ W D 's Pressure v 2 (S PARE) 1 (a 5'2 d ?t. i'/ V Sd-(/8 T/,.S f ? D. Pt. - Dow Point RilD - Relative Humidity Detector, ',.n .-) U ' t d j f,- 2. i U)
- Pressure, Terminal Operator M O-4
- ~ 3/16/79 OPERATII;C PnocrDUnn 13100.1, PAGE 53 INTIER ATI:D l.!:AK H ATE TEST APPE!!DTX D AMBIENT TDiPERATURE [/ !!OUR NO. BAROMETRIC PRESSURE
- 30. 0 9 Y DATE 20 hb/ 77.
ROTAMCTER FLCU A/d VERIFIED BY /, / //* ' ._ILRT DATA S!!CFA ~ Qt9 Q*j I 2-) Q3J TIME /SAMPl.E NO. O/@ / di C// I / T O C/30 / 'I 7/'-/f/ 92 { RTD 0 1 '7 4. I f '7 'j. )[ '79. / 3 '7Ci./ 3 RTD 0 2 7G M 7i.24 70 24 7: A'i RTD # 3 76 4 r 7'i. 4 5 7 'r'. 44 774 4 RTD D 4 7c 47 / 9. -4 7 '74 4 7 7.y; RTD 0 5 7e;. ~2 V 79.27 7027 70.2 7 RTD ti 6 7ti. O / 79.0/ 7 9. Of) J ci. c o RTD 0 7 79.4 V ~19. 4A 31.4$ 7G. 1.? RTD # 8 7 9. 2 f 7 </. J i 7127 7 </. ) 4 RTD t! 9 79.9) JG. rc, 74 7's 79.ix, RTD 0 10 79.3.2 79.3 2 7742 79 x 2 RTD 0 11 7?.96 79.'I5'
- 79. '/ t 7 ?, 9 +
RTD is 12 -) ?. 'l L-7 Y p f.
- 99. Qu 7 c:, 'j s~
RTD # 13 7c77 7e,77 75 7? 7 's, / 3 RTD D 14 79.01, 7 4.e ta
- 2 rf. M.
7t; f.i:, RTD 0 lb
- 19. 3 r 76.54 Sq 34 79 3; RTD # 16 79. t'/
- 79. c'u 7 Q. y 7 1,c G
~ RTD # 17 7 9 7_D 7?70 ~7 's'. 7 8 7. N RTD 0 18 7 9,.2 5 '79 2 7~ 71.24 79.1 4 RTD 0 19 7? 7V 79, '7 V 7E 7 Y
- 79. 7 7 RTD l' 20 7 9, Vf 7 ?, 9 62 79.' f 79.3 s
RTD r. 21 (.s P.A K E ) 7 </. 3 4-7 cf..:s x 70 3 I 7v. 3 O RTD 0 22 (S PARE) 7 9. ~2 2 7 ef. 2 2, 7G. 2.1 7/7. 2 / D. Pt. 0 1 / 3?,t. I /,.3 7 3 / 373 /, 373 D. Pt. # 2
- T 7ef f, 3 */4
) 3 74-
- f. 42.7.
(- D. Pt. p 3 t 3 (- 2 ih2 3 f-4 I 2/p ~ L. D. Pt. 0 4 1 3 td /. 3 ?l l. 3 ?.Z 't. -i?'F Prcncurc ? 1 2 T:f Jf .$5'5' 2 <)- )(53 23 VF', 2) Pressure e 2 (S PARE ) f/., f /.3 C/. 5 ; 4 g/a.S /3 w 5 /2 ~ D. Pt. - Dow Point RllD - Relative Humidity Detcetor,
- Pressure,
.._,, q u.; 4 U },') b " lC. /WU Terminal Operator eo # -
3/16/79 OPERATIric PRDCEDUlte 13100.1 PACE 53 1!1 TIER ATED f.1:AK lt ATE TEST APPet!DTX D AMBIE!!T TE!!PERATURE [/ HOUR NO. BAROMETRIC PRESSURE 30.O 6 0 DATE AB /M. /. 71 ROTAMETER FLC'1 M VERIFIED BY s ALRT DATA S!!EET, n m U.'W (IJ ' Q) QZ. ' 5 TmE/SAMP1.E NO. 02cD / 4.T o.2/5 / '7V-
- 2 3.' / b
(>24 T/ 76 RTD # 79.// '79, / / 77 // '2 I- / O RTD # 2 ~1G,2 3 7G. 'l 4 7'i 2.3 7 ';, ) 2-RTD C 3 7cj. ct-3 7c; 4 2. 7 :l '+ 2. 4 =i 9 2-RTD # 4 76.4s' 7 tl. 4.f 7 9. 4 3 76.4 5 RTD U 5 TA. 2 h 7'i. A is 79 26 7 'i 2 b RTD ti 6 7 9 c; ct 79 00 79 6/ s}-
- 72. 9 c/
RTD # 7
- 79. 4 7 79 47
'l'i 4 7 7'i 'l l RTO # 8 7 '/, 2 3 7<1. 2 3 7'i.22-7-i.23 RTD # 9 7 '), 3 (1 '79. 5% ~14
- >2'>
- 79. S7 RTD # 10 74, Ti 7'i.32 79.3 1 10 3i RTD # 11 7f, 'l 't-7 9.'/ f 74 (/ 4-
- 75. 9 ~3 RTD is 12
'79, */ /c 7 P. (j 6 7 c. '/ (+ 7 &M RTD # 13 7T, 7 t' 79 79 77 7C 7'<. J 's RTD # 14 '79.6 6 79 (6 ~7'i.C 0 74 CS RTD # 15 7<T. 75 7% Ff-7/ 3.5 78,. 3 4 RTD R l6 1 p* 6 '/ 7 T. if 'l
- 79. C A
- 79. rj 7 RTD # 17 9V 70 7 F. '70 R. 70 7 T'. 7 /
RTD C 18 ) 1. 2 '5 9<.2 2 ,r} 2 2. 7c 2 2 RTD # 19 78 7% 77, 7 ') 79 77 71 79 RTD # 20 77 W,
- 70. W.
7 c Vf, 7 ? '?[- RTD F 21 (S PARE ) 7J. l'y 7 0.,2 ? 7 <j. 2 7 vo ' f, RTD # 22 (S PARE) 79./9
- 77. J o 7 '7, / 9
~74. j ej D. Pt. # 1 f,3CY J.375 j.371 l, 3 74 D. Pt. # 2 ) 777 p. 3 ';'d / $$-0
- l. 3 7 <j D.
Pt. ia 3 o. A c. f,. p 8 N.~., p a t cs I,3 7j ,D. Pt. # 4
- 1. 3.Y'4 l.397 r.393
/, 3 7 '/ Prensurc # 1 R T X *) l T 5 3,2 Cl .V58 / 9 95'$ l ') Pressure r! 2 (S PARE ) .% 5 11 5' 0 5 / 0 E 5 o r/ 34 3 ov D. Pt. - Dew Point RllD - Relative llumidity Detector, O ' 'q 177 a G l )I
- Pressure, I
Terminal Operator 1NL 9
3/16/79 OPERATI::C Pn0CEDunE 13100.1, PACE 53 IllTIT.R ATEI) 1.!:AK lt ATE T!!ST APPE!JDTX D AMDIE!!T TDIPERATURE SO HOUR NO. b BAROMETRIC PRESSURE
- 30. Cif DATE 7C }+1,M 7 5' ROTAMETER F1.09
/b/M VERIFIED BY e ( ALRT DATA SilEET_ m 2 W;v ( *9 ) L23 (&JU 1 TIllE/sAMP1.E "o. 03cc / 97 o u s / G V_ c3r / </ </ c3 M/ /c o RTD # 1 7% 6 '/
- 79. Eff 7e/. O Y 7'I47
( RTD 0 2 7=), 2 ] 7 ti. A / ~1'i. 2 0 Y. t -? RTD # 3 7.; 4 2_ 7 </. 4 / 7 ;. 9 l rG 40 RTD 0 4 ~79. <) f 7(). n i ? < 't A lt- '.' i. 4% RTD 0 5 79.2 9 76.2 4-74.2 4-
- 77. 23 RTD U 6
- 70. C 0 7fi. 00 7 G. 'JO 7.C.').V RTD #
7 7 '/. 4 7 7'7.97 70 46 7%f 6 RTD 0 8 7c-) ) 2 7Q.2.1 79.LI 7 'i..L O RTD # 9 7'/. G? 7G. A <1 74.3 f 7'1 s + RTD # 10 7t/ 3 c) 7'7 40 7ei. 3/) 7<;, 4 0 RTD 0 11 7 ?.f/3 17')3 7 9:'].3
- / '!. 'i,2 RTD U 12
?"i' 9 V 7 ?. <I C ~77<i5' 1:. ?4 RTD # 13 7 C' /~i 7 ?, 7; . f c> 70 7;- RTD C 14 7'J. O i-
- 77. e 5 7'7. /(-
7 G, ( </ RTD # 1$ '7</. 3 3 7 4 _3 '3 79._3 3 79.32. RTD C 16 ? '? 'i 7 7 '+. <! 'l 7 ti. C / 77 ';'t RTD # 17 79.7O ~7 C ( 'I 7* / // 7 '~. / ? RTD C 18 7'). 2 i 7 '). s /
- / 'i. 2/
7 'i 2& RTD f 19 7f,76 7P,7 7 7B / 7 7 7. / << RTD 0 20 7 7..y I 7 P O6 7_','. a ;, 7 v. ? </ RTu v 21 (sPARC) 7<j.J f 7ei. 2 3 79.2 3 7</. 2 / RTD 0 22 (S PARE) 7 f. / </
- 79. / r/
7 '/. / 7 90/ 7 D. Pt. # 1 / 377 /.390 /. 3 ?b / 7C D. Pt. # 2 /, i.) I. 3J 3 s, 3.s 3 ,, _e-z D. Pt. U 3 / t '7f e, ;t y c. .? 7 7 ,,),. .D. Pt. 0 4
- 1. A.96 l.%97 i.3Q0 r, Vl/
Pressurc # 1 Rfy/f '? G /. 6 Dil' / 43 .V U/[ Prensure e 2 (S PARE) '%.5//!/ T65 Of> 9/-5 ce YA'5e f D. Pt. - Dew Point RllD - Relative !!umidity Detector, ?74] 153
- Pressure,
~ Terminal Operator 1d d
3/16/79 Ol'ERATING PROCrDUrtE 13100. I, PACE S3 INTIT.R ATI:n I.!:AK lt ATE TEST APPEND 7X D AMBIENT TDiPERATURE Il0UR NO. BAR0!!ETRIC PRESSURE 38.O4 [ DATE .2 ff W w'r 7'[ ROTAlfETER FLOW M'M VERIFIED BY.' -I / A LRT DATA SHEET - m L3p l'ah Tmr./sA !PLE no. c4ch / /vi 04 W / 102 v+w/ /A cste / v4 RTD 0 1 79.O7
- 79. C C, 93.06
~7u).cs RTD 0 2 79 /Ci 7'). / '<' 7M /R 72 if RTD l' 3 7 ff. 3 'l '7 *). 3 'l 9-1. 3 H 'M AF RTD D 4 7 '}. 'l 2 7'] 4 *L 73 "! ~~J
- 4O RTD # 5 79 2.5 79 2 L 70 2%
- 74. 2 -
RTD v 6 7 9. '/ P 79, G 7 7F, 9 6 / F. *//,, RTD J 7 7 9. 4 /<. 7<7.4 5' 79 4-6, 79.4 9 RTD 0 8 7'i,)9 79.20 77- /9
- 79. i 9 RTD # 9 7 Q. 55 79. fe/-
77 w 4-7J il RTD # 10 77 2 */ 7 'J. 2 '/ 7'J. 2-9 7+f. 2J. RTD 0 l1 9 C' 'i / 7P ') / 7f. 9 / 7f.91 RTH P 12 7 9. ') { 7P. 'j A-1 P,* '7F 94-1 RTD # 13
- 79. 7/,-
7< 74 7F 7.*5-7F.7? RTD C 14 7(f. OS 79 /'5 70, 0.3 7G. (.4 RTD 0 1b 7ci 2 3 7ti. 31 7.-L. 3 2 7*). 3 2-RTD # 16 '79, (C 7 E' (/ f 7 /. 9 -7 2 F. '7 f. RTD 0 17 7 9. f V ?.?' / (' 7 f. (, V. 7 F'. f, 7 RTU U 18 ~ 7 '). 2 0 7 ') : / 'l 72 19 '7 -). I '-) RTD 0 19 70.}7 7G 74, 7f. 7!:, 7f. 7G3 DTD ? 20 7? ?S 7Y % 7f. f 4 7f. Ed RTD le 21 (S PA R E ) 7 c/. 2 0 74 /9 ~;a. f 9
- 73. / a RTD # 22 (S PARE )
7 t/. / (3 7 9. /f 7 7. / 6 79./4 D. Pt. 0 1 1.ASK l>382 /,377 /= dP/- D. Pt. 0 2 'l. R S l
- l. 75 b "T F 3
I._777 i 3%5~ /MS /~ NF S k D. < - 9 7 F, / R 7e D. Pt. # 4 /,390 /,g93 /. 4 *7,-T /. 391-Prennurc 0 1 WE3 l9 .iSY /3 PST, / 2 ),'SP l2 Pressurc # 2 (S PARE) %5 C4 .Y(o f o 3 , P (~ s o;e, P r s C2, e D. Pt. - Dew Point RllD - Relative llumidity Detector, i*q t7o /_. 't J iJ7
- Pressure, Teminal Operator N'MM J
0 en e. # .e
3/16/79 OPERATI::C rn0CrDunr. 13100.1, PAcr. 53 IllTIER ATI:D I.l:AK !! ATI: TI:ST g tunix D AMBIEliT TDlPERATURE [8# 110UR liO. BAROMETRIC PRESSURE 3C,0.70 DATE 20 M44CY/ /979 ROTAMETER FLOW /Y,M VERIFIED BY / IIAT DATA Sili.ET - ~ CSN,4 OS/5'A/ Q1 (Zb dv) Q9? Tnic/sA!!Pl.E no. c.M //c5 Eu / /d o <r v / - Sr/ ic i ( RTD B 1 7'): O s~ 77,#4
- 79. e 3 7%03 RTD D 2 9'). J k 7t]. / 9 7<}. I. ~
- 7. i - l 5 RTD # 3 79.JS 7 <> 3's 79.34 7% 30 RTD C A 7 '; c./.2L 7 )'. 4 D 7 9, A ',
7v f) RTD # 5 7cf,20 7<;. A / 7</. ) O 7</, f Q RTD U 6 y y. ci T '7:+. <} 5* 7v'. C (, 75'. ej5 i RTD 0 7 -P) 45 7') +G 7r).44 7<j. 9 4 RTD # 8 77./f ~7 c /.t' 70./7 77./7 RTD 11 9 7').6~2 c'i f2 7 ', % Z 7%>l ~ RTD 0 10 7'7.27 7ti. 2 8 7(). 2 7 "19 2 b RTD 0 l1 7.9, Y ll 7 ?. cy 9 7 y, 4 9 7 cp,y.] RTD (i 12 7 ;7./ 4 7 P, () 3 7 g <j 1 7.r. </ A RTD # 13 7.? '/ 2 7 % J2 7v.7/
- 7., /0 RTD C 14 9(7. O 3 7t]. r 2.
7002 9y04 RTD 0 15 2 <). 3 / 70 3.2. 9 c;. 3 i 7<7 3 O RTD // 16 7 pr. 'f y 7F. </ 7 7.?, <j X 7 'r. <, 0 RTD e 17 79.C(- 7 9. / ~7 9 ?'t.? (, 7?.!..f RTD C 18 7'). t.1 7 <j. j.>< jc;, jW -):]. t y RTD 0 19 7T.74
- 79. Zf 7.9. 74-79./4 RTD f 20 7'.15 79 Y -f 7 F, 9".2.
7 y. r A / RTD i. 21 (.8 PAN E ) l 7 '/. /.i 7q j ? 7 c;.,7,, y y., tj RTD # 22 (S PARC ) l 7'/. /f -77. / 6 1 7C/4 79f3 D. Pt. # 1 /. 3.Fi /. 39 / /. 3 5' $' /.3d6 D. Pt. # 2 /. 3.id /. 4 ') U ) 3 '/[/ _f J (/ 2 r D. Pt. F 3 / 3 F '/ /.3YO /,.3 'g 3~ g. 3.jj . D. Pt. 0 4 1 3 'I 'l 1, 3 ') / j 3 c; #7 ) 3 <;,7 Prcscurc 0 1 R 5'$ // .$'5.T /0 4 7.5 / O ~,',5.S 0 '{ Pressurc l' 2 (S PARIO f'6S 6/ 4'r,</ 9'</ _?g.4 '/l3 .Y(,4 c)ly D. Pt. - Dew Point 2 "' :; 1 14') RllD - Relative liumidity Dctcetor,
- Prescurc, Terminal Operator bMM V
' V e
3/16/79 OPERAT7!1C PROCrDURE 13100.1, PACE 53 7 f1 TIT:R ATI.Il I.!!AK 1( ATE TF.ST APPEfiDIX D AMBIE!!T TD!PERATURE 88 Il0UR NO. I BAR0!iETRIC PRESSURE 3 d. C%[ DATE 25 //,',-/ 9'7 ROT / DIETER FLOW VERIFIED BY y ll.RT DATA SIICET~ ^ TI!!E/S/JtP1.E t'O. Obc 0 / / C6/-s' / (6 10 / vM r'/ e RTD 0 1 ~7c),g 3 7Q. p.2 7c), o / 7960 ~ RTD 0 2 79 15* 7 '7. / *;' 70.s4- -7 ': 14 RTD # 3 79 R. 7 </. M. 70 5.5 ~7/ 6 RTD # 4 '79 T '/ 7 9 W~ 7 3 '/ 77 -; j RTD 0 5
- 79. }cj 7 c), t c, 79 j9
- 74. f.s-RTD ti 6
9 57 ') 4 '7 y. 414 7 '*, 9 4- ? ?, r)q RTD # 7 79.44-9944 7'7,4 4- -74 41 RTD J 8 7 (f. / 7 J ci. / 5 7 'i. / (-
- 76. / >~
RTD V 9 7C, T/ 7c; 7c 7c; q na; Sj RTD # 10 79.2 7 7']. 2 6 7 ;). 2 (. rf L'. RTD # 11 7 Y* t 'l 7's" f T 7 Y,.V'/ 'J P, i- / RTD l' l.' ? G. 'j 2 7 C' t / 7 T-
- 1 /
179/ _RTD # ?3 79 '; / 7e 7/ 1 2. /. c> 7 '.' /. '.' RTD C 14 7 C/,62 7 9. e 'A 7 <7. M / 7ti 0 / RTD 0 15 7'i. 3 1 7 s). 3 r 7'i.31 7 *7 i A RTD 0 16 7.7. ') O '7O 92 7 "I'. i 'l- ~7 C 'Id' RTD # 17
- 72. b 5 79 65 7R',6 5 1 e /A RTD C 16 7 '/. /.V 7e/ /.C
> (f /7 '7 v./ / _RTD # 19 79, Je/- 79 73 7.?. 7 3 7073 RTD ? 20 7 %'. Y.L
- 75. V 2 7 ? ?}
7 '. :,L RTD F 21 (.s PA R F. ) '7 'i, / 4 79./ % 7'i. / 3 - ~/ /.'. RTD # 22 (S PARE ) 79./ J 7//./.3 7 7, / / 7'/ /7 D. Pt. O I /. 3'2 O /.3 75 /. 3 '/.3 /, $ '/ 3 D. Pt. # 2 / 3 'J4- /. I 3 / 3 ',3 ' f V9't D. I' t. F 3 ). 3 /) i 3 Y// / 3 c/ /..UI/ .D. Pt. 0 4 I. 'f-C6 I. k P 2. i a d t; \\' /. 4-0 5 _ Prennurc l' I 9 S(6 f WS' C '7 T W9/7 MF C6 Prensurc # 2 (S PA RE ) y64y7 ,, h'6 4 9 G XC4 v c- % 4 0. - D. Pt. - Dev Point R11D - Relative !!uctidity Dctcctor, [ ' i] ) [f ]
- Preinurc, Terminal Operator, b
M J J U
3/16/79 OPERATI::C PnocCDUnr.13100. !, PACE 53 1 NTIT.R ATLD l.CAK P ATE TEST APPENDTX D AMBIE!!T TD!PERATURE !!OUR liO. /9 DARO:iETRIC PRESSURE 38< r7 7 DATE So Mh/ 7f ROT / DIETER H.C'1 NM VERIFIED BY N C e-Ih2T DATA SNEET p (35,/ i QW Q // TDIE/SA!!Pl.E !!O. M 7et' / / / [/ e 7/5~ / //T C 7/O / //( n 7./(/ ///3 t RTD 0 1 '79. C/ 79.0/ 9 c?. 6 0 7'j.dd RTD 0 2 79 /3 7c /3 % / 3 7'I /3 RTD # 3 7 </. 3 s ' 79 34 7 4 d'4 74,3.3 RTD C 4 7c). E T 7. 3 'c
- 7) 3/
- 79. M RTD v 5
7 9, //
- 79. / E' 7 ej. f 7 7(/,/g' RTU U 6 7 b <> 2
~) ?. ') & ~72. Li 3 79'/2 RTD 0 7 7 </, </ 4 77.4 3 7%45 7742 RTD 0 8
- 79. / +
'70. / 4-79 /S' 79 / 3 RTD e 9 7c; <; <) 7 <p 9 -l
- )., + 7 1 <i e/
RTD 0 10 7 4..ls' 7 9. 4 7a.,z $ 7 i. 2 O RTD # 11 7 C..$ 'l 7s'.'es' 7 9. Y 7 / 5'. % RTD << 12 7 's. <j / 7 /, 'f v 7 5., v '/ 7 9.. -<, RTD 11 13 7.f* /[ ~7 '?.,'.. ') 7 *F C, 'I ~7l Il RTD 0 14 ~7 7. r'/ 79 46 70.00 <7 9 ( <' RTD # 15 7 'J. "2 '/
- 77. 2'/
7 9. */ */ '70, J../ RTD # 16 7 C 7 e/ 79'/2 7 7,/.3 '7 ~r. 9 2 RTD # 17 77 65 7?f5 7%/4 ~7 9. c. 4-RTD # 18 7 <j, / 7 <f. / G
- 70. / r, 7e; / i-RTD 0 19 7X*. 'J3 7.?. '72.
74 J3 7V.7-'. RTD 0.7D /.5. 5.4 7v..ru / P. '< / 7y.v/ RTD i. 21 (S PA R E ) l 79./2 -7</. / u 7 <) f D 7.',. eO RTD C 22 (S PARE ) l 77.//
- 79. /J.
7 & p(/ -/ 9. / O D. Pt. 0 1
- 1. 3 (i G
- 1. 2 </ 2 i Ap/7 1, 3 'j,~
D. Pt. 0 2 l 3 ') b I. *V, '/ .,l0 I f..'; (' I } o D. Pt. F 3 / 5'i e/ i 5c/ i N4 /, Uf 7 . D. Pt. # 4 I,407 I. 60 f i, d C17 I,4/I Pressure a ! l P.$VfG 8540$ N,,'O.5 .y5[k4 Prensure <! 2 (S PARE) 9 / el ') et $'L cf (/4 ?6494 Q (3 9.;/ A D. Pt. - Dew Point RllD - Relative liumidity Detcetor, d.., ' t d ) '4 2 ,s , f n r
- Pressure, Terminal Operator N-, M "
V el e
3/16/79 Ol'ERATINC PRDCCDut:C I 2100.1, PACC 53 111 TIER ATI:n I.rAK lt ATE Tr.ST APPENDTX D AMBIENT TRIPCRATURE 5M 110 UR N O. // DATE_ 20 MwI fi BARO iETRIC PRESSURE N'/0 ROT /JfETER 1LCU [f/ ~ VERIFIED BY L V &c- -.--
- /
Il.RT DATA SilCET - TIlf E/S/JfPl.E !'O. Of9M / //7 0f/f / // /T30/ /f ( (q.Jf/ ) RTD # 1 '7 9. ( d 7 c ') b 7b 96 7F.47 ( RTD # 2 79,/L 79 f t 74 ft 7 0.// RTD 0 3 7ei. 2.1 74 4% ' -t ! (.- ? 9 62 RTD # li 7e? 3 5 79 25 L- ~/
- 2, 7 ') -5 1;TD 0 5
J ci 17 74 I *i' ?').I T 79./3 RTD # 6 7 p. </ 2 >M 93 7e 90 7%.92 RTD 0 7' 79 4-2. 7 c3 4 2-. 79 42 7 cy. 4. ; RTD 0 8 7ti. / L 71 12 i4. ! % 7') /I RTD I! 9 7 <7 S '/ 74 49 /9 202 7c: 9* RTD 0 10 19 2S 7 '-).14 / ') 2.+ 79 2S RTD # 11 7F % 7F-h-2' M- /'F H-RTD to 12 ? G. T1 7 H y '/ /r ' ~ r. 7 %.' O RTD 0 13 7?. 7 / 7 F (c9 7 P. 1, 7" 7/ RTD f 14 ~J 9. (f '/ 7,4 M 9
- 79. OL 79 C D nTD # 15 7 c/; 2 'i
/9.2/< 79 2 F.
- 29. JP RTD 0 16
-7 9.tj 2. 7 ? 't?. 7F HI JC T RTD f 17 7,P./ / 8 4 4-. 7 *..(c'i 78 /r 4-RTD # 18 7 el. / i' 79 a c. 7 -2 s5 /- /J RTD f 19 79 72 7 6 /L 78 72-
- //
RTD 0 ?O ~7? J'O 7 F.F L nTo a 21 ( 2, Pa k t i i rn. T, / t >.0/- / e e.-. p c.. r 7 RTD # 22 (S PARE ) { 7 9. j d 7 9. C ') /4CF 79 C F D. Pt. # 1 1.392 I..? 9 /g ) %0 1.dcl D. Pt. # 2 f,4c3 (2o5 r. a 4- !. a c. T c D. Pt. i. 3 i, 2,99-s..to L
- 104 l.i c l.-
,D. Pt. # 4 ), 4 j.,2. i J-13 p.1! 6 ! 4/O P'essurc # 1 ,C6TC i M 'i' ff S'5PC > M 'it? C ? Pressure v 2 ( S PA R C ) .y'g-4 c/.2 ,a.492 r t-a o / 9 e:9-9 / D. Pt. - Deu Point RllD - Relative llumidity De tector, 7 $ [j }O
- Pressure,
- tr"'
( - M Terminal Operator v o d
9 3/16/79 OPERAT7!:0 Pn0CrDUnt 13100.1. PACC 53 111Tir:n ATI:n 1.!:AK ft ATE TI:ST APPEfinfX D e AMBIE!!T TDIPERATURE 65 iiouR no. !L-DAROMETRIC PP. ESSURE .3 0,/I
- part, 2_O M Ac2FF V ROTA11CTER TLOW e'b VERIFIED BY ' (d 24
~ - - _ O rILRT DATA S!!EETm (2 m Q43 1 (4 > 44) QL f tit!E/SA'1Pl.E !!O. C 9C'(' / l lI C' ff/ / l 2. L. C93C/ CJ)J f/ / 2 4-RTD # 1 7 s. ') 7 7 d.'/(c 7 do. C) (o 70 9 T g RTD 0 2 / -i <0 J 's, ! O '9 L ') 7 N t.. 9 / RTD 0 3 / us ^Z. ^) L; As /H 'I i u. 3 L' RTD # 4 F-> - J-- b- "r P '). r,4-1 'i,, llTD 0 5 79.I4- ) 9. I d- / '). l & 7* I3 RTD ti 6 ? N '90 7t. P ') 9 7 ~. L) O 76.UC RTD 0 7 7 L). 41 ^) 4. 4 ) 7 '). A - l 7H.LZ. RTD 0 8 } 4. 1i / ').1 2 7 '). II ?" IV RTD l' 9 m. 4 ') / ').in ?a). * : f' 7a w RTD # 10 7 '/ 2. 3 7 '). 7 4 - 79 2;; 79 23 RTD # 11 75 P 'i / N hb 76 Wi l '- .) RTD is 12 9r.rn /' h. h H ~/ v-, ?. /- 's m RTD 0 13 7% 7' 7.k ~/4 /,k RTO C 14 7r.Wi 7 F. {> t) 7 F. ' )') , ~ ' 'N RTD # 15 ?st ! r. 79 7') 7 '). L ') 7'-). 2 7 - RTD ll 16 Ji ' or n '?- ) ? F 3) I 'r ') ; RTD f 17 7 8. (- d. 7 c. /.. /c. 7 8 (;- L. RTD C 18 /~ t3 ? '). I t, - 7 e), I } ^* ') ! ~/ RTD # 19 7E. // 7/4. / 3 7 P, '/ 2 7s.7.L. RTD ? 20 ie ?.I / > J. I / ('. t:. I 7. . h c. RTD 1 21 (S PARI:) / * + o v-p s t v.. 79 c, / -> en RTD C 22 (S PARE ) 7t# C 9 7 9. Ch 7 9. C. ; J' '). c r. D. Pt. 0 1 i L O C; i L o le J. JC 4-i. d C 4-D. Pt. # 2 1 4 t14-t. L('c-l -1 C ') / 4! # i-D. Pt. i; 3 i. A 'n) / : 1. ( ' n i. a t' ; N, D. Pt. 0 4 I .L l t I.4Ib i Ai6 I..] I y Prennurc # 1 F 'T P C 2. G Y Of F i b C l C l ' I Prennure t' 2 (SPARE) l 9 / 4 10 M t.- d '-) O ps ic4 ')(.+ "!J4L D. Pt. - Dew Point RilD - Relative llumidity Detector, ? '.s,'; 1 1/r 4 u a i
- Presnure, i /
e Terminal Operator N l,! 'A' - M J v u .e
g 3/16/79 OPERATING Pn0CEDURE 13100.1, PACC 53 I NTIT.R ATI:D I.!:AK lt ATF. TI:ST APPENDIX D ( AMBIENT TDIPERATURE !!OUR NO. O BAR0!iETRIC PRESSURE 30 /d DATE NO hM N ROTAliETER FLCW d VERIFIED BY / ? yy7?/ / (IIST DATA SlinETm m m TIMC/SAMP1.E NO. /CCO / ! (Otf/ I2_ I e W/ l /c1i N ( _RTD 0 1 ')P 'li' } t'.4' C 'l V.'h T ~/ 9 4 (~ RTD 0 2 '/: / "I ' G. t. 'I It-7. C' -/' I t i:, i RTD I' 3 </-/. h en n // -< / /C, :- o '7tt 's i RTD # 4 '/4 3 'd 'A/ V-i ~/(1 % 70 % g% RTD # 5 '/r/. / 'i 'Y/3 7G. I ;l '7;1 l3 / RTD v 6 '/ ( s '/ 99.4/ / 7 9,(.t n
- W/tt RTD #
7 '/4/,e/'L. ^-/ 4/L Tv.u2 Y, 4 3 h RTD 1 8 'M / / 'N/ / / 7(-i. I f 7f. ir RTU t' 9 'xt, *i, G:l..,'/ 3 9.%n > c,.c, o RTD # 10 '7'/ ;/ 2. 4 /.? 2 7(,. '? g 9 c, 't! RTD # 11 '/t'. ( e/ '1 9. Y C l'.. N '7 Y. y!1 RTD v 12 '7 V s ( O v. Y x 79 e s 7 r. <c N $J RTD # 13 'n /5 ; c. 78 7q.~){, is. 7 'i N RTD C 14 'Iy t 'i O 'c ~/ "';i.c () is. ' s ( i 1 RTD # l$ '7(/. / '/ '?t. M Mo 'i r 7(: 'v-; I RTD # 16 '/). '/ / '/ G. 4/ / -/ '<, M /', Tx, \\ < l'TD l' 17 '/ \\ /.~~
- )
- .'/
7.: i (. 1-(. 1 RTD C IS
- 54. / r
' // i') -ri./t 9: 2i RTD # 19 '/ \\ '/'/ 9 7. 4 6 '- 77 ' c M "?,. m RTD 0 20
- /h t /
'?S. 9 0 7 ?. 9 =, ?{. ( RTD i.' 21 (SPANE) 'su. i s r/ ^r i id > <, i,. t
- n c-[
RTD # 22 (S PARE) '/ '/ / '/ 5'- r,) G ' 7G. / > '/ '; e / D. Pt. C 1 / J/f V /. * / f. h / - d '? / f. < t r.R f D. Pt. # 2 /.+// L /. / / / '; /. u/ / I. tl l '4 Yt. U 3 /. 4/l/,3 / <-/ / /// 'l,~,* ), /t'1 */ i. et (, / L D. ,D. Pt. 0 4 /. '/ /P /. C'l f) / /J 2 t/ t. G 2.O Prensurc D 1 8.T 5 (> / 'T.T9 f.)O 4 T XC()ec in NT\\OO Pressure t' 2 (SPARE) \\ e a f e/ v <. <!_ / 7 c, v j / s #... / ' 'l D. Pt. - Dew Point RilD - Relative llumidity Detcetor, > >ra 1/r
- Pressure, i.; ld 1 '1 J Terminal Operator d0MM J
d Al0TG /0 %~ ENb of.nxT.
3/16/79 OPERAT7!1C PROCEDURC 13100.1, PACC 53 IllTIT.R ATI:D !.1:AK I! ATE TI:ST C L E_1 APPCilDIX D AMBIEllT TDiPERATURE HOUR NO. BARO 1ETRIC PP. ESSURE 3 D. I O DATE .3 " 10 ~ N ROTAMCTER FLC1 3' k VERIFIED BY .'C /I Wec b U ILRT DATA S!!EET TIME /SAMPl.c no. / / lldo / !! W/ g ~7 0J h 5' 7 6 ') Le RTD # 1 RTD 0 2 'J C) ('. C) ~~1 '1. !
- RTD # 3
/w a/ n. 3 4-RTD # 4 74 L 7" ?L RTD 0 5 } '). / > '7 % H - RTD (/ 6 76 90 78 9/ RTD # 7 7 '). 4 / 7 '), 4 4 RTD 0 8 7 '-). I I 79.I2.- RTD I! 9 7 '/. 5 /_. '7 u '; 4.- RTD F 10 7 '-) 2.', 7925 RTD # 11 7 F l' 6 3 7.' ' t '7 RTD ti 12 M t-') 7' tjr 1 RTD # 13 7 M. 74 7.. c-o RTD C 14 7M.99 7 '/. C f RTD # 15 / w 3 2-7 v. ; $ RTD # 16 7.2. C; i 7l-:. 9 7 _RTD I' 17 { 7 A. (c h 7C /c ItTD G 18 74 2s 7, 2_(i RTD # 19 74.71 '.e II. 7 $ RTD l' 0 ' ' ': a *.
- '- ' /;-
RTD is 21 (S PARE )
- n a p a c *;
RTD 0 22 (S PARE) 7y C 7 ,.w 7(f. C h korAMrira Fuu' s.2 S C Fm 3,1 3 Cr,q D. Pt. # 1 /.4 2C l.c li D. Pt. # 2 1.4 I h I.1 : P, D. Pt. i: 3 i s.1 s. n.* u . D. Pt. # 4 / /.2 7,2, [. 4 44-2.7 P >IG Pressure C 1 T T'79 9 C' 'T / 0 7 Pressure r! 2 (SPARE) <f Ge4 5O A ir d M $ D. Pt. - Dew Point RllD - RcIntive Huctidity Detector, h f v, g 7 u a 274-
- Pressure, 0
Teminal Operator M\\ 'l'oli,, 5 d
3/16/79 OPERATI!;C PROCrntinE 13100.1 PACE 53 ItJTir:R ATI:Is I.!:AK R ATE TI:ST C L. R \\ APPEtIDTX D AMBIE!!T TDIPERATURE !!OUR NO. BAR0!!ETRIC PRESSURE
- 30. C) b DATE - 0 Al N ROT / METER F1.00 b1 VERIFIED BY t'LCflhurd_.
6/ ILRT DATA SIIEET TI!!E/S/.!!Pl.E t.'O. I2.00/ f Lt T/ l 13 #'/ e t/--T'/
- S.') L-
- V t5 ') T
- ] Y. L/ 9 TR'.M b RTD #
1 / RTD # 2 79.O' 7 c). r.A // 0,. 7 '. r.. C ' 7 RTD # 3 7N W ' 7 <-> 30 ~/ c's );/
- r.
RTD # 4 79 52. /9 -? P. -i, M/ -'I RTD # 5 2% t 7._ ?%,I2_ 7:1 /() % ii RTD t/ 6 76.90 7 8. (>O
- / P.E 7 7c
.1 RTD # 7 7 9.17.__ 7 ') 42 ~/(-/ 4 / 7c, a e. '/, D'i 7:s j a ;A RTD # 8 7 9. I e 7C3.// r RTD # 9 7 <-) iL 7 ca. 5 L- ' c. c- ), 7". e. RTD # 10 / 9 ? r; 7 9 ?_+- '7 '1 '? 8 9" 22-7 F. ? L-7 P. ! L-I'S'. ? <- ~~ :' V RTD # 11 RTD /d 12 7 5< M's 7 F Fr-7'/ ? 7 7s. w RTD # 13 7M.7F 7 V f-c. ' 7. cn 7 en RTD # 14 7C) Do 74.CO 7.G i 70, c'c).. 6 t RTD # IS 79 79.52- '74 31 e't.;<a RTD # 16 7 A' /.5! h / '"<, d n 7 V. G r. RTD # 17 780 F, 7F (r 9 '7 7, /.. re 7C, / P P.TD # 16 /V dr 5 -i,/ 2-v '7Q_;) RTD # 19 75./3 7 c. 7 t~~ --/. 7 5 % ;'2 RTD # 20 7 f:, l '.] ?.7 i -7 > >~ ~ RTD ie 21 (S PARC ) 79.03
- -> c a 7t 0.2.
7t C1 RTD # 22 (S PAitE ) 7 '). O 7 7') 07 ~7<i M, -Fi. c. S.2. 5C F m 39 3,), YoT/ir,rT;R EL e,c, 3, D. Pt. # 1 1.J/C (. 41 T /. / 2 2, f yeG D. Pt. # 2 f..a 2_ C l 4 /_ L /. u /,3 i,U 2 3 D. Pt. i; 3 o 1 o r. t ut, s. u ') < - D. Pt. # 4
- 1. d 2. T r,4 2. 5
/ d ~J 7
- f. 4 Ak 27 27 A7 A7 Prensurc # 1 c.1 % 7 9 6-P S-)C) 7 f7 t ' t.' d T c y e'i 3 Pressure v 2 (SPARE)
G 6 4-t; & Ft.-~) P -s '< / - d '<' / Q 0 tl C O D. Pt. - Dew Point RilD - Relative !!umidity Detector, .j,.q gf7 .s5u I 'r /
- Prennure,
\\ .\\ Teminal Operator 'E.\\ '_. O C'
3/16/79 OPERATIric PnDCrDU;tr. 13100.1, PACE 53 IllTIT R ATI:D 1.l:AK 1< ATE TCT.T 0L5\\ APPE!!DTX D AMBIE!!T Tf21PERATL'RE !!OUR NO. BARO!iETRIC PRESSURE O.07 DATE OO / s1R ROTA!iETER FLON N% VERIFIED BY b /_ t > /d'~ c,- V ILRT DATA SilEET TUfE/SA!!Pl.E NO. I MlJ / r a t s' / t 350 / 8.N'T/ RTD B 1 794/1. 7991. 7 h '/~2- ~7 P,'1'2. RTD 0 2 ?/. OR 7'l, && 'I'l O 7 ~7'1. C(s RTD 0 3 7tu *)'/ ~H 4t. i '7 't. P/ T:s. :i RTD 0 4 irt. 'fr 7'l. 16 1 7'l - DO ~% At RTD 0 5 ~) / 1. ~~ 'i 1 I ~i'i 1 O ~~ 'r. s a '/. RTD f! 6 7rg.(c/ jq,x g 7%. y'/ 7 4, p p RTD # 7 7(f. /1 ~74 4-( %.44 ~74, Ret RTD # 8 7/. / O ~/fl.I C VI t0 7 (i
- f.
RTU II 4 '7 9 i d I't 6 f.. '2' o. rA R b. C,J RTD 0 10 17.']2. ~in hl 77. *} 4 3i 2 RTD # 11
- 79. M.
'M, Y /r 7 f. f-7 ~7,.- C RTD // 12 7 v. ( Q 'e 3. v-r 1A.< f- -n. 7 RTD # 13 7 7. 7'/ /t TD /e re 7 '< I RTD I' 14 7/ ('l i.C! A.' / f .r RTD # 1$ '7/1. ;,' 1 7er.3l '/ ' ;. 7,c 7 $.,i RTD # 16 7T. Cff 7T,4 ) 78.4i ~7 0 4 /', RTD I' 17 7's.i q 7 Y./ 'l 75'. ( < 3 '7 s-,,, RTD Il 18
- 7. ? >
77-i y 7 f ;. - 4.. RTD # 19 7 q.74 / s. 7 5-79 7f
- m. T RTD f 20
';g. %, 7\\.\\/o -7 5,3 p '7 <,i b RTu i. 21 (S PARE ) r.<, , < r t.;;__ /N.ca 7., v t RTD # 22 (S PARE) 7C.(/o ~7q.c/z 7c).Of 74.og~ 1 2 c TA tu r-m=e b e ( O
- 3. b
- 3. L 32-3L D.
Pt. ? 1 /_ 'J / 't /. '! 2. /
- l. (J J?
- 1. V 2 'L.
D. Pt. # 2 /. sl1_ d / d.2 f. /_ V. 2 (~ / U -] Y D. Pt. F 3 /At <*, ~ / ~/1 /-
- f. V / (..
- f. %%*
\\.. D. Pt. C 4 /.1/ 2.9 / - L/_;2 '7 /.<J.2'i / L,J 17 .;2 7 27 27 Pressurc # 1 d6 79 2 3 C 7 t/ 2_ 7 C '7(1 / 95'/5'1 Pressure t' 2 (SPARE) S f., 4 i C <c L-4 '/ (/ 5 t,- U 7 '( 'W ! 72 D. Pt. - Dew Point RilD - Relative llumidity Detector,
- Pressure, q7 1 o
'n oJ 't o Terminal Operator 0iO'- e $ s
3/16/79 OPERATI!1G PROCEDURP. 13100.1. PACC 53 I f1 TIT.R AT!.D l.l:AK lt ATE TI:ST C L TR 1 APPENDTX D AMBIENT TD!PERATURE Il0UR NO. BARO 1ETRIC PRESSURE 220. A 6 DATE 2 0 /d49 73 ROTA!1ETER FLOW 3.b VERIFIED BY / 0) O' -&c.- Y ILRT DATA SIICET TD!C/ SAMPLE NO. 14cO/ ea#5 / ., p h ra.3c/ fid E/ RTD # 1 ~79 F1 l hj.lr, 40 ~7E' 4 0 ~7 9. @ RTD # 2 ~7CT.CV:i 7'1. ( A ~ ~/4 0 5 ~7'l-t 4 RTD # 3 -K,. 1 c '/ 'i J r,- '~,x r 27 7 (L 37 RTD # 4 Af.Ut ~ !i. J \\ '74.)( 7417 r JTD # 5 1-r. i c
- 79. < -
t i Ch / 4. c 'r RTD f/ 6 7R. s '1 7A7 7.,'. W W y/- RTD # 7 79.4i '79 4 "L.-
- 79. d f
~7c/,c/O RTD # 8 li.c 8 7G.ch irl ( F 7 't./ / RTD I! 9 1c,.5 ', 7C.c / 7/, qu 'J y, 5 2 r RTD # 10 %. ) *L 'F. ') I '? I 1 1 7tl. 2 5 RTD # 11 7i V ~Y / 4 'IV.5 4 / y 51- / 3 RTD te 12 %.O 7\\ \\ 7 7.07 7vs7 RTD # 13 7c.79
- s Y,
%.51 71 80 RTD # 14 ^G.' e % -13 ' ai1 i <. ~ i (- 7 Y. Qi RTD # 15 '-m. h t 7 c,
- c. r.
7: 3r 7 t/. 4.- RTD # 16 78.'10 77.9 9 '7\\'.41 774/ RTD I' 17
- 75. b l
'I A + E -8h47 ')'i O Y RTD I' 18 7C M ~74 % l'i ; 7 14 J> RTD # 19 , K 14 70 10 ~/y. 7 3 79 M RTD # 20 7936 K. N R-74.xt, 7y y5 RTD is .l (.i PA R F. ) 7 s.c p A ,y '/ 3 3 j y. </ 3 RTD # 22 (S PARE ) 7/ i'(-
- 74). 0/-
~~;c. c d-7t/g3 t k cTA tur reit E c(c .S. 1 ~3 1 - 3,1 .3 1 D. Pt. # 1 l. H 2.-3 /. 4 ] 2 .M'TM 3/l f.41 A f;_Q 3.2 iij. f s.; !" D. Pt. # 2 I Hl'1 f.4 SC '.r iJt y L g.q 3L .w.~ v H => L. ~" D. l't. i; 3 l. LL 2.f., f. Ll J (n p.pt t. 6 u y,;;.', i 9 4 -) 5 wp4 .s -. D. Pt. # 4 I. 4- &4 l. a b=> v urt y E(., f.qWl i 1 1.p) \\ nos t A1 17 27 27 Presnurc # 1 % 5 7 6' R $ $ 75/ SC,~7</- .96 7 Y.5 Pressure t' 2 (SPARC) 'e b 4 /s ., (,. O '/ v 4; /.-t.) ) o % er ' 4 / D. Pt. - Dew Point RllD - Relative Humidity Detector, a,*q ?.
- Pressure, S U 1
6 a i Terminal Operator \\ LIO -W 4
3/16/79 Ol' ERAT 111G PROCEDUnE 13100, ;, pygg 53 111TirR ATI:D 1.1:AK R ATE TI:ST O L-. iD APPE!!DTX D AMDIE!!T TD1PCRATURE 110 UR liO. BAROMETRIC PRESSURE S0' DATE 8 5 ROTAMETER FLOU 3} VERIFIED BY : UM1 ILRT DATA SilEET TI}f E/S AMPt.E f 0. fTCD/ f TlT/ f S ~so / 15457 RTD 0 1 78 'f'l
- 79. Y'/
P /. W 7 5', t'/ (- RTD 0 2 7(1 C L/ ~/tf C 4 7'l 9 d 7 4 t: 4 RTD # 3 7 4. > 7 7 7. M.
- 74. L 7:/ M-RTD 0 4
74.2 1 7'l J.7 ~7 ;! -N- ~10 29 RTD 0 5 7'i 0 Y 7tl r 5' '7 4 e 5' 70 6Y RTD v 6 7V.94 7 5* V6 7 f 16 7 Y s c.- RTD 0 7' 74 4I 7t? 4/ 74'/6 7T #/6 RTD 0 8 70.07 79 CS 7'l-c7 4l.c 4 RTD # 9 7 t/. S S 7 </. 55' -r C 5 6 7 c). 5.. RTD 0 10 7tl. 22- '7'l22-7'i 32-7'l :L/ RTD # 11 79 N 7Y YV 7S' W 7 y 3' 5 RTD ti 12 7y 97 7y 9 7 7y47 75's 7 RTD # 13
- 79. YO 7 Y Y/
7 Y 'y/ 75' V/ RTD 0 14 7 5". 4'/ 7 Y '/'/ 7Y t/) 7v yv RTD 0 15 l'f.JI 7c/ -ir
- 70. A u gel.J ef RTD # 16 77t//
7Y 90 7 T-5 V 7 Y. </: RTD P 17 9.Y. OY 7Y69 7Y 64 19 L5' RTD # 18 74 4/0 7 '/ 3 '/ 7ti. G/ 7cd // RTD # 19 7Y 73 7 i" 7'/ 7 y 7d 79 76 RTD 0 20 7 Y Y6 7.Y V 7 7y 9/ 77 RTD i. 21 (SPARE) 73t/f 7 y. V f 77.#1 7y4y RTD # 22 (S PA RE) 7 (J.e 4 7 9.c4 '74.f4 74 (.5 C '( L' 5* A b' A b'A $*.2 Lf c - S p c'T r-t D. Pt. 0 1 fo '/2S' /
- 42 '/
- f. 4 -id
/*430 D. Pt. 0 2 <, ',f d A l 435 /. 4% 1467 D. Yt. i; 3
- 1. <J,2 V
- f. s/8 6 f../dn
/. t/ 5 t' D. Pt. 0 4 /, yM /. H'3v
- s. %fV
- l. f/ /
~. 27 97 $7 27 Prcncurc 0 1 6' S 7 9' l-l 86 75'2-85 7 b~ l 2 5 7 b'O ~ Pressure v 2 (S PAR E) .s'u 4 7 t/ YuA/76 8e 4/ O(/ b e 4 (* 7 D. Pt. - Dow Point RilD - Relative llumidity Dctcetor, ?'- ' ' U 'T 9 ]Ju
- Pressure, i
Terminal Operator l-- i - I U -- A v v v d
W 3/16//y OPERATiliG PROCEDURE 13100.1 PACE 53 IllTIT R ATI.D l.l:AK 1( ATE TI'.ST APPEf! DIX D AMBIE!iT TD!PERATURE Il0UR NO. BAR0!!ETRIC PP. ESSURE DATE ROTA!iETER F1.0W 3,1 VERIFIED BY '.. ' M,l-ILRT DATA SilEET TIME /SA:iPI.E t:0. [00 / /h II/ I /o-Id/ /046/ / RTD # 1 ~77. V(/ '7 9. W 7 9 %> <7 9 y 7 RTD 0 2 'T!d.0Y 7 'l 0 6 7 'l
- C A
'7 'I. C7 RTD 0 3 7 tl
- u.*
"iti. 2i. Jul.:7l: 7 ' u s i.' RTD C 4 74 27 7'l 27 29.'27 7't. 2 7 RTD # 5 /-/ f 7 7/(7 7 'l - ( 7 7tl 0 7 RTD v 6 7y.yd 7 af 96 7 y. Y5 79, y / RTD # 7 7#. */O 74/. '/ / 7 4. S') 7#. 3'/ RTD 0 8 741 07 74 r7 7#.c41 7 'i (5' RTD e 9 1 co..sn , <>. g s 7 t]. <J 4 7(1 <72. RTD # 10 7 f. 2/ 7 4. x' 74/. %/ 7ti.2 / RTD # 11 ?E '72.45 7Y54 7Y >4 75'.5J RTD is 12 7 y. '/ / 7 Y '1D 7YYV 7 Y *> o RTD 0 13 '7 y 'il 7 "$. 91 7V.fi 7 Y. S'l RTD l' 14 ~7 }' t'/(/ 7 Y. '/ i 75'.<i7
- 7) 'ni RTD I' 15 7 (/ 4 /
7 r/ -i J. 7 (f. *;. 7ce. 9 RTD 0 16 7 Y '// 7V t/O 7 9 t/c y <g cta RTD I' 17 7 5' li'/ "/ 3'. 0 41 7YC5
- 7) C '/
RTD # 1H 7(/.4/ 7 '/.
- 7(/ -I'/
7 +'. 4 / RTD # 19 7"/ 74 7'f. 75 7 Y 7V 7 S' /5 RTD 0 20 7Y 3 *i 75 $6 7 520 7 ? '$ 7 RTD i, 21 (.iP u r.) 7y. y 7
- /fd/
7 'y. t4 / 7 Y. vu RTD # 22 (s PANE) 7 </. 04. 74.c2 7 9. c.2 7ct.0L SniqcTrP-G r,.., 3.'2. S. ).
- 3. 2.
.3.2. D. Pt. 0 l /.436 /< '/ $U
- l. 'l 5 5 lo 45,L D.
Pt. 0 2 t.437 I. 4 5 'l t. s/ 61 /. s/.s t i D. Pt. ei 3 14% f.up/ 1, e/ -> f 1.4.57 k_,D.Pt.
- 4
/. Y d/ 5 /.4#( /, '/(/ 6 /, 44/ '.f 97 17 17 27 Pressurc # 1 S'57 7 'l .9577I 85777 $6 770-Prcnnurc !! 2 (S PA R C ) 5 OH DG' Yl; dif 6 & v H c. 4 n:l/C 6 D. Pt. - Dow Point __ RllD - Relative llumidity Detcetor, [, J) i U
- Pressure,
'I f (~ i' n o M,. Terctinal Opcrator J e +
3 M /79 OPERATING Pitocromen g3gno, g, pygg 33 111 TIT.Tt ATI.D f.EAK RATE TI:ST APPE!! DIX D AMBIE!!T TD1PERATURE 75 n0ua tio. BAROMETRIC PRESSURE d d' DATE N 7 '7 ROTAMETER FLOW
- 3. >
J n t/ VERIFIED BY,1 -~ ILRT DATA SHEET TI11C/S/J1Pl.E NO. /7CO/ /7/8 / /780 / /746/ RTD # 1
- 79. (f 7 7$'.4 7 7% Y7 79 %
RTD 0 2 70/. (3 ~7Cl ( 2 7t/. fG ~7 'I c' 2 RTD U 3 7Ll. 75 7tj 'M 7 tt. 2f )sj. M RTD C 4 7tl. 2 G
- 74. JU
^7t? J 1 Hl..- : RTD 0 5 74 67 7 tl.CV 7tl. t v 7c/.c5 RTD # 6 7 y,y3 757 yj_ 79 W 7'y, <f f RTD # 7 781 4 7t/40 76 6Y 74 5Y RTD # 8 7c/.07 7 (f. 0 7 T(/.0 / '7(/.e 7 RTD # 9 7e/. 5 d 7'/. 5 2 77.S'1 7 '/ T ' RTD # 10 74.1I 742/ 7e/. 2 / 7 9*.J r RTD l' 11 7Y V5 79 'M 79 '1I 7 's 1.5 RTD to 12 ~1 'r 's S 7 9' 'sv 7Y.Y5 7 's. 'i5 RTD # 13 7 5 Yu 71'r/- 7 V. 75 7 'r 7 (1 RTD # 14 7 Y (/ 7 7 'i c/ 7 7%'/7 7 'f '/'T RTD 0 lb 7 '/. 4/ 7ct.40 7et. Se 7ci &> RTD # 16 '79 'F/ 7 S. '/F 7 9 Gr. 7 f P/ RTD # 17 76 M 7770 7 V e-(/ '7.T. /.4 RTD # 18 '7(1 4 /
- </ 4 /
7t/../ / 7tf. e/ / RTD # I t) 7 Y. 70 ?? 75 73 75 7v 7T , g, RTD # 20 7? Yi 7 i y.7 77Y/ J '.,.. </ RTD u 21 ts?ARG) 7 c. </v 7 ',r 'iu
- 11. */7 r;U "rf 13,%
e r RTD # 22 (SPARE) 7 t/,() / r/c/.(/ -y r/. (/ 7c/, O / ora N rTOL brec0 d1 3M 3.2
- 8..'2.-
D. Pt. O l / </ 56 f.HHI /r L/ l/ C /*42s D. Pt. # 2 I a 'it/ O /. q ti i /. 445 / i+ u t/ D. Pt. F 3 /. Lt.6 5' /. J 3t{ j J LJ 6 !. :! J C (L ,D. Pt. 0 4 /.i/'/( l. Lf L{ 7 / 'lHU
- f. H 4 Cl
- 7 27 D7 39 Pressure 0 1 9 5 7 7'J SI 7 7 4 Fr 5' 7 7 3
.Y5 77 / Prensurc # 2 (S PARC ) Yo 4/O 2- .) to '/ (c I Fr/4eC 'itc 4 5 '/ D. Pt. - Dew Point RIID - Relative !!umidity Detector, 1 u, ") Ls J iJL
- Pressure, Terminal Operator b'-
S 4
3/16/79 OPERATIt'C PROCEDU!!C 13100.1, PAGE S3 1 liTIT.!! ATI:D I.!:AK R ATE Tf:ST ERO Oc CLRT APPE!!DTX D AMBIE!iT TDIPERATl!RE Il0UR NO. BAROMETRIC PRESSIRE OdOA DATE__ 3 C ROTAMETER F1.ON 3, % VERIFIED BY !, c. 'T ILRT DATA SHEET TIttc/s AMPI.E 1:0. / 7(o / / / / RTD # 1 ~/.7 - T(.- ?g.ye /" ( (' RTD # 2 74 C'L 0
- n u iq.cs N
) RTD 0 3 7 Q. *LS -7ti 14 ) / RTD # 4 7 G 2 /.- 74 JO s RTD # 5 7Q.cT 7'/. 6 5' \\ i RTD f/ 6 7S.34 y y. W \\ e RTD # 7 74 3Y 74.3 7 / \\ RID # 8 74.C7 7si.cu 1 RTD <! 9 7 '/. W 7t/S4 \\ RTD # 10 7(/.Je 7</.M 1 RTD o !l 7V 73 7YY5 ltTD u 12 7'r YS 79' W \\ RTD # 13 '7 Y 7'/ 7V. 73 i RTD # 14 7Y.45 /V </S RTD # 15 7'i. AC -7c/At-s RTD // 16 7? Yf 79.00 RTD # 17 7Y 67 7T47 i nTn o ls 7<! sic ga..m RTD # 19 79 75' 7V 7d RTD # 20 7 9 V'.; W TT RTD v 21 (S PARE ) 7 y../g 7 5 </ s RTD # 22 (SPARE) 79 c0 77.c0 4 D. Pt. d I / s 4 tf(' /. i(q l. D. Pt. i' 2 /
- f W t.445 D.
Yt. F 3 f. *f t./.L /<Of -, D. Pt. # 4 /s c/ 5 6 f. 454 Pressurc # 1 96 77D 6'6 7D f/ Prensure il 2 (SPARC) Se4JY W 'f 57 D. Pt. - Dew Point RilD - Relative !!umidity Detcetor, 22^J l53
- Pressure, Terminal Operator
. f / f( U - s ~ d
3/16/79 OPERAT7::C Pn0CEDU::C 13100.1. PACC 53 I!!TII R ATI'D I.! AK R ATI'. TI:ST STATdTED Btotooce y APPE!! DIX D C P Og -gg g AMBIEliT TDiPERATURE !!OUR 110. /- BARO:iETRIC PRESSURE DATE OO 7 ROTAMETER FLOW VERIFIED BY it ILRT DATA SIIEET a t} u-;;p fril) TI!!E/S A!!Pl.E !!O. //R$% / /(740 /.'2-coa / "*. 7' ( RTD # 1 RTD # 2 RTD (' 3 RTD # 4 JTD 0 5 RTD ft 6 RTD # 7 RTD # 8 RTD (! 9 RTD # 10 RTD # 11 RTD it 12 RTD # 13 RTD l' 14 RTD # 15 RTD # 16 RTD l' 17 RTI) # 18 RTD # 19 RTD # 20 RTD i. 21 (S PA R E ) RTD # 22 (S PARE ) PSin ya o D. Pt. # 1 D. Pt. # 2 D. Pt. 3 t , D. Pt. # 4 Pressurc # 1 l'6 *7 C f -J' ') i 2 u l--[ L .J. s - };.'{,[; g. Pressure it 2 (S P.t RC ) 4 6. u 5 4 p 9 5 3 c, o, r,i c;-7 -g 7 % w D. Pt. - Dow Point i'1 1 I.4 e iJ l J '+ RllD - Relative llumidity Detector,
- Pressure, blA N1 C bis 3 bb dt,Id bb A M
~ v Terminal Operator e
- 3/16/79 OPERATI!;C Pn0CEDUnC 13?.00.1, PACE 53 I tiTIT,R AT F.D I.EAK PATE TEST
\\ W C-M. % APPEtIDIX D ^ AMBIENT TEMPERATURE HOUR NO. BAROMETRIC PRESSURE DATE 9 0 9C/ ROTAMETER H.0W VERIFIED BY ft mp ILRT DATA SHEET TDIE/ SAMPLE NO. 7/#8 / 3/30/ 2.D(b/ 319/ ( RTD # 1 s RTD # 2 RTD (: 3 RTD 4 4 RTD 18 5 RTD 17 6 RTD # 7 / RTD # 8 RTD le 9 g RTD # 10 4 RTD ^ l1 RTD 12 RTD # 13 _RTD # 14 ttTD f; 15 RTD 4 16 RTD (7 17 RTD F 18 RTD If 19 RTD o 20 RT D i, 21 (S ?A RE ) RTD # 22 (S PARE ) 463c tuTE PCG E4. 7 3 4. /, 3:2.7 s'),9 D. Pt. # 1 D. Pt. d 2 D. Pt. 3 , D. Pt. # 4 Pressure n 1 ~7 C f,, f 0 TC4*iu (. C Wje '2 9 2.. Pressure # 2 (S PAR E ) f A / 9ts 7 c, # M O /-/,'7/ g, 63&co D. Pt. - Dew Point J l55 RllD - Relative Huctidity Detector, Pressure, b.7 O$I d Terminal Operator
I [/16/79 3 ) W ( L 6 A.L % OPERATING Pn0CEDURF. 13100.1, PACE 53 3 INTirR ATED I.1:AK RATE TT.ST APPEf; DIX D ( AMBIENT TDiPERATURE Il0UR NO. / 3O~ [!7 k BAROMETRIC PRESSURE DATE i ROTAMETER FLOW VERIFIED BY ILRT DATA S!!EET TIlfE/ SAMPLE NO. M!O / ' ,23 9 / dd/ CC;D/ { RTD # 1 RTD # 2 RTD (' 3 RTD # 4 RTD # 5 RTD # 6 RTD # 7 RTD # 8 RTD F 9 RTD fi 10 RTD o 11 RTD it 12 RTD # 13 RTD ^ 14 RTD # 15 RTD !! 16 RTD # 17 RTD # 16 RTD # 19 RTD d 2D RTD ie 21 (S PA n d ) RTD # 22 (S PARE) PS)R D '). l5 2 7. sD .2 6.1 > 2 4 4 5' D. Pt. M 1 D. Pt. d 2 D. Pt. r-3 ( D. Pt.
- 4 Pronsucc n 1
<!) / F n fff. S*c7 52 7f5~ 4 J G.,; Pressure !! 2 (SPARE) %OuAO JS9 FO C 2 cf 9 47 p,s.i., f D. Pt. - Dcw Point 3 r* EllD - Relative ilumidity Detector, c J lU fb
- Pressure, i
Terminal Operator
Em 3/16/79 OPERATI!iG PROCEDURE 13100.1, PAGE 53 I?;TECR ATI:D !.EAM P ATE TEST APPE? DIX D \\ AMBIE!iT TCiPERATURE HOUR liO. ~3!2/!'/f BAROMETRIC PRESSURE DATE ROTAMETER FLOW VERIFIED BY ILRT DATA SIIEET TI11E/S?d!PLE ??O. d/rd /
- /3 0 /
d2.o") / ' Jo / f RTD # 1 RTD l' 2 RTD I: 3 RTD # 4 RTD # 5 RTD # 6 RTD # 7 RTD # 8 RTD F 9 RTD 5 10 RTD # 11 RTD 1 12 RTD t' 13 RTD l' 14 RTD (! 13 RTD ti 16 RTD I' 17 RTD ti 18 RTD !! 19 RTD F 20 RTD re 21 (S PARE ) RTD # 22 (S PARE) 93ll0 sl3 3 1 3.2. / 2.
- 21.00 19 9 D. Pt. #
1 D. Pt. # 2 D. Pt. F 3 .D. Pt. # 4 Pressure a 1 47/27 5 '16 'l C N 2 -1 C"5' - l i ' I Pressure e 2 (SPARE) 9 7 7 'f t? 4 *t ' 2 C 4 1 8?x 4 <* '+ O ) i l D. Pt. - Dew Point RilD - Relative llumidity Detector, ,,f j77 r,d'd 1J/
- Pressure, Terminal Operator
Euw 3/16/79 OPERATING P".0CEDURE 13100.1, PACE 53 I NTlY;R ATED f.EAK R ATE TEST APPENDIX D AMBIENT TD!PERATURE HOUR NO. BAROfETRIC FP. ESSURE DATE 2 / f I / ROTAMETER FLO'J VERIFIED BY ILRT DATA SHEET C { eof e 430/ TI?IE/Sl11PLE No. 03CO / C330/ T ( RTD # 1 RTD # 2 RTD # 3 RTD # 4 RTD # 5 RTD # 6 RTD # 7 RTD 8 ^ RTD t' 9 RTD # 10 RTD # 11 RTD F 12 RTD # 13 RTD # 14 RTD 9 15 RTD # 16 RTD # 17 RTD # 18 RTD # 19 RTD ? 2D RTD u 21 (Siwrm ) RTD # 22 (S PARE ) PSIA iMT 15 18 1745W is. 30 D. Pt. # 1 D. Pt. il 2 D. Pt. i' 3 .D. Pt. # 4 Pressure # 1 3 94 Y# 36 '2 6 (J .3 52 C. 7 3 3 r/ 6 / Pressure v 2 (SPARE) 3 :y.5 0 (- 2 / w e/r> 35_792 3> yr. / D. Pt. - Dev Point f 72 Jf 8 C A'0 RilD - Relative Humidity Detector,
- Pressure,
^'*1 5 rn J lJO Terminal Operator
T 3/16/79 OPERATING FROCEDURE 13100.1, PSCE 53 IN11' Cit AT!.D i.EAK H ATE TERT APPENDIX D AMBIENT TFliPERATURE 110UR NO. BAROMETRIC PRESSURE DATE 3 2/~77 ROTAMETER FLOW VERIFIED BY ILRT DATA SHEET TI1!E/S AMPLE NO. O f40 / CT3e/ o 7ove / c( h / RTD # 1 s RTD # 2 RTD F 3 RTD # 4 RTD # 5 RTD # 6 RTD # 7 RTD # 8 RTD (* 9 RTD # 10 RTD # 11 RTD v 12 RTD # 13 RTD l' 14 RTD # 15 RTD /! 16 RTD # 17 RTD (/ 18 RTD # 19 RTD ' 20 RTD F 21 (.s PA RE ) RTD 4 22 (S PARE) l' bl.0 IN N is 7f /.5.3 8 /5 16 D. Pt. # 1 D. Pt. i' 2 D. Pt. te 3 D. Pt. # 4 Pressure # 1 3 2 94 C 3 / /[( f Q// Q 3.'ii73-Pressure v 2 (SPARE) 32930 T j 9 9.-; g j / p et %p grf D. Pt. - Dcu Point f -]3328 090 RilD - Relative liumidity Detector, 3-j c.g'
- Pressure, t-
' iJ iJ/ Terminal Operator /
3/16/79 OPERATING ITOCEDURC 13100.1, PACC 53 INTLY:nATED f. EAR MATE TEST APPENDIX D AMBIENT TCPERATURE HOUR NO. BAROMETRIC PRESSURE DATE 3 d/9 Y ROTAMETER FLOW VERIFIED BY ILRT DATA SHEET TmE/SAMP1.E '!O. C7tC / O7#A / / / ( RTD # 1 Of.1 '! RTD # 2 7 4I '/ / KTD F 3 o r. 71 RTD # 4 4 V. V/ RTD 0 5 r13 72 RTD # 6 7.t,9 f RTD # 7 75.<f 9 RTD # 8 7 5.3 7 RTD # 9 h. ei 7 fD G lO 'li,.i f RTD # 11 7C60 RTD it 12 7 7,0.F RTD # 13 '7E ~7 7 RTD f 14 7 F. 4 / RTD # 15 7/. 69 RTD # 16 9 C /.f RTD (t 17 75 <f '/ RTD # 18 7 t. 6/ RTD # 19 7f,34 RTD (f 20 7(.. A.Y RTD i; 21 (.s i'Ai' C ) f+t- :L*/ /6 3 0,g/ RTD # 22 (S PARE ) 7g,f A P3 I A IA.54 /4. 'If D. Pt. l 37s* D. Pt. # 2 'T r).5~ l't. F 3 L,. D. A S.; s D. Pt. # 4 ,468 ~ Pressure # 1 30/66 2 'I k W ? Prensure il 2 (SPARE) .40420 2159/ D. Pt. - Dew Point RllD - Relative Humidity Detector, q-j 3
- Pressure, Terminal Operator
3/16/79 OPERATING PROCEDURE 13100.1, PACE 54 INTECRATED !.EAK RATE TEST I i APPENDIX E Data Sheet for Manual Calculations ] }v'} ') - m G
3/16/79 OPERATING PROCEDURE 13100.1, PACE 55 INTECRATED LEAK RATE TEST FOR INFORMATION ONLY INTECRATED LEAK RATE TEST DATA SHEET I. CALCULATIONS [Pf,,, Wf Pg,Uf l (Ti ) Tf ) L= [100x24 ,fPi Wi\\ l Ti / At I k or (PfU)T L= [100x24 1 f i .( A t (Pi-W)Tf
- 7. per day i
A. At = Duration of test = hours B. Pi-Wi= psia C. Tg= F + 459.69 = R, D. Pf-Wf= psia = E. Tf= F + 459.69 = R In the unlikely event that the coquter is lost, a desk calculator or similar unit may be utilized and shall be available for this purpose. II. RESULTS L = 2400 1-( ) ( )
- 7. per day
= (24) ( ) ( ) All parameters to be recorded for all test phases except pressuricatio and depressurization. All readings taken at one (1) hour intervals, m imum.
- 'a 1 1 ]
4_. iV 1v Verified by: Date: .-,e e. e e>
3/16/79 OPERATI!!C PROCCDt3tE 13100.1, PACE 56 INTEOR ATED ! CAK R ATE TEST \\, i APPENDIX F I & C Instrument List r,. n j 3[.- () $U e
3/9/79 OPERATING FRCCEDL'RE 13100.1, PAGE 56 INTECRATED LEAK RATE TEST d.kd O 3se M. Aswua CONTAIWENT EOUIPMENT CHECK LIST c-1. Fischer Porter /Haran Transmitters - On all below listed transmitters, insure cover o-rings are installed and in good repair. Tighten cover hand-tight. Transmitter # l Function Ferformed Bv Restored-0C l PI-3-138 Excess Ltdn Line Press J-e5 7 Y .* -L
- - 1t, I f C4 FT-3-436 RC Flow Loop C cc FT-3-435 RC Flow Loop C cc FT-3-932 Sa f e ty Inj. Line Flow Loop A FT-3-933 Safety Inj. Line Flov Loop B CC.
EC FT-3-434 RC Flow Loop C CC FT-3-424 RC Flow Loop B I'r FT-3-425 RC Flow Loop B cc_ FT-3-426 RC Flow loop B .cc. PT-3-402 RCS Wide Range Press. A PT-3-403 RCS N.R. Press. EC-PT-3-405 RCS W.R. Press. CC FT-3-416 RC Flow Loop A E" ZC-FT-3-415 RC Flow Loop A =h E FT-3-414 RC Flow Loop A 14 Ec. PT-3-1004 RCS Drain Tank Press. MM fc PT-3-155 RCP "B" Seal Delta P h M PT-3-128 RCP "B" Thermal Barrier Delta P CC LT-3-484 Stm Cen "B" N.R. Level Ch. 1' F oc. LT-3-485 Stm Gen "B" N.R. Level Ch. 2 cc LT-3-486 Stm Cen "B" N.R. Level Ch. 3 Y~' CC-LT-3-487 Stm Gen "B" W.R. Level H^~ tc PT-3-455 Przr Press. Proc. Ch. I te fc PT-3-456 Przr Press. Prot. Ch. II /- ~ - cc. PT-3-457 Przr Press. Prot. Ch. III W-EC. PT-3-445 Przr Press. Control fed - LT-3-462 Przr Level Control ec.
- u. <
PT-3-444 Przr Press. Control EC-PI-3-458B Przr Press. Cal. s <- l'C PT-3-92 3 Acc. Tank A Press. icC ' ZC PI-3-131 RCP C Therc:a1 Barrier -;4C E f-PT-3-156 RCP A Seal Delta P +++--- C C-PT-3-4 72 PRT Pressure 84- ,, fC b LT-3-4 74 Stm Gen A N.R. Level Ch. 1 tt LT-3-4 75 Stm Con A N.R. Level Ch. 2 fC LT-3-4 76 Stm Gen A N.R. Level Ch. 3 WCC. ' f,,. LT-3-4 7 7 Stm Cen A N.R. Level .ru 2c PT-3-921 Acc A Press. N i c. PT-3-925 Ace B Press. E PT-3-92 7 Ace B Press. ff. PI-3-929 Acc C Press. E pc LT-3-494 Stm Gen C N.R. Level Ch. I } ec LT-3-4 95 Stm Cen C N.R. Level Ch. II c/l g LT-3-496 Stm Gen C N.R. Level x ec LT-3-497 Stm Gen C W.R. Level @jo,% tsc PT-3-931 Acc C Press vnJ N-lz PT-3-154 RCP 3C Seal Water Delta P @d"' r_c PT-3-125 RCP Loop C Shaf t Seal Delta P Ec FT-3-494 Stm Cen C Stm Flow Ch. I 'P ' /d c FT-3-495 Stm Con C Stm Flow Ch. II W Y cc pf,r._ n, ,n -J 104
T/'1179. OPERATING FROCEDURE 13100.1, PAGE 57 % 7-INTECR ATED LEAK RATE TEST _jg Transmitte r # Function Pe r fo rmed By Restored-CC FT-3-485 Stm Gen B Stm Flow Ch. II -vu-J-26-71 # 4-EC FT-3-484 Stm Cen B Sem Flow Ch. I fc. FT-3-4 74 Stm Cen A Stm Flow Ch. I J T-3-4 7 5 Stm Con A Stm Flow Ch. II pscd_. g 2. Barton Le el Transmitters - On all below listed transmitters, insure cover o-rings are installed and in good repair. Tighten covers. \\ Transnitter # Fun ct ion Performed By Restored-0C o a i.r.e.d G-LT-3-459 Press. Level Prot. Ch. I e LT-3-460 Press. Level Prot. Ch. II j T c, ,hs [ /E C LT-3-461 Press. Level Prot. Ch. III 3 Barton Flev Indicatine Switches - Loosen the covers on all of the below listed equipment. Transmitter # Function Per f o rmed By Restored-0C ! FIC-3-4')0 RTD Bypass Flow A u,,,,,,,
- 7. - u ni CC e W--
P C-FIC-3-491 RTD Bypass Flow B FIC-3-492 RTD Bypass Flow C u.,o w cc 4. Brocks Flev Indicator / Transmitters - Loosen the covers on all of the below listed equipt.ent. Transmitter # Func tion Performed Bv Restored-0C FT-3-15 6A RCP A Seal Leak Off (Hi) }e5-35
- 8. - t -%
- 2. -% Tr Cf FT-3-156B RCP A Seal Leak Off (Lo) cc FT-3-155A RCP B Seal Leak Off (Hi)
+ cc FT-3-155B RCP B Seal Leak Off (Lo) Q r e_ .C C FT-3-154A RCP C Seal Leak Off (Hi) 4G FT-3-154B RCP C Seal Leak Off (Lo) FIC-3-154 Low Flow RCP C Seal Water g FIC-3-635 RCP C Low Flow CCW 'Cr_
- ^
h< cc FIC-3-629 RCP A Low Flow CCW FIC-3-632 RCP B Low Flow CCW f-2C FIC-3-155 Low Flow RCP B Seal Water 3-5 cc FIC-3-156 Low Flow RCP A Seal Water f IA y EC 5. Pressurizer Instrument Cabinet Heaters - De-energize heaters by performing th e ) ~ "' t t following. 's4J !uJ Transmit te r r/ Function Performed By Restored-CC TC-3-440A B/S switch to tes t (Rack 2) 3-es-71 ph 3-3-7f cc TC-3-4 41A B/S switch to test (Rack 12) J. < s 11 +'C-RC l TC-3-44 2A B/S switch to test (Rack 15) 3-it-7f T c. TC-3-4 4 3A Remove output fuse (Rack 7) 3 - e r - 77 h-f cc.,
3/9/79 OPERATING PROCEDURE 13100.1, PAGE 58 INTECR ATED LEAK RATE TEST g Jbs 6 M. if < e :M 6. Remove.the following equipment from the Centainment. ,, y i. Ecuipment Perfor-ed Bv ( Restored-OC Flux mapper Gas Bottles 33-7F j dtf
- 3 -2I. m f R.C.
C-e 4 - ~ n : Lc:p ~'ca:MIb66 073C # M66 ARMS G.M. Tubes
- 3.,r-77 p%
2-2G-M O Dillion Load meters (manipulator & polar crane) g.,s rr g 3.y,. m g 7. Install the following jumpers, with Temporary jue:per tags. Ra ck J Terminals i Performed By i Restored-0C l 3Q R 51 P1 to 5 3 -' = - 7 '/ .s e - 3 n -19 sC h* cc 3Q R 51 33 to 35 I 3Q R 51 23 to 25 f.c 3Q R 50 9 to 11 +* pr 3Q R 50 39 to 41 8' i 3Q R 50 373 to 377 h f w y' cc 8. Conduct inspection of all levels in Containment and ensure l Pe rf o rme d Bv ! Restored-0C All Local Gauges (Pressure and Temp) faces are y,.r- / / -tw ' 3-24 M etc. removed All Local flowrators have at least one glass f ace M ' '? 3 g.] q gg removed 9 ": ify Cm. ai. c.: mr L:c:1 :j; a i; emLtb oTSC, # 4(o6 ~ YY05 O Qi D ~ 22 -- f - ~2 y v t n\\o a, \\ of N*W Psys 5 6, s '1.5 g wA S S v. -i-Ri\\M eM "a er b d oi-3lldM g ( U-;% % eM mA .5 m wmu m-Wsm, v na a wu scim u aut uo a we % '%ed C, s chE" b .\\.T * ( T O ' i. TN3 ch ny gv (- g d e k sc w %%er. 9 d t* Ys H-l -6 I E M P'" W. T's .,J 3 w. 56-5% w-n p 'n w..pu s bb, c % n 3._ o,s z b
- C'bl.3 3{ 86f 7 i vm iU s U lL u
3/9/79 CPERATINC PROCEDURE 13100.1, PACE 59 INTECRATED LEAK RATE TEST AIR OPERATED CONTAI! MENT VALVE FAILCRE MODE VALVE FAILURE MODE CV-3-200 A 3-/5-79 Closed r - CV-3-200 B l Closed f,h"~ CV-3-200 C Closed 3'* CV-3-307 Closed M CV-3-310 A Open CV-3-310 B open F CV-3-311 Closed M" CV-3-387 Closed h h"" CV-3-460 Open CV-3-455 A Closed [2.* ?pga g D.6/tt) 6dd CDC O$ 664 MC N CV-3-4555'8//L Closed h *- CV-3-455 C Closed M * -C V M S Ef>s Dd ' GrG cl ::dpt (D6t.dTef) Odd CGC AS5 CV-3-519 A Closed ds~ CV 2 522 & D6Ldf6 Clcc=d }yn (Oc!Lere), bdd ofbc 4GG CV-3-519 B Closed j)
- CV-3-522 A
' Closed y/" CV-3-522 B Closed y CV-3-522 C Closed tAA*- CV-3-523 Closed fd'- CV-3-549 Closed d'* CV-3-544 open dMi" CV-3-389 Dive r t.;2!." CV-3-853 A Closed @W CV-3-851 A Closed M CV-3-852 A Closed g2
- Closedjg"'"
CV-3-850 A CV-3-850 B Closed t(8 CV-3-853 B Closed #1'* 3 CV-3-851 B Closed (MM CV-3-85 2 B Closed,g ** CV-3-850 C / Closed?h # CV-3-850 D Closed g! CV-3-850 E Closed 423'" (~ CV-3-850 F Closed //!'* I CV-3-852 C ClosedjlP"" CV-3-85 3 C Closed,82 # CV-3-851 C Closed.d F CV-3-936 Closed'pI
- Closed [U "
CV-3-951 Closed t ""'U UI CV-3-953 CV-3-955 B ClosedM"" CV-3-95 5 C Closed 4 " CV-3-955 D Closedg'* Closed CV-3-955 E v LCV-3-1003 A ), Closed d" Closed d'" LCV-3-100 3 B v
3/16/79 OPERATItiC PROCEDURE 13100.1, PACE 61 ItiTECP. ATED !, EAR R ATE TEST 5 APPENDIX G Breaker I.ist p ,,O n,,, IL J. J C
3/9/79 OPERATINC PROCEDLHE 13100.1, PACE 61 INTEGR ATED LEAR RATE TEST ELECTRICAL EQUIPMENT INSIDE UNIT #3 CONTAI!NENT Canister No. T3C21 Containment Cooling Fan A MOV-3-865A Accumulator A Discharge to a Cold Leg 3B0518 3B0532 RCP #3A 011 Lif t Pu=p 3B0554 Containment Sump Pump 3A ~ / 3B0667 _ Canister No. T3C22 Conrain=ent Cooling Fan B 3B0642 Control Rod Drive Mechanisms Cooler 3A 3B0629 MOV-3-750 Loop C Hot Leg to RHR ~ ' 3B0615 MOV-3-744B RER Return to Cold Legs 3B0613 MOV-3-866B Delayed HH SI to Loop B Hot Leg 3B0621 MOV-3-865B Accumulator B Discharge to B Cold Leg MOV-3-535 Pressurizer Power Relief Isolation 3B0631 3B0606 Reactor Coolant Pump 3B Oil Lif t Pump 3B0679 Reactor Coolant Drain Tank Pump 3A Thermal Cut-Out 3B0662 Canister No. T3Cl3 Containment Cooling Fan 3D B0829 'lJ. '3 ') 1 0 IU/ .u Capigger No. T3C23 Containment Cooling Fan 3C 3B0742 Control Rod Drive Mechani:m 'n d3 3 ,,1
- 3B
.~ 3B072 7 Reactur Coolant Pump 3C 011 Lxf t Pump "' ~ ' - 3B0762 V-3-865C Accumulator 3C Discharge to Loop C Cold Leg ' 3B07f }. HOV-3-536 Pressuri:cr Power Relief Valve Isolation 3n075,! A '$. )'~ me
3/16/79 OPERATING PROCEDURE 13100.1, PACE 62 INTEGRATED LI:AK R ATE TEST ELECTRICAL EOUIPMENT INSIDE UNIT #3 CONTAINMENT Canister No. T3C21 Containment Cooling Fan A 3B0518 MOV-3-865A Accumulator A Discharge to a Cold Leg 3B0532 RCP #3A 011 Lift Pump 3B0554 Containment Sump Pump 3A 3B0667 C. Canister No. T3C22 Containment Cooling Fan B 3B0642 Control Rod Drive Mechanisms Cooler 3A 3B0629 MOV-3-750 Loop C Hot Leg to RHR 3B0615 MOV-3-744B RHR Return to Cold Legs 3B0613 MOV-3-866B Delayed HH SI to Loop B Hot Leg 3B0621 MOV-3-865B Accumulator B Discharge to B Cold Leg 3B0631 MOV-3-535 Pressurizer Power Relief Isolation 3B060a Reactor Coolant Pump 3B Oil Lift Pump 3B0679 Reactor Coolant Drain Tank Pump 3A Thermal Cut-Out 3B0662 Canister No. T3C13 Containment Cooling Fan 3D B0829 2 ) [] Canister No. T3C23 Containment Cooling Fan 3C 3B0742 Control Rod Drive Mechanism Cooler Fan #3B 3B0727 Reactor Coolant Pump 3C 011 Lif t Pump 3B0762 MOV-3-865C Accumulator scharge to Loop C Cold Leg 3B0733 s : MOV-3-536 Pressurizer Power Relief Valve Isolation 3B0713
m. 3/16/79 OPERATING PROCEDURE 13100.1, PACE 63 INTEGRATED l.EAK RATE TEST Canister No. T3C23 (continued) MOV-3-751 Loop C Hot Leg to RHR Pump Suction 330731 Mov-3-744A RIIR Return to Cold Legs 3B0722 MOV-3-866A Delayed High Head SI to Loop A Hot Leg 3B0732 Reactor Coolant Drain Tank Pump 3B Thermal Cut-Out 3B0787 Canister No. T3Pil ( Emergency Containment Filter Fan 3A 3B0611 Normal Containment Cooler Fan 3B 3B0642 Control Rod Drive Mechanisms Cooling Fan 3A 3B0629 Lighting Transformer 36 3B0658 Containment Elevator #3 3B0619 Canister No. T3P21 s. Reactor Crane 3 3B0104 Normal Contal- ..t Cooler Fan 3A 3B0518 Lighting I-a El D.C. Feed 3YO605 Canister No. T3P32 480 Volt Receptacle #17 and #17A 3B0653 ( Reactor Coolant Drain Tank Pump 3A 3B0662 Canister No. T3P33 480 Volt Misc Containment Distribution Panel (3P11) 3B0673 0 1?] t, d I /
3/16/79 OPERATING PROCEDURE 13100.1, PACE 64 INTEGRATED LEAK RATE TEST Canister No. T3P12 Emergency Containment Filter Fan 3C 3B0719 Normal Containment Cooler Fan 3C 3B0742 Control Rod Drive Mcchanism Cooler Fan 3B 3B0727 Lighting Transformer #37 3XO7 Containment Entrance 3B0768 Canister No. T3P22 ( Emergency Containment Filter Fan 3B B0806 Normal Containment Cooler Fan 3D B0829 Canis ter No. T3P35 480 Volt Misc Containment Distribution Panel #1 (3P10) 3B0771 Reactor Coolant Drain Tank Pump 3B 3B078 7 s Canister No. T3P41 Pressurizer Heaters 2, 23, and 50 3B1101 Pressurizer Heaters 26, 53, and 54 3B1103 Pressurizer Heaters 7, 29, and 5 7 3B1105 Pressurizer Heaters 10, 32, and 60 3B1107 Pressurizer Heaters 12, 35, and 64 3B1102 Pressurizer Heaters 38, 67, and 68 3B1104 Pressurizer Heaters 17, 41, and 71 3B1106 Pressurizer Heaters 19, 44, and 75 3B1108 Emergency Containment Cooler Fan 3A 3B0650 ' q ,f a d i L i
- u. a
->mmm
3/16/79 OPERATING PROCEDURE 13100.1, PAGE 65 INTECRATED T.EAK R ATE TEST Canister No. T3P51 \\ Misc AC Instruments 3P0610 Space Heaters 3YO439 Space Heaters 3Y0521 MOV-3-865B Accumulator B Discharge to B Cold Leg 3B0631 Reactor Coolant Pump 3B 011 Lif t Pump 3B0679 MOV-3-866B Delayed HH SI to Loop B Hot Leg 3B0621 ( s MOV-3-535 Pressurizer Power Relief Isolation 3B0606 Containment Sump Pump 3A 3B0667 MOV-3-744B RHR Return to Cold Legs 3B0613 MOV-3-750 Loop C Hot Leg to RHR (IMB) 3B0615 Canister No. T3P42 Pressurizer Heaters 21, 47, and 48 3B1201 ( Pressurizer Heaters 3, 24, and 51 3B1203 Pressurizer Heaters 5, 27, and 55 3B1205 Pressurizer Heaters 8, 30, and 58 3B1207 Pressurizer Heaters 33, 61, and 62 3B1209 Pressurizer Heaters 13, 36, and 65 3B1202 Pressurizer Heaters 15, 39, and 69 3B1204 Pressurizer Heaters 18, 42, and 72 3B1206 Pressurizer Heaters 20, 45, and 76 3B1208 Emergency Containment Cooler Fan 3B B0820 3,7 4 v i* 3
3/16/79 OPERATINC PROCEDURE 13100.1, PAGE 66 INTECRATED LEAK RATE TEST Canister No. T3P53 Space Heaters 3YO467 Space Heaters 3YO501 Space Heaters 3YO502 Space Heaters 3YO504 Space Heaters 3YO503 Space Heaters 3YO505 ( Space Heaters 3Y0506 Space Heaters 3Y0507 Space Heaters 3YO508 Misc AC Instruments 3P0814 MOV-3-865C Accumulator 3C Discharge to Loop C Cold Leg. 3B0733 Reactor Coolant Pump 3C 011 Lift Pump 3B0762 MOV-3-866A Delayed high Head SI to Loop A Hot Leg 3B0732 MOV-3-536 Pressurizer Power Relief Valve Isolation 3B0713 MOV-3-744A RHR Return to Cold Legs 3B0722 MOV-3-751 Loop C Hot Leg to RHR Pump Suction 3B0731 Containment Sump Pump #3B 3B0778 Fuel Tilting Winch Panel 3B (IC) 3B0763 i3 a le4 Canis ter No. T3P43 Pressurizer Heaters 1, 22, and 49 3B1301 Pressurizer Heaters 4, 25, and 52 3B1303 Pressurizer Heaters 6, 28, and 56 3B1305 Pressurizer Heaters 9, 31, and 59 3B1307 Pressurizer Heaters 11, 34, and 63 331309 Pressurizer Heaters 14, 37, and 66 331302
3/16/79 OPERATING PROCEDURE 13100.1, PACE 67 INTEGRATED LEAK RATE TEST Canister No. T3P43 (continued) Pressurizer Heaters 16, 40, and 70 3B1304 Pressurizer Heaters 43, 73, and 74 3B1306 Pressurizer Heaters 46, 77, and 78 3B1308 Emergency Ccatainment Cooler Fan 3C 3B0729 Canister No. T3P S 2 (' Misc AC Instruments 3P0917 Space Heaters 3Y0439 Space Heaters 3Y0521 Edsc A.C. Instruments 3P0714 MOV-3-865A Accumulator A Discharge to a Cold Leg 3B0532 RCP #3A Oil Lift Pump 3B0554 Space Heaters 3YO403 ( Space Heaters 3YO404 Space Heaters 3YO410 Canis ter No. SKV "A" RCP Reactor Coolant Pump A 152-3AA01 f Canister No. SKV "B" RCP Reactor Coolant Pump B 152-3AB01 Canis te r No. SKV "C" RCP Reactor Coolant Pu=p C 152-3AB06 L
- j }/3
3/16/79 OPERATING PROCEDURE 13100.1, PACE 68 INTECRATED LEAK RATE TEST MISC RCP 3A Heater 3reaker 3AA01 RCP 3B Hester Breaker 3AB01 RCP 3C Heater Breaker 3AB06 Canister No. T3Cl2 Fuel Tilting Wench 3FTS/3C08-T3C12/1 Fuel Tilting Wench 3FIS/3C08-T3C12/2 Code Call & Fire Alarm W6 Canister Wire ref. 26 Spare Canister Wire ref. 6 & 8 Canister No. T3C31 Spare Canister Wire ref. 7 & 12 Public Address Communication System Canister Wire ref. 11. PAX Telephone W3 Canister Wire ref. 9 Canister No. T3C41 Spare Canister Wire ref. 12 Telephone Circuit for Maintenance W7 Canister Wire ref. 11 Public Address Communication System Canister Wire ref. 7 (w Canister No. T3Cll Spare Canister Wire ref. 5, 6, 8, 18 & 22 Remote Control LP 37 Canister Wire ref. 2 Canister No. T3P31 Spare Canister Wire ref. 25 & 26 ][ ] O}}