ML20138P364
| ML20138P364 | |
| Person / Time | |
|---|---|
| Site: | Hope Creek  |
| Issue date: | 11/20/1985 |
| From: | Hight G, Jacqueline Thompson WYLE LABORATORIES |
| To: | |
| Shared Package | |
| ML20138P358 | List: |
| References | |
| 17761-1, 17761-1-R-A, NUDOCS 8512260075 | |
| Download: ML20138P364 (74) | |
Text
4 CERTIFICATION TEST REPORT OF AIR VS. WATER CORRELATION FOR LEAK TESTING OF I
HOPE CREEK REACTOR COOLANT .
BOUNDARY VALVES 8512260075 851223 4 DR ADOCK 0500 les
^
REVISIONS neviSiou TEST REPORT NO. 17761-1 s November 20, 1985 DATE:
SCIENTIFIC SERVICES AND SYSTEMS GROUP REV.NO. I DATE PAGES AFFECTED BY APP't. DESCP,IPTION oF CH ANGES A 11/20/85 1 through 8 [g ]g,pgpranges in text and organization for
[] customer clarity.
9 New page, " Appendix I" 10 through 29 Page number change only.
30 New page, " Appendix II" _,
4 31 through 36 Page number change only.
37 through 71 !@M, , New pages: Appendix III - Field Te.c_
"/#[ Calib ration Shee ts . _
1 Form 1054 3 Rev 4 74 k
CERTlFICATION M S s F M 5""" "S LABORATORIES GROUP Huntsville, Alabama 35807 TWX (810)726 2225, Phone (205)837-4411 RDOM REPORT NO. 17761-1 Public Service Electric & Gas Company Hope Creek Generatine Station CUSTOMER P. O. NO. 083496 P.O. Box A Hancocks Bridge, NJ 08038 CONTRACT NUMBER OF PAGES November 6,1985 DATE 1.0 REQUIREMENTS i A The specimens for laboratory testing were subjected to tests in accordance with Wyle Test Procedure No. 17761-1, Rev.1. The specimens for field testing were subjected to tests in accordance with PSE&G LLRT Procedure PSSUG-PTP-GP-2, as indicated in the Wyle Test Procedure.
The objective of the test program, which this report is intended to support, is to provide PSE&G with analytical and empirical justification that satisfactory compliance to 10CFR50 Appendix J, Type C testing will meet or exceed the requirement that reactoc coolant pressure boundary isolation valves, at reactor coolant pressure, have an individual leakage of less than one gallon per minute for any valve.
The establishment of such justification would eliminate a need to perform the high pressure leak test prior to returning to power after an outage, or after valve repairs. In other words, elimination of the high pressure leak tests could be justified on a correlation of Type C tests at 48.1 psig to high pressure leak tests with water at 1020 psig.
WY *** "* "a h*D'"'r ' 88'"*See os any a.no io corson or proceny.
STATE OF ALABAMA I $$ incluomo soecial or consequential darrages, resusting from Wyie e providmq l
l npson '
f b ~
,being durv eworn, d pos and says: The information contained in this report of cornplete and P D *
y' ' //"
- ' N h [']"*[
- e. '****"",**"" APPROVEDB h %b S E e re me th48 8 d%/M/ .teJL f g' < //7 /g s
NotQPublic in and for the State of Alabama at p,s. 2 4//L.1e..,nn.
large.u,c..n.
/
FORM 1019A, Rev. Jan '84 6
PAGE NO. 2 TEST REPORT NO. 17761-1 REV. A 2.0 SPECIMEN lA For laboratory tests: six local prepared orifices with nominal diameters as follows: .012 in
.020 in.
.031 in.
.040 in.
.052 in.
.060 in, and two 1/4 inch micrometer valves.
For field tests: Identified penetrations as per PSEG.
~
3.0 PART NO.
lA There are no part numbers for the local prepared orifices. For the field tested valves, sufficient data for fullidentification is provided in the Field Test Data Sheet, Table 5, Appendix I. For the micrometer valves:
Mfgr. - HOKE P/N 1315G4Y
- NUPRO P/N SS-2M-S6 4.0 SERIAL NUMBERS - None.
4 5.0 PROCEDURES fA The flow of fluids through an orifice may be expressed as follows (see reference 2.4 of the Test Procedure, " Crane Technical Paper No. 410"):
q = YCA where q = rate of flow Y = net expansion factor for compressible flow through orifices, nozzles, or pipe C = flow coefficient for orifices and nozzles A = cross sectional area of the orifice 2g = gravitational constant AP = differential static pressure (head) across the orifice or nozzle P= weight density of the fluid WYLE LABORATORIES Huntsville Facility
PAGE NO. 3 TEST REPORT NO. 17761-1 REN . A The expansion factor (Y) for compressible flow is a function of:
- 1. The specific heat ratio k, which varies slightly with different pressures and temperatures. For air and nitrogen at 68 F and 14.7 psia, the specific heat ratios are 1.4 and 1.41 respectively.
- 2. The ratio (# ) of orifice or throat diameter to inlet diameter.
- 3. Ratio of downstream to upstream absolute pressures.
If all tr above conditions were held fixed except for area, the flowrate R through a set of similar orifices would be directly proportional to the area of the orifice, and 9 plot of flowrate versus area would be linear.
For the laboratory tests, a series of six different sizes of orifices were prepared by drilling holes in metal plates. No particular attention was given to accurate sizing or to finishing the edges of those holes. These orifice plates along with two micrometer valves were used as specimens to gather correlated flowrate data for nitrogen at low pressure, and then water at high pressure over a range of areas and valve openings (valve turns).
For a meaningful correlation to exist between the laboratory data for the nitrogen versus water flowrates it was assumed that the laboratory data for each fluid would exhibit close correlation with the above linear relationship of flowrate versus area. This further assumed that variations in the finish of the edges of the six orifices, and that slight variations in temperature of the nitrogen (compressible) fluid would not be significant. The following analyses of th'e laboratory test data show these assumptions to be valid and that a close linear relationship exists for flowrate versus each set of specimen area variations. .
WYLE LABORATORIES Huntsvme Facinty
r PAGE NO. 6 TEST REPORT NO. 17761-1 REV. A 5.1 Laboratory Tests Six orifice sizes and two micrometer valves were installed and tested as required. The test data is included in Appendix I, Tables 1 through 4. Two runs were made using the HOKE micrometer valve. The first run provided good data but was considered insufficient in coverage of the lower range of fluid flow. A second run was made providing a greater range of data.
Test fluid temperatures were local ambient and varied slightly between tests.
For the water (incompressible) test fluid, the temperature differences are considered insignificant. For the nitrogen (compressible) test fluid, temperatures varied not more than 2 F throughout the duration of a given test. On an absolute temperature basis, the effect of this temperature variation is considered insignificant regarding flow variation.
Water flow data was recorded in gallons per minute (GPM) and nitrogen gas flow data was recorded in actual cubic centimeters per minute (ACCM) and converted to standard values (SCCM).
5.1.1 Analysis of the Laboratory Test Data The flowrate data for each test orifice and valve versus the orifice area or number of turns opened (Valve Turns) for the micr> meter valves was plotted using a linear plotting program. A least square fit was computed for each and a slope and intercept provided. In each case, the data plotted (Figures 1, 2, 3, 4,9 and 10) shows a high linear correlation over significant range of the data.
The data plotted for the NUPRO micrometer valve appeared to be bilinear.
Two fits were determined and two plots are provided for each test fluid. A straight line is plotted for a low range valve opening below 0.5 turns, Figures 5 and 6, and for a higher range above 0.5 turns, Figures 7 and 8.
The reason for the bilinear relationship is assumed to be a result of the non-linear relationship of the valve area opened with respect to valve turns. The decreased flowrate for the more " opened" valve setting supports this assumption. Regardless, the straight line relationships of the data as shown in all cases, figures 1 through 10 of Appendix I, exhibit the correlation desired.
WYLE LABORATORIES HuntsvtHe Facihty
g PAGE NO. 5 TEST REPORT NO. 17761-1 REV. A 5.1.2 Correlation of Nitrogen Versus Water Flowrates The laboratory tests were conducted such that for each test condition with lA nitrogen at 48.1 psig and ambient temperature, an identical test was run using water at 1020 psig and ambient temperature. A plot of the nitrogen flowrate versus the water flowrate for each identical test specimen area or opening is shown in Figure 11, Appendix I. The best fitting straight line through each of the four sets of data points was determined by linear regression methods. The slope and intercept of each line was computed by the linear regression program used. The correlation of these lines with the data points was computed to be very high, over 99%
^
The four test specimen lines are shown on the correlation plot, Figure 11. and the slope and intercept for etch is as follows:
Slope Intercept Line 1 Orifices 38532 -1149 Line 2 IIOKE Micrometer Valve, Run 1 34556 -2236 Line 3 NUPRO Micrometer Valve 38667 -8791 Line 4 IIOKE Micrometer Valve, Run 2 33157 -1968 The equation of Line 3 is:
SCCM = 38667 x GPM -8791 or for conversion: GPM = SCCM + 8791 Equation (1) 38667 The equation of Line 1 is:
SCCM = 38532 x GPM -1149 or for conversion: GPM = SCCM + 1149 Equation (2) 38532 WYLE LABORATORIES Huntsvitte FACshty I
i
PAGE 950. 6 TEST REPORT NO. 17761-1 REV. A in 5.1.3 Equipment Certification and Calibration l Instrumentation equipment and calibration sheets for the laboratory test system are included in Appendix II. A photograph of the laboratory test system is shown in Figure 12, Appendix I.
5.2 Field Tests In that a satisfactory correlation between the water and the nitrogen h flowrates was shown by the laboratory tests, field tests were conducted in accordance with the Test Procedure (PSSUG-PTP-GP-2). 'These field tests are similar to the laboratory tests. Completed test procedures for each of the 20 valve sets selected and tested are available from Hope Creek Generating Station records. The data obtained in these field tests is shown in Table 5, Appendix I. Of the twenty data sets obtained in the field, none has a flowrate value greater than the least value recorded during the laboratory tests. Data for each air test in the field was converted to a water flowrate value using the A Equations (1) and (2). The computed water flowrates are shown in Table 6, Appendix I as the Correlated Data. The two equations provide a most conservative and least conservative correlation.
The Line 1 correlated data is conservative for all but 4 of the actual field test R data and is the least conservative of the two. Line 3 correlated data is conservative for all actual field test data and is the most conservative. A factor of conservatism is shown for each correlation shown in Table 6 and was obtained by dividing the Correlated Data by the Field Test Actual Water Flow. ,
5.2.1 Equipment Certification and Calibration Instrumentation equipment and calibration sheets for the field test system are e included 1.; Appendix III.
WYLE LABORATORIES Huntsville Facihty
l PAGE NO. 7 j TEST REPORT NO. 17761-1 REV. A ,
I 6.0 RESUL1B AND CONCLUSIONS 6.1 n*=dts The laboratory tests showed a high correlation of nitrogen and water flowrates A versus area of orifice or valve opening over a significant range of the data (Figures 1-10).
The flowrates for nitrogen versus water for identical orifice areas or valve settings were plotted using linear regression methods. Four lines were determined with very high linear correlation to the data. Two of these lines provide a bounds to the four lines determined within the ranges:
0 - 38000 SCCM Nitrogen at 48.1 psig 0 - 1.2 GPM Water at 1020 psig These two lines represent a least conservative and a most conservative approach for correlation of nitrogen or air tests at low pressure to water tests at high pressure (see Figure 11).
The field tests provided lower flowrate data than any obtained during laboratory tests.
For each of the twenty field tests, the air test flowrate was used with Equations (1) and (2) to compute Correlated Data for Water flowrates. Using the least conservative approach, Equation (2), all but four of the correlated data obtained are conservative. Using the most conservative approach, Equation (1), all correlated data are very conservative.
WYLE LABORATORIES Huritsville Facility
PAGE NO. 8 TEST REPORT NO. 17761-1 REV. A 6.2 Conekasions G
6.2.1 Equation (1) of this report provides a conservative correlation from nitrogen or air flowrates to water flowrates for the fluids, pressures, and ranges below:
from: 0 - 38000 SCCM Nitrogen / Air at 48.1 psig to: 0 - 1.2 GPM Water at 1020 psig.
6.2.2 Equation (1) of this report, applied as set forth in the above Conclusion, provides a valid and conservative correlation approach to eliminate the need to perform l high pressure water leak testing on valves which have been satisfactorily tested at low pressure using air or nitrogen.
7.0 QUALITY ASSURANCE All laboratory work performed on this test program was completed in accordance with Wyle Laboratories' Quality Assurance Program which complies with the applicable requirements of MIL-Q-9858A, MIL-I-45208A, and NASA's NHB 5300.4 (IB & IC).
8.0 TEST EQUIPMENT AND INSTRUMENTATION All laboratory instrumentation, measuring, and test equipment used in the performance of this test program were calibrated in accordance with Wyle Laboratories' Quality Assurance Program which complies with the requirements of Military Specification MIL-STD-45662. Standards used in performing all calibrations are traceable to the National Bureau of Standards by report number and date. When no national standards exist, the standards are traceable to international standards or the basis for calibration is otherwise documented.
WYLE LABORATORIES Huntsnele Facesity
PAGE NO. 9 TEST REPORT NO. 17761-1 REV. A APPENDIX I 4
1 4
i i
I I
WYLE LABORATORIES Huntsville Facility
AIR VERSUS WATER CORRELA110N FOR LEAK TESTING TABLE 1 For Public Service Electric and Gas Company, Hope Creek Generating Station APPENDIX I LABORATORY TESTS Conducted 7/1/85 through 8/27/85 WYLE LADORATORIES, Huntsvine, Alabama Test Size-in / Flowrate Nitrogen Flowrate Water Line Specimen Setting-Turns (Meter Type *) F psig ACCM SCCM (Meter Type *) F psig GPM I,ine 1 ORIFICE 0.012 in. dia. 2 (SS float) 72 48.1 4400 4301 5 78 1020 0.12 1 2 ORIFICE 0.020 3 (glass 72 48.1 9200 8992 5 78 1020 0.29 2 float) 3 ORIFICE 0.031 1 72 48.1 22000 21504 5 78 1020 0.58 3 4 ORIFICE 0.040 1 72 48.1 36000 35188 5 78 1020 0.96 4 5 ORIFICE 0.052 1 72 48,1 63000 61579 5 78 1020 1.60 5 6 ORIFICE 0.060 72 48.1 79500 1 77707 5 78 1020 2.06 6
?
Flowrate Meter Type -see item no., Instrumentation Equipment Sheet oo FF 5s'
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l MITR0 GEN F141 (SCCM) YSORIFICE AREA (SQ IN.) LSQ Flf FOR 1.139974E-94 :(X(:
I 2.827434E-93 , SLP 2.763453E+97 INTRT 842.8265 l i i
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+.69E+95 +
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+.49E+95
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+.29E+95 .
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, + . NE+M gg i < l I
+ NE+M +.10E-92 +.29E-92 +.39E-92 5d .
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IRTER FLOW (GlH) YS, ORIFICE AREA (SQ IM.) LSQ Flf FOR 1.139974E-94 :M:
2.827434E-93 , SLP 717.2145 INTRT 5.165318E-92 I I o
+.29E+01 -
+.15E+01 43 E!
+19E+01 5
+.59E+M '
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+ . NE+M M
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+.NE+N +18E-92 . +.29E-92 +.39E-M . -[ E 5i!
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TABLE 2 AIR VERSUS WATER CORRELA*110N FOR !EAK TESTING APPENDIX I For Pihlie Service Electrie and Gas Company, Hope Creet: Generating Station LABORATORY TESTS Conducted 7/1/85 throegth 8/27/85 WYLE LABORATORIES, Huntsville, Alabama Test Size-in /
2 Flowrate Nitrogen Flowrate Water ACCM SCCM (Meter Type *) UF psig GPM Line Line Specimen Setting-Turns (Meter Type') F psig 2 Turns - - - - - 5 68 1020 0.09 1
IIOKE 3 3 72 48.1 4600 4496 5 68 1020 0.18 2 2
1/4 neh 3 4 3 72 48.1 5800 5669 5 68 1020 0.24 3 Miemmeter 4 5 3 72 48.1 9200 8992 5 68 1020 0.32 4 Valve 5 6 3 72 48.1 11400 11143 5 68 1020 0.38 5 (flun 1) 6 7 3 72 48.1 13100 12804 5 68 1020 0.44 6 7 8 3 72 48.1 15500 15150 5 68 1020 0.51 7 8 9 3 72 48.1 17000 16616 5 68 1020 0.56 8 9 10 3 72 48.1 19400 18962 5 68 1020 0.62 9 10 11 3 72 48.1 21400 20917 5 68 1020 0.68 10 11 12 3 72 48.1 23400 22872 5 68 1020 0.73 11 12 13 3 72 48.1 25300 24729 5 68 1020 0.75 12 g oo 13 14 3 72 48.1 27800 27173 {
14 v 15 3 72 48.1 28820 28170 ff N30
- Flowrnte Meter Type -see item no., Instrumentation Equipment Sheet >[
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MITR0 GEN FIAll (SCCM) YS, UALUE film LSQ Flf FOR 3 :M: 14, SLP 2952,297 l
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! HATERFLOW(GPM)YS,YALYEfURNS(' HOME 1315G4f LSQ FIf FOR 3 :M: 12 , SLP
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AIR YERSUS WATER CORRELNI10N FOR LEAK TESTING TABLE 3 For Ptblic Service Electric and Gas Company, llope Creek Generating Station APPENDIX I LABORATORY TES13 Conducted 7/1/85 through 8/27/85 WYLE LABORATORIES, Huntsville, Alabama Test Size-in / Flowrate Nitro Flowrate Water Line Specimen Setting-Turns (Meter Type *) gen F psig ACCM SCCM (Meter Type *) F psig GPM Line 1 0.04 - - - - -
5 73 1020 0.31 1 NUPltO 2
1/4 inch 0.08 1 72 48.1 18000 17593 5 73 1020 0.61 2 3
Micrometer 0.12 1 72 48.1 23000 22481 5 73 1020 0.77 3 4
Valve 0.16 1 72 48.1 28500 27857 5 73 1020 0.97 4 0 0.20 1 72 48.1 34000 33233 5 73 1020 1.12 5 6 0.24 1 72 48.1 40000 39097 5 73 1020 1.35 6 7 0.28 1 72 48.1 45500 44473 5 73 1020 1.38 7 8 0.40 1 71 48.1 62500 61205 5 73 1020 1.85 8 9 0.60 1 71 48.1 76500 74915 5 73 1020 2.12 9 10 0.80 1 71 48.1 80000 78342 5 73 1020 2.20 10 11 1.00 1 71 48.1 84000 82259 5 73 1020 2.40 11 12 1.20 1 71 48.1 87500 85687 5 73 1020 2.50 12 g
?a 13 1.40 1 71 48.1 89500 87645 5 73 1020 2.58 13 "
14 E
1.60 1 71 48.1 Note 1 5 73 1020 2.60 14 12 15 1.80 71 48.1 Note 1
?$
1 - -
5 73 1020 2.70 15 xz oo 16 V ' '
2.00 1 70 48.1 Note 1 -
5 73 1020 2.84 16 :n .-.
Note 1: Flow meter readings not on calibration curve; no data.
EZ*
Flowrate Meter Type -see item no., Instrumentation Equipment Sheet
l l .
! NITROGEN FLOW (SCCN) YS, YALUE TURNS.' NUPR0 SS-2M-S6 LSQ Flf FOR .98 :M: .4
, SLP 137122.9 INTRI 6142.47 i
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WATER FLOW (GPM) YS, YALUE filRNS' NDPR0 SS-2M-S6 LSQ Flf FOR .94 :M: ,24 , sLr 4,949999 INTRT .1629991 I I I I
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I NITR0 GEN FLOW (SCCM) YS, YALUE TURNS' NDPRO.SS-2M-S6 LSQ FIf FOR .6 :M: 1.4 l , SLP 16402.5 INIRI 65367 13 -
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. _ _ . - I WATER FLOW (CPM) YS, YALYE TURHS' HUPR0 SS-2M-S6 LSQ Flf FOR ,4 :(X(: 2 , SLP
.55666-7 INIRI 1,753111
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- - - - _ _ - _ _ L--- - - -
TABLE 4 (pg.1 of 2)
AIR VERSUS WATER CORRELATION FOR LEAK TESTING APPENDIX I For Public Service Electrie and Gas Company, flope Creelc Generating Station Conducted 7/1/85 through 8/27/85 LABORATORY TESTS WYLE LABORATORIES, Huntsville, Alabama 2 Flowrate Water Test Size-in / Flowrate Nitrogen SCCM (Meter Type *) F psig GPM Line Specimen Setting-Turns (Meter Typc*) F psig ACCM Line
- - 1 1 2A 78 48.1 440 425 - -
1 IlOKE 1160 - - - - 2 1-1/2 2A 78 48.1 1200 2
1/4 inch 78 48.1 2200 2126 5 75 1020 0.08 3 3 2 2A Micrometer 3248 5 75 1020 - 4 4 2-1/2 2B 78 48.1 3360 Valve 4460 4311 5 75 1020 0.16 5 5 3 2B 78 48.1
( 2) 4800 4639 5 75 1020 - 6 6 3-1/2 3A 78 48.1 3A 78 48.1 6200 5992 5 75 1020 0.25 7 7 4 48.1 6600 5379 5 75 1020 -
8 8 4-1/2 3A 78 5 3A 79 48.1 8400 8104 5 75 1020 0.32 9 I 9 3A 79 48.1 9400 9069 5 75 1020 -
10 10 5-1/2 6 3A 79 48.1 10000 '9647 5 75 1020 0.38 11 s 11 3A 79 48.1 11000 10612 5 75 1020 -
12 12 6-1/2 E
13 7 3A 79 48.1 12000 11577 5 75 1020 0.44 13 3A 79 48.1 12800 12349 5 75 1020 -
14 14 7-1/2 15 v 8 3A 79 48.1 14400 13892 5 75 1020 0.50 15 x-w Qd "
?
>L,
- Flowrate Meter Type -see item no., Instrumentation Equipment Sheet
AIR VERSUS WATER CORRELATION FOR LEAK TESTING TABLE 4 (pg. 2 of 2)
For Public Service Electric and Gas Company, Ilope Creek Generating Station APPENDIX 1 LABORATORY TES'IS Conducted 7/1/85 through 8/27/85 WYLE I.ABORATORIES, iluntsville, Alabama 2
Test Size-in / Flowrate Nitr en Flowrate Water Line Specimen Setting-Turns (Meter Type *) F psig ACCM SCCM (Meter Type *) F psig GPM Line 16 8-1/2 3B 79 48,1 16200 15629 5 75 1020 -
16 IlOKE 17 9 3B 79 48.1 16800 16208 5 75 1020 0.55 17 1/4 inch 18 9-1/2 3B 80 48.1 18200 17525 5 75 1020 -
18 Micrometer 19 10 3B 80 48.1 19000 1829S 5 75 1020 0.62 19 WWe ,
20 10-1/2 3B 80 48.1 20200 19452 5 75 1020 -
20 (Run 2) 21 11 80 48.1 - -
5 75 1020 0.65 21 22 12 80 48.1 - -
5 75 1020 0.69 22 23 13 80 48.1 - -
5 75 1020 0.73 23 24 14 1 78 48.1 24500 23680 5 75 1020 0.77 24 25 15 - - - - -
5 75 1020 0.81 25 26 16 - - - - -
5 75 1020 0.85 26 27 17 1 78 48.1 28500 27546 5 75 1020 0.87 27 5'
28 18 0.89
}s' 75 5 1020 28 na 29 19 - - - -
5 75 1020 0.93 29 zz 30 ??
20 1 78 48.1 31000 29963 5 75 1020 0.94 30 g-g
." g
>T -
- Flowrate Meter Type -see item no., Instrumentation Equipment Sheet
l
\
HITR0GENFLOW(SCCM)YS,YALUETURNS;H0XE1315G4VLSQFIfFOR1:M:19 l
, SLP 2007,51 INTRf-2938,39 i -
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+,29D95 _
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+,19D95 s
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+,99D99 m bb I I I I .g
+,59D91 +,19D92 +,15D92 +,20DB2 +,25D92 " '
+,99D99 l
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WAfERFLOW(GPM)YS,YALYEfURNSLSQFITFOR3:M:19,SLP6.333338E-92 INIR M ,167262E-93 a
+,75E+00k ..
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,+ +
ts
+,59E+99 %S 3 '
- ly
+,25E+99 E
e i s' 3%
+,99E+99 4 zz l I I I
+,00EiB9 y 5 's
+.59E+01 +.10E+02 +15E+92 +.20E+92 ;i
+.25E+02
TABLE 5(pg.1 of 2)
AIR VERSUS WATER CORRELATION FOR LEAK TESTING APPENDIX I For Pub!ic Service Electric and Gas Company, Ilope Creek Generating Station FIELD TESTS Conducted 7/09/85 through 10/17/85 WYLE LABORATORIES, Iluntsville, Alabama LLRT DATA AIR TEST W ATER TEST Penetra- Pressure Leakage Date tion Valve (s) Valve Valve Type Valve Pressure Leakage Date Size psig SCCM '85 psig GPM '85 Line Line I.D. No. Description Gate 20" 48.3 256 10/12 1020 0.04 10/13 1 i 1 P3 IlC-V164 RilR Shutdown Cooling Suction Gate 20" 48.5 470 10/12 1020 0.03 10/13 2 2 P3 BC-V071 RIIR Shutdown Cooling Suction BC-V013 RIIR Shutdown Gate 12" 48.1 18 8/15 1015 0.005 8/15 3 3 P4A.
Cooling Return 4 P4A BC-V014 Stop Check 12" 48.2 15 8/08 1015 0.002 8/08 4 P4A BC-V118 Globe 1" 5 P4B BC-V110 Globe 12" 48.4 50 8/14 1020 0.005 9/10 5 6 P4B BC-Vill Stop Check 12" 165 1020 0.003 9/10 6 48.3 9/03 g P413 BC-V117 "
Globe 1" g n
7 PSA BE-V003 Core Spray Gate 12" 48.2 7/20 1020 0.014 7/10 7 i
8 PSA BE-V002 Stop Check 12" 230 1020 0.013 9/10 8 48.4 9/18 ,,
IlE-V072 Globe 1" ff C E$
9 P513 BE-V007 y Gate 12" 48.3 2.78 9/17 1020 0.056 9/?4 9
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I AIR VERSUS WATER CORRELA*110N FOR LEAK TESTING TABLE 5 (pg. 2 of 2)
For Public Service Electric and Gas Company, Ilope Creek Generating Station APPENDIX 1 FIELD TESTS Conducted 7/09/85 through 10/17/85 WYLE LABORATORIES, iluntsville, Alabama LLRT DATA i Penetra- AIR TEST WATER TEST l tion Valve (s) Valve Valve Type Valve Pressure Leakage Date Pressure Leakage Date Line 1. D. No. Description Size psig SCCM '85 psig GPM '85 Line 10 Core Spray Sto Check 12" 48.3 2.78 9/17 1020 0.048 9/24 10
, 11 P10 BC-V020 RilR, RPV Globe 6" 48.3 27.1 10/01 1020 0.001 10/17 11 IIcad Spray 12 P10 BC-V021 P Gate 6" 48.4 2.0 10/02 1020 0.001 10/17 12 13 PGA BC-V004 RIIR, LPCI Gate 12" 48.1 0.9 '1020 0.004 13 14 PGA BC-V005 Stop Check 12" IGA BC-V122 48.3 1267 1020 0.002 14 Globe 1" 15 P6B BC-V016 Gate 12" 48.1 40.9 9/11 1020 0.04 9/10 15 16 P6B BC-V017 Stop Check 12" P6B BC-V120 48.3 437 9/09 1035 0.03 9/10 16 Globe 1" 17 PGD BC-V101 Gate 12" 48.4 315 9/11 1035 0.01 9/12 17 i
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18 P6D BC-V102 Stop Check 1" 48.5 360 9/11 1035 0.004 9/12 18 :o P6D BC-V121 Globe 1" -@ .u O4 19 P6C BC-V113 Gate 12" 48.3 40.8 7/09 1020 0.05 8/30 19 20 PGC BC-V114 EU Stop Check 12" P6C BC-V119 f 48.5 305 7/29 10:20 0.004 8/30 20 bb Globe 1" y "'
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Page No. 28 Test Report No. 17761-1 REV. A For Public Service Electric and Gas Company, Hope Creek Generating Station FIELD TEST DATA COMPARISON TO TABLE 6 LABORATORY TESTS' CORRELATION DATA APPENDIX I WYLE LABORATORIES, Huntsville, Alabama 2 3 4 1 Field Test Field Test Lab Test 5 Lab Tesi 0 7 Line Actual Actual Correlated Data Factor Correlated Data Factor Air Flow Water Flow Most Conservative Least Conservative SCCM GPM GPM GPM 1 256 0.04 0.233 5.8 0.036 0.9 2 470 0.03 0.239 7.9 0.042 1.4 3 18 0.005 0.227 45. 0.030 6 4 15 0.002 0.227 113 0.030 15 5 50 0.005 0.228 45 0.031 6.2 6 165 0.003 0.231 77 0.034 11 7 0.014 0.227 16.2 0.030 2.1 J 8 230 0.013 0.233 17.9 0.036 2.8 1 9 2.78 0.056 0.227 4 0.030 0.6 10 906 0.048 0.250 5.2 0.053 1.1 11 21.7 0.001 0.228 228 0.030 30 12 2.0 0.001 0.227 227 0.030 30 13 0.9 0.004 0.227 56 0.030 7.5 14 1267 0.002 0.260 130 0.063 31.5 15 40.9 0.04 0.228 5.7 0.031 0.8 16 437 0.03 0.238 7.9 0.041 1.4 17 315 0.01 0.235 23.5 0.038 3.8 18 360 0.004 0.236 59 0.039 9.75 l 19 40.8 0.05 0.228 4.6 0.031 0.6 20 305 0.004 0.235 58 0.038 9.5
- 1. Line No. of Field Test Data, Table 5 Appendix I .
- 2. Actual Field Test Leakrate in SCCM
- 3. Actual Field Test Leakrate in GPM
- 4. Lab Test computed correlation using Field Test Air Flow Actual SCCM with equation (1),
for most conservative correlation Line 3, Figure 11, Appendix I, in GPM.
- 5. Factor indicating conservatism = Correlated Data (computed) GPM, most conservative.
Actual Field Test Water Flow GPM
- 6. Ditto 4 above, but for least conservative Line 1, equation (2), in GPM.
- 7. Ditto 5 above for least conservative.
PAGE NO. 29 TEST REPORT NO. 17761-1 REV. A h
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1 PAGE NO. 30 TEST REPORT NO. 17761-1 l REV. A APPENDIX H WYLE LABORATORIES Huntsville Facility
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[A04 t44 Test Report No. 17761-1 gp
- i. Oh h LIQUID AND GAS - FLOWMETER CAllBRATION SERVICE 3335 Cerritos Avenue Los Alamitos, Calif. 90720 Phone 541559 DATE 1-1-AR SU.BMITTED FOR CAllBRATION BY Wyla tahnratorian TYPE OF INSTRUMENT Flce ster Tube SERIAL NO. .
B A659 MODEL NO. 1/6 M FG R.
GilFont RATED ACCURACY 152 Fc -
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l I CALIBRATED BY COMPARISON WITH THE FOLLOWING STANDARDS Test unit A-? N.B.S. Traceability *M-1959 As per MIL-STD-45662. Ne Dato 5-1-85.
ALL INSTRUMENTS USED TO ACCOMPLISH ABOVE CALIBRATION HAVE,.D} RECT TRACEABILITY TO THE NATIONAL BUREAU OF STANDARDS, WASHINGTON, D.C. ,/
I i RM APPROVED BY
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/c03 W Test Report No. 17761-1 REV. A l 5
~,. LIQUID AND GAS - FLOWMETER CAllBRATION SERVICE Phone 5961559 3335 Cerritos Avenue Los Alomitos, Calif. 90720 J
DATE 12-17-84 Wyle Laboratories SUBMITTED FOR CALIBRATION BY TYPE OF INSTRUMENT Flowmeter Tube SERIAL NO. C5715 MODEL NO. 1/4" MFGR. __
Gil.Tont RATED ACCURACY 1 2% F.S.
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! I CAllBRATED BY COMPARISON WITH THE FOLLOWING STANDARDS Test units A-2 a A-1. N.B.S. Traceability *M-1854 As per MIL-STD-45662. Calibration Due Date 5-1-85.
ALL INSTRUMENTS USED TO ACCOMPLISH ABOVE CAllBRATION HA' DIRECT TRACEABILITY TO THE NATIONAL BUREAU OF STANDARDS, WASHINGTON, D.C.
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PAGE NO. 37 TEST REPORT NO. 17761-1 , REV. A APPENDIX E 6 l' WYLE LABORATORIES Huntsville Facility
+
PSEG Rese:irch Corpor: sion RESEARCH AND TESTING LABORATORY INSTR UHENT C AL IBR ATION PROCED. PRESSURh. CAllBRATION TEST NO. FOR Leak Race Monitor TYPE PAGE SERIAL No. Mi Co. No. O O C & 2. -S DATE HFR. V 'o -
' CAP. 2# # 3 1"* U" #
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l Cate Calibraticn duc 1 8 Page No. 38 l l ! l l Test Report No. 17761-1 l l Darce.ctric Pressure Tf I RW. A l Serial ::c. '26 86, I ' ' I Cate Calibr.:ed 6.- D- Br- I l l I Da t o Ca ' ' ' , - cuc l 1 i r,-M sc i l l l
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'#* PSE&G RESEARCH CORP RESEARCH & TESTING LABORATORY LRM FLOW CALIBRATION
( MFG VOLUMETRICS SERIAL NO 115 PS NO 5806 { STANDARD LRM ( TEMP BAR PRESS TIME FLOW FLOW RESULTS F PSIA MIN SCCM SCCM % ( 74.4 14.7 1.00 1978.9 1993.0 .70 OK 74.4 14.7 1.00 1575.3 1592.0 .83 OK 74.4 14.7 1.00 1183.3 1196.0 .63 OK .{- 74.4 14.7 1.00 988.1 998.0 .49 OK 74.8 14.7 .99 794.3 800.0 .28 OK 74.8 14.7 .99 596.6 599.0 .11 OK { 74.8 14.7 .99- 398.7 399.0 .01 OK 74.8 14.7 .95 207.4 208.0 .02 OK -( 0.0 0.0 0.00 0.0 0.0 40.00 0.0 0.0 0.00 0.0 0.0 +0.00 BROOKS FLOW RATE CALIBRATORS SERIAL NO. 8306H67406 BAR PRESS SERIAL NO. ( 2686 CALIBRATION PERFORMED BY J.SODAN ( DATE CA'.IBRATED 8/2/85 ( l ( L ,, i L k Page No. 40 Test Report No. 17761-1 b REV.A -L L L L
** PSE&G RESEARCH CORP
{- RESEARCH & TESTING LABORATORY ,
- p. LRM FLOW CALIBRATION MFG VOLUMETRICS SERIAL NO 115 PS NO 5806
( '( TEMP BAR PRESS TIME STANDARD FLOW LRM FLOW RESULTS F PSIA MIN SCCM SCCM % 76.6 14.7 .99 198.8 198.2 f.34 OK 76.6 14.7 .98 175.3 176.0 .32 OK 76.6 14.7 1.00 148.4 150.3 .92 OK ( 76.6' 14.7 1.00 122.9 124.2 .62 OK 76.6 14.7 .98 100.5 100.2 t.17 OK 76.6 14.7 .97 76.2 75.0 t.60 OK ( 76.'6 14.7 .97 50.8 49.5 f.69 OK 76.6 14.7 . 9'7 25.4 24.6 f.42 OK o.o -0.0 0.00 0.0 0.0 +0.00
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( BROOKS FLOW RATE CALIBRATORS SERIAL NO. 8306H67406 ( BAR PRESS SERIAL NO. 2686 CALIBRATION PERFORMED BY J.SOBAN k DATE CALIBRATED 8/5/85 (
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.97 176.0 175.1 f.47 OK
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---- - MFG VOLUMETRICS SERIAL NO 6981 PS NO 7038
( STANDARD LRM ilhE iLUW FLOW iiESUL TS i r.dr Dis rRE55 { F PSIA MIN SCCM SCCM % 0.97 1998.0 1986.0 +0.60 OK S2.2 14.6 ( 1601.0 +0.43 OK i 02.2 14.6 0.96 1609.6 ( 82.2 14.6 0.95 1221.0 1204.0 +0.85 OK 82.2 14.6 0.94 825.5 803.0 +1.12 OK ( 603.0 +1.20 OK 82.2 14.6 0.93 627.0
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( 02.2 14.6 0.91 425.7 402.0 02.2 14.6 0.94 206.1 191.0 +0.75 OK 0.0 0.00 0.0 0.0 +0.00 0.0 k 0.0 0.00 0.0 0.0 +0.00 0.0 0.0 0.00 0.0 - 0.0 +0.00 0.0 ( BROOKS FLOW RATE CALIDRATORS SERIAL NO. 8306H67406 BAR PRESS SERIAL NO. 2687 CALIBRATION PERFORMED DY RJR k OATE CALIGRATED 10/31/95 L L . Page No. 53 L Test Report No. 17761-1 REV.A L L .- L.
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STANDARD LRM TEnF BAR FRE55 TliiE FLOW FLOW RE5 ULT 5 {o F PSIA MIN SCCM SCCM % 81.8 14.6 1.00 19521.7 19530.0 -0.04 OK { 81.8 14.6 0.97 18114.8 18200.0 -0.42 OK 81.8 14.6 0.98 15835.0 15980.0 -0.72 OK 81.8 14.6 0.98 13832.0 13940.0 -0.53 OK ( 82.0 14.6 0.97 12062.0 12130.0 -0.33 OM ( 82.0 14.6 0.97 10053.0 10030.0 +0.11 OM 82.0 14.6 0.95 8204.0 8130.0 +0.37 OK 82.2 14.6 0.95 6149.8 6010.0 +0.69 OK 82.2 14.6 0.92 4202.1 4050.0 +0.76 OM G2.2 14.6 0.92 2110.3 - 1990.0 +0.60 OK ( ( DROOKS FLOW RATE CALIDRATORS SERIAL NO. 8306H67406 BAR PRESS SERIAL NO. 2687 CALIBRATION PERFORMED D( RJR k DATE CALIDRATED 10/31/05 L L . Page No. 54 L - Test Report No. 17761-1 REV.A L L L.
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naanmo =sinume=r co., inc. . moarvius. N.J. oroas e taoi[asuses e ratex: tues: DATA SHEET Mark V Flow Meter CUSTOMER Public Service Electric & Gas Research Corp. DATE 12/20/84 P.O.No. Pt067291 '- REFERENCE MODEL Mark V- -SJ SERIAL NO. 30795 SIZE h" MATERIALS: Sensing Element 17-4 PH Seal Teflon Targ'et T303 s.s. Housing T304 s.s. Flange i LINE CONNECTIONS Threaded Pipe Housing " MNPT NATURAL FREQUENCY (in air) 137.0 Hz: TARGET TYPE
- ACR-604 VISCOSITY AT CALIBRATION 1.0 eps SPECIFIC GRAVITY 1.0 FLOW RANGE 0. 2 - 2.0 callons/ Minute FLUID wa ter REYNOLDS NO. (RD ) RANGE AT CALIBRATION 1,016 - 10,160 PRESSURE RATING 3000 psi Maximum Pressure Sensing Element
, Element #39056 Schedule 40 TEMPERATURE RANGE - 65 to + 300 *F
(' BRIDGE RESISTANCE, Input FORCE FACTOR ON 0.895 351.2 ohms, Output mV/V/kg 351.2 ohms. 75 15 y Recommended Maximum Volts AC or DC FULL SCALE OUTPUT standard piping (see " Installation") 1.009 Millivolts / Volt Excitation at 2.0 CPM FULL SCALE OUTPUT short straight run Millivolts / Volt Excitation at , with
- I straight run pipe diameters upstream, downstream Calibration Resistor ----
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'mV/V Accuracy % f, of full scale Data based on: ( ) fo'rce calibration, ( X) flow calibration cn G ELECTRICAL CONNECTIONS:
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Paga No. 69 Ramapo Instrum:nt Co. , Inc. Test Report No. 17761-1, Rsv. A DATA SHEET MARK X FLOWMETER SYSTEM CUSTOMER Public Service Electric & Cas Research Corporation DATE 4/11/85 i FLOWMETER MODEL Mark x-00000I SERIAL NO. 16686 . ELECTRONICS DTA-8401RD15 16688 , MODEL SERIAL NO. FLOWMETER DETAILS: Outline drawing 32076 MATERIAIS : Metering Tube & Float ' Type 18 S.S. Core 17-4 PH Housing T303-304 S.S. Seal T*flon Damper Teflon (Special) FLUID Wa ter SPECIFIC GRAVITY 1.00 t FLOW RANGE 0.005 - 0.25 GPM METERING TUBE SIZE 253 x 3 MAXIMUM FRESSURE 3500 Paig: TEMPERATURE RANGE . 65 to 250 op VISCOSITY: Op3 rating 1.0 cps : at calibration 1.0 cps FULL RANGE OUTPUT (Open Circuit) 256.856 mV/V at 3000 Hz(Approx.) LVDT type K-220-002 ADDITIONAL FEATURES OR DATA: ( x) None, ( ) See next page For other details, see specification S 32110 ELECTRONIC DETAILS: Outline drawing _ 32738 System Wiring 33416-1 FUNCTION: (x ) Flow rate transmitter, (x) Indicator, ( ) Totalizer, ( ) Controller set point (s), contact rating EXCITATION: 3.469 Volts, 3.033 KHz { OUTPUT: Flow Rate signal4 to 20 mADC () into 1K ohm load ( X) max. DIS PLAY:( ) Analog meter, (x) Digital meter. Scale 0 1.999 TOTALIZING: Full scale count rate counts per , equivalent to per , with scale factor of
. (Example reads .)
Counter ( ) included, ( ) remote, ( ) not supplied. ( ) Batch Control, contact rating Counter resets ( ) none, ( ) manual, ( ) electric, ( ) remote POWER: (x) 105-125V. 50/60 Hz, ( ) 200-250V, 50/60 Hz, ( ) ENCLOSURE TYPE: Rack Mount
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ADDITIONAL FEATURES OR DATA: (X) None, ( ) See next page For other details, see s,pecification S 33375 Set Set SCALE
, CALIBRATION SIGNAIE Switch position: CAL 1 CAL 2 FACTOR UNITS Simu.lates Flowmeter Signal 68.339 188.416 -
mV/V , Equivalent Flow Rate 0.050 0.1875 - CPM Count Rate (Totalizer) - - - - Output Signa 1 7.2 16.0 - - mADC Meter Reading 0.400 1.500 - - { , 0.188 Meter Reading (scaled) - CPM
'In all correspondence, refer to complete model designation and serial number, fr i.s., /. km a ri,.c, , c4
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PRESSURE GAGE CALIBPATION DATA Performed for ATM $55f>f/&'}f ORD 17?AX bd. > Location of Test #32=r 6- f c fE/cgsp/ ca g p d ud /j/t,/. Test No. Test Procedure Identification Fe/d -6 #Sc/. 6 Test Date f//9/87~ Description of Test Item 0-Jcco fss,c 6Ga <E e Gage ~ No. ,k @ C 7 3 i v' Manufacturer /:n,4rAprA) Model foJ-57,33 Accuracyf e in f. Standard GAGE READING Pressure I PSI PSI Uo Down Average Correction o n o o O 2c0 p rc ?c) 770 (3 g reO Sco rao coo 0
'770 770 77C '7sD C Mco /CCO /CCO /CCC C
- /7s'O /24$~ /2 s#O I 2'l$ + 2. O
/35C /$~C C / S?'0 /W0 CD
_ /75~0 / 7CO -
/ ')S~C C a
3 a W*r . i. , ? 1.w r.u e . , - . . . , ) . .i b [ S //' n b . o. . d.I, Permanent Set Test: Calibrated by . Nar Performed / g 4 Not required y/ Date l'~~2 J -?.]~~ , Test Standard / Equipment HM5 heTAL GrM C. (. Serial No. '/7d-, C - Tdt'O As t Date of Last Calibration /0 /29/g-(/ Page No. 71 Test Report No. 17761-1 Date of Next Calibration /0[2'?PI REV.A L 461 10/84 4}}