Text

Instrument Uncertainty Associated W/Flow Instrumentation Used for IT-11 SFP Cooling Pump Inservice Test
	ML20134D401
Person / Time
Site:	Point Beach
Issue date:	12/12/1996
From:	; WISCONSIN ELECTRIC POWER CO.
To:	;
Shared Package
ML20134D254	List: ML20134D250; ML20134D295; ML20134D331; ML20134D373; ML20134D381; ML20134D394; ML20134D401;
References
	96-0272, 96-272, NUDOCS 9702050126
	Download: ML20134D401 (120)
	v • d • e

, NUCLEAR POWER EUSINESS (W CALCL1ATION REVTEW AND AFFROVAL Calculation :

() ' CD k j pgg T 744 Number of Pages Title of Calculatica: T nETeoint.ST U ntu U W f\\ b % oc. nTock % s w F\o w

1. wWomnTG co 0%CcI ko\ B-11 SVV CcAo hp1hwieraTes;T

/ Original Calculat on O #QA-Scope I

C Revised Calculaticn. Revision #

C Superseding Calculation. Supersedes Calculation #

Modif1:stion #

Description:

N/A :

Other

References:

l l

Prepared By: Dste:

Q/so/96 _

This Calculation has been reviewed in accordance with NP 7.2.4. The review was ac:omplished by one er a combination of the following (as checked):

A review of a representative sample of repetitive / A detailed review of the original calculation.

calculatiens.

/ A review of the calculuion against a similar A review by an alternate, simplified, or calculation previously performed. sppteximate method of calculation.

Comments:

9702050126 970122 PDR ADOCK 05000301 p PDR Reviewed By: Date: Apped Sy: D2te:

/Af// lp ( l l0 A N fBF.1603 g o;;, , m- fu Refm seM N?"*4 S

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TITLE: Instrum:nt Une:rtrinty Ars:citt:d CALCULATION # : 96-0272 with Flow Instrumentation used for IT-11 Prepared By: JAK SFP Cc,oling Pump Inservice Test Date: 12/10/96 Page 1 of 4 A.

Purpose:

The purpose of this calculation is to determine the instrument uncertainty associated with the flow instrumentation used for the performance of the spent fuel pool cooling pump inservice test (IT-11).

B. References

1. PBNP inservice Test, IT-11, " Spent Fuel Pool Cooling Pumps", Revision 9, October 4,1996.

2. Barton Model 200 Differential Pressure Indicator Instruction Manual

3. PBNP Instrumentation and Control Procedures ICP 4.19 Data Sheet 21, Revision 28, May 23,1996.

4. " Process / industrial Instruments and Controls Handbook", Fourth Edition, Douglas M. Considine, McGRAW-HILL, INC.

5. DG-101 " Instrument Setpoint Methodology", Revision 1, September 12, 1995.

6. PBNP Instrumentation and Control Procedures ICP 8.9 Data Sheet 5, Revision 8, January 16,1996.

C. Assumptions j 1

1. The temperature effect on the instrumentation will be assumed to be negligible as the indicators are calibrated and used in essentially the same temperature environment.

2. The measuring and test equipment (M&TE) uncertainty for the flow instrument was calculated from uncertainties associated with test instruments which were used for calibration in the recent past. It is assumed that test instruments of similar accuracy are always used.

3. Uncertainties associated with drift of an instrument have been assumed to be equal to the calibration setting tolerance of the instrument. This assumption is based on a review of recent documentation of instrument calibrations which have shown that as-found values are typically within the tolerance allowed by the calibration procedure.

4. It is assumed that dialindicators can be read accurately to one-half of their smallest division / increment.

_ . . _ . =- _ . _ . _ . .. .m TITLE: In:trument Uncutainty A:sscirt:d CALCULATION # : 96-0272 with Flow Instrumentation used for IT-11 Prepared By: JAK SFP Cooling Pump inservice Test Date: 12/10/96 Page 2 of 4 D. Inputs The inservice test (IST) for the spent fuel pool pumps is performed per IT-11.

The IST currently adjusts P-12A and P-12B differential pressure to 23 psid by ;

throttling SF-11 and SF-12 respectively. The loop flow is recorded from F1-652 at the combined heat exchanger discharge to the spent fuel pool. (Reference 1]

For this calculation, the total uncertainty associated with the flow instrumentation (Fl-652 & FE-652) used to perform the IST must be taken into account. Error contributors to this total uncertainty include:

e Instrument Accuracy

Calibration Setting Tolerance e Dnit

. Indicator Readability e M&TE Uncertainty l 1. Instrument Uncertainties for FI-652 (discharge differential pressure flow l indicator, Barton Model 200). The flow indicator has a range of 0-2700 gpm which corresponds to a full scale differential pressure input range of 0-200" H 20. [ Reference 3]

l a. Instrument accuracy; Performance specifications for the Barton Model l 200 meter show an accuracy 0.5% of full scale differential pressure (0-200" H 2O) [ Reference 2]. F1-652 measures differential pressure, therefore the uncertainties given in Reference 2 are associated with the l differential pressure reading. The following method was used to convert the uncertainty seen in the differential pressure reading to an uncertainty in flow.

l Q = Constant (dP) (Equation 1, See Reference 5- Appendix C) f Q = Volumetric flow rate dP = Differential Pressure measured across the orifice Using Equation I recognizing that a dP of 200" is expected with a flow rate l

of 2700 gpm, solve for the constant:

7700 gpm = Constant (200")"*

1 Constant = 190.92 Uncertainty: 0.5% of full scale differential pressure (200") = i1" i

The dP @ 2700 gpm plus uncertainty = 201" Using Equation 1 this dP corresponds to a flowrate of:

Q = 190.92(201")'2 = 2706.8 gpm The corresponding uncertainty in gpm = 2706.8 gpm-2700 gpm = 16.8 gpm

TITLE: Instrument Unc:rtainty A::ccistid CALCULATION # : 96-0272 with Flow Instrumentation used for IT-11 Prepared By: JAK ,

SFP Cooling Pump Inservice Test Date: 12/10/96 j Page 3 of 4 1

b. Calibration Setting Tolerance; The as-left tolerance for the instrument is 127 gpm. [ Reference 3]

c. Drift;i 27 gpm (See Assumption C.3)

d. Indicator Readability; The minor division of F1-652 is 20 gpm, therefore it will conservatively be assumed that the instrument can be read accurately to within 110 gpm. (See Assumption C.4)

e. M&TE: Test instrument TI-206 was used to calibrate FI-652. The uncertainty associated with the test instrument TI-206 will be calculated via the SRSS method including the calibration instrument setting tolerance i0.25" [ Reference 6], assumed instrument accuracy of 10.25", indicator readibility of 10.01", and an M&TE of 10.1 % of range of Tl.206 (0-250") or i 0.25". (See Assumption C.2)

I M&TE = i](0.25")' +(0.25")' +(0.01")' + (0.25")'

M&TE = i 0.43 "

Following the process used in Section D.1.a, the uncertainty defined above is:

Uncertainty = 0.43" The dP @ 2700 gpm plus uncertainty = 200" + 0.43" = 200.43" l Using Equation 1 this dP corresponds to a flowrate of:

Q = 190.92(200.43")v2 = 2703 gpm l The corresponding uncertainty in gpm = 2703 gpm-2700 gpm = 3 gpm !

l

2. Uncertainties for FE-652 (flow orifice associated with F1-652) i The nominal accuracy for a flow orifice is 0.6% [ Reference 4] of maximum flow (2700 gpm) or i 16.2 gpm.

E. Calculation

1. The uncertainties of the instrumentation described in the input section will be combined using a systematic method established in Reference 5. Reference 5 also provides the basis for identifying, quantifying, and characterizing the error effects which must be considered in the development of an instrument f

uncertainty calculation. This methodology does not determine the maximum uncertainty possible, but rather determines the best estimate uncertainty.

The best estimate or realistic approach combines independent and random uncertainties using the statistical square root sum of squares (SRSS) method.

Non-random or directional uncertainties would be combined algebraically (straight sum) according to their sign with the results of the SRSS

k

. . TITLE: In:trument Unrrtainty Aisocist:d CALCULATION # : 96-0272 with Flow Instrumentation used for IT 11 Prepared By: JAK SFP Cooling Pump inservice Test Date: 12/10/96 Page 4 of 4 computation. However, this calculation does not contain any directional uncertainties.

Total Uncertainty associated with Fl-652 & FE-652 (see Sections D.1 & D.2)

U6s2 = 1](6.8)2 +(27)2 +(27)2 (,g)2 +(3)2 + (16.2)2 U652 = i 43.3 gpm F. Results A best estimate total uncertainty associated with the flow instrumentation (F1-652 & FE-652) used for the performance of the spent fuel pool cooling pump inservice test (IT-11) was determined to be 143.3 gpm.

o CR 0b -

W//o OPERABILITY DETERMINATION L Degraded or potentially nonconforming equipment:

Spent Fuel Pool Cooling Pumps (P 12 A & B)

2. Safety function (s) performed:

The SFP cooling system is required to remove decay heat from the fuel assemblies stored in the SFP pool. The pumps are required to provide design flow to the SFP heat exchangers (HX-13A & B) so that they can remove the decay heat being generated in the pool..

3. Circumstances of potential nonconformance, including possible failure mechanisms:

Condition Report 96-416 identified a potential concern for adequacy of the IST program to ensure that pumps meet design basis as well as ASME Section XI requirements. This evaluation supports determination of operability pending completion of detailed analysis.

4. Requirement or commitment established for the equipment, and why it may not be met:

FSAR Section 9.3 Table 9.3 3 lists the design flow rate to the SFP heat exchangers as 1250 gpm, and the design rated flow of the pumps as 1250 gpm.

FSAR Section 9.3 states that one train of SFP cooling is capable of removing 23.9 million bru/ hour and maintaining SFP temperature at or below 145F.

NRC SER Transmitted April 4,1979 states " we agree with WEPCO that for any of the postulated accidents the SFP outlet temperature will not go above 145F. His is an acceptable temperature."

He most limiting condition for the spent fuel pool cooling system is determined in calculation 96-090. This is with a full core offload of 23.9 million BTU /hr heat load and at a service water temperature of 75 F. Calculation 96-090 shows that, 1239.4 gpm SFP side flow with 75 F service water and 23.9 million bru/hr heat 'oad in the pool is adequate to maintain pool temperature at or below 145F.

IST acceptance criteria: P-12A,1250 gpm at 22.82 psid to 25.03 psid, P-12B,1250 gpm at 22.10 psid to 24.30 psid IST acceptance criteria may not be conservative when compared to design basis criteria.

5. How and when the potentially nonconforming equipment was first discovered:

His generic concern was first identified in June 1996 as a specific concern for safety injection pump acceptance criteria from ASME Section XI versus design requirements

6. Basis for declaring affected equipment operable:

De IST tests performed under IT-Oli sets the required flow at 1250 gpm and measures the differential pressure developed.

P-12A & B are both operating a' 1250 gpm and within the ASME acceptance criteria for developed head (see attached data and pump curves). De pumps are tested at 1250 gpm while lined up from the pool through the heat exchanger and back to the pool. His is the normal lineup and the required lineup under worst case conditions of design core offload and maximum service water temperature, ne IST testing shows that the pumps provide 1250 gpm of flow which is above the required calculated flow of 1239.4 gpm. He 1239.4 gpm of flow was derived from the heat exchanger data sheets which lists the required flow as 620,000 lhlhr. He test data indicates that the pumps meet the IST requirements and are above the design basis requirement of 1239.4 gpm and thus the pumps are determined to be operable.

Note: the differential pressure or 1, cad developed is not critical in that as long as 1250 gpm is provided to the SFP heat exchangers the design basis has been met. He differential pressure determined by the test provides information to show if pump performance is degrading.

PUMP TEST FLOW RECENT TESTED DP ASME XI ACTION RANGE l l

PBF-I553 i

Revbion 0 06/24/94 j

P12A 1250 gpm 24 psid 22.1 - 25.2 psid P12B 1250 gpm 23 psid 21.4 - 24.5 psid

'*repared By: _ Date: h[/!9/

Approved By: _ Date: /3' -

bd.

SES Manacer Reviewed By:

Date: /#!/ d l

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l PDF 1553 Revision 0 06/24/94 .

Pump Reference

- PRESSURE TEST ** Values and Limits Date Established: 6/25/91 Pump #: P12B IT-011 Entered By:

Reference Values Reference Pressure: 23.80 psig . Flow: 1250.00'gpm Reference Vibration Motor End Pump End Vertical: .021 ips Vertical: .024 ips Horizontal: .040 ips Horizontal: .033 ips l Axial: .028 ips Acceptable Range Pressure: 22.10 psig to 24.30 psig l

Vibration Motor End Pump End ,

Vertical: 5 .053 ips Vertical: 5 .060 ips Horizontal: 5 .100.ips Horizontal: s .083 ips Axial: $ .070 ips Alert Range Low Pressure: 21.40 psig to 22.10 psig High Pressure: 24.30 psig to 24.50 psig Vibration Motor End Pump End Vertical: .053 ips to .126 ips Vertical: .060 ips to .144 ips Horizontal: .100 ips to .240 ips Horizontal: .083 ips to .198 ips Axial: .070 ips to .168 ips Required Action Range Low Pressure: 21.40 psig High Pressure: 24.50 psig i

Vibration Motor End Pump End

{

Vertical: > .126 ips Vertical: > .144 ips Horizontal: > .240 ips Horizontal: > .198 ips l Axial: > .168 ips ;

Comment: VIBRATION CHANGED FROM DISPL TO VEL - BEARING TEMP.

DELETED (REF PRR-7,8) 6/3/92. REF VALUES ESTABLISHED WITH P12A DISCH VALVE CLOSED f

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I TEST DATA FOR CNE PLHP 4/08/*' Page 2

( Pumpi P128 Tesc: 011 sure Test Vibrations (ipal Vert Hors Vert Horz Test Date Diff P Indd Inbd Axial Outbd Outbd Int Remarks 11/10/95 24 .046 .070 .024 .036 .052 LEH ROWINE SURVEILLANCE 2/09/96 21 .039 .074 .037 .043 .061 LEH ROUTINE SURVEILLANCE 3/21/96 24 .028 .030 .025 .019 .025 LEH INCREASED FREQ, P128 5/05/96 24 .039 .039 .044 .035 .040 LEH ROWINE SURVEILLANCE 8/07/96 23 .040 .041 .054 .030 .033 LRD ROUTINE SURVEILLANC3 3M = rs.get v

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Pump Reference

- PRESSURE TEST ** Values and Limits i Date Established: 2/23/90 !

Pump #: P12A IT-011 Entered By* !

i Reference Values Reference Pressure: 24.52 psig l

Flow: 1250.00 gpm i l

Reference Vibration Motor End Pump End Vertical: .030 ips Vertical: .022 ips l Horizontal: .030 ips Horizontal: .030 ips !

Axial: .046 ips L !

j Acceptable Range [

Pressure: 22.82 psig to 25.03 psig Vibration Motor End Pump End Vertical: $ .075 ips Vertical: s .055 ips !

Horizontal: $ .075 ips Horizontal: $ .075 ips Axial: s .115 ips l 1

Alert Range I Low Pressure: 22.10 psig to 22.82 psig High Pressure: 25.03 psig to 25.20 psig Vibration Motor End Pump End Vertical: . 075 ips to .180 ips Vertical: .055 ips to .132 ips Horizontal: . 075 ips to .180 ips Horizontal: .075 ips to .180 ips Axial: . 115 ips to .276 ips Required Action Range Low Pressure: 22.10 psig High Pressure: 25.20 psig l Vibration Motor End Pump End !

Vertical: > .180 ips Vertical: > .132 ips Horizontal: > .190 ips Horizontal: > .180 ips Axial: > .276 ips Comment: VIBRATION CHANGED FROM DISPL TO VEL - BEARING TEMP.

DELETED REF PRR-7,8) 6/3/92. DELTA P BASED ON P12B ;

DISCHARGE VALVE CLOSED !

-, -,n,

TEST 0ATA FOR ONE PLNP S/08/96 Page 2 Pump P12A Tast: 311

'sure Test Vibrations (aps)

Vert Hers Vert Hort Test Date Diff P Inbd Inbd Axial Outbd Outbd Int Remarks 8/07/96 24 .035 .035 .043 .031 .025 LRD RolffINE SURVEILLANCE I

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POINT BEACH NUCLEAR PLANT BACKGROUND DOCUMENT INSERVICE TESTING PROGRAM APPENDIX J THIRD INTERVAL Revision 0

- June 13,1991 SPENT FUEL PIT COOLING l

Safety Function:

l The spent fuel pit cooling system is designed to provide long-term cooling for spent fuel and i components in the pit.

NOTE: This system is kciudad as a reaut d a past ineamel commhment. ir does not neceanerRy reRect he IST scope dontMon presensed k nW-1100 or n6P-1100 shce here is no specnnd accident (irt he stict deRrMan of 8he word) ior which mnigselon is required. The spent kelpH cooling pwnpa are ampiled elece1\c power kom an emergency source except shat nhey do not assommeice#P ressert h he emnt af ioss and recomry W ahe respecebe electic N==== Loss 1 or caosing so he spent lu.;per generasy does not present an acues problem. Assuming iorcod cooling is lost waft an initfel sorripensture of 120 *F and a conquises roecear core scored k she pt 6eorst probable imensory condiaians) 11.15 hows wiV naarma bekre sii- L _^: SFP imeneary ,

bow occurs. (Ref. NEPB-86479)

Components:

P412A&B (110E018. Sh 4)

Spent Fuel Pit Cooling Water Pumps These pumps circulate water from the spent fuel pits through the spent fuel pit heat exchangers to remove decay heat from fuel stored in the pits. j Test Requirement: IWP-3000 l 1

l SF40009A and 00010A (110E018, Sh 4)

Spent Fuel Pit Cooling Pump Discharge Check Valves These valves open to provide flowpaths from the spent fuel pit cooling water pumps to the spent fuel pit heat exchanger and close to prevent reverse flow through an idle pump. In the event of excessive leakage through the valve associated with an !dle pump, the result would be reduced cooling capacity of the operating system, potentially below the design minimum. Thus, these valves should be subjected to a functional leak test.

Test Requirement: CV-O CV-C SLT-B L

i i

I Page 1 of 1

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INTERNAL CORRESPONDENCE we PBM 97-0036 To: [

From:

Date: January 17,1997

Subject:

NRC 96EC ACTION #40 U2R22 RESTARTITEM #10/

Copy To:

File ;

A review of the IST stroke time acceptance criteria for all of the valves in the IST program has been completed. This review consisted of three phases as described below.

The first phase of the review was completed by NPTS, Inc. A list of all of the valves in the IST program was generated along with applicable preliminary design times. A total of 191 valves were listed for Unit I and common and 144 valves were listed for Unit 2. The source of the i preliminary design time was also listed along with the current IST acceptance range. In cases in which a design time could not be found, the design time was assumed to be the same as what the original purchase order specification called out. The Unit I and common and Unit 2 valve lists are attached to this memo (Attachment 1). This completed the first phase of this project.

The second phase of this project involved comparing the preliminary valve design times with the current IST acceptance range and actual valve performance data. In some cases, the current IST acceptance criteria exceeded the preliminary design time but the actual valve performance was within the design time. In other cases, both the actual performance time of the valve and the IST l acceptance criteria times exceeded the preliminary design time. None of the valves in this I category had preliminary design time requirements from Tech Specs or the FSAR. In both of the above cases, further analysis of the valve design time was completed. All valves in which the l' preliminary design time was a stroke rate based on the valve diameter (i.e.,12"/ minute) were also analyzed. There were 13 valves for Unit 2 in which the actual performance data and ;

acceptance criteria exceeded the preliminary design time,10 valves for Unit 2 had IST l acceptance criteria which exceeded the preliminary design time but the actual valve performance was within the preliminary design time, and 12 valves for Unit 2 needed further analysis due to l the preliminary design basis time being a stroke rate based on valve diameter. Two additional valves from Unit I which were not already included in the Unit 2 valve analysis were required to be analyzed due to the IST acceptance criteria exceeding the preliminary design basis time. Two common valves required further analysis due to the actual valve performance and acceptance criteria exceeding the preliminary design time.

i d

. 3 c

January 17,1997 Page 2 The third phase of this project was to further evaluate the valves in which discrepancies were identified from phase two. This phase was completed by the design basis group with preliminary reviews by system engineering. A total of 86 valves including Unit 1, Unit 2 and common were j evaluated to determine the stroke time performance requirement and basis. This number is l greater than the total from the paragraph above due to some valves that were analyzed had j similar functions to other valves in which there was not a discrepancy (i.e. MS-2015 has the i same function as MS-2016 therefore design stroke times are equivalent). Attachment 2 is a list of the valves that were analyzed with the stroke time perfonnance requirement and basis.

Attachment 3 is a discussion of CIV closure times referenced in Attachment 2. The results from Attachment 2 were compared to the current IST acceptance criteria and the valves actual performance. The only required action generated from this list was to change the upper limit in the shut direction for valves 1/2SW-2880 to 16.5 seconds. This action has been completed. A condition report documenting the potential for these valves to exceed the design basis time is being submitted. Also discovered from this review was that RHR core deluge valve ISI-852A had not been tested since 1994. This valve is supposed to be stroke tested every refueling outage. A condition report with action items to follow has been issued documenting this finding.

All of the other valves identified from phase two are performing within the stroke time requirements and have IST acceptance criteria within the required stroke time.

The actions completed above should enable NRC commitment NRC 96EC Action #40 and Unit 2 restart issue U2R22 Restart Item #10 to be closed out. However, all of the valves in the IST program which were not further analyzed by the design basis group (phase 3) should be evaluated. This evaluation should be completed in order to prevent future questions if a valve would fall outside ofits preliminary design time. This could occur due to normal valve degradation or valve maintenance. I strongly recommend that this effort continue.

cah Attachments:

Attachment 1: Unit I and common, Unit 2 valve lists produced by NPTS, Inc Attachment 2: Valves identified as potentially being outside of required design basis stroke times.

Attachment 3: DBD group response to Brad Fromm question on the basis for CIV closure times.

8 $?!"- UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re-review of Westinghouse Spec G676258 Page1 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION AF-00026 BT-C MANUAL 6 NONE NONE REQ'D MANUAL 1P-29 Suction AF-00039 BT-C MANUAL 4 NONE NONE REQ'D MANUAL 1P-38A Su:; tion AF-00052 BT-C MANUAL 4 NONE NONE REQ'D MANUAL 1P-38B Suction AF-04000 BT-C DBD Sec 4.5.1 3 15 Nom 17.7-24 1B S/G AFWlsolation ;

AF-04001 BT-C DBD Sec 4.5.1 3 15 Nom 18.7-25.3 1A S/G AFWisolation [

AIR 1P-29 Mini-flow b

AF-04002 BT-C M-181 1 NONE 9.98-16.64 3 s

AF-04002 BT-O M-181 1 NONE - 1.4-4.19 AIR 1P-29 Mini-flow AF-04006 BT-O DBD 4.6.1 6 30 Nom 24.03-32.51 29 Service Water

[~pp y AF-04007 BT-C M-181 1 NONE 4.94-14.9 AIR P-38A Mini-flow AF-04007 BT-O M-181 1 NONE 1.5 - 4.5 AIR P-38A Mini flow AF-04009 BT-O DBD Sec 4.6.1 4 30 Nom 24.88-33.66 c Water

[upp^y AF-04012 BT-O M-181 3 NONE 8.28-13.8 AIR

{-38A Pressure AF-04014 BT-C M-181 1 NONE 3.63-10.89 AIR P-38B Mini-flow AF-04014 BT-O M-181 1 NONE 1.14-3.4 AIR P-38B Mini-flow AF-04016 BT-O DBD Sec4.6.1 4 arvice Water 30 Nom <40 [ pp u y

8 ES UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re. review of Westinghouse Spec G676258 Page 2 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION BT-O M-181 AIR P-38B Presssure AF-04019 3 NONE 4.46-13.4 AF-04021 BT-C DBD Sec 4.4.1 3 15 Nom 45 Max 16.01 -21.65 AFW to 1 A S/G I

AF-04021 BT-O DBD Sec 4.4.1 3 15 Nom 45 Max 15.84-21.44 AFW to 1 A S/G AF-04023 BT-C DBD Sec 4.4.1 3 15 Nom 45 Max 15.62-21.14 AFW to 1 A SIG i AF-04023 BT-O DBD Sec 4.4.1 3 15 Nom 45 Max 15.55-21.02 AFW to 1 A S/G CC-00719 BT-C DBD Sec 3.8.18. G676258 6 0 01 8.86-11.98 {pnta nment CCW <

BT-O DBD Sec 3.8.1 & G676258 10 44.46-60.16 HR ooling Water 0738A [C $u HR BT-O DBD Sec 3.8.1 & G676258 10 [C 43.88-59.36 hupp,Cookng Water 0738B BT-C DBD Sec 3.8.1 & G676258 4 6.7-11.18 CP ooling Water 0754A hC hu P

BT-C DBD Sec 3.8.1 & G676258 4 OC 6.82-11.36 bup ooling Water 07548 CC- DBD Sec 3.8.1 & G676258 Page <= 10 & 10/10 7/20 # 4 CIO 60 Sec Max 7.15-11.91 g,CP t Cooling Water 00759A CC- DBD Sec 3.8.1 & G676258 Page <= 10 & 10/10 '

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4 7.27-12.11 ""9 00759B 7/20 # CIO 60 Sec Max Ret CC-00769 BT-C W 676270 / DBD-02 # 2 NONE I No Time 4.5 AIR ce s etdo n HX

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8 $W UNIT 1 AND COMMON VALVES WITH STROKE TIMES

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After re-review of Westinghouse Spec G676258 Page 3 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION BT-C PB Spec 540 / DBD-02 6 < 10 Sec I10 1.62-4.85 AIR CW Su ply to 3

CCW4W- BT-C PB Spec 5401 DBD-02 W Su ply to g 6 < 10 Sec /10 1.63-4.89 AIR BT-O DBD Sec 3.35.1 & G676258 4 10 & 10/10 OIC 7.4 -12.34 QT to Charging 01128 ,

BT-C DBD Sec 3.35.1 & G676258 4 10 & 10110 OIC 7.27-12.11 VCT to Charging Pump 0112C W 676270 Page 6/30 Modulaiting CV-00142 BT-O yaive 3 NONE 2.1 - 6.3 AIR Charging Flow Control CV-00313 BT-C W 676258 # P '

3 10/10 OIC 10.17-13.77 (t m

" CP SealWater BT-C WE Spec 109 Appx A # 3 9.83-16.39 AIR l 0313A ose 5 Max CV-00350 BT-O W 676258 2 10/10 OIC 7.12-11.86 Emergency Boration CV-00371 BT-C W 676270 Page 5130 # 2 NONE O-2 AIR etdown CV. Open 10 Max - OP 4.54 - 13.64 BT-C WE Spec 109 Appx A # 2 AIR RCS Letdown isoladon !

00371A Close 5 Max CL 4 - 12.02 CV-01296 BT-C W 676279 Page 5/30 # 2 NONE 2 AIR Aux Charging Isotaltion CV-01296 BT-O W 676279 Page 5/30 # 2 NONE 2 AIR Aux Charging isolattion DA- No individual valve test- VRR 17 & 0.

AIR i

EDG Starting Valve 375 NONE NONE

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8 $@ UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re-review of Westinghouse Spec G676258 Page 4 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION DA- No individual valve test-VRR 17 & AIR BT-O 3f5 NONE NONE EDG Statting Valve 03057B 25 DA- No individual valve test- VRR 17 & 0. AIR EDG Starting Valve 03058A 25 375 NONE NONE DA- No individual valve test- VRR 17 & 0. AIR EDG Starting Valve 03058B 25 375 NONE NONE DA- No individual valve test- VRR 17 & 0.

SOLENOID EDG Start Air Relay 06316A 25 375 NONE NONE DA- No individual valve test-VRR 17 & 0.

NONE SOLENOID EDG Start Air Relay 06316B 25 375 NONE A No individual valve test-VRR 17 &

06b BT-O 3f5 NONE NONE SOLENOID EDG Start Air Relay DA- No individual valve test-VRR 17 & O BT-O NS NONE NONE SOLENOID EDG Start Air Relay 063178 25 DA No individual valve test-VRR 17 & Motor BT-O NONE SOLENOID

-S 3NS NONE Sgrtin BT-O SOLENOID Sa n Motor D^b8B-S 6 5 3f5 NONE NONE DA- BT-O individual vane test-m U & SOLENOID Motor

-S "5 375 NONE NONE S[artin D^ No individual valve test-VRR 17 & S rtin Motor BT-O SOLENOID 63 9B-S 3N5 NONE NONE DA- No individual valve test-VRR 17 & G-03 South Bank NONE NONE SKID 06356A 25 Pressure Regulator

8 $@ UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re-review of Westinghouse Spec G676258 Page 5 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION DA- No individual valve test- VRR 17 & G-03 North Bank BT-O NONE NONE SKID 06356B 25 Pressure Regulator DA- BT-O No individual valve test- VRR 17 & SKID G-04 South Bank 06357A 25 NONE NONE Pressure Regulator DA- No individual valve test- VRR 17 & G-04 North Bank BT-O NONE NONE SKID 063578 25 Pressure Regulator DA- No individual valve test-VRR 17 & G-03 South Bank BT-O NONE NONE SY.lD 06364A 25 Starting Air Starter DA- BT-O No individual valve test-VRR 17 & G-03 North Bank NONE NONE SKID 06364B 25 Starting Air Starter DA- No individual valve test-VRR 17 & G-04 South Bank BT-O NONE NONE SKID 06365A 25 Starting Air Starter DA- No individual valve test- VRR 17 & G-04 North Bank BT-O NONE NONE SKlD 063658 25 Starting Air Starter FO-03930 BT-C M-91 1 No Time 6.85-11.41 fneI FO-03930 BT-O M-91 1 No Time 7.56-12.6 "

fnfef FO-03931 BT-C M-91 1 No Time 6.38-10.64 Inef FO-03931 BT-O M-91 1 No Time 6.65-11.09 fnfeI H 2-V-04 BT-O MANUAL # 2 MANUAL st Accident Purge NONE NONE H2-V-05 BT-O MANUAL # MANUAL st cident Purge 2 NONE NONE

o $@ UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re-review of Westinghouse Spec G676258 Page 6 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION H2-V-12 BT-O MANUAL # NONE MANUAL s -Ac dent Service 2 NONE H 2-V-13 BT-O MANUAL # MANUAL ent Service 2 NONE NONE {os -A H2-V-19 BT-O MANUAL # MANUAL P t Acci ent 2 NONE NONE H2-V-20 BT-O MANUAL # 2 NONE NONE MANUAL t-A i ent H2-V-22 BT-O MANUAL # MANUAL st Accident Supply 2 NONE NONE H2-V-23 BT-O MANUAL # 2 NONE NONE MANUAL Pos,t-Accident Supply Drain IA-03047 BT-C DBD Sec 3.7.3 # s en ir to 2 -5 .94-2.82 AIR IA-03048 BT-C DBD Sec 3.7.3 # 2 ~5 1.11-3.65 AIR g Is en r to IA-06310 No Stroke Time Req's - BT-EE 0.25 NONE NONE REQ'D NO TIME R 430 itro en I A-06311 No Stroke Time Req's - BT-EE 0.25 NONE NO TIME R 431C trogen NONE REQ'D Main Steam MS-02015 BT-C WE PB-584 6 30 20.65-34.41 AIR Atmospheric Steam Dump Main Steam MS-02015 BT-O WE PB-584 6 30 4.06-12.18 AIR gtmospheric Steam Main Steam MS-02016 BT-C WE PB-584 6 30 16.39-27.31 AIR gt spheric Steam

SE$f UNIT 1 AND COMMON VALVES WITH STROKE TIMES -

After re-review of Westinghouse Spec G676258 Page 7 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION Main Steam MS-02016 BT-O WE PB-584 6 30 4.38-13.12 AIR Atmospheric Steam Dump MS-02017 BT-C M-87 Spec 5.6.1 # 30 <= 4 5 AIR Main Steam Isolation 2017A-S SOLENOID 0.75 NONE NONE SOLENOID MSIV 2017 Air Pilot MS- BT-020178-S PV SOLENOID 0.75 NONE NONE SOLENOID MSIV 2017 Air Pilot MS- BT-02017C-S PV SOLENOID 1 NONE NONE SOLENOID MSIV 2017 Air Pilot .

MS- BT-02017D-S PV SOLENOID 1 NONE NONE SOLENOID MSIV 2017 Air Pilot ,

MS-02018 BT-C M-87 Spec 5.6.1 # 30 <= 4 5 AIR Main Steam isolation MS- BT-02018A-S PV SOLENOID 0.75 NONE NONE SOLENOID MSIV 2018 Air Pilot 20188-S V SOLENOID 0.75 NONE NONE SOLENOlD NISIV 2018 Air Pilot MS- BT-02018C-S PV SOLENOID 1 NONc ' NONE SOLENOID MSIV 2018 Air Pilot MS- BT-02018D-S PV SOLENOID 1 NONE NONE SOLENOID MSIV 2018 Air Pilot DRD Sec 4.7.1 Op - 50, DB Close MS-02019 BT-O 3 21 Nom 18.27-24.71 AFW Steam Supply Unknown DBD Sec 4.7.1 Op ~ 50, DB Close MS-02019 BT-C 3 21 Nom 18.59-25.15 AFW Steam Supply Unknown

7 8?$$P UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re-review of Westinghouse Spec G676258 Page 8 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION

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MS-02020 3 21 Nom 19.06-25.78 AFW Steam Supply O known BT-C D Sec 4.7.1 Op - 50, DB Clos MS-02020 BT-C 3 21 Nom 19.51-26.39 AFW Steam Supply MS-02082 BT-C (TURBINE OVERSPEED TRIP) 3 NONE NONE ($pSteam to AM MS-02083 BT-C M-181 # 0.75 NONE 0-2 AIR S/G Sample Isolation MS-02084 BT-C M-181 # 0.75 NONE 0-2 AIR S/G Sample isolation MS-02090 BT-O DBD Sec 4.15.2 Open Max 2 AIR to AFW Pump P-1 0-2 0-2 MS-05958 BT-C WE Spec 109, Appx A # 2 5 MAX 15 AIR

{/ Blowdown MS-05959 BT-C WE Spec 109, Appx A # 2 5 MAX 15 AIR / B wdown RC-00430 BT-C W 676270 2 NONE O - 2.3 AIR Power Operated Relief RC-00430 BT-O W 676270 2 NONE O - 2.3 AIR Power Operated Relief ;

00431C W 676270 2 NONE O - 2.3 M Pow @ed W BT-O W 676270 2 NONE O - 2.3 AIR Power Operated Relief 00431C RC-00508 BT-C DBD Sec 4.8.4 # 2 <= 15 3.06-9.18 AIR PRT Fill Line Isolation RC-00515 BT-C DBD Sec 4.14.4 3 120 15.32-20.72 PORV Block Valve

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EiMS7 ' UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re-review of Westinghouse Spec G676258 Page 9 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION RC-00516 BT-C DBD Sec 4.14.4 3 120 15.36-20.78 PORV Block Valve RC-00538 BT-C DBD Sec 4.10.4 #

375 <= 15 3.58-10.76 AIR PRT Sair.ple RC-00533 BT-C DBD Sec 4.10.4 # 4.74-14.24 AIR PRT Sample 375 <= 15 BT-O SOLENOID 1 NONE NONE SOLENOID RX Vesset Vent 00570A BT-O SOLENOID 1 NONE NONE SOLENOID RX Vessel Vent 0570B BT-O SOLENOID 1 NONE NONE SOLENOID X Vess/ Pressurizer 00575A BT-O SOLENOID 1 NONE NONE SOLENOID X Vess/ Pressurizer 0575B BT-O SOLENOID 1 NONE NONE SOLENOID Pressurizer Vent 00580A BT-O SOLENOID 1 NONE NONE SOLENOID Pressurizer Vent 00580B RC-00595 BT-C MANUAL # 0.75 NONE NONE MANUAL PRT Nitrogen Supply RH-00700 BT-C W 676258 10 120 8.69-11.75 RHR Loop Isolation RH-00700 BT-O W 676258 10 120 8.98-12.16 RHR Loop Isolation RH-00701 BT-C W 676258 # 10 120 88.54-119-78 RHR Loop Isolation RH-00701 BT-O W 676258 # 10 120 92.4-125.01 RHR Loop Isolation

W

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8i$@ UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re-review of Westinghouse Spec G676258 Page 10 VALVE TEST _

DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION BT-C MANU#.L 8 NONE NONE MANUAL RHR Pump Suction 00704A BT-O MANUAL 8 NONE NONE MANUAL RHR Pump Suction 00704A BT-C MANUAL 8 NONE NONE MANUAL RHR Pump Suction 0704B BT-O MANUAL 8 NONE NONE MANUAL RHR Pump Suction 007048 RH-00720 BT-C W 676258 # 10 120 92.78-125.52 RHR Rerurn to RCS RH-00720 BT-O W 676258 # 10 120 96.17-130.11 RHR Rerum to RCS RM. containment BT-C M-181 # 1 NONE 4.5 AIR 03200A gt osphere Sample RM. BT-C M-181 #

containment 1 NONE 4.5 AIR 032008 gtm phere Sample RM. containment BT-C M-181 # 1 NONE 4.5 AIR 03200C gtmo phere Sample RS-SA-09 BT-C AIR 3 NONE 4.07-12.21 AIR Radwaste Steam Supply SC-00951 BT-C W 676270 # 10.27-17.12 AIR fess rizerSteam 375 NONE a SC-00953 BT-C W 676270 # 3.32-9.94 AIR es rizer Liquid 3NS NONE SC-00955 BT-C W 676270 # 3.54-10.64 AIR Hot Leg Sample 375 NONE

oi$MP UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re-review of Westinghouse Spec G676258 Page 11 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION SC-00959 BT-C W 676270 8.24-13.73 AIR RHR Sample 375 NONE BT-C W 676270 # 3.09 -9.27 AIR 0966A 375 NONE {ress rizer Steam W 676270 # 3.78-11.34 AIR 0966B 375 NONE {ress rizerLiquid BT-C W 676270 # 3.96-11.88 AIR Hot Leg Sample 0966C 375 NONE SI-00834A BT-C W 676270 1 NONE 0-2 AIR SIS AcwmulatoWent SI-00834A BT-O W 676270 1 NONE 0-2 AIR SIS Accumulator Vent SI-00834B BT-C W 676270 1 NONE 0-2 AIR SIS AccumulatorVent SI-00834B BT-O W 676270 1 NONE 0-2 AIR SIS AccumulatorVent SI-00836A BT-O 2 NONE 9.23-15.39 AIR NaOH Supply SI-00836B BT-O 2 NONE 8.52-14.2 AIR NaOH Et.pply SI-00841 A BT-C W 676258 ul r 10 1"/SECOND 8 62-11.66 $l$cuge SI-00841B BT-C W 676258 '

10 1"lSECOND 9.08-12.28 glS^c a ge SI-00846 BT-C W 676270 # AIR Accumulator Nitrogen 1 NONE 0-2 Supply 0258 ** Revised Design SI-00850A BT-C ., 10 NONE 3.28-9.84 gi"Nsnt S" P uI ton h

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81$W UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re-review of Westinghouse Spec G676258 Page 12 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION W 676258 ** Revised Design Containn ent Sump SI-00850A BT-O 10 NONE 3.28-9.84 Time Hydraulic isolation 6258 ** Revised Design SI-00850B BT-C 10 NONE 3.12-9.35 " P

$]t"$s"1 r ul on W 676258 ** Revised Design SI-008508 BT-O 10 NONE 2.98-8.93 " P f4 Str ul$ s" on t SI-00851 A BT-C W 676258 Page 15 Rev 3# 10 10/10 O/C 88.02-119.08 hsoE) inment Sump SI-00851A BT-O W 676258 Page 15 Rev 3# 10 10/10 OIC 88.63-119.91 n fso) inment Sump SI-008518 BT-C W 676258 Page 15 Rev 3# 10 10/10 O/C 86.55-117.09 fsoEIbn nt Sump SI-008518 BT-O W 676258 Page 15 Rev 3# 10 10/10 OIC 88.59-119.85 n fso j nment Sump SI-00852A BT-C W 676258 Page 15 Rev 3# 7.18-11.98 low Head Core 6 10/10 O/C $e"Ng SI-00852A BT-O W 676258 Page 15 Rev 3# 6 10/10 OIC 7.43-12.39 $,HR Low Head Core 9

SI-00852B BT-C W 676258 Page15 Rev 3# 7.12-11.88 low Head Core 6 10/10 O/C $,H g SI-008528 EsT-O W 676258 Page 15 Rev 3# 6 10/10 OIC 7.45-12.41 $,HRg9l0w Head Core SI-00856A BT-C W 676258 Rev 2 Page 16 10 12"/ Minute O/C 90.42-120 RHR Pump Suction SI-00856B BT-C W 676258 Rev 2 Page 16 10 12"/ Minute O/C 87.55-118.45 RHR Pump Suction SI-00857A BT-O MANUAL G676258 6 10!12t1 OIC NONE REQ'D MANUAL H o SIS Pump

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UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re-review of Westinghouse Spec G676258 Page 13 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION SI-008578 BT-O MANUAL G676258 6 10/120 O/C NONE REQ'D MANUAL SIS Pump

{HR SI-00860A BT-O W 676258 Rev 2 Page 18 6 1"lSecond 9.69-13.11 hfsb" amp 1-P14A SI-00860B BT-O W 676258 Rev 2 Page 18 6 1"lSecond 9.78-13.22 $$$" amp 1-P14A SI-00860C BT-O W 676258 Rev 2 Page 18 6 1"/Second 10.24-13.86 P

$$$"*g,1-P148 SI-00860D BT-O W 676258 Rev 2 Page 18 6 1"lSecond 9.84-13.32 1

@$$"a ge -P14B SI-00866A BT-C W 676258 # 4 12"/ MINUTE 47.06-65.02 SIS Pump Discharge SI-00866A BT-O W 676258 # 4 12"/ MINUTE 48.3-65.34 SIS Pump Discharge SI-008668 BT-C W 676258 # 4 12"/ MINUTE 48.45-65.55 SIS Pump Discharge SI-00866B BT-O W 676258 # 4 12"/ MINUTE 49.3-66.7 SIS Pump Discharge SI-00870A BT-C W 676258 6 12"/ MINUTE 8.64 -11.7 fMT to CS Pump SI-00870A BT-O W 676258 6 12"/ MINUTE 8.86-11.98 $T to CS Pump SI-00870B BT-C W 676258 6 12"lMINUTE 8.92-12.06 h@T to CS Pump SI-00870B BT-O W 676258 6 12"lMINUTE 8.95-12.11 h@T to CS Pump SI-00871 A BT-C W 676258 6 12"/ MINUTE 7.38-12.3 RHR to CS Pump 14A

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8?$I$7 ' UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re-review of Westinghouse Spec G676258 Page 14 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION SI-00871 A ST-O W 676258 6 12"/ MINUTE 8.63-11.67 RHR to CS Pump 14A ;

SI-008718 BT-C W c16258 6 12"lMINUTE 7.37-12.29 RHR to CS Pump 148 SI-00871B BT-O W 676258 6 12"/ MINUTE 7.39-12.31 RHR to CS Pump L:8 SI-00878A BT-C W 676258 2 10 6.23-10.39 s W

$fe((on$ '

SI-00878A BT-O W 676258 2 10 7.04-11.76 $feUfo$$n '

SI-008788 BT-C W 676256 2 10 d.76 - 11.27 SIS Loop injection SI-00878B BT-O W 676258 2 10 8.51 -11.51 SIS Loop Injection SI-00878C BT-C W 676258 2 10 6.5-10.82 s

$f,[fon$ '

SI-00878C BT-O W 676258 2 10 6.65-11.09 R '

gn e on SI-00878D BT-C W 676258 2 10 6.91 -11.51 SIS Loop Injection SI-00878D BT-O W 676258 2 10 7.26-12.1 SIS Loop Injection SI-00896A BT-C W 676258 Rev 2 Page 20 6 12"lMINUTE 8.92-12.06 SIS Pump Suction SI-008968 BT-C W 676258 Rev 2 Page 20 6 12"/ MINUTE 9.35-12.65 SIS Pump Suction SI-00897A BT-C W 676270 2 NONE .9 - 2.72 AIR SIS Test Line Retum SI-008978 BT-C W 676270 2 NONE 1.19-3.57 AIR SIS Test Line Retum

8?N"' UNIT 1 AND COMMON VALVES WITH STROKE TIMES -

After re-review of Westinghouse Spec G676258 Page 15 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION SI-00957 BT-C W 676270 1 NONE 10.58-17.64 AIR N2 Supply Vent / Relief SI-00957 BT-O W 676270 1 NONE 2-6 AIR N2 Supply Vent / Relief SW-00286 BT-O MANUAL 12 NONE NONE MANUAL CCW 1HX-12A Inlet SW-00290 BT-O MANUAL 12 NONE NONE MANUAL CCW HX-12C Inlet SW-00296 BT-O MANUAL 12 NONE NONE MANUAL CCW 2HX-12D Inlet SW-00307 BT-O MANUAL 12 NONE NONE MANUAL CCW 2HX-12D Outlet SW-00315 BT-O MANUAL 12 NONE NONE MANUAL CCW HX-12C Outlet SW-00322 BT-O MANUAL 12 NONE NONE MANUAL CCW 1HX-12A Outiet SW-00346 BT-O MANUAL 12 NONE NONE MANUAL CCW HX-12B inlet SW-00360 BT-O MANUAL 12 NONE NONE MANUAL CCW HX-12B Outlet SW-02816 BT-C DBD Sec 4.12.2 6 30 Nom 21.34-28.88 'd9

$*oj"g [3oiat?on SW-02818 BT-O DBD Sec 4.8.2 3 15 < 35.96 $IMPM9ppiy SW-02819 BT-O DBD Sec 4.8.2 3 15 <36.24 " '

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SW-02838 BT-O DBD 4.13.2 4 1.42-4.23 AIR G02 EDG HX Outlet stablished SW-02839 BT-O DBD 4.13.2 4 1.39-4.17 AIR G01 EDG HX Outlet stablished

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8i4E"' UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re-review of Westinghouse Spec G676258 Page 16 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL FUNCTION SW-02869 BT-C DBD 4.10.2 (48.79 - 66.01 Open) 14 60 Nom 49.21 -66.57 S " r Mest) is ati SW-02870 BT-C DBD 4.10.2 (49.78 - 67. A34 Open) 14 60 Nom 49.92-67.54 S " d r(west) s ai n SW-02880 BT-C DBD 4.11.3 (12.68 - 17.16 Open) 6 15 Nom 12.65-17.11 Turb Hall Coolers Inlet SW-02890 BT-C DBD 4.7.1 (65.22-88.24 Open) 24 80 Nom 65.35-88.41 SW Header Cross-tie SW-02891 BT-C DBD 4.7.1 (63.07 - 85.32 Open) 24 80 Nom 63.12-85.4 SW Header Cross-tie SW-02907 BT-O DBD Sec 4.9.3 12 30 Nom 23.61 -31.95 " ""

kNr "F o SW-02908 BT-O DBD Sec 4.9.3 12 30 Nom 23.66-32.02 [ ",ta nment cochng p9 SW-BT-C DBD Sec 4.12.2 8 Not Spec 14.44-19.54 SFP Cooier Supply 42930A SW-BT-C DBD Sec 4.12.2 8 Not Spec 16.2-21.02 SFP Cooler Supply 029308 SW-LW-61 BT-C S&W PBS-18 Page 17/33 8 NONE 2.76-8.3 AIR BDENent Cond Inlet SW-LW-62 BT-C S&W PBS-18 Page 17/33 8 NONE 3.48-10.42 AIR BDENent Cond Outlet VNPSE- BT-C DBD 3.17.2 # Containment Purge 36 10 Nom 10 AIR 03212 Exhaust BT-C DBD 3.17.2 # 36 10 Nom 10 AIR ontainment Purge 03213 N SE- BT-C DBD 3.17.2 # 36 10 Nom 10 AIR {on nmemt Purge 3

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8? ESP UNIT 1 AND COMMON VALVES WITH STROKE TIMES After re-review of Westinghouse Spec G676258 Page 17 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME ISI TIME SPECIAL ~ FUNCTION I

" BT-C DBD 3.17.2 # 36 10 Nom 10 AIR {on nmemt Purge 3 5 WG-01786 BT-C W 676270 # 1 NONE 4.68-14.06 AIR RCDT Vent WG-01787 BT-C W 676270 # 1 NONE 4.42-13.26 AIR RCDT Vent WG-01788 BT-C W 676270 # 0.75 NONE 2.62-7.86 AIR RCDT Sample WG-01789 BT-C W 676270 # 0.75 NONE 2.2 - 6.6 AIR RCDT Sample BT-C W 676270 # 3 NONE 15.89-26.49 AIR RCDT Pump Suction 1003A BT-C W 676270 # 3 NONE 15.52-25.88 AIR RCDT Pump Suction 1003B WL-01698 BT-C W 676270 # 2 NONE 1.48-4.46 AIR RCDT to 19' Sump WL-01721 BT-C W 676270 # 3 NONE 23.71 -39.51 AIR C T Pumps Suction WL-01723 BT-C W 676270 # 3 NONE 15.15-25.85 AIR Cont Sump Drain WL-01728 BT-C W 676270 # 3 NONE 14.27-23.79 AIR Cont Sump Drain

Unit 2 Valves with Stroke Times

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After Re-review of Westinghouse Spec G676258 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIALl FUNCTION AF-00064 BT-C MANUAL VALVE 6 NONE NONE MANUAL 2P-29 Suction AF-04000 BT-C DBD 3 15 NOM 16.34-22.13 2B S/G AFWisol AF-04001 BT-C DBD 3 15 NOM 17 - 21 2A S/G SFWlsol AF-04002 BT-C M181 1 NONE 4.17-12.5 AOV 2P-29 Mini-flow AF-04002 BT-O M181 1 NONE 1.49-4.47 AOV 2P-29 Mini-flow AF-04006 BT-O DBD 6 30 N 27.06-36.6 2P-29 Ser Wtr Sup AF-04020 BT-C DBD 3 15-45 16.15-21.85 AFW TO 2B S/G AF-04020 BT-O DBD 3 15-45 15.67-21.21 AFW TO 28 S/G AF-04022 BT-C DBD 3 15-45 15.76-21-32 AFW TO 2A S/G AF-04022 BT-O DBD 3 15-45 15.27-20.67 AFW TO 2A S/G CC-00719 BT-C DBD & G676258 6 <=10 &10 to 9.34-12.64 Cont CCW Sup 120 O/C CC-00738A BT-O DBD & G676258 10 <=10 &10 to 44.88-60.72 RHR Cooling Wtr Sup 120 O/C CC-007388 BT-O DBD & G676258 10 <=10 &10 to 45.67-61.79 RHR Cooling Wtr Sup 120 O/C CC-00754A BT-C DBD & W676258 4 <=10 & 10/10 6.38-10.62 RCP C!g Water Sup p5/17 O/C CC-00754B BT-C DBD & W676258 4 <=10 & 10/10 7.39-12.31 RCP Cig Water Sup !

p5/17 O/C CC-00759A BT-C DBD# 4 <=10 6.93-11.55 RCP Cig Water Ret

_ _ _ . _ _ . - -_u_ _ _ _ __._ _ . _ _ _ __ . _ _ . . _ _ . _ . _ . . - _ - _ _ _ _ _ . _ _ _ _ _ _ _ _ - _ _ . _ _ _ _ _ . _ . _ _ _ _ _ _ _ _ _ _ - _ . _ _ _ _ . _ _ _ _ _ _ - _ ~ _ . _ _ - - _

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nw Unit 2 Valves with Stroke Times After Re-review of Westinghouse Spec G676258 g ,e 2

~i VALVE TEST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIAL FUNCTION CC-00759B BT-C DBD# 4 <=10 6.64-11.08 RCP Cig Water Ret CC-00769 BT-C W676270 p12/30 2 NONE 4.5 AOV Ex LD HX Cig Wtr Ret CV-001128 BT-O DBD & G676258 4 10 & 10/10 7.13-11.89 RWST to Chg Pump OIC CV-00112C BT-C DBD & G676258 4 10 & 10/10 7.21-12.01 VCT to Chg Pump OIC CV-00142 BT-O W676270 p6/30 3 AIR 1.84-5.54 AOV Charging Flow Cont MODULATIN G

CV-00313 BT-C W6762598 # 3 10/10 O/C 10.09-13.65 RCP SealWir Ret CV-00313A BT-C WE SPEC 109 4 5 max 9.52-15.88 AOV RCP Seal Wtr Ret Appx-A OPEN 10 max #

CV-00350 BT-O W676258 p2/17 2 10/10 O/C 7.38-12.3 Emerg Boration CV-00371 BT-C W676270 p5/30 # 2 NONE 0-2 AOV RCS Letdown Iso CV-00371A BT-C WE Spec 109 Appx- 2 5 max 8.62-14.38 AOV RCS Letdown Iso A OPEN 10 max #

CV-01296 BT-C W676270 p5/30 # 2 NONE .99-2.97 AOV Aux Charging isolation CV-01296 BT-O W676270 p5/30 # 2 NONE .82-2.46 AOv Aux Charging isolatio, H2-V-04 BT-O MANUAL # 2 NONE NONE MANUAL Post Accident Purge Disch H2-V-05 BT-O MANUAL # 2 NONE NONE MANUAL Post Accident Purge Disch i

_ _ . . _ _ - . . _ _ _ . . _ _ . _ _ _ _._.m. _ ___..____________._____._._______m_ _ . _ _ _ _ _ _ _ _ _ _ _ . _ _ _ _ _ . . _ _ . . . -_ _ _ - _ _ - , - - ~ - . - e

g3ap Unit 2 Valves with Stroke Times P,ge 3

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After Re-review of Westinghouse Spec G676258 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIAL FUNCTION H2-V-12 BT-O MANUAL # 2 NONE NONE MANUAL Post Accidem .3vc Air Sup H2-V-13 BT-O MANUAL # 2 NONE NONE MANUAL Post Accident Svc Air Sup H2-V-19 BT-O MANUAL # 2 NONE NONE MANUAL Post Accident Alt Vent H2-V-20 BT-O MANUAL # 2- NONE NONE MANUAL Post Accident Alt Vent H2-V-22 BT-O MANUAL # 2 NONE NONE MANUAL Post Accident Sup Drain H2-V-23 BT-O MANUAL # 2 NONE NONE MANUAL Post Accident Sup Drain IA-03047 BT-C DBD # 2 ~5 1.18-3.56 AOV Inst Air to Cont IA-03048 BT-C DBD # 2 ~5 1.06-3.24 AOV Inst Air to Cont IA-06342 BT-EE NO TIMING 0.25 NO TIME NO TIME NO TIME PORV 430 Nit Sup Reg REQUIRED IA-06343 BT-EE NO TIMING 0.25 NO TIME NO TIME NO TIME PORV 431C Nit Sup Reg REQUIRED i MS-02015 BT-C WE PB-584 6 NONE 20.48-34.14 AOV MS Atmos Stm Dump MS-02015 BT-O WE PB-584 6 NONE 4.55-13.65 AOV MS Atmos Stm Dump MS-02016 BT-C WE PB-584 6 NONE 20.48-34.12. AOV MS Atmos Stm Dump WE PB-584

^

MS-02016 BT-O 6 NONE 6.09-13.49 AOV MS Atmos Stm Dump MS-02017 BT-C M-87 & TS 14.4.7 30 4 & 5 5 Aov Main Steam isolation MS- BT-PV SOLENOID 0.75 NONE NONE SOLENOID MSIV 2017 Air Pilot 02017A-S

l 8? iip Unit 2 Valves with Stroke Times Page 4

- t After Re-review of Westinghouse Spec G676258 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIAL FUNCTION MS- BT-PV SOLENOID 0.75 NONE NONE SOLENOID MS'V 2017 Air Pilot 02017A-S MS- BT-PV SOLENOID 0.75 NONE NONE SOLENOID MSIV 2017 Air Pilot 02017A-S '

MS- BT-PV SOLENOID 0.75 NONE NONE SOLENOID MSIV 2017 Air Pilot 02017B-S MS- BT-PV SOLENOID 0.75 NONE NONE SOLENOID MSIV 2017 Air Pilot 02017B-S MS- BT-PV SOLENOID 0.75 NONE NONE SOLENOID MSIV 2017 Air Pilot 020178-S MS- BT-PV SOLENOID 1 NONE NONE SOLENOID MSIV 2017 Air Pilot 02017C-S -

MS- BT-PV SOLENOID 1 NONE NONE SOLENOID MSIV 2017 Air Pilot 02017C-8 MS- BT-PV SOLENOID 1 NONE NONE SOLENOID MSIV 2017 Air Pilot 02017C-S M S- BT-PV SOLENOID 1 NONE NONE SOLENOID MSIV 2017 Air Pilot -

02017D-S MS- BT-PV SOLENOID 1 NONE NONE SOLENOID MSIV 2017 Air Pilot 02017D-S MS- BT-PV SOLENOID 1 NONE NONE SOLENOID MSIV 2017 Air Pilot 02017D-S -

MS- BT-PV SOLENOID 1 NONE NONE SOLENOID MSIV 2017 Air Pilot 02017D-S 1

8M W Unit 2 Valves with Stroke Times ge,e 8

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After Re-review of Westinghouse Spec G676258 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIAL FUNCTION i MS-02018 BT-C M-87 & TS 15.4.7 # 30 4&5 5 AOv Main Steam isolation MS- BT-PV SOLENOID 0.75 NONE NONE SOLENOID MSIV 2018 Air Pilot 02018A-S MS- BT-PV SOLENOID 0.75 NONE NONE SOLENOID MSIV 2018 Air Pilot 02018A-S MS- BT-PV SOLENOID 0.75 NONE NONE SOLENOID MSIV 2018 Air Pilot 02018A-S MS- BT-PV SOLENOID 0.75 NONE NONE SOLENOID MSIV 2018 Air Pilot 020188-S MS- BT-PV SOLENOID 0.75 NONE NONE SOLENOID MSIV 2018 Air Pilot 02018B-S MS- BT-PV SOLENOID 0.75 NONE NONE SOLENOID MSIV 2018 Air Pilot 020188-S MS- BT-PV SOLENOID 1 NONE NONE SOLENOID MSIV 2018 Air Pilot 02018C-S MS- BT-PV SOLENOID 1 NONE NONE SOLENOID MSIV 2018 Air Pilot 02018C-S MS- BT-PV SOLENOID 1 NONE NONE SOLENOID MSIV 2018 Air Pilot 02018C-S MS- BT-PV SOLENOID 1 NONE NONE SOLENOID MSIV 2018 Air Pilot 02018D-S MS- BT-PV SOLENOID 1 NONE NONE SOLENOID MSIV 2018 Air Pilot 02018D-S MS-02019 BT-C DBD & M-91 3 UNK &15 19.01-25.73 AFW Steam Supply

Unit 2 Valves with Stroke Times

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After Re-review of Westinghouse Spec G676258 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIAL FUNCTION MS-02019 BT-O DBD 3 21 NOM, 50 20.28-27.44 AFW Steam Supply MAX MS-02020 BT-C DBD & M-91 3 UNK & 15 NONE AFW Steam Supply MS-02020 BT-O DBD 3 21 NOM, 50 30 AFW Steam Supply MAX MS-02082 BT-C (AUX FEED TURB 3 NONE NONE Main Steam to AFW Pump OVERSPEED TRIP)

MS-02083 BT-C M-181 # 0.75 NONE 1.86-5.56 AOV S/G Sample isol MS-02084 BT-C M-181 # 3 NONE 1.02-3.06 SG Sampie isolation MS-02090 BT-O DBD 1 2 MAX 0-2 AOV SW to AFW Pump P-029 MS-05958 BT-C WE SP-109 # 2 5 MAX 2.76-8.28 AOV SIG Blowdown Isolation MS-05959 BT-C WE SP-109 # 2 5 MAX 2.64-7.94 AOV S/G Blowdown Isolation RC-00430 BT-C W676270 p1/30 2 NONE 0-2 AOV Power Operated Relief RC-00430 BT-O W676270 p1/30 2 NONE 0-2 AOV Power Operated Relief RC-00431C BT-C W676270 p1/30 2 NONE 0-2.3 AOV Power Operated Relief RC-00431C BT-O W676270 p1/30 2 NONE 0-2.3 AOV Power Operated Relief i RC-00508 BT-C DBD # 2 <=15 2.67-8.01 AOV PRT Fill Line Iso :

RC-00515 BT-C DBD & G676258 3 120 & 15.85-21.45 PORV Block Valve l 120/120 O/C t RC-00516 BT-C DBD & G676258 3 120 & 18.81-25.45 PORV Block Valve 120/120 OIC

giga- Unit 2 Valves with Stroke Times P2, After Re-review of Westinghouse Spec G676258 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIAL FUNCTION RC-00538 BT-C DBD # 0.375 <= 15 4.03-12.08 AOV PRT Sample RC-00539 BT-C DBD # 0.375 <= 15 15 AOV PRT Sample RC-00570A BT-O SOLENOID 1 NONE O-2 SOLENOID RX Vessel Vent RC-005708 BT-O SOLENOID 1 NONE O-2 SOLENOID RX VesselVent RC-00575A BT-O SOLENOID 1 NONE O-2 SOLENOID RX Vess/ Press Vent t RC-00575B BT-O SOLENOID 1 NONE O-2 SOLENOID RX Vess/ Press Vent RC-00580A BT-O SOLENOID 1 NONE O-2 SOLENO!D Pressurizer Vent RC-005808 BT-O SOLENOID 1 NONE O-2 SOLENOID Pressurizer Vent RC-00595 BT-C MANUAL 0.75 NONE NONE MANUAL PRT Nitrogen Supply RH-00700 BT-C W 676258 10 120 8.87-12.01 RHR Loop Isolation RH-00700 BT-O W 676258 10 120 8.97-12.13 RHR Loop Isolation RH-00701 BT-C W 676258 # 10 120 95.7-129.48 RHR Loop isolation RH-00701 BT-O W 676258 # 10 120 98.29-132.98 RHR Loop Isolation RH-00704A BT-C MANUAL 8 NONE NONE MANUAL RHR Pump Suction RH-00704A BT-O MANUAL 8 NONE NONE MANUAL RHR Pump Suction RH-007048 BT-C MANUAL 8 NONE NONE MANUAL RHR Pump Suction RH-00704B BT-O MANUAL 8 NONE NONE MANUAL RHR Pump Suct' RH-00720 BT-C W 676258 # 10 120 88.66-119.95 RHR Return to RCS RH-00720- BT-O W 676258 # 10 120 95.35-129.01 RHR Return to RCS

gijip Unit 2 Valves with Stroke Times ga,, , .

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After Re-review of Westinghouse Spec G676258 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIAL FUNCTION RM-03200A BT-C M-181 # 1 NONE 4.5 AOV Cont Atmos Samp Retr RM-03200B BT-O M-181 # 1 NONE 4.5 AOv Cont Atmos Samp Sup RM-03200C BT-C M-181 # 1 NONE 4.5 AOV Cont Atmos Samp Sup RS-SA-10 BT-C 3 NONE 15 AOV Radwaste Steam Supply SC-00951 BT-C W 676270 # 0.375 NONE 4.34-13.02 AOV Press Stm Sample SC-00953 BT-C W 676270 # 0.375 NONE 3.23-9.69 AOV Press Liq Sample SC-00955 BT-C W 676270 # 0.375 NONE 4.44-13.34 AOV Hot Leg Sample SC-00959 BT-C W 676270 # 0.375 NONE 4.34-13.04 AOV RHR Sample SC-00966A BT-C W 676270 # 0.375 NONE 3.04-9.14 AOV Press Stm Sample SC-009668 BT-C W 676270 # 0.375 NONE 4.54-13.62 AOV Press Stm Sample SC-00966C BT-C W 676270 # 0.375 NONE 8.09-13.49 AOV Hot Leg Sample SI-00834A BT-C W 676270 1 NONE .78-2.34 AOV SIS Accum Vent i

SI-00834A BT-O W 676270 1 NONE 1.04-3.1 AOV SIS AccumVent SI-008348 - BT-C W 676270 1 NONE 0-2 AOV SIS Accum Vent ,

SI-00834B BT-O W 676270 1 NONE 1-2.99 AOV SIS Accum Vent SI-00836A BT-O W 676270 2 NONE 20 AOV NaOH Supply SI-00836B BT-O W 676270 2 NONE 20 AOV NaOH Supply SI-00841 A BT-C W 676258 10 1"/SEC O/C 7.4-12.32 SIS Accum Disch SI-00841 B BT-C W 676258 10 1"/SEC O/C 8.88-12.02 SIS Accum Disch

. _ _ . __ . _ _ . _ _ _ _ _ ______.m_ _ _ . .___._ . . . _ _ _ _ . _ _ _ _ _ . _ _ _ _ . _ _ _ . _ . _ _ _ _ _ . _ _ _ _ _ _ _ _ ________.___m_ _ _ _ _ _ _ _ _ _ _ _ _ . _ _ _ _ _ . _ _ _ ____.__ _ _

gt,ip Unit 2 Valves with Stroke Times P,ge ,

After Re-review of Westinghouse Spec G676258 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIAL FUNCTION l

SI-00846 BT-C W 676270 # 1 NONE 0-2 AOV Accum Nitrogen Supply SI-00850A BT-C W 676258 10 NONE 3.42-10.26 [o"jainment, Sump Hydraulic n

SI-00850A BT-O W 676258 10 NONE 3.37-10.1 [fj ["nment Sump Hydraulic SI-00850B BT-C W 676258 10 NONE 2.99-8.96 [fj [nment n Sump Hydraulic SI-00850B BT-O W 676258 10 NONE 4.02-12.06 [ "j ["nment Sump Hydraulic SI-00851 A BT-C W 676258 # 10 12"/ MINUTE 89.24-120 cont Sump isolation SI-00851 A BT-O W 676258 # 10 12"/ MINUTE 89.26-120 Cont Sump isolation SI-008518 BT-C W 676258 # 10 12"/ MINUTE 89.22-120 Cont Sump iscialtion SI-008518 BT-O W 676258 # 10 12"/ MINUTE 90.45-120 Cont Sump isolation SI-00852A BT-O W 676258 6 10/10 O/C 8.89-12.03 RHR/LH Core Deluge SI-00852B BT-O W 676258 6 10/10 OIC 8.56-11.58 RHRILH Core Deluge SI-00856A BT-C W 676258 10 120/120 OIC 89.03-120 RHR Pump Suction SI-00856B BT-C W 676258 10 120/120 O/C 86.53-117.07 RHR Pump Suction SI-00857A BT-O MANUAL 6 NONE NONE MANUAL RHR to SIS Pump Suction I SI-00857B BT-O MANUAL 6 NONE NONE MANUAL RHR to SIS Pump Suction SI-00860A BT-O W 676258 6 10/10 O/C 10.01-13.55 CS Pump 1-P14A Disch SI-00860B BT-O W 676258 6 10/10 O/C 15 CS Pump 1-P14A Disch .

SI-00860C BT-O W 676258 6 10/10 O/C 10 CS Pump 1-P14A Disch l

t

gijigu. Unit 2 Valves with Stroke Times Po,e ,o After Re-review of Westinghouse Spec G676258 VALVE . .iST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIAL FUNCTION l

SI-00860D BT-O W 676258 6 10/10 O/C 10.5-14.23 CS Pump 1-P14A Disch SI-00866A BT-C W 676258 4 12"/ MINUTE 46.16-62.44 SIS Pump Disch OIC SI-00866A BT-O W 676258 # 4 12"lMINUTE 46.5-62.9 SIS Pump Disch OIC SI-00866B BT-C W 676258 # 4 12"/ MINUTE 47.76-64.62 SIS Pump Disch OIC SI-008668 BT-O W 676258 # 4 12"/ MINUTE 46.72-63.2 SIS Pump Disch OIC SI-00870A BT-C W 676258 6 12"/ MINUTE 8.97-12.13 RWST to CS Pump P14A OIC r SI-00870A BT-O W 676258 6 12"lMINUTE 9.11-12.33 RWST to CS Pump P14A OIC SI-00870B BT-C W 676258 6 12"/ MINUTE 9.2-12.44 RWST to CS Pump P14B '

OIC SI-00870B BT-O W 676258 6 12"/ MINUTE 9.04-12.24 RWST to CS cump P14B '

OIC SI-00871 A BT-C W 676258 6 12"/ MINUTE NONE RWST to CS Pump P14A OIC SI-00871 A BT-O W 676258 6 12"/ MINUTE 15 RWST to CS Pump P14A OIC SI-00871 B BT-C W 676258 6 12"/ MINUTE 7.09-11.81 RWST to CS Pump P14B O/C

.I.

Unit 2 Valves with Stroke Times

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After Re-review of Westinghouse Spec G676258 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIAL FUNCTION SI-00871 B BT-O W 676258 6 12"/ MINUTE 7.47-12.45 RWST to CS F ump P148 OIC SI-00878A BT-C W 676258 2 10/10 O/C 6.87-11.45 RX Vessel Safety inj SI-00878A BT-O W 676258 2 10/10 O/C 7-11.66 RX Vessel Safety inj SI-00878B BT-C W 676258 2 10/10 OIC 7.16-11.94 sis Loop injection SI-00878B BT-O W 676258 2 10/10 O/C 7.14-11.9 SIS Loop injection SI-00878C BT-C W 676258 2 10/10 O/C 6.66-11.1 RX Vessel Safety inj SI-00878C BT-O W 676258 2 10/10 O/C 6.8-11.32 RX Vessel Safety inj SI-00878D BT-C W 676258 2 10/10 O/C 3.8-11.34 sis Loop injection SI-00878D BT-O W 676258 2 10/10 O/C 6.8-11.34 sis Loop injection SI-00896A BT-C W 676258 6 12"/ MINUTE 8.81-11.93 SIS Pump Suction OIC SI-00896B BT-C W 676258 6 12"/ MINUTE 7.33-12.21 SIS Pump Suction OIC SI-00897A BT-C W 676270 2 NONE .78-2.34 AOV SIS Test Line Return SI-008978 BT-C W 676270 2 NONE .88-2.62 AOV SIS Test Line Return SI-00957 BT-C W 676270 1 NONE 2.2-6.6 AOV N2 Supply Vent /Rel SI-00957 BT-O W 676270 1 NONE 1.78-5.34 AOV N2 Supply Vent /Rei SW-02817 BT-C M-91 6 15 12.8-17.32 wr Service water inlet SW-02880 BT-C DBD 6 15 12.21-16.51 Turb Hall Cirs in

=y Unit 2 Valves with Stroke Times P ,, ,2

~

After Re-review of Westinghouse Spec G676258 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIAL FUNCTION SW-02907 BT-O DBD 12 30 23.26-31.46 Cont Ctr Emerg Flow SW-02908 BT-O DBD 12 30 22.14-29.96 Cont Clr Emerj Flow '

VNPSE- BT-C DBD # 36 10 10 AOV Cont Purge Exhaust 03212 VNPSE- BT-C DBD # 36 10 10 AOV Cont Purge Exhaust ,

j 03213 VNPSE- BT-C DBD # 36 10 10 AOV Cont Purge Supply 03244 VNPSE- BT-C DBD # 36 10 10 AOV Cont Purge Supply f

03245 WG-01786 BT-C W 676270 # 1 NONE 5.04-15.11 AOV RCDT Vent WG-01787 BT-C W 676270 # 1 NONE 4.24-12.74 AOV RCDT Vent WG-01788 BT-C W 676270 # 1 NONE 1.74-5.2 AOV RCDT Sample WG-01789 BT-C W 676270 # 1 MONE 1.89-5.67 AOV RCDT Sample WL-01698 BT-C W 676270 # 2 NONE 3.29 -9.87 AOV RCDT to El-19' Sump WL-01721 BT-C W 676270 # 3 NONE 16.82-28.04 AOV RCDT Pumps Suct Con

WL-01723 BT-C W 676270 # 3 NONE 21.74-36.24 AOV Containment Sump WL-01728 BT-C W 676*df) # 3 NONE 20.04-33.4 AOV Containment Sump j WL-OiOO3A BT-C W 676281 # 3 NONE 14.14-23.58 AOV RCDT Pump Suction WL-01003B BT-C W 676281 # 3 NONE 13.43-22.39 AOV RCDT Pump Suction c._ _ _ _ _ _ . _ _ - . _ _ _ _ . _ . _ . _ - . _ _ _ _ _ . _ . _ _ _ _ _ _ _ . . _ _ . _ _ _ _ . _ _ . _ . _ _ . _ _ . _ _ _ . _ _ _ _ _ _ _ _ _ _ _ _ _ . _ . _ _ _ _ _ _ _ _ _ . _ _ _ _ _ _ _ _ _ . - _ _ _ _ _ _ _ _ . . - _ . _ _ _ _ _ _ _ _ _ _ _ _ _ _ . _ _ . _ . _ _ _ . _ _ _ . _ _ - . _ _ _ _ _ _ . _ _ _ _ . _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _

g;gy Unit 2 Valves with Stroke Times go,, ,3 After Re-review of Westinghouse Spec G676258 VALVE TEST DESIGN SOURCE l SIZE DESIGN TIME IST TIME SPECIAL FUNCTION ZZZ-AF- BT-C ZZZ's have been 6 MANUAL 2P-29 Suction 00064 dropped from program ZZZ-AF- BT-C ZZZ's have been 3 DELETED 2B S/G AFWlsol I 04000 dropped from program ZZZ-AF- BT-C ZZZ's have been 3 DELETED 2A SIG SFWlsol 04001 dropped from program ZZZ-AF- BT-C ZZZ's have been 1 AOV 2P-29 Mini-flow 04002 dropped from program ZZZ-AF- BT-O ZZZ's have been ! 1 AOV 2P-29 Mint-flow 04002 dropped from program ZZZ-AF- BT-O ZZZ's have been 6 DELETED 2P-29 Ser Wtr Sup 04006 dropped from program ZZZ-CV- BT-C ZZZ's have bien 2 MANUAL Charging Line HCV Outlet 003848 dropped from V 've program ZZZ-MS- BT-C ZZZ's have been 3 DELETED AFW Steam Supply 02019 dropped from program

Unit 2 Valves with Stroke Times gijigy. go,, ,,

After Re-review of Westinghouse Spec G676258 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIAL FUNCTION ZZZ-MS- BT-O ZZZ's have been 3 DELETED AFW Steam Supply 02019 dropped from program ZZZ-MS- BT-C ZZZ's have been 3 DELETED AFW Steam Supply 02020 dropped from program ZZZ-MS- BT-O ZZZ's have been 3 DELETED AFW Steam Supply 02020 dropped from program ZZZ-MS- BT-C ZZZ's have been 3 DELETED Main Steam to AFW Pump 02082 dropped from program ZZZ-MS- BT-O ZZZ's have been 3 DELETED Main Steam to AFW Pump 02082 dropped from program ZZZ-MS- BT-O ZZZ's have been 3 DELETED Main Steam to AFW Pump 02082 dropped from 1 program ZZZ-MS- BT-O ZZZ's have been 1 AOV SW to AFW Pump P-029 02090 dropped from program ZZZ-SI- BT-O G676258 12 1"/Sec O/C DELETED SIS Pump Suction 00825A ZZZ-SI- BT-O G676258 12 1"/Sec O/C DELETED SIS Pump Suction 00825B

h

=p Unit 2 Valves with Stroke Times P.,, , s After Re-review of Westinghouse Spec G676258 VALVE TEST DESIGN SOURCE SIZE DESIGN TIME IST TIME SPECIAL FUNCTION ZZZ-SI- BT-C G676258 12 1"/Sec O/C DELETED SIS Pump Sution 00826A ZZZ-SI- BT-O G676258 12 1"/Sec O/C DELETED SIS Pump Suction 00826A ZZZ-SI- BT-C G676258 8 1"/Sec O/C DELETED SISPump Redundant Suc 00826B ZZZ-SI- BT-O G676258 8 1"/Sec OIC DELETED SISPump Redundant Suc 00826B ZZZ-SI- BT-C G676258 8 1"/Sec O/C DELETED SISPump Redundant Suc 00826C ZZZ-SI- BT-O G676258 8 1"/Sec O/C DELETED SISPump Redundant Suc 00826C i

_ _ . _ _ _ _ _ _ _ _ . _ _ . _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ . _ _ _ _ _ . _ _ _ _ _ _ _ _ _ _ _.____a _ __ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ . _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ . . _ _ _ _ _ _ _ _

6 N

g Eq%- 4ID Functions Related no - . Functmn Struke'llime i Bases for Sooke Time Performance Rsqdrement -

StrokeRequhements -

-^ Classification Performance

U CC-719 Requim This nortnally open valve shall provide remote- SR i None See Note I below, remote-enanual(no autornatic manual isolat on of the RCP and excess letdown q heat exchanger cooling water supply heeder to signal to close) valves have no required stroke 4 peclude leakage of CCW to the containment in tirne to accomplish their function.

the event that the CCW lines located inside the missile barrier (RCP cooling water 1mes) are rupuned as a consequence of a IDCA. CC-719 provides the necessary Neuhy to remote-macualisolation valves CC-754A,B to ensure isolation of the break and thereby reserve CCW system integrity for long-terrn cooling ofsafety relatedloads. [WCAP-13938.1/7/941 CV-112B

'Miis normally closed valve shall au'=Wcally Non SR See Basis ,

open on low VCTlevel to provide a t!owpath Exact nme basis is not well defined. Original from the RWSTto the charging pumps. design provision was such that CV-112C did not

% [WCAP-13644, dated 3/93] start to close until CV-112B left its fully closed q position to ensure a continuous suction sourte u [WCAP-13644, Sections 433.E.6 and ,

E 5.6.2.53.D), and did not consider ulve stroke a tiroc. If stroke times are considered, this valve O should only need to be partially open (exact %

[

+

open unknown) when CV-112C is fully closed to provide a continuous suction source. Current IST accer*nce range appears to be adequate.

Page1ofII l

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g < EgulpmentID ; FunateamsReleend to -

- Phnenon -cSeekeTyne '

Strake * - ' .

7,2f w BassibrSmokeTimie hP=q._jp N -

~ Classification.

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h aainsnent

% yvu CV-112C - :

h mannally open valve shall automatacally Non SR <l mmute 1n An exact time basis is est well defined. Origmal cJose on low VCT level to prevent drawmg VCT gas into the chargeg pumps design allowed a two mi== delay to transfer to

[WCAP-13644, dated 3/93) the RWST DE r=laMoe RFS-W-168] however, this only considered see operstang chargmg puunp. Catest stroke time mpiirement is evaluated as follows: Fmergency makeup is pnmded frora RWST at 4% VCTlevel [STPT 5.5]. At 4% indicated VCT level, >200 gallons remain in VCT from tank level book [from TLB-4 VCThas200 gmHans @ = 1% VCTlevel). 3 cheging purops operating at full design How

, (I Bl.5 gpm) therefore ragmire > ! minute to fully -

drain VCT. CV-112C shutting in less aban I i minute peevaits gas fsem being drawn to charging CV-313 These nonnally open valves M-m a pumps for all possible d 3 ng i pump Imeups.

CV-313 A SR None Refer so DBD Group Response so the Brad

contanasient isolauon function for the excess Frerna question on the technical basis for letdown /RCP seal water netwn line. He valves automatically clone on a containment isolation contamment isolation valve closwe tirnes.

("O signal dang a LOCA. [FSAR Section 5.2]

CV-350 m normally closed valve provides remuse-Non-SR None See Note 1 below; remose-manual (no ausomatic manual capability for the operater to borate the signal to close) valves have runequired stroke RCS from the Boric Acid Storage Tanks during normal plant :====' ion. time to accomphsh their function.

CV-371A Dis nonnally apen valve performs a SR None Refer so DBD Group Response to the Brad containmet isolation function for the CVCS Fromm question on the technical basis for letdown line. The valve amoniatically closes on a cantainme-t isolanon (T) signal dwing a contamment isolanon valve closure times.

LOCA. [FSAR Sectaan 5.21 MS-5958 These normally opeo e-Ass perform a MS-5959 SR None Refer to DBD Group Response to the Brad conennament isolation function for the steam See Note 2 generater blowdown Inne freen each SG. He Fromm question on the technical basis for valves automaatically close on a contaenment contamanent isniation volve closuse times.

i isolation (T) signal during a LOCA. [FSAR .

Section 5.2]

I Page 2 of1I

_ _ . _ _ . _ __ __ _ __ - . _ _ _ _ . . _ _ _ _ - . _ . _ _ _ _ _ . _ _ . . _ . _ _ _.______.________m_.__ _ _ _ _ _ _ _ _ _ _ . _ _ _ . _ _ _ _ _ _ _ _ . _ _ _ _ _ _ _ _ _ _ _ _ _ . _ __ _ _ _ _ _____.__ _ __ ______m

2 .

D AmpmentIDc ..- Functions Related t> Fim: tion '

g -

Stmke Requirements

.- f Stroke Time . Bais fair SamkeTimeb6w Requirement -

- Classification Pertormacee

- J:1.- e /

SI-852A,B Rcquia-r t. '

s These oc==!!y cl<W valves shall open SR 521.7 wwods A automatically to permit low-head safety The large break LOCA accident (FSAR Section 143.2) was recently evaluated for increased injection into the RCS for accident mitigation.

[WCAP-14205,12/2/94] safety injection delay times by Westinghouse (WEP-97-500,1/10/97). The low head safety injection delay time was increased to 23.7 seconds and is made up of the following components: 2 seconds for SI signal processing,7 seconds for sequencer plus uwwy delay, and I4.7 sewnds for the RHR pump start to full speed [CR 97-0071}. The SI-852A B valves receive an 51 signal and will begin to open after the SI signal processing deley (2 seconds). Therefore the SI-860A,B,C,D valves must be fully open in s 2 f.7 seconds.

These normally closed valves shall open SR s 16.5 seconds The Containment Integnty Evaluatice, FSAR automatically following accidents requiring mntainment spray to permit spray Dow to the Section 143.4, assumes that containment spray is containment in support of containment coolicg actuated 60 seconds afterevent initinuon. This and the control of containment airborne assumption was questioned via CR bl486, radioactivity. [WCAP-14205,12/2/94) which resuhed in an evaluation of containment spray actuation time. The valve will receive a signal to open at the same time the pump time delay relay receives (TDR-18) receives the signa!.

The SI-860 valves stroke times must therefore be s 16.5 seconds (the sum of TDR 18 delay of11.5 seconds plus the pump aweleration delay) to be conservative with respect to the evslustion in CR 96-1486.

Page 3 ofIi

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4 (EquipioeptID Puncues Rahead to . :Str%eJams;f- :

D '~ <

SeekcRequinenents

Function . Basis forSamka TanePetfmm=== Requirement c1===rication Jerfonnance - '

V 5.a

.w--firement -

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. SI-841 A,B Dese normally open vr% shall remam open SR None These valves de not have to stroke in order to dunng the SI injection phase to permit the flow perfonn their SR faction.

of borated accuenulseor water mio the RCS for accident mitigation. [WCAP-14205,12/2/94]

SI 841 A,B Aall open automatically following Non SR None his N ' i function does not innpose a stroke .

accidems resprirmg accumulator injecten to time pc" acerequarament. Technical pernut flow of borased wanar into the RCS.

Specific 415.3.3.A.2.a allows one accumulator Closwe of SI-84 I A,B is permitted for a limited to be isolated orotherwise inoperable for periods penod(LCO)daring power operation, of up to one how.

[WCAP-14205,12/2/94)

SI-850A,B Dese mornelly closed valves shall provide SR None See No1e I below; remosemamal(no automatic remote-=====1 actuatinn from the mam control signal to open) valves have no required stroke board to establish post,= mat long-tenn time to accomplish their function.

recirculation from the amp. [WCAP-14205, 12/2/94]

SI-851A B Dese L L. Ily closed valves shall provide SR None See Note i below;remotesmanual(no automatic reencne<nanaal acusation from the main concret signal to open) valves have no required stroke board to establish post-accidet long-term time to accomplish their function.

recirculation from the sump. [WCAP-14205, 12,194]

Dese normally closed valves #crm a SR None Refer to DBD Group Response to the Brad containment isolation functum for the Fromm question on the technical basis for containment sump recuculation lines. They containment isolation valve closure times.

shall provide remote manual isolatiam of an outside-contamment leak durmg the SI recirculation phase. [F5AR Section 5.2)

_ SI-866A,B None. Dese normally open valves shall rernam SR Nonc 'Ibese valves do not have to stroke in order to open during the SI injection and long-term perfonn their SR function recircutseien phases to permit the flow of borated water into the RCS for accident mitigation. [WCAP-14205,12/2,94)

Page 4 of11

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Eqmpment ID Funcitoe6 Related to Function Su9ke Time Basis for Stroke Tune I% fw -e Requirmnent Seroke Requhements t'laamification Performance p SI-570A,B hese nortnally open valves shall provide Requimt' SR None See Note I below; remote. manual (no automatic rernote-manual actuation frem the main control signal to close) valves have no required stroke board to isolate the RWST from sump tune to accomplish their function.

recirculation water during the transition from the SI injection phase to the post-accident long term recirculation phase. [WCAP-14205,12/294)

SI-571 A,B hese normally closed valves shall provide Nan SR None See Note 1 below;rernose manual (no automatic remote-manual actuation from the main control signal to open) valves have no required stroke board durmg the transition between the Si time to accomplish their function.

injection phase and the po t-accident long-term recirculation phase to permit alignment of the containment sprmy pump suction to the discharge of the RHR pump to suppon continued delivery of spray flow to the contamment [WCAP-I4205,12/2/94l SI-S%A,B These normally open valves shall provide SR None See Note I below; remote-rnanual(no autanatic remote-mannalisolmion of the RWST from signal to close) valves have no required stroke sump recirculation water durmg the transition time to accomplish their function.

fmm the SI injection phaw to the post-accident long-term recirculation phase [WCAP-14205, 12/2/941 CC-754A,B These nonnally open valves shalf provide SR None See Note 1 below, remotcananual (no automatic reruote-enanual isolation of RCP cooling water signal Io close) valves have no required stroke supply Imes in order to preclude leakage of tirne to accornplish their function.

CCW to the containment in the event that the CCW liries located inside the missile barrier (RCP cooling water lines) are ruptured as a consequence of a LOCA. CC-754A,B provide the necessary redundancy to remote-martual isolation vahes CC-719 to ensure isolmion of the break and thereby preserve CCW systern integrity for long-tenn cooling of safety related loads. lWCAP-13938,17M4]

ISge 5 of II

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b Equipment ID Functions F* tan ~i to Funcugn Booke1 h - Easa for Strehm hna Perfarnance Requirement -

Samke Requirements Classification Performance

[ CC-759A.B These normally open valves shall serve as SR RQ.

None t

Rett to DBD Group Response to the Brad containment isolation valves and provide Fr mirn question on the technical basis for remote-manual isolation of the RCP cochng cataintnent isolation valve closure limes.

water return hnes outside containment following accidents in order to preclude the release of radioactivity to the envimnment. [FSAR Section 5.2}

These normally open valves shall provide SR None See Note i below; remote-manual (no automatic remose-manual isolation of RCP cooling water signal to close) valves have no required stroke rerum Imes in order to prevent outleakage of time to accomplish their function TW in the event that time CCW lines located inside the missile barrier are ruptured as a consequence of a LOCA, Oeck valve CC-745 I pmvides the necessary redundancy to ensure isolation. [WCAP-13938. IU,H]

i hese normally open valves shall provide SR None See Note 1 below; remote-manual (no automatic remote-manual isolation of RCP coolmg water signal to close) valves have no required struke return lmes in order to preclude leakage of high time to accomplish their function pressure radioactive flaid outside of contamment as a result of a thermal barrier rupture. [IST Background Document)

Ril-701 Valve RH-701 shall serve as a contamment SR Nome Refer to DBD Group Response to the Brad ;

isolation valve and shall provide remote manual Frornm question on the technical basis for i isolation of the RIIR supply line to limit the containment isolation valve closure times.

release of potentially radioactive materials so the '

environmo.: fo!! ewing accidents. (FSAR Section 5.2} !

This valve shall provide means 10 initiate RilR Non SR None See Note I below; remote-manual (no automatic systern operatson remotely from the main signal to close or open) valves have no required control board during plant cooldown and stroke time to accomplish their function.

subsequently isolate RHR from the RCS during plant heatup. [WCAP-1430I, W16/94]

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- _ _ _ _ _ - _ _ - _ - _ _ - _ - _ _ = _ _ . _ - _ - _ _ _ _ _ . _ - _ - _ - _ _ _ _ - - - - - - _ _ _ - _ - - _ _ _ _ _ _ - - _ _ _ - _ _ - _ _ _ _ _ _ - - _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _

. . _ _. ._ _ _ _ . _ _ _ . _ . _. __ ..- m _ _ m. _ _

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+o p EqutprnentID Functsoas Related to Function Stroke Tune Basis for Strwhe Tane Pcrformarm Requirement J Stroke Requirements Classification Performance n Requitunent Rii-720 This valve shall serve as a coctainsnent isolation SR None Refer to DBD Group Response to the Brad valve ami shall provide remote manual isolation Fromm question on the technical basis for of the RiiR return line to limit the release of contamment isolation valve clostare times.

potentially radioactive matenals to the environrnent followmg accidents {FSAR Section 5.2]

nis valve shall provide the means to initiate Non SR None See Note I below; remote enanual (no autownstic RifR operation remotely frorn the main control signal to close or open) valves have no required

room dwing plant cooldown and subsequently sarole time to accounplish thetr function.

isolare the RHK system from the RCS during plant bestup. [WCAP-1430I. 5/I@4]

SI-875U,D None. Ecse nonnally open valves shall remam SR None Dese valves do not have to stroLe in order to open during the 51 injection and long-serm perform their SR function rectreulation phases to permit the flow of borated water into the RCS for accident mitigation. lWCAP-14205.12/2M4]

SI-878A.C Bese normally closed valves shall provide SR None See Note i below; rernote-manual (no automatic remote-manual actuation froni the snain contml signal so open) valves have no required stroke board diaring the post-accident long-term tirne to accomphsh their function recirculation phase within 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> after a SBLOCA accident. His allows realignment of the safety injection system permitting simultaneous injection into both the cold legs and the vessel as an added safeguard against the potential for boron precipitation. [EOP 1.2, WCAP-14205.12/294]

I Page 7 of'I1

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% Equqmnant ID Fumethm - Stmie Time Basis for Sarnke Time Perfcomance Rsqiurament FunctionsAtleted to Strole Requirencents casificatka Perfortomace 4

y ~ ' '

Requi:unent 2SW-2880 This nonnally open valve shall autornatically SR sl61/2 seconds The service water (SW) hydraulic nuxlel is a close when less than 4 of 6 service water pumps steady-state rnodel that regni- - .fi valves to be in start followmg a Unit 2 accident, to isolate non- their final position wishin 60 secteds. 60 seconds essential Unit 2 Turbme Buikling users and is the time at which full heat removal is assumed I provide suflicient flow to safety-related heat in the containment integrity analysis [CR %- i exchangers. [DBD-12, Rev.0, Section 4.11] 1486]. To meet the containment integrity !

accident anafysis and the assumptions in SW ,I hydraulic models related to the SW System response during the irijection phase of a LOC A (i.e Calculation 96-117), the stroke ttrne or!.SW-2880 must be s 16.5 seconds based on the following:

I/2 seconds - time for contamroent pressure to reach SI signal setpoint 2 seconds - signal processing delay 10 seconds - EDG start time delay 31 1/2 seconds - acceptance limit for TDR 20 based on "as-founif' limits in ICP 158 16 U2 seconds - valve stroke time 60 seconds 1SW-2880 This normally open valve shall automatscally SR sl61/2 seconds Basis is similar to 2SW-2880 to achieve valve close when less than 4 of 6 service water pumps closwe within 60 seconds, except no specific start following Unit I =ccMent, to isolate non- calculation exists which requires valve operation essential Unit 1 Turbme Building usas and under power failare conditions.

provide sufficient flow to safety-related heat exchangers. [DBD-12, Rev. O, Section 4.11]

i i Page 8 of I1

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o EquipecarID hiians Related to Function Stroke Time Basis for Stroke Time Pedormance Requirement Seroke Reqmrernents Classifa: anon Performance i

Requiressent i 5 SW-2818 This valve shall automatically open upon startup Non SR See Basis 'The cable spreadmg room chiller is almost always of the cable spreading room chiller, to provide loaded during normal operation, therefore, this cooling water to the cable spreadmg ruem valw is typically "open" and not required to j condensers.

change positirm. A design basis stroke time hmit I has not been dermed for this valve, however,if '

one were developed it would be based on preventing a high refrigeram pressure trip on initial startup of the chiller urut. Current IST limits for this valve are considered acceptable since operating experience has demonstrated that (1) delays in the A/C unit in achieving operating temperature, and (2) the significant flow that occurs when the MOV is partialty open have prevented this trip fmm occurung.

SW-2819 This valve shall automatically open upon startup Non SR See Basis The control rooni chiller is almost always loaded of the control room chiller, to provide cooling during nornial opeention, therefore, this valve is water to the cor. trol rnom condensers. typically "opcm" and not required to change position. A design basis streite time limit has not been defined for this valve, however, if one were developed it would be based on psevestmg a high refrigerant pressure trip on initial startup of the chiller imit Current IST limits for this valve are considered acceptable since operating experience has demons *, rated that (1) delays in the A/C u .it in achieving operating temperature, and (2) the significant flow that occurs when the MOV is partially open have prevented this inp from l occurring l

e i Page 9 of I 1

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O q Equipmc= TID . functions Reinted to Function - $troke Tune Basis for Stroke Time Paformance Requirement ..

~

Strcke Requisements rian=dication Nivi --- 2 Requirement '

@ MS-2015 Rese valves shall be capable of being manually SR None See Note 1 below; renmal (no automatic MS-2016 opened (remote or locally) to cool down the signal to open) valves have no requimi stroke t RCS during a Steam Generator Tube Rupnare time to accomplish their function event coincident with loss ofoffsite power.

[FSAR Section 14.2 4) ,

'Ihese valves diall be capable of rernete-manual Non SR Noce See Note I below; remote-rnanval (no automatic operation during routine reactor shutdown to signal to opea) valves have no required stroke !

remove decay heat and maintain hot shutdown time to necomplish their function (or cooldown to RHR entry conditions).

[FSAR Section 10.2]

'Ibese valves shall automatically open at a preset Non SR s 20 seconds Westinghouse Steam Systems Criteria (PBW-SG pressure during load trjectam events, to WMP-992 date 11/8/68) gan a stroke criterion supplement the condenser steam durup valve for " Steam generator power relief valves". He function and minimize lifting the steam - criterion was "the relief valves shall be of the i genierator code safety valves. Note that the modulating type, with a maximum full stroke time atrnospheric steam dump valves are asssumed of twenty seconds."

not to operate for the I. mss of LoaJ licensing basis analysis. [FSAR Section 14.1.9) l ,

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i Page 10 ofI1 l

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i

, Footnotes 1.

Valves equipped with remete-enanual e,perators (i.e. no automatic signals) do not have a minmuum required seeke tirse so accomplish their p hmetion. The basis for this conclusion is that te time necessary to re-positica a manual valve inchales te valve inovement plus the time needed for plant opermor recognition, decision, and action. Placing a specific limit an a marmal valve's stroke time is unnecessary, without also imposing specific time limits on the opastor actsons leadmg up to the valve movement; such operator action time limits for rnarual valves do not exist.

2. He SG blowdown hnes are closed inside containmer.t, and provide an adequese passive contamrnent barner durmg LOCA without the need for isolation valves; the blowdown valve isolation function is currently under review in the Design Basis Documesit Program, arx! the classification of this function rney dange to non-safety-relmed in the furure. !

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]

h OldrW f f) l ct ]

, Response to Design Basis Question on l l

Containment isolation Valve (CIV) Closure Timts g i Question What is the real design basis number for PBNP containment isolation valve ,

closure times? Ten (10) seconds is mentioned for air-operated valves in FSAR Table 7.51 for EQ requirements. Sixty (60) seconds is mentioned in CHAMPS. !

What do we take credit for and what do we need? '

Resoonse I

t Based on the lack of containment isolation closure time requirements in actident analyses or in the FSAR, no specific limits exist for containment isolation closure times. i The following sources were searched ?o reach this conclusion: i 1

1. PSARs for Unit 1 and Unit 2 No statements that addressed CIV closure times were found in either unit PSAR or in

, our response to AEC questions on the PSAR. l

2. FSAR Section 5 2. Containment isolation System This FSAR section describes containment isolation criteria, penetration configurations, and containment isolation valves. Although this is the logical place to find information on CIV closure times. closure times are not mentioned in the text, tables, or figures. '

3. FSAR Section 6.2. Safety iniection System Page 6.2 22 states: "For those valves which must function on a safety injection signal, fast operators are provided to allow for reaching design flow within 10 seconds. ".

Based on its location in the SIS section of the FSAR, this capability statement specifically applies to valves that establish safety injection flow (not the containment isolation function). The statement is also supported by an FSAR reference to an IST valve stroke time analysis specifically for achieving Si flow'. This FSAR section does not address either the containment isolation function or any corresponding valve closure time limits.

4 FFDSAR Section 6.2. Safety Iniection System The original FFDSAR also included a capability statement for 10-second valve operating time, but in a different context than the current FSAR: "For those valves which rnust function on a safety injection signal,10 second operators are provided. *. Although this statement is in the SIS section of the FFDSAR, it could be interpreted to iriclude all Letter VPNPD 90-310/NRC-90-064, ' Guidance on IST Program, Generic Letter 89-04 Follow-up*,

dated June 28,1990 , ,

i s

f v & of l valves that receive an Si signal (not just S1 valves). The statement is mentioned for two reasons!

l

1) Si is the signal that isolates containment isolation valves, and ,

2) If taken out of context, this sentence could have been misinterpreted as a licensing commitment to provide containment isolation valves with 10-second operators (since CIVs receive an Si signal) and require CIVs to close within 10 seconds.

This misinterpretation may have occurred (see next rtem).

5. FSAR Table 7.5-1, General Operatina Time Reauirements for Environmental Quali*ication of Electrical Eouloment FSAR Table 7.5-1 is a table of EQ requirements. The table includes a column labeled '

" Time to Operate" for various electrical equipment. The table defines Time to Operate as the time after an accident in which it is expected that the item will have completed its safety function. Under the Table 7.E-1 heading Valve Ooerators. the entry "Alr Operated Conteinment isolation" has a corresponding Time to Operate of 10 seconds2 . !

It has been suggested that tnis EQ Time to Operate is the same as the required CIV closure time. :

l The following points attempt to explain why the EO Time to Operate is not the same as i the required CIV closure time:

l

a. Table 7.5-1 is titled as an EQ requirements table for ELECTRICAL equipment. '

The air solenoid is the only electrical valve component associated with closing a typical air-operated CIV. Air-operated CIVs are designed to fail closed either when air is removed from their actuator or when power is removed from their air solenoid. To perform its function, the solenoid must deenergize on an SI signal and vent the air operator to close the valve. Once the actuator vent path is established through the solenoid, the solenoid has completed its function. From discussions with John Hinck, the EQ requirements in this table only apply to the air solenoid and its deenergize-to-vent function. As mechanical components, the air actuator and valve body are outside the EQ program scope, 10 seconds is sufficient time for a solenoid to " drop out" to its vent position after being deenergized by an (SI) signal. Once doenergized, the solenoid will remain in the vent position under a harsh environment. The 10-second EQ time applies only to solenoid operation, and does not represent the total tirr.5 it takes to close the isolation valve. 1

b. Table 7.5-1 was added to the FSAR in 1984. Before that time, the EQ Time to Operate information was found in the FFDSAR, under the WE response to AEC question 6.4 (Tabic Q 6.4-1). Instead of specifically mentioning containment isolation valves, the FTDSAR table contained a more general entry " Air Operated isolation Valves" with a *10 seconds after signal" operating time'. A footnote stated that environmental testing was not required because all in-containment i 2 Footnote 2 in Table 7.51 exempts the purge supply and exhaust valves from the 10-second time and lists their time to operate as 60 seconds. i 3

FFOSAR paGa O 6.4-7 dated Apn! 20.1970

l P) 3 c5 7

( . air operated isolation valves fail in the closed position.

l The important point about the FFDSAR table is that in the context of the original l

AEC question response, "10 seconds after signal" resembles the Section 6.2 statement "For those valves which must function on an SI signal,10-second l operators are provided". As stated earlier, this last statement was specifically addressing valves in the SI flow train, not containment isolation valves.

Since 10-second valves are not discussed elsewhere in the FFDSAR, it appears that the response to AEC Ouestion 6.4 incorrectly translated a Si valve capability statement in FFDSAR Section 6.2 into an EQ operating requirement for all air-operated valves. Although this is speculation, it seems like a reasonable guess, because the AEC question was specifically directed at FFDSAR Section 6 and the only place the FFDSAR mentioned 10 seconds was related to Si valve operation in Section 6.2.

Evidence that the overall stroke time for containment isolation valves was not limited to 10 seconds is found on FFDSAR page 7.5-10, which contained the following statement under Environmental Cacability:

The expectedlength of time that equipment will be required to function following an accident is ...

e. Air and motor operated containment isolation valves (operation completed in first five minutes after accident).

Since this statement coexisted with the AEC Question 6.4 response', it seems clear that the 10-second operating time in the table was inter'Jed to apply only to the air solenoid, and'was not intended as a CIV closure time requirement.

c. Table 7.51 Footnote 2 was added in 1992, and contains what appears to be a legitimate valve closure time requirement for the purge supply and exhaust valves. However, the 60-second time limit in Footnote 2 only applies to a fue!

handling accident. which is a non-EQ event. Since fuel handling accidents do not create harsh EQ environments, including this footnote in an EQ Time to Operate table is inappropriate. The table was apparently a convenient place in the FSAR to put a closure time limit for these valves, although closing these valves within 60 seconds has nothing to do with environmental qualification.

(See later discussion on the origin of the generic 60 second closure time Jimit and see Conclusion #1 for the validity of a 60-second closure lirnit for purge supply and exhaust valves)

6. FSAR Sections 14.21 and 14 3.5 From a design standpoint. the logical source of any CIV closure time requirements is the l offsite dose analyses. These FSAR sections cover the offsite dose consequences of a l fuel handling accident and a LOCA, respectively. There is no mention in either section of an assumed CIV closure time for establishing containment integrity. The limiting fuel handling accident is assumed to occur in the spent fuel pool area, so containment isolation / integrity is not involved in the !imiting fuel nandling accident offsite dose This statement also appears in the first version of the AEC Question 6.4 response dated January 16.

1970. The statement was replaced by Table Q 6.4-1 in the second version dated March 13.1970.

l t

b 4 cl 7

, analysis. Although MSSM 89-20 Attachment A stated that there is a 60-second containment isolation time limit in FSAR Section 14.2.1, no such time limit was found -

l in the current FSAR. A review of FSAR changes indicates that a purge isolation time limit has never been str.ted in FSAR Section 14.2.1.

For the LOCA ana8ysis, the analysis assumes a " buttoned up" containment throughout the accident G.e., no puff of radioactivity escapes before containment integrity / isolation is achieve. ). Carl Onesti confirmed that CIV closure times are not modeled in the LOCA offsite dose analysis. The analysis assumes that no direct release paths exist through open containment penetrations to the outside atmosphere throughout the LOCA event. From a CIV closure time standpoint, this assumption amounts to saying that any closure time would be acceptable provided containment integrity is achieved before radioactivity releases occur through any [non-essential) penetration. Based on the maximum containment leakage rate assumed in the dose ar'alysis and the torturous path that containment radioactivity must take to escape through an open penetration before isolation occurs, it is expected that the offsite dose analysis will be insensitive to CIV closure time.

7. CHAMPS 2 The data sheets for some containment isolation valves in CHAMPS 2 contain a note implying a 60-second closure time limit, based on NRC Standard Review Plan 6.2.4 As discussed below, the SRP 60 second value is only guidance, and there is no known PBNP commitment to meet the SRP guidance.

8. Current Licensino Basis Database The CLB database was searched for information on CIV closure times. Keywords searched for included " Containment isolation" and " Isolation Valve" No licensing documents were found that require ClV closure within any time limit.

CONCLUSION #1:

Based on lack of specific CIV closure time assumptions in the offsite dose analyses and lack of CIV closure time criteria it' the FSAR and other licensing documents, it can be reasonably concluded that no specific design requirements exist for PBNP containment isolation valve closure times.

The 60-second closure tirne for purge supply and exhaust valves in FSAR Table 7.5-1 is a current licensing commitment. However, no design basis has been found requiring these valves to close within 60 seconds. The offsite dose analysis for a fuel handling accident inside containment' assumes the entire radioactivity inventory from the damaged fuel assembly was released from containment to the environment during the accident. The calculation took no credit for purge isolation to limit the radioactivity release, and in fact showed no purge isolation was necessary to achieve acceptable offsite dose consequences. .Therefore, based on the calculation assumptions and results, a 60-second purge valve closure time is not a PBNP design requirement to limit offsite dose.

Calculation N-90-078. Site Boundary Whole Body and Thyroid Dose following a Fuel Handling Accident, dated 11/7/90 ~

]g

p) 2 c, I The remaining discOssion addresses closure time guidance found in the NRC Standard Review Plan and ANS 56.2, and valve stroke time limits in the in-Service Testing (IST) program.

1. Standard Review Plan Section 6.2.4 The SRP contains guidance for NRC reviewers of licensee Safety Analysis Reports.

Section 6.2.4 covers containment isolation review guidance. This section defines containment isolation valve closure time as the time it takes for a power-operated valve to be in the fully closed position after the actuator power has reached [or been removed from) the operator assembly; it does not include the time to reach actuation signal setpoints or instrument time delays. The SRP suggests two closure time limits, as follows:

e forlines which provide an open path from the containment to the environs; e.g.

the containment purge and vent lines, isolation valve closure times on the order of 5 seconds orless may be necessary. The closure times of these valves should be established on the basis of minimizing the release of containment atmosphere to the environs, to mitigate the offsite radiological consequences, and assure that emergency core cooling system (ECCS) effectiveness is not degraded by a reduction in the containment backpressure. Analysis ... should be provided tojustify the selected valve closure time.

e in general, valve closure times should be less than one minute, regardless of valve size.

It is apparent from this wording that the five second and one minute closure times are guidance, not hard requirements. Since Point Beach is not committed to meet the SRP guidance, these numbers have no direct bearing on the CIV closure times for PBNP, other than as a licensing perspective on how containment isolation is reviewed for newer plants.

The SRP wording also shows how closure times are related to the dose analyses.

Without specific isolation time assumptions in the dose analyses, it is unreasonable to assign an arbitrary requirement for valves to close within one minute.

Attached is a memo describing a 1988 conversation with NRC personnel about the origin of the one minute guideline in SRP 6.2.4.

2. ANS-56.2-1984. Containment Isolation Provisions for Fluid Systems After a LOCA This standard does not apply to the Point Beach design. However, Section 4.4.4 of the standard is titled valve Closure Time, and provides insight into more recent industry criteria developed for CIV closure times, as follows:

The objective to establishing valve closure times shouldbe to limit the release of radioactivity fmm the containment. ...

In general, power-operated valves three and one-half inches to 12 inches in diameter should be closed at least within a time determined by dividing the nominal valve diameter by 12 inches per minute. ... %Ives three hches andless should generally close within 15 seconds. All valves larger than 12 inches in diameter should close within one minute unless an accident radiatiorLdose_.

-;; e

1

. s l l

l 1

f.LdT

, l

.. J calculation is pctformed to show under accident conditions that the longer l closure times do not result in radiation releases significant enough that accident i dose allowances are exceeded. ...

1 In determining appropriate valve closure times, consideration shallbe given to j time delays due to instrument and control delay times as welles valve motive l power delay times. ...

I 1

3. IST Valve Stroke Time Limrts !

l Containtnent isclation valve stroke times are periodically measured as part of the in-Service Testing UST) program. An increase in valve stroke time may indicate stem friction or actuator problems, which could lead to valve binding. The stroke time limits established for IST are intended to detect performance degradation, and are not necessarily related to any absolute ClV closure time requirements.

I IST stroke time limits are typically established using actual valve times. An initial timing test establishes a b seline stroke time. The IST acceptance limits are based on adding margin (+ and -) to the baseline time. The margin allows for some normal variation; when a stroke time falls outside the margin, some action is needed to correct the problem causing the increased stroke time, to stop further degradation.

l if a valve operating time requirement exists (e.g. Si flow established within 10 l seconds), the requirement is an upper limit on valve operation. However, when no specific valve requirement is known to exist. then the IST stroke time criteria have no i connection with any required closure for opening) time. !

Since there is no known CIV closure time requirement, the stroke time limits for l

Containment Isolation Valves covered by the IST program are based only on detecting l' valve degradation, not on a CIV closure time requirement.

CONCLUSION #2 The guidance in SRP 6.2.4 and the valve stroke times in the IST program are not sources of i any specific CIV closure time requirements for Point Beach. However, the one-rninute SRP guideline may be useful for assessing valve stroke times for

reasonableness"

] :\ ]

. \

i

, l l

i HEMORANDUM '

TO:

i FROM: j DATE: 10/31/88

SUBJECT:

SRP 6.2.4 1 discussed the question regarding SRP 6.2.4-9 paragraph 5 with an NRC technical reviewer and an assistant director.

A reviewer in the Mechanical Engineering Branch, indicated that he had been I performing reviews of Containment Systems for several years and was not aware of the basis for the one-minute valve closure time guidance in SRP section 6.2.~4.

He considers the one-minute value as general guidance and not an acceptance j criteria except in certain cases. When queried whether the basis for the one- '

minute closure time might be related to an ISI requirement the reviewer was certain that was not the case. In fact he noted personal knowledge of plants with valve closure times of up to 200 seconds and one plant of 240 seconds in their Technical Specifications. He indicated that in conducting his reviews he closely evaluates lines with direct pathways to the environment to assure that closure times for these lines are minimized to mitigate the offsite radiological 1

consequences, as discussed in paragraph (n) on p~ age 6.2.4-6 of the SRP. He also noted that closure times can become a review consideration where ECCS effectiveness could be degraded by a reduction in containment backpressure. In cases where ECCS analysis may be affected, the Reactor Systems Branch would review the analysis and provide input to the containment systems reviewer.

Except in situations where there is an analytical basis for closure times or where there is a direct path to the environment, there is no firm guidance or value that is clearly unacceptable given proper justification.

The question was also directed through an /0 to a Director, who had spent considerable time in the review of Containment Systems. Recollections were that there was possibly some basis for the one minute valve closure in a Technical Information Document (TID), perhaps TID-14844. Nevertheless, based on transport phenomenon and dispersion considerations, as a general rule, if the containment was sealed in on the order of one minute, other elements of the offsite dose calculatkos were generally acceptable.

l These discussions suggest that the one-minute closure time is general guidance I for containment systems unless lines communicate directly with the environment l such as the Containment Purge .or those of sufficient size that could adversely affect ECCS or other accident analysis. Otherwise valve closure times in excess of one-minute which are properly justified could clearly be acceptable as evidenced by precedence. . _ _ _ _ . .

ACTION ITEM STATUS REPORT PAGE 1 4****************************** Responsible Person: 01/23/97

- Trkid: NRC 96EC

Urgency: DONE

- Action Number: 43 Work Priority: 99 i

$d67WG~ /722rf *//

l Activity Pending is: DONE ASSOCIATED WITH A COMMITMENT l ----------TITLE AND TASK DESCRIPTION------------------------------------------

NRC 09/12/96 Enforcement Conference IST: Review all installed instrumentation used in the IST program. (1)

Identify all installed instruments used within the IST program. ,2) ( Review performance of these instruments over the past 3 years. (3) Review the suitability of the installed instrumentation for use in the IST program.

(4) Review all IST data for the past year for adverse trends

DATES-- -- ---------------------------------------------------------

Sourge Record: 11 13 96 ******* Evaluation ********* ****** Correction ** ***

Commitment: 03 31 97 Eval Due: Corr Act Due: 03 31 97 Action Create: 11 14 96 Orig Eval Due: Orig CA Due: 03 31 97 Action Closed: 01 23 97 Eval Done: Corr Act Done:01 22 97

PEOPLE--------------------------------------------------------------

Responsible for Overall Action: NMS Responsible for Current Pending Activity:

Issue Manager:

Initiator:

Punchlist Administrator:

--._------UPDATE--------------------------------------------------------------

(11/18 /96 DPH) Issued purchase requisition to NPTS to provide review of scoping of present IST program. Included in the review: List all inservice tests and the instrumentation used in the test. Trends seen in tests for last 24 months. Trends seen in instrumentation for last 36 months.

Suitability of the instrumentation used in the IST program. Issued report on NPTS findings. NPTS made 17 recommendations for improvements to the present IST program and associated instrumentation. Initiated 17 NUTRK items based on the recommendations and had them assigned to I+C IPE and SE groups. Drafted new NP - NP 7.1.4. Sent copy to SDB and CJN In review and comment. ;

(11/19/96 WAH) Set Work Priority to 27. Initial prioritization. Same as l EWR 96-114.

(12/05/96 DPH) Delivered IST instrumentation review to clerical and I requested that it be inserted into plant file system under IST.

(12/17 NPTS report accomolishing items 1-3 dated 9/28/96 was <

receive /96 d 10DPH96. My review was finished on 10/26/96. 17 NUTRK items were l issued under/1 WR 96-114 IPE and various system !

engineers in site engineering. and assigned Item # to 4 I+C,h whic deals with assessing pump data,tmentwas commi re-assigned to Craig Neuser as item #11 on the PBNP startup list.;

(01/03/97 DPH) Passed to for acceptance of work.

(01/03 Passed to . for Verification.

Purchas/97 WAH) e requisition 1000v m1 was issued to NPTS to provide a review of the scoping of the present IST program. This request was entered in August I of 1996 with a due date of September 30, 1996. Report was received on '

October 1 1996 and review was complete October 25, 1996. NPTS made 17 recommendations for improvements to the IST program and associated instrumentation. 17 M RK items were initiated based on the report and assigned to I+C and various site engineering personnel under EWR 96-114.

The report was put into the plant filing system under IST This satisfies items 1-3. Item number 4 which deals with assessing pump performance data was assigned to - as item #11 on the PBNP startup commitment list. There are no tQrther actions required and this item may be closed. l (01 Returned to - for additional work.

This/07/97 item JAP) can not please closed out to the unit 2 restart list because the list is not enterea into NUTRK as a commitment.

Pleaaa cornlete the IST review as requested. If needed transfer this item to t (01/07/97 WAH) Changed Responsible Person: From (DPH) to (CJN)

i ACTION ITEM STATUS REPORT PAGE 2 01 Changed Responsiblg Group: From (IPE) To (ISE).. Reassigned to Craig /23/97 )

'Neuser for completion of acti^n #4 of the described actions. Other three

' items have been completed by -

(01/08/97 FAF) Changed the Due Date from: << BLANK >> to 03/31/97 '

(01/19/97 CJN) Passed to for acceptance of work.

(01/22/97 PWH Passed to Review of all)IST pump hydraulic datafor

_.._ Verification.

over the past year for advgrse trends has been completes. Several negative trends were identified however, the c9rrective actions have already been completed in all c,ases.

No new action items are needed based on this review. The following paragraphs identify the adverse trend and the corrective action completed.

Safety injection pumps IP-15B and 2P-15A exhibited inconsistent differential pressure measurements. Calibration records indicated a problem with the respective pumps dischar Modifications96-049 (U1) disgharge pressure and 95-050 indicators with a[U2more)ge pressure replaced all ofindicator. the SI pumps reliable indicator. No further action is necessary.

RHR pumps 2P-010A/B differential pressure measurements had been i approximately 10,psid lower since maintenance was done on common flow element 2FE-660 in 1992. Work order 96-03159 revealed the flow element was installed backwards following the 1992 maintenance. The flow element 1 was corrected and differential pressure measurements are again consistent with pre 1992 results. No further action is necessary.

Flow measurements for service water pump P-32E have increased due to the pump being rebuilt. No further action is necessary.

Auxiliary feedwater pumps IP-029, P-38A and P-38B showed a one time decrease in measured pump differential pressure. This step change gan be attributed to a change in test methodology. Differential pressure is now measured at the design flow of eagh respective pump in lieu of pump recirculation. No further action is required.

Component cooling water pumps 2P-011A/B showed a one time decrease in measured pump ditferential pressure. This step change can be attributed to a change in test methodology. Differential pressure is now measured at a pump flow of,3500 2600 gpm. No further action is required. gpm versus the old value of Cable spreading room and control room chill water pumps P-111A/B and P-112A/B had some minor fluctuations of measured pump differential pressure ( 1.5 psid). Although these fluctuations are very small they are being mentioned because they have caused several pumps to be declared inoperable or place on IST increased surveillance testing. These recent occurances were caused by the very small IST acceptance rang not because of the instrumentation The differential pressure of P-111A 8 is 21 psid and P-112A/B is 24.5 psid. Pre and post instrumentation ca ibrations further conclude that the involved instruments are acceptable. No further action is required. '

B9ric acid transfer pump 2P-004A had a decreasing trend for measured differential pressure. This was due to pump degradation. The pump was l rebuilt per WO 96-05180. No further action is required. :

l No other pumps in the IST program exhibited any negative hydraulic performance trends. This action item may be closed out.

(01/23/97 JAP) Passed to ~

~ )r Final Close Out.

Item is complete.

(01/23/97 FAF) PLA Closure of Item.

REFERENCES----------------------------------------------------------

IR 96-003 IR 96-006 EWR 96-108 IR 96-011 WO 96-03159 MR 96-049 -

j MR 96-050

MISCELLANEOUS---------------------- --------------------------------

Originating Agencv: S stem: XX NRC Open Item Number: N C Status: O Related Outages:

Engineering work Type: None Specified

.- 2196 CL H.S IST INSTRUMENTATION REVIEW 1/20/97 NPTS was tasked with the review ofinstrumentation used in the IST program. The fmal report was received on October 1,1996. The scope of the project is as follows.

l SCOPE IDENTIFICATION

. Identify all IST-related procedures

. Identify all in-scope instrumentation

. Document instrument information CALIBRATION IIISTORY

. Run equipment history report from MRLIN

. Document all out-of-calibration incidents and any adverse trends

. Screen IT's for adverse trends ASME APPLICABILITY

. Compare actual instrument range / accuracy to ASME requirements HUMAN FACTORS

. Determine readability ofinstruments Attached is the recommendations from the NPTS report (labeled ITEM A). This report contains all the discussion leading up to the recommendations on pages 11 through 13. My commen's and recommended owners of the action items are noted on the left in red ink. Included in the package is " ATTACHMENT 1" which should be forwarded to I&C for their use in recommendation A (review / update CilAMPS records). Also included in the package is " ATTACHMENT 2" This attachment should be included with each action item along with a copy of" ITEM A" for their guidance.

It i my recommendation that the following action items be generated as child items to EWR 96-114.

ACTION GROUP / DESCRIPTION FROM ITEM "A" ITEM # PERSON 1 I&C Recommendation A 2 SEJ Recommendation B - turbine driven AFW pmp TC's 3 JAS Recommendation B - service water pump ammeters 4 BDO Recommendation B - charging pump oil press. gauges 5 IPE Recommendation C - analyze 1&2 PI-653A&B i

6 I&C Recommendation D - portable instrument accuracy 7 I&C Recommendation E - cal. procedure IRI frequency f""

^

M cHccLd Fle x g l t= d 96-ny cre k W Uzb7

IST INSTRUMENTATION REVIEW 1/20/97 i

l ACTION GROUP / DESCRIPTION FROM ITEM "A" ITEM # PERSON 8 I&C Recommendation F - PI-6354&55 add to procedure-9 JAS Recommendation F - P-32A - P32F ammeters, cal. & CHAMPS id ,

10 BDM Recommendation F - 1&2 F1-3087 4 BDO Recommendation F - charging pmp oil press gauges CHAMPS id 11 SB Recommendation F - SI pmp ammeters, cal & CHAMPS id 12 I&C Recommendation F - PI-5976&77 add to cal. procedure l 13 I&C Recommendation F - TI-665 add to cal. procedure ;

14 IPE Recommendation G & H - evaluate instrumentation suitability 15 I&C Recommendation I, J & K 16 BDO Recommendation L - evaluate full scale range discrepancy FT-128 I 17 JRZ Recommendation L - evaluate full scale range discrepancy FT-619 16 BDO Recommendation M - consider using PPCS in IT-21 vs indicator 17 JRZ Recommendation M - consider using PPCS in IT-22 vs indicator dph/10-26-96 i

i 3

CROSS-MATRIX FOR ENFORCEMENT CONFERENCE COMMITMENT ITEM NUMBER 43 AND ENGINEERING WORK REQUEST NUMBER 96-114 NRC 96EC Action Item EWR 96-114 Number 43 Action Item Recommendation Number A 9 B '

10 B 11 B 12 C 13 D 14 l

E 15 F 12 l F 16 F 17 F 18 F 19 I F 20 -

F 21 G 22 H 22 I 23

J 23 K 23 L 24 L 25 M 24 M 25 John A. Palmer January 22,1997

ID:

FROM:

DATE: 09/28/96

SUBJECT:

IST Instrumentation Review Final Report The review ofIST instrumentation consisted of several main processes including: scope identincation, calibration history review, ASME Section XI test trending, verification ofinstrumentation applicability, and identification of human factors concerns. The following is a synopsis of each of these processes, concluding with recommendations:

1) Scone Identincation The focus of this review was to identify concerns associated with the instrumentation used in the performance of ASME Section XI Pump & Valve Testing. Therefore, the objective of the scope identification was to determine which instruments (installed and portable) are being used in the ASME Section XI in-Service Tests (ITs). The criteria for inclusion of the instrumentation in the scope was that it is used to determine a quantitative parameter and the data from it is recorded in the IT. Thus, if a prerequisite to the IT states that "RCS pressure must be greater than 500s", the RCS pressure instrumentation would not be included in the scope of this review. A further breakdown of the scope was performed in order to identify the instrumentation which is used to verify the various pump & valve ASME requirements (suction' differential pressure, flow rate, speed, vibration, valve timing). Thus, the installed instrumentation scope consists of two types ofIST instrumentation: ASME-Required Instrun entation and Supporting Instrumentation.

Each ASME Section XI IT was reviewed line-by-line and the instrumentation identined was documented (reference attachment 1). If the indicator identined is a part of an instrumentation loop, the portions of the associated loop which are applicable for the indication were identi0ed and included in the scope. Also, data from previous ASME Section XI ITs was reviewed to identify the portable test equipment used in the tests. The following information was identiGed for the in-scope instrumentation and documented in Attachments 2,3:

Instrument ID l

Instrument loop designation (if applicable)

. ASME required? (Yes,No) e Calibration procedure / frequency

. Reference value (only for ASME-required instruments)

Required instrument full-scale range (only for ASME-required instruments)

Actual instrument full-scale range e Required instrument accuracy (only for ASME-required instruments)

,;

Actual instrument accuracy a Loop accuracy (if applicable)

Additionally, the following information was identiGed and documented in Attachment 4:

. Actual instrument accuracy

ASME required? (Yes/No)

. Indicator readability (only for ASME-required instruments)

Indicator scale divisions (only for ASME-required instruments)

Instrument ID e Manufacturer /Model#

Attachment 5 identines the ASME Section XI Pump IT's and the associated ASME required instrumentation.

I

1 j

The following sources were utilized ta acct.rately identify the above information:

CHAMPS database Instrument Calibration Procedures (ICP's) e Instrument vendor manuals

Plant draw ings e Plant walk-downs It should be noted that some of the instrumentation information was not identi6ed during the review process. The designation "UNK" is used in the attachments to denote this. It will be recommended that the CHAMPS database equipment record for each of the IST instruments be reviewed / updated to ensure that it is complete and accurate. Additionally, there were no CHAMPS database records identi6ed for the following components:

PB1,2 Turbine Driven Aux Feedwater Pump turbine & pump bearing temperature thermocouples

. Service Water Pump Motor Ammetera i

e PBl/2 Charging Pump Oil Pressure gauges It will be recommended to assign component ID's to these components and generate the CHAMPS database records for them.

11) Calibration History An equipment history report was run from the Maintenance Rule / License Renewal program (MRLIN) for all of the in-scope plant-installed instrumentation. A manual search of the CH AMPS Equipment History database was performed for the portable instrumentation. The scope of this search includes failure incidents which were identified in the previous 36 months. All out-of-calibration (OOC) incidents were documented and the As-Found data was recorded in order to identify any adverse trends (reference attachments 6,7). An instrument was identified as potentially exhibiting an adverse trend ifit met one or both of the following criteria:

e instrument had three or more failure incidents of any kind e Instrument had two consecutive OOC conditions with the drift in the same direction AND was OOC in the last calibration check The following is a discussion of tLe results of this calibration history search:

A) ASME-Recuired instrumentation The following potential concerns were identi6ed and should be investigated further:

1) Unit 2 Boric Acid Transfer Pumos Discharge Pressure Indicatm (PI-00108)

Three OOC incidents were identified for this instrument over the past 3 years.

2) P-12A SFP Cooling Pumo Suction Pressure Indicator (PI-00658A)

Two consecutive OOC LOW incidents were identified for this instrument including the last calibration check. The instrument was found to be 0.2 - 0.3 psi LOW in 3/95 and 0.3 - 0.5 psi LOW in 3/96.

2

3) St Pumn Dischefressure Indic; den.(PB1,2 P!-00913 A, B) l Several failure incidents were identified for these instruments as follows

l

16 Out-of-Calibration incidents e 2 " Gauge Failure" incidents l Two Condition Reports were identified associated with failures of these indicators (reference CR 96-453,96-756) and EWR 96-107 was initiated to evaluate replacing the instrumen:s. The recommendation from the EWR evaluation is to replace the existing local pressure gauges with digital (Red Lion) displays.

4) Unit 2 P-014B CS Pumn Suction Pressure Indicator (PI-00933D)

Two OOC incidents and two " Gauge Failure" incidents were identified for this instrument over the past 3 years.

5) Unit 2 RC Loon A Intermediate Leg Wide Range Pressure Transminer (PT-00420A)

Four OOC incidents were identified for this instrument over the past 3 years.

No PM program tasks were identified for the following ASME-Required instruments:

PB0 F1-03905 PB0 FI-03928 PB0 F1-03929 PB0 Pl.03973A PB0 PI-03973B PB0 el-03974A PB0 PI-039748 A calibration check task with a I A2 frequency was recommended for PI-03973 A, PI-03973B, PI-03974 A, and PI-03974B in the DISPLAYS Component Maintenance Program (CMP 6.5).

It will be recommended that calibration check tasks with a IRI frequency (every refueling outage) be added for F1-03905, FI-03928, and F1-03929.

The CH AMPS database lists "lCP-06.069" and "lCP-06.070" as procedures for F1-03928 and F1-03929 respectively. These procedures could not be located and do not show up in the ICP index. Therefore, these procedure references are assumed to be

,; invalid.

It should be noted that each of these instruments had calibration stickers on them with the following calibration dates:

PB0 F;-03905 6/21/94 PB0 Fl.03928 6/21/94 PB0 Fl.03929 6/21/94 PB0 PI-03973A 2/26/94 PB0 Pl.03973B 2/26/94 PB0 Pl.03974A 2/26/94 PB0 PI-03974B 2/26/94 l

3

l B) Suggortine Instrumentation For the Supporting Instrumentation, all out-of-calibration (OOC) incidents were documented (reference attachment 7). The following potential concerns were identined and should be l

l investigated further:

l l l} SI Accumulator Lesel Instruments (PBI,2 LC/LT-00934,935,938,939)

Several failure incidents were identified for these instruments as follows:

l e 9 "Subcomponent Part Failure" incidents

= 8 " Air in Sensing Line" incidents e 6 "Out-of-Calibration" incidents I

e 2 " Instrument Failure" incidents Several Condition Reports associated with failures of the St Accumulator Level instrumentation (reference CR 94-175, CR 94-373, CR 95-296, CR 95-307 CR 95-316) have been previously identided during the generation of the TRANSDUCERS CMP 8.6). The main concerns identided have been (1) power supply is undersized and (2) the microprocessor loses bits which cause indication spikes and spurious level alarms. As a l result of these concerns, EWR 95-010 hu been initiated recommending replacement of l this instrumentation with Rosemount 305 lC Smart D/P Transmitters and digital l

indicating controllers.

2) Unit 2 P-015B Si Pumn Discharce Flow Transmitter FT-00924 I I

Four OOC incidents were identided for this instrument over the past 3 years. j

3) Unit 2 P-029 AFP Pumo Discharee Flow Transmitter FT-04002 3 OOC incidents were identiGed for this instrument over the past 3 years.

No PM program tasks were identided for the following IST support instruments:

PB0 PI-06354B PB0 PI-06354D PB0 PI-06355B PB0 PI-06355D "

PB0 LE-03992A PB0 LE-03992B

PB0 LIT-03992A PB0 LIT-03992B PB0 P-032A-M Ammeter (No CHAMPS ID)

PB0 P-0328-M Ammeter (No CH AMPS ID)

PB0 P-032C-M Ammeter (No CHAMPS ID)

PB0 P-032D-M Ammeter (No CHAMPS ID)

PB0 P-032E-M Ammeter (No CHAMPS ID)

PB0 P 032F-M Ammeter (No CHAMPS ID)

PB1 F1-03087 PB2 F1-03087 PBl P-002A Oil Pressure Gauge (No CH AMPS ID)

PB1 P-002B Oil Pressure Gauge (No CilAMPS ID)

PB1 P-002C Oil Pressure Gauge (No CH AMPS ID) l PB2 P-002A Oil Pressure Gauge (No CH AMPS ID) l PB2 P-002B Oil Pressure Gauge (No CH AMPS ID) l PB2 P-002C Oil Pressure Gauge (No CilAMPS ID)

PBI P-015A-M-AMI PBl P-015B-M-AMI 4

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

l PB2 P-015A-M-AMI PB2 P-015B-M AMI PBI PI-05976 I PBl PI-05977 l PB2 PI-05976 PB2 PI-05977 l

l PB0 TI-00665 A calibration check task with a IRI (every refueling outage) was recommended for LE-03992A, B in the TRANSDUCERS Component Maintenance Program (CMP 8.6).

A calibration check task with a IM2 (every 18 months) was recommended for LIT-03992A, B in l the TRANSMITTERS Component Maintenance Program (CMP 6.1).

l It will be recommended that calibration check tasks with a IRI frequency be added for the ,

following components ,

l PB0 PI-06354B PB0 PI-06354D PB0 PI-06355B PB0 PI-06355D PB0 P-032A-M Ammeter (No CHAMPS ID)

PB0 P-032B-M Ammeter (No CilAMPS ID)

PB0 P-032C-M Ammeter (No CHAMPS ID)

PB0 P-032D-M Ammeter (No CHAMPS ID)

PB0 P-032E-M Ammeter (No CHAMPS ID)

PB0 P-032F-M Ammeter (No CHAMPS ID)

Pal F1-03087 PB2 F1-03087 PB1 P-002A Oil Pressure Gauge (No CH AMPS ID)

PBl P-002B Oil Pressure Gauge (No CHAMPS ID)

PBI P-002C Oil Pressure Gauge (No CHAMPS ID)

PB2 P-002A Oil Pressure Gauge (No CHAMPS ID)

PB2 P-002B Oil Pressure Gauge (No CHAMPS ID)

PB2 P-002C Oil Pressure Gauge (No CH AMPS ID)

PBI P-015A M AMI PBl P-015B-M-AMI PB2 P-015A-M-AMI PB2 P-015B-M-AMI PB1 PI-05976 PBl PI-05977 PB2 PI-05976 PB2 PI-05977 PB0 TI-00665 The Cil AMPS database lists "lCP-06.069" and "lCP-06.070" as procedures for PI-06354B, D and PI-06355B, D respectively. These procedures could not be located and do not show up in the ICP index Therefore, these procedure references are assumed to be invalid.

C) Portable Inst umentation No multiple failure incidents were identified for the in-scope por.able instrumentation.

5

l I

til) ASME Segtion XI Test Trends i Data recorded for the ASME Pump ITs was reviewed to identify potential adverse trends associated with the ASME Required instrumentation. The As Found data for the past 24 months for this instrumentation was imported from Paradox tables and recorded in Excel files. Graphs were then generated in an effort to identify any potential adverse instrumentation trends (reference attachment 8). The following is a discussion of the instrument trends for each IT: 1 e IT - 1 (Unit 1 Safety Iniection Pum;n)

A potential adverse trend is indicated for P-015B St Pump Discharge Pressure Indicator PI-00913B. Reference Section ll.A.I above for discussion of this instrument.

NOTES: j IT l gives the component ID "F1-00659" Per the CHAMPS database, the component ID is " FIT-00659" l l

= IT - 2 (Unit 2 Safety IniectigaPumns) j l

A potential adverse trend is indicated for P-015 A Si Pump Discharge Pressure Indicator PI-00913A. Reference Section ll.A.I abose for discussion of this instrument. ,

NOTES:

IT-2 gives the component ID "Fl.00659" Per the CH AMPS database, the component ID is " FIT- l 00659"

. LI_ 3 (Unit i Residual Heat Removal Pumns)

A potential concern is indicated for P-010A RHR Pump Suction Pressure Indicator PI-00653 A.

Afier tracking lock-step with P-010B RHR Pump Suction Pressure Indicator PI-00653B for six consecutive quarterly ITs, PI-00653 A's indicated pressure decreased approximately 8% from 4/22/96 to 7/1/96 while PI-006538's indicated pressure increased less than 1%. I believe this indicates a potential adverse drift in PI-00653 A and this indicator should be checked out prior to l the next performance ofIT-3. l l

I NOTES: 1 (1) RHR Pump now rate is adjusted during the IT and not recorded. Thus, FIT-00660 is not trended.

J (2) IT-3 gives the component ID "Fl 00660" Per the CHAMPS database, the component ID is " FIT-00660" e IT- 4 (Unit 2 Residual Heat Removal Pumns)

No adverse trends are indicated for the Unit 2 RHR Pump IST instrumentation. l NOTES:

(1) RHR Pump How rate is adjusted during the IT and not recorded. Thus, FIT-00660 is not trended.

(2) IT-4 gives the component ID "F1-00660" Per the CHAMPS database, the component ID is " FIT-00660" l

6

e IT - 5 (Unit 1 Containment Snrav Pumns) I One data point (12/4/94) for P-014 A CS Pump Suction Pressure Indicator PI-00933C was found to be signincantly higher than expected. However, the indicator has not shown any additional abnormalities in the six performances ofIT-5 since that time and thus no adverse trends are l currently indicated.

i l

i NOTES:

(!) CS Pump How rate is adjusted during the IT and not recorded. Thus, FIT-00661 is not trended. 1 (2) IT-5 gives the component ID "F1-00661" Per the CH AMPS database, the component l ID is " FIT-00661" e IT - 6 (Unit 2 Containment Sorav Pumos)

One data point (11/28/95) for P-014B CS Pump Suction Pressure Indicator PI-00933D was found to be significantly higher than expected. A work order was written for this incident and it was determined that the indicator was out-of-calibration and unable to be re-calibrated (see previous section II.A.3 for cal history discussion). The gauge was replaced and the indicator has read satisfactorily during the two performances ofIT-6 since that time. No adverse trends are currently indicated.

NOTES:

l (1) CS Pump dow rate is adjusted during the IT and not recorded. Thus, FIT-00661 is not trended.

(2) IT-6 gives the component ID "F1-0066 l" Per the CHAMPS database, the component ID is " FIT-00661" e IT - 7 (Service Water Pumns)

No instrumentation trends were generated for the SW Pump IST instrumentation (reference NOTES below).

NOTES: l (1) SW pumps discharge pressure is adjusted during the IT. Thus, P!-02815, PI-02846, PI-02847, PI-02848, PI-02849, PI-02850 are not trended.

(2) Forebay Level varies considerably between tests. Thus, Forebay ! : vel instrumentation is not trended.

J (3) Not enough SW pump flow rate (header flow) instrumentation (FI-04459A, B) data points identified to trend.

(4) EWR 96-168 identined a concern with the reliability of the SW Pump Discharge Pressure gauges and the inaccuracies associated with reading the SW Header Flow Rate indicators (indicators " jump around"). The discharge pressure gauges are planned to be replaced with better quality (and more accurate) gauges. The Dow rate indicators will be upgraded to increase the damping to make the indicators easier to obtain an accurate reading.

l 7

l o IT- 8A (Unit 1 Turbine Driven Aux Feedwater Pumo)

No adverse trends are indicated for the Unit i Turbine Driven Aux Feedwater Pump IST I instrumentation.

NOTES:

(1) P-029 suction pressure (PI-04013A) varies with CST level / temp and thus is not trended.

(2) IT-8A gives the component ID "F1-04049", Per the CHAMPS database, the component ID is " FIT-04049" e

IT - 9A (Unit 2 Turbine Driven Aux Feedwater P1Unn)

No adverse trends are indicated for the Unit 2 Turbine Driven Aux Feedwater Pump IST instrumentation.

NOTES:

i (1) P-029 suction pressure (PI-04013 A) varies with CST level / temp and thus is not trended. I (2) IT-9A gives the component ID "F1-04049" Per the CHAMPS database, the component ID is " FIT-04049".

. IT- 10 (Motor Driven Aux Feedwater Pumns)

No ads erse trends are indicated for the Motor Driven Aux Feedwater Pump IST instrumentation.

]

NOTES:

(1) Not enough AFP flow rate instrumentation (FIT-04050A, B) data points identified l to trend.

(5) IT 10 gives the component ID's "F1-04050A" and "F1-04050B" Per the CH AMPS database, the component ID's are " FIT-04050A" and FIT-04050B"

IT - 11 (SFP Cooling Pumes)

The trend graphs for the SFP Cooling Pump Discharge Pressure Indicators Pl-00631 A, B reflect a fairly erratic pattern of data points and it is unclear whether any adverse trends are indicated for these gauges. Considering the minimal failure history identified for these gauges (one out-of-calibration incident identified), it is unlikely that these graphs reflect an adverse trend.

It should be noted that the trend graphs for the suction pressure indicators (PI-00658A, B), taken

.: separately, also vary considerably. However, when compared to each other it can be seen that they track each other fairly well. Since these gauges measure the pressure in essentially the same line, this make> sense and thus no adverse trends are indicated.

NOTES:

SFP Cooling Pump llow rate is adjusted during the IT. Thus, F1-00652 is not trended.

IT - 12 (Unit 1 Comnonent Cooling Water Pumns)

No adverse trends are indicated for the Unit 1 Component Cooling Water Pumps IST instrumentation.

NOTES:

Component Cooling Pump flow rate is adjusted during the IT. Thus, F1-00619 is not trended.

8

e IT- 13 (Unit 2 Comconent Cooling Water Pumos)

A potential adverse trend is indicated for the Unit 2 Component Cooling Water Pumps Suction Pressure Indicators PI-00692A, B. These indicators, due to their location, should indicate approximately the same pressure. As indicated on the graphs, this was the case for the tests run from 9/94 to 2/96 where the gauges remained within an average of 4% of each other. However, during the performance of the 2/14/96 test, these indicators indicated approximately 15% different .

and on the performance of the 6/2/96 test, these indicators indicated approximately 9% differe : l This may indicate a drift concern for either one, or both, of these gauges. It is recommended that these gauges be checked prior to the next performance ofIT-13.

NOTES:

Component Cooling Pump flow rate is adjusted during the IT. Thus, FI-00619 is not trended.

IT - 14 (Fuel Oil Transfer Pumm)

No adverse trends are indicated for the Fuel Oil Transfer Pumps IST instrumentation.

NOTES:

(1) Not enough DG Fuel Oil Transfer Pump P-206A, P-207A flow rate instrumentation (F1-03905) data points identified to trend.

(2) Not enough DG Fuel Oil Transfer Pump P-206A, P-207A discharge pressure instrumentation (PI-03973A, PI-03974A) data points identitled to trend.

[T- 15 (Chilled Water Recire Pumns) .

I No adverse trends are indicated for the Chilled Water Recire Pumps IST instrumentation.

e IT - 17 (Unit i Boric Acid Transfer Pumos)

One data point (6/15/96) was identified as being considerably higher than average for Unit i Boric Acid Transfer Pumps Suction Pressure Indicator PI-00184. The gauge read satisfactorily on the next (and last) performance ofIT-17. No adverse trends are currently indicated.

Two consecutive data points (3/16/96,5/3/96) were considerably lower than average for Unit i Boric Acid Transfer Pumps Discharge Pressure Indicator PI-00108. A work order was written for this condition (9604948) and the gauge was found to be out-of-calibration low and failed.

The gauge was replaced and has indicated satisfa:torily for the three performances ofIT-17

.: since. No adverse trends are currently indicated.

I NOTES: 1 1

(1) Boric Acid Transfer Pump flow rate is adjusted during the IT. Thus, FT-00185 is not ;

trended.

l (2) PI-00108 and PI-00184 are currently calibrated in ICP 6.41 which is performed every 3 l years (3 A2). It will be recommended that the calibration check frequency of these gauges be changed to annually (1 A2) which would be in keeping with the other IST l instrumentation.

l 9

l

I e IT - 18 (Unit 2 Boric Acid Transfer Pumns)

Fairly erratic data points were identified for both the Unit 2 Boric Acid Transfer Pumps Discharge and Suction Pressure Indicators PI-00108 and PI-00184.

l PI-00108 has been previously identified as having an adverse failure history. A recommendation I will be made to evaluate this instrument, in light of the failure history data identified in the IST instrumentation review, to determine the appropriate course of action. This gatge is currently calibrated in ICP 6.41 which is performed every 3 years (3A2). It will be recommended that the {

calibration check frequency of this gauge be changed to annually (I A2) which would be in j keeping with the other IST instrumentation. '

PI-00184 was identified in Condition Report 96-485 as not having been calibrated for approximately 31/2 years. It was subsequently found to be OOC (reference WO 9607883).

Action I of the CR calls for an evaluating the possibility of using Perma-Cal gauges within the Boric Acid Transfer system. This gauge is currently calibrated in ICP 6.41 which is performed every 3 years (3 A2). It will be recommended that the calibration check frequency of this gauge be changed to annually (1 A2) which would be in keeping with the other IST instrumentation. l NOTES:

Boric Acid Transfer Pump flow rate is adjusted during the IT. Thus, FT-00185 is not trended.

. IT - 21 (Unir 1 Chargine Pumns)

No adverse trends are indicated for the Unit 1 Charging Pumps IST instrumentation.

. IT - 22 (Unit 2 Chargine Pumns)

No adverse trends are indicated for the Unit 2 Charging Pumps IST instrumentation.

IV) Instrumentation Annlicability I

A comparison was made between the actual accuracy of the ASME-Required instrumentation and the accuracy requirements of ASME Section XI. No discrepancies were noted. I A comparison was made between the actual full-scale range of the ASME-Required indicators and the range requirements of ASME Section XI. The following potential discrepancies were noted and should be investigated further:

I J (1) HX-2 Regenerative Heat Exchanger inlet Flow Indicators (PBl/2 F1-00128) l The most conservative (lowest) values of reference flow for these indicators are 42.8 gpm for Unit I (IP-002B) and 42 gpm for Unit 2 (2P-002C). This gives the maximum allowed values of full-scale range (3X reference) for the mdicators of 128.4 gpm for j Unit I and 126 gpm for Unit 2. The actual full-scale range for these indicators is 140 gpm. Therefore, these indicators do not meet the ASME requirement for full-scale range. j 10

(2) HX 12A!B Comnonent Cooling Heat Exchan-er Return Flow Indicators (PBl/2 fi-00619)

The most conservative (lower) w.im oficicicece flow for these indicators cre 2583 gpm for Unit I (IP-011B) and 2600 gpm for Unit 2 (2P-011B). This gises the maximum allowed values of full-scale range (3X reference) for the indicators of 7749 gpm for Unit I and 7800 gpm for Unit 2. The actual full-scale range for these indicators is 8000 gpm. Therefore, these indicators do not meet the ASME requirement for full-scale range.

V) I&C Human Factors The instrumentation full-scale range and scale divisions was documented for each of the ASME-Required indicators in order to determine the " readability" of the instrument. It is assumed that the indicator can be read accurately to one-half of the smallest division. A " readability accuracy" was calculated for each ASME Required indicator simply by dividing the full-scale range of the instrument into one-half of the smallest division / increment. If this " readability accuracy" was reasonable, compared to the indicators instrument accuracy, then it was considered acceptable. No adverse conditions were noted.

In addition to the instrument full-scale range and scale divisions, the physical location and instrument size was noted in order to determine if any conditions exist which may hamper the accurate reading' recording of the required information. No adverse conditions were noted.

The following instrumentation loops contain control room indicators which are used to verify ASME Section XI Pump IST requirements:

. HX-2 Regenerative Heat Exchanger inlet Flow (PBl/2 F1-00128) e RC Loop A Intermediate Leg Wide Range Pressure (PBl/2 PT-00420A)

The HX-2 Regenerative Heat Exchanger inlet Flow instrumentation loop using the control room indicator gives a loop accuracy of approximately 1.601% (indicator accuracy of 1.5%, transmitter accuracy of 0.25%

and signal conditioner accuracy of 0.5%). The RC Loop A Intermediate Leg Wide Range Pressure instrumentation loop using the control room indicator gises a loop accuracy of approximately 1.871%

(indicator accuracy of 1.5%, transmitter accuracy of 1.0% and signal conditioner accuracy of 0.5%). Both of these loops output to computer points which have an accuracy of approximately 0.025%. The HX-2 Regenerative Heat Exchanger inlet Flow instrumentation loop consisting of the transmitter, signal conditioner and computer point has an overall accuracy of 0.560% which is nearly three times more accurate than the indicator loop. The RC Loop A Intermediate Leg Wide Range Pressure instrumentation loop consisting of the transmitter, signal conditioner and computer point has an overall accuracy of 1.118%. In order to take advantage of the improved accuracy, it will be recommended to consider the use of the computer point in lieu of the control room indicators for these loops in their respective ITs.

VI) Recommendations A. Review / update CH AMPS database equipment records for each of the IST instruments to ensure that they are complete and accurate.

B. Assign component ID's and generate the CHAMPS database records for the following components:

. PBl 2 Turbine Driven Aux Feedwater Pump turbine & pump bearing temperature thermocouples e Service Water Pump Motor Ammeters e PBl/2 Charging Pump Oil Pressure gauges C. Identify the accuracy of ASME-Required instruments PB1/2 Pl.00653 A/B (need manufacturer /modet#) to determine if they meet ASME requirements (gauges not walked down; l they are located in a locked high radiation area). j q

l 11 j

i D. Identify the accuracy of the following ASME-Required portable instrumentation to driermine if

. they meet ASME requirements (accuracy not identified during review): l e Palomar Technology Model 6101 Microlog Vibration Data Collector

. Cronus & Cole-Parmer Stopwatches E. Add calibration check tasks with a IRI frequency (every refueling outage) for the following components:

PB0 F1-03905 PB0 F1-03928 l PB0 F1-03929 F. Add calibration check tasks with a IRl frequency (every refueling outage) for the following components:

PB0 PI-06354B 1 PB0 PI-06354D PB0 PI-06355B PB0 PI-06355D l

PB0 P-032A-M Ammeter (No CHAMPS ID)

PB0 P-0328-M Ammeter (No CHAMPS ID) l PB0 P-032C-M Ammeter (No CHAMPS ID) l 1

PB0 P-032D-M Ammeter (No CHAMPS ID)

PB0 P-032E-M Ammeter (No CHAMPS ID)

PB0 P-032F-M Ammeter (No CHAMPS ID) ,

PBl F1-03087 !

PB2 FI-03087 PBI P-002A Oil Pressure Gauge (No CHAMPS ID) l PBl P-002B Oil Pressure Gauge (No CHAMPS ID) ,

PBl P-002C Oil Pressure Gauge (No CHAMPS ID) '

PB2 P-002A Oil Pressure Gauge (No CHAMPS ID) i PB2 P-002B Oil Pressure Gauge (No CHA'MPS ID) l PB2 P-002C Oil Pressure Gauge (No CHAMPS ID)

PBl P-015A-M-AMI PB1 P-015B-M-AMI PB2 P-015A-M-AMI PB2 P-015B-M-AMI PBl PI-05976 PBl PI-05977

PB2 PI-05976 PB2 PI-05977 PB0 TI-00665 l G. Evaluate the following ASME-Required Instrumentation, in light of the failure history data identified in the IST instrumentation review, to determine the appropriate course of action

e Unit 2 Boric Acid Transfer Pumps Discharge Pressure Indicator PI-00108 l

e P-12A SFP Cooling Pump Suction Pressure Indicator PI-00658A e Unit 2 P-014B CS Pump Suction Pressure Indicator PI-00933D e Unit 2 RC Loop A Irtermediate Leg Wide Range Pressure Transmitter PT-00420A 12

ATTACllMENT 1 IST Instrumentation & Associated IT Unit CampID Loop IT PB0 DPIS-02936 N/A 12,13 PB0 DPiS-02937 N/A 12,13 PHO DPIS-02938 N/A 12,13 PB0 Ell-03510 3510 7

)

PB0 F1-00636 N/A 530, 530A, 5308,535,535 A, 535 B I PB0 Fi-00652 N/A II I PB0 F1-03905 N/A 14 PB0 F1-03928 N/A 14 PB0 F1-03929 N/A 14 PB0 F1-04007 4007 10,290,295 PB0 F1-04014 4014 10,290,295 a

PB0 F1-04459A N/A 7 PB0 F1-044598 N/A 7 PB0 F1-04666 N'A 15 l PB0 F1-04667 N/A 15 l

PB0 FIT-04050A N/A 10,290,295 PHO FIT-040508 N/A I0,290,295 PB0 FIT-04459A N/A 7 PB0 FIT-04459B N/A 7 PB0 FM-04007A 4007 10,290,295 PB0 FM-04007B 4007 10,290,295 PB0 FM-04014 A 4014 10,290,295 PB0 FM-04014 B 4014 10,290,295 PHO FT-04007 4007 10,290,295 PB0 FT-04014 4014 10,290,295 PB0 G-01 API-l N/A 100 PB0 G A PI-2 N/A 100 PB0 G-02-A Pl- 1 N/A 100 PB0 G-02-APl-2 N/A 100 PB0 LE-03992A 3992A 14 PB0 LE-03992B 39928 14 PB0 LI-00171 ,

171 17,18 PB0 LI-04038 4038 290,295 PB0 LI-04039 4039 290,295 PB0 LIT-03992A 3992A 14 PB0 LIT-03992B 39928 14 PB0 LM-00171 171 17,18 j PB0 LM-04038- 1 4038 290,295 PB0 LM-04039-1 4039 290,295 PB0 LT 00171 171 17, 18 PB0 LT-04038 4038 290,295

~

PB0 LT-04039 4039 290,295 _

PB0 P-032A-M Ammeter N/A 7 PB0 P-032B-M Ammeter N/A 7 PB0 P-032C-M Ammeter N/A 7 PB0 P-032D-M Ammeter N/A 7 1

J -

i PB0 P-032E-M Ammeter N/A 7 PB0 P-032F-M Ammeter N/A 7 PB0 P-038A Inboard Pump Bearing Temp TC 2000 8,8A,10 PB0 P-038A Outboard Pump Bening Temp TC 2000 8,8A 10 PB0 P-038B Inboard Pump Searing Temp TC 2000 8,8A,10 PB0 P-038B Outboard Pump Bearing Temp TC 2000 8. 8A,10 PB0 PI-0063 i A N/A Ii PB0 PI-00631B N/A i1 PB0 PI-0065i N/A 530, 530A, 530B, 535, 535 A, 535 B PB0 PI-00658A N/A II PB0 PI-00658B N/A 11 j PB0 PI-02815 N/A 7 j

PB0 PI-02844 2844 7 ;

PB0 PI-02845 2845 7 PB0 PI-02846 N/A 7 PB0 Pl-02847 N/A 7

{ PB0 PI-02848 N/A 7 PB0 PI-02849 N/A 7

} PB0 PI-02850 N/A 7 l PB0 PI-03973A N/A 14 PB0 PI-03973B N/A 14 1

PB0 Pl-03974A N/A 14 PB0 Pl-03974 B N/A 14 PB0 Pl.04010A N/A 10,290,295 PB0 PI-040II N/A 290,295 PB0 PI-04012 4012 10 j PB0 PI-04017A N/A 10,290,295 PB0 PI-04018 N/A 290,295 PB0 Pl-04019 4019 10 PB0 PI-04741 N/A 15 PB0 PI-04742 N/A 15 PB0 PI-04743 N/A 15 !

. PB0 PI-04744 N/A 15 PB0 P!-04745 N/A 15 i 'PB0 PI-04746 N/A 15 PB0 PI-04747 N/A 15 PB0 PI-04748 N/A 15 -

PB0 PI-06354B N/A 100 i PB0 PI-06354D N/A 100 PB0 PI-063558 N/A 100 PB0 PI-06355 D N/A 100 PB0 PM-02844- 1 2844 7 PB0 PM-02845-1 2845 7 PB0 PT-02844 2844 7

PB0 PT-02845 2845 7 PB0 PT-04012 4012 10 l PB0 PT-04019 4019 10

. PB0 T3510 (PPCS) 3510 7 PB0 TI-00633A N/A 11 PB0 TI-00633 B N/A ii I

4

= 2 i

l PBL I M65 N/A 11 PB0 __

+045 N/A 8A,9A 10,290,295 PB0 T104046 N/A 8, 9A 10,290,295 PB1 E/1-03598 3598 7 )

PBl F619(PPCS) 619 12 PBi F1-00115 N/A 21 ;

PBl F1-00l l6 N/A 21 )

PSI Fl.00128 128 21 PBl Fl.00619 619 12 Pal F1-00626 626 3 A, 750 PBl F1-00924 924 760 PBI F1-00925 925 760 PBl F1-00928 928 3 A, 750 PBI F1-00930 930 5 PBI F1-03087 N/A i10 PBI F1-04002 4002 8A,290 PBl F1-04036 4036 8 A, 9 A,10, 290, 295 PBI F1-04037 4037 8 A, 9A,10, 290, 295

~ PBI FIT-00659 N/A 1,520A PBI FIT-00660 N/A 3, 520A PBl FIT-00661 N/A 5 PBl FIT-00930 930 s PBI FIT-04049 N/A 8,8A,290 PB1 FM-00128 128 21 PB1 FM-00626 626 3 A,750 PBI FM-00924-2 924 760 PBl FM-00925-2 925 760 PBI FM-00928-2 928 3 A, 750 PB1 FM-04002A 4002 8 A,290 PBI FM-040028 4002 8A,290 PBI FM-04036A 4036 8 A, 9 A,10, 290, 295 PBl FM-04036B 4036 8A, 9A,10. 290,295 PB1 FM-04037A 4037 8 A, 9 A,10, 290. 295 PB1 FM-04037B 4037 8 A, 9A,10, 290, 295 PB1 FT-00128 _

128 21 PBl FT-00185 N/A 17,730

~

PBl FT-00619 619 12 PB1 FT-00626 626 3 A, 750 PB1 FT-00924 924 760 l

PBI FT-00925 925 760 '

PB1 FT-00928 928 3 A,750 PBI FT-04002 4002 8A,290 l PB1 FT-04036 4036 8 A, 9 A,10, 290, 295 PBl FT-04037 4037 8 A, 9 A,10, 290, 295 PBl L3598(PPCS) 3598 7

, PBI LI-00172 172 17 PBI LI-00934 934 1,520A PBI Li-00935A 935 1 4

PBI LI-00938 938 1,520A PBI LI-00939A 939 1 3

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

PBl LI-00972 972 760 PBl LM-00172 172 17 PBI LM-00972-1 972 760 PBl LT-00172 172 17 PBl LT 00972 972 760 PBI LT-03598 3598 7 PB1 LT/LC-00934 934 i PBI LT/LC-00935 935 1 PBI LT/LC-00938 938 i PBl LT/LC-00939 939 i PBl P-002A Oil Press Gauge N/A 21 PBi P-w2B Oil Press Gauge N/A 21 PBl P-002C Oil Press Gauge N/A 21 PBI P-015 A-M- AM I N/A 1,760 PB1 P-015 B-M-AM 1 N/A 1,760 PBI P-029 Inboard Pump Bearing Temp TC 2000 8, 8 A,10 PBl P-029 Inboard Turbir.e Bearing Temp TC 2000 8. 8A,10 i PBI P-029 Outboard Pump Bearing Temp TC 2000 8, 8 A,10 PBI P-029 Outboard Turbine Bearing Temp TC 2000 8, 8 A,10 PB1 P2289(PPCS) 2289 300 ,

PB1 P2290 (PPCS) 2290 300 PBI PI-00108 N/A 17 PB1 PI-00139 139 21,730 PBl PI-00184 N/A 17 PB1 PI-00420A 420 21 PB1 PI-00468 468 8 A, 9A,10, 90, 290, 295 PB1 PI-00478 478 8 A, 9 A,10, 90, 290, 295 PBl PI-00617A N/A 12 PB1 PI-00617B N/A 12 PBl PI-00628 625 520A, 530, 530A PBl PI-00629 629 520A,530,530B PBI PI-00653A N/A 3, 40, 520A PBl PI-00653B N/A 3, 40, 520A PBl PI-00655A N/A 3 PB1 PI-00655 B N/A 3 PBl Pl.00692A N/A 12 PBl Pl-006928 N/A 12 PBl PI-00913 A N/A 1

)

PB1 PI-00913 B N/A 1 l PBI PI-00922 922 $20A,520B,530B,760 PBl PI-00923 923 530A,760 PBl PI-00933A N/A 5 PBl PI-00933B N/A 5 PB1 PI-00933C N/A 5 PBI PI-00933D N/A 5 PB1 PI-00974 N/A 1,760 PBI PI-04004 N/A 290 PBl Pl.04005 4005 8,8A PB1 PI-04013 A N/A 8, 8 A, 290 l PBl PI-04458 N/A 8, 8 A i

l l

PB1 PI-05976 N/A 280,280A PB1 PI-05977 N/A 280,280A PB1 PM-00420A-1 420 21 PB1 PM-00468A 468 8 A, 9 A,10, 90, 290, 295 PBI PM-00468B 468 8A,9A 10,90,290,295 PBI PM-00478A 478 8 A, 9A,10, 90, 290, 295 PBl PM-00478B 478 8 A, 9 A,10, 90, 290, 295 PB1 PT-00139 139 21,730 PB1 PT-00420A 420 21 PBi PT-00468 468 8 A, 9 A,10, 90, 290, 295 PB1 PT-00478 478 C A, 9 A,10. 90, 290, 295 PB1 PT-00628 628 520A,530,530A PBl PF-00629 629 520A,530,530B PBl PT-00922 922 520A,5208,530B,760 PB1 PT-00923 923 530A,760 i PBI PT-02289 2289 300 PB1 PT-02290 2290 300 PBI PT-04005 4005 8, 8 A PBI T2104 (PPCS) 2104 300 PB1 T2105 (PPCS) 2105 300 PBl TE-00140 140 21 PBi TE-00622 622 3 PBl TE-00623 623 3 PB1 TE 02104 2104 300 PB1 TE-02105 2105 300 PB1 TE-03510 3510 7 PBl T1-00140 140 21 PBl TI-00622A 622 3 PBl TI-00623A 623 3 l PBI TI-00960 N/A 1,5,760 PBl TM-00149 140 21 PB1 TM-00622 622 3 PBl TM-00622-2 622 3

~

PB1 TM-00623 623 3 !

PB1 TM-00623-2 623 3 PBl TR-2000B 2000 8, 8 A,10 PB2 E/1-03598 3598 7 PB2 F619 (PPCS) 619 13 PB2 F1-00l l 5 N/A 22 PB2 F1-00 l l 6 N/A 22 PB2 F1-00128 128 22 PB2 F1-00619 619 13 PB2 F1-00626 626 4A,755 PB2 F1-00924 924 765 PB2 FI-00925 925 765 PB2 F1-00928 928 4 A, 755 PB2 F1-00930 930 6 PB2 F1-03087 N/A i15 PB2 FI-04002 ~

4002 9A,295 PB2 F1-04036 4036 8 A, 9A,10, 290, 295 5

PB2 F1-04$37 4037 8 A, 9 A,10, 290, 295 PB2 FIT-00659 N/A 2, 525 A PB2 FIT-00660 N/A 4, 525 A PB2 FIT-00661 N/A 6 PB2 FIT-00930 930 6 PB2 FIT-04049 N/A 9A,295 PB2 FM-00128 128 22 PB2 FM-00626 626 4 A, 755 PB2 FM-00924-2 924 765 PB2 FM-00925-2 925 765 PB2 FM-00928-2 928 4A,755 PB2 FM-04002A 4002 9A,295 PB2 FM-04002B 4002 9A,295 PB2 FM-04036A 4036 8 A, 9 A,10, 290, 295 PB2 FM-040368 4036 8 A, 9 A,10, 290, 295 PB2 FM-04037A 4037 8 A, 9A,10, 290, 295 PB2 FM-04037B 4037 8 A, 9 A,10, 290, 295 PB2 FT-00128 128 22 PB2 FT-00185 N/A 18,735 PB2 FT-00619 619 13 PB2 FT-00626 626 4 A, 755 PB2 FT-00924 924 765 PB2 FT-00925 925 765 PB2 FT-00928 928 4 A, 755 i PS2 FT-04002 4002 9A 295 l

PB2 FT-04036 4036 8 A, 9 A,10, 290, 295 PB2 FT-04037 4037 8 A, 9 A,10, 290, 295 PB2 L3598 (PPCS) 3598 7 PB2 L1-00172 172 18

PB2 Li-00934 934 2, 525 A

( PB2 L1-00935A 935 2 PB2 L1-00938 938 2,525 A PB2 LI-00939A 939 2 PB2 L1-00972 972 765

~PB2 LM-00172 172 18 PB2 LM-00972-1 972 765

~

PB2 LT-00172 172 18 PB2 LT-00972 972 765 PB2 LT-03598 3598 7 PB2 LT/LC-00934 934 2 PB2 LT/LC-00935 935 2 PB2 LT/LC-00938 938 2 PB2 LT/LC-00939 939 2 PB2 P-002A Oil Press Gauge N/A 22 PB2 P-002B Oil Press Gauge N/A 22 PB2 P-002C Oil Press Gauge N/A 22 PB2 P-015 A-M- A M I N/A 2,765 PB2 P.0158-M- A M I N/A 2,765 PB2 P-029 inboard Pump Bearing Temp TC 2000 8,8A,10 PB2 P-029 inboard Turbine Bearing Temp TC 2000 8,8A,10 1

6

1 I

i e i). P-029 Outboard Pump Bearmg Temp TC 2000 8, 8 A,10

! ' t#MI P-029 Outboard Turbine Bearing Temp TC 2000 8, 8 A,10 hiY P2289 (PPCS) ~

2289 305 ,

( PB2 P2290 (PPCS) 2290 305 PB2 PI-00108 N/A 18 PB2 PI-00139 139 22,735 l

l PB2 PI-00184 N/A 18 PB2 Pl.00420A 420 22 PB2 PI-00468 468 8 A, 9 A,10, 95, 290, 295 PB2 PI-00478 478 8 A, 9 A,10, 95, 290, 295 I PB2 PI-00617A N/A 13 l PB2 P!-00617B N/A 13 l PB2 PI-00628 628 525 A, 535, 535 A PB2 PI-00629 629 525 A, 535, 535 B PB2 PI-00653A N/A 4,45, 525 A PB2 PI-00653B N/A 4, 45, 525 A PB2 PI-00655A N/A 4 PB2 PI-00655B N/A 4 PB2 PI-00692A N/A 13 PB2 PI-00692B N/A 13 l

PB2 PI-00913 A N/A 2 PB2 PI-00913B N/A 2 l PB2 PI-00922 922 525 A. 525 B, 535 B, 765 PB2 PI-00923 923 535A,765 PB2 PI-00933A N/A 6 PB2 PI-00933B N/A 6 PB2 PI-00933C N/A 6 PB2 PI-00933D N/A 6 l PB2 PI-00974 N/A 2,765

! PB2 PI-0400'E N/A 295

( PB2 P!-04005 4005 9A i PB2 PI-04013 A N/A 9A 295 PB2 Pl-04458 N/A 9A l PB2 PI-05976 N/A 285,285 A PB2 PI-05977 N/A 285,285 A l PB2 PM-00420A-1 420 22 l PB2 PM-00468A

468 8 A, 9 A,10, 95, 290, 295

! PB2 PM-00468 B 468 8 A, 9 A,10, 95, 290, 295 PB2 PM-00478A 478 8 A, 9 A,10. 95, 290, 295 PB2 PM-00478B 478 8 A, 9 A,10, 95, 290, 295 PB2 PT-00139 139 22,735 i PB2 PT-00420A 420 22 l PB2 PT-00468 468 8 A, 9 A,10, 95, 290, 295

'PB2 PT-00478 478 8 A, 9 A,10. 95, 290, 295 PB2 PT-00628 628 525 A, 535, 535 A I

PB2 PT-00629 629 525 A, 535, 535 B

, PB2 PT-00922 922 525A,525B,535B,765 PB2 PT-00923 923 535A.765 PB2 PT-02289 2289 305 PB2 PT-02290 2290 305 l

l 7

t i

PB2 PT-04005 4005 9A PB2 T'104 (PPCS)

, 2104 305 PB2 T2105 (PPCS) 2105 305 PB2 TE-00140 140 22 PS2 TE-00622 622 4 PB2 TE-00623 623 4-PB2 TE-02104 2104 305 32 TE-02105 2105 305 PB2 TE-03510 3510 7 PB2 TI-00140 140 22 PB2 TI-00622A 622 4 PB2 TI-00623A 623 4 PB2 TI-00960 N/A 2.6.765 PB2 TM-00140 140 22 PB2 TM-00622 622 4 PB2 TM-00622-2 622 4 PB2 TM-00623 623 4 PB2 TM-00623-2 623 4 PB2 TR-20008 2000 9A l

l l

4 8

ATTACIIM ENT 2 Installed IST Instrumentatinn

Unt ^ . Comp ID..- . Loop- . c ASM E - Cal Procedure - 'Freq Reference .. Max F.S. . F.S. Range.? . Required . ..' Actual ' . Loop. i

Required c Value ' 'Rangei f(FSR) : .f Accuracy : 2. Accuracy . Accuracy V/N : (RV) l ' (3X RV)) (%)i: l(%) ' ' .(%)

PBl FI-00 d 28 128 Y IICP-04.032-1 IA2 42.8 GPM 128.4 GPM I40 GPM 2.0 (L) 1.5 1.601 PB2 FI-00128 128 Y 2ICP-04.032-1 IA2 42 GPM 126 GPM 140 GPM 2.0(L) 1.5 1.601 PBl FM-00128 128 Y l lCP-04.032-1 IA2 N/A N/A N/A N/A 0.5 N/A I PB2 FM-00128 128 Y 21CP-04.032-1 IA2 N/A N/A N/A N/A 0.5 N/A PHI FT-00128 128 Y IICP-04.003-4 1A2 N/A N/A N/A N/A 0.25 N/A PB2 FT-00128 128 Y 2 tCP-04.003-4 IA2 N/A N/A N/A N/A 0.25 N/A Pill PI-00139 139 N ICP 6.21 IM2 N/A N/A 100 PSI N/A 1.5 1.581 ;

Pil2 PI-00139 139 N ICP 6.21 IM2 N/A N/A 100 PSI N/A 1.5 1.581 i PBl PT-00139 139 N ICP 6.21 IM2 N/A N/A N/A N/A 0.5 N/A PB2 PT-00139 139 N ICP 6.21 IM2 N/A N/A N/A N/A 0.5 N/A l Pill TE-00140 140 N N/A N/A N/A N/A N/A N/A UNK N/A I PIl2 TE-00140 140 N N/A N/A N/A N/A N/A N/A UNK N/A i PHI TI-00140 I40 N ICP 6.21 IM2 N/A N/A 300 F N/A- I.5 UNK i Pill TI-00140 140 N ICP 6.21 IM2 N/A N/A 300 F N/A I.5 UNK Pill TM-00140 140 N ICP 6.21 IM2 N 'A N/A N/A N/A 0.5 N/A PB2 TM-00140 140 N ICP 6.21 IM2 N/A N/A N/A N/A 0.5 N/A Pilo LI-00171 17I N ICP 4.16 IA2 N/A N/A 100 % N/A 1.5 1.658 PHO LM-00171 171 N ICP 4.16 IA2 N/A N/A N/A N/A 0.5 N/A '

PHO LT-00171 171 N ICP 4.16 IA2 N/A N/A N/A N/A 0.5 N/A ,

Pill LI-00172 172 N ICP 4.16 iA2 N/A N/A 100 % N/A 1.5 1.658 Pil2 LI-00172 172 N ICP 4.16 iA2 N/A N/A 100 % N/A 1.5 1.658 PBl LM-00172 172 N ICP 4.16 IA2 N/A N/A N/A N/A 0.5 N/A PB2 LM-00172 172 N ICP 4.16 IA2 N /A N/A N/A N/A 0.5 N/A PB1 LT-00172 172 N ICP 4.16 IA2 N/A N/A N/A N/A 0.5 N/A Pil2 LT-00172 172 N ICP 4.16 iA2 N/A N/A N/A N/A 0.5 N/A PBI P-029 Inboard 2000 N N/A N/A N/A N/A N/A N/A UNK N/A Pump Bearing Temp TC PB2 P-029 Inboard 2000 N N/A N/A N/A N/A N/A N/A UNK N/A Pump flearing Temp TC Pill P-029 Inboard 2000 N N/A N/A N/A N/A N 'A N/A UNK N/A I Turbine Bearing Temp TC i

PB2 P-029 inboard 2000 N N/A N/A N/A N/A N/A N/A UNK N/A Turbine Bearing Temp TC PBI P-029 Outboard 2000 N N/A N/A N/A N/A N/A N/A UNK N/A P"mo Bearing

'l emp TC PB2 P-029 Outboard 2000 N N/A N/A N/A N/A N/A N/A UNK N/A Pump Bearing ,'

Temp TC PBI P-029 Outboard 2000 N N/A N/A N/A N/A N/A N/A UNK N/A Turbine Bearing Temp TC PB2 P-029 Outboard 2000 N N/A N/A N/A N/A N/A N/A UNK N/A Turbine Bearing Temp TC P110 P-038 A Inboard 2000 N N/A N/A N/A N/A N/A N/A UNK N/A Pump Bearing Temp TC PB0 P-038A Outboard 2000 N N/A N/A N/A N/A N/A N/A UNK N/A Pump Ilearing Temp TC PIl0 P-03811 Inboard 2000 N N/A N/A N/A N/A N/A N/A UNK N/A Pump Bearing Temp TC PB0 P-038El Outboard 2000 N N/A N/A N/A N/A N/A N/A UNK N/A Pump Ilearing Temp TC PBI TR-02000H 2000 N ICP S.43 1A2 N/A N/A 250 F N/A 0.25 UNK PB2 TR-02000ll 2000 N ICP 5.43 iA2 N/A N/A 250 F N/A 0.25 UNK PBI T2104 (PPCS) 2104 N llCP 5.32 IA2 N/A N/A 450 F N/A 0.025 UNK PB2 T2104 (PPCS) 2104 N 21CP 5.32 1A2 N/A N/A 450 F N/A 0.025 UNK PBl TE-02104 2104 N N/A N/A N/A N/A N/A N/A UNK N/A PB2 TE-02104 2I04 N N/A N/A N/A N/A N/A N/A UNK N/A PBI T2105 (PPCS) 2105 N IICP 5.32 IA2 N/A N/A 450 F N/A 0.025 UNK PB2 T2105 (PPCS) 2105 N 2ICP 5.32 iA2 N/A N/A 450 F N/A 0.025 UNK PBI TE-02105 2105 N N/A N/A N/A N/A N/A N/A UNK N/A PB2 TE-02105 2105 N N/A N/A N/A N/A N/A N/A UNK N/A PHI P2289 (PPCS) 2289 N ICP 5.53 IA2 N/A N/A 1600 PSIG N/A 0.025 0.501 PB2 P2289 (PPCS) 2289 N ICP 5.53 IA2 N/A N/A 1600 PSIG N/A 0.025 0.501 ,

PBI PT-02289 2289 N ICP 5.53 IA2 N/A N/A N/A N/A 0.5 N/A PB2 PT-02289 2289 N ICP 5.53 1A2 N/A N/A N/A N/A 0.5 N/A PB1 P2290 (PPCS) 2290 N ICP 5.53 lA2 N/A N/A 1600 PSIG N/A 0.025 0.501 2

_. _ ._ - _.m _. _ _._... . - _ _ . _ . _ . . - . . _ .- _.-- _ . - . .- - _ _ . _ _ .-_... _ - . . - m .m ... . . _ _ .. _- -

1 6 t

PB2 P2290 (PPCS) 2290 N ICP 5.53 1A2 N/A I N/A 1600 PSIG N/A 0.025 0.501 PBI PT-02290 2290 N ICP 5.53 1A2 N/A N/A N/A N/A 0.5 N/A Pil2 PT-02290 2290 N ICP 5.53 1A2 N/A N/A N/A N/A 0.5 N/A l PB0 PI-02844 2844 N 2lCP-06.050 IA2 N/A N/A 150 PSIG N/A 1.5 1.658 I PB0 Pht-02844-1 2844 N 2ICP-06.050 IA2 N/A N/A N/A N/A 0.5 N/A l PIl0 PT-02844 2844 N ICP-06.059 IA2 N/A N/A N/A N/A 0.5 N/A '

PB0 PI-02845 2845 N llCP-06.050 lA2 N/A N/A 150 PSIG N/A 1.5 1.658 !

PB0 Pht-02845-1 2845 N g. IICP-06.050 lA2 N/A N/A N/A N/A 0.5 N/A '

P110 PT-02845 2845 N ICP-06.059 1A2 N/A N/A N/A N/A 0.5 N/A '

PB0 E/1-03510 3510 N ICP 6.29 iA2 N/A N/A N/A N/A 0.5 N/A i PHO T3510 (PPCS) 3510 N ICP 6.29 1A2 N/A N/A 100 F N/A 0.025 UNK ;

PBl TE-03510 3510 N N/A N/A N/A N/A N/A N/A UNK N/A l Pil2 TE-03510 3510 N N/A N/A N/A N/A N/A N/A UNK N/A !

Pill E/I-03598 3598 Y ICP 6.42 IA2 N/A N/A N/A N/A 0.5 N/A I PH2 E/I-03598 3598 Y ICP 6.42 1A2 N/A N/A N/A N/A 0.5 N/A [

PHI L3598 (PPCS) 3598 Y ICP 6.42 IA2 N/A N/A 243" N/A 0.025 I.000 ;

PH2 L3598 (PPCS) 3598 Y ICP 6.42 IA2 N/A N/A 243" N/A 0.025 1.000 I Pill LT-03598 3598 Y ICP 6.42 IA2 N/A N/A N/A N/A 1.0 N/A ,

PH2 LT-03598 3598 Y ICP 6.42 IA2 N/A N/A N/A N/A I.0 N/A P110 LE-03992A 3992A N NONE N/A N/A N/A N/A N/A UNK N/A

, PHO LIT-03992A 3992A N NONE N/A N/A N/A 100*i N/A 0.1 UNK {

PHO LE-03992B 399211 N NONE N/A N/A N/A N/A N/A UNK N/A !

PB0 LIT-03992B 3992B N NONE N/A N/A N/A 100*6 N/A 0.1 UNK PHI FI-04002 4002 N IICP-04.032-1 IA2 N/A N/A 400 GPh1 N/A l.5 1.732 Pil2 F1-04002 4002 N 2iCP-04.032-1 IA2 N/A N/A 400 GPh1 N/A 1.5 1.732

, PHI Fht-04002A 4002 N llCP-04.032-1 1A2 N/A N/A N/A N/A 0.5 N/A PB2 Fht-04002A 4002 N 2iCP-04.032-1 1A2 N/A N/A N/A N/A 0.5 N/A I PHI Fhi-04002B 4002 N IICP-04.032-i IA2 N/A N/A N/A N/A 0.5 N/A i PB2 Fht-04002B 4002 N 21CP-04.032-1 IA2 N/A N/A N/A N/A 0.5 N/A [

PBI FT-04002 4002 N llCP-04.003-5 1A2 Nr N/A N/A N/A 0.5 N/A 7 PB2 FT-04002 4002 N 21CP-04.003-5 IA2 N/A N/A N/A N/A 0.5 N/A PHI PI-04005 4005 Y l lCP-04.010-2 IA2 N/A N/A 1600 PSIG 2.0 (L) 1.5 1.581 !

PH2 PI-04005 4005 Y 2lCP-04.010-2 iA2 N/A N/A 1600 PSIG 2.0 (L) 1.5 1.581 j PHI PT-04005 4005 Y llCP-04.010-2 IA2 N/A N/A N/A N/A 0.5 N/A '

Pil2 PT-04005 4005 Y 2lCP-04.010-2 lA2 N/A N/A N/A N/A 0.5 N/A !

PB0 FI-04007 4007 N ICP 13.8 1A2 N/A N/A 300 GPh1 N/A I.5 1.820 !

PRO Fht-04007A 4007 N ICP 13.8 iA2 N/A N/A N/A N/A 0.5 N/A PB0 FN1-04007B 4007 N ICP 13.8 iA2 N/A N/A N/A N/A 0.5 N//. [

P110 FT-04007 4007 N ICP 13.8 IA2 N/A N/A N/A N/A 0.75 N/A [

PHO PI-04012 4012 Y ICP 13.8 IA2 N/A N/A 1600 PSIG 2.0 (L) L5 1.581 i Pilo PT-04012 4012 Y ICP 13.8 IA2 N/A N/A N/A N/A 05 N/A 3 i j i

- . . - - . . -- _ _ - __.-m_-. ..--s. .. -.-m.- _..-s., _. . - - _ _ ^_.____um-- - --w.- - - - . , .w , a+ y

i PB0 F1-04014 4014 N ICP l3.8 IA2 N/A N/A 300 GPM N/A l _5 1.820 PHO FM-04014 A 4014 N ICP 13.8 IA2 N/A N/A N/A N/A 0.5 N/A PB0 FM-04014B 4014 N ICP 13.8 IA2 N/A N/A N/A N/A 0.5 N/A PB0 FT-04014 4014 N ICP 13.8 IA2 N/A N/A N/A N/A 0.75 N/A ,

Pfl0 PI-04019 4019 Y ICP 13.8 IA2 N/A N/A 1600 PSIG 2.0 (L) 1.5 1.581 PHO PT-04019 4019 Y ICP 13 8 IA2 N/A N/A N/A N/A 0.5 N/A PHI F1-04036 4036 N IICP-04.032-1 1A2 N/A N/A 500 GPM N/A 1.5 1.820 ['

PB2 F1-04036 4036 N t 2ICP-04.032-1 IA2 N/A N/A 500 GPM N/A 1.5 1.820 Pill FM-04036A 4036 N l lCP-04.032-1 IA2 N/A N/A N/A N/A 0.5 N/A l PB2 FM-04036A 4036 N 21CP-04.032-1 IA2 N/A N/A N/A N/A 0.5 N/A PBI FM-0403611 4036 N I ICP-04.032-1 IA2 N/A N/A N/A N/A 0.5 N/A !

PB2 FM-04036B 4036 N 21CP-04.032-1 1A2 N/A N/A N/A N/A 0.5 N/A ,

PBI FT-04036 4036 N I ICP-04.006-3 lA2 N/A N/A N/A N/A 0.75 N/A ,

PB2 FT-04036 4036 N 21CP-04.006-3 IA2 N/A N/A N/A N/A 0.75 N/A l PBI FI-04037 4037 N IICP-04.032-1 1A2 N/A N/A 500 GPM N/A l.5 1.820 l PB2 F1-04037 4037 N 21CP-04.032-1 1A2 N/A N/A 500 GPM N/A 1.5 1.820 [

PBI FM-04037A 4037 N IICP-04.032-1 IA2 N/A N/A N/A N/A 0.5 N/A L Pil2 FM-04037A 4037 N 2iCP-04.032-1 N/A N/A N/A N/A 0.5 N/A PBI FM-04037B 4037 N llCP-04.032-1 ... N/A N/A N/A N/A 0.5 N/A l IA2 N/A N/A N/A N/A PB2 FM-04037B 4037 N 2lCP-04.032-1 0.5 N/A PBl FT-04037 4037 N I ICP-04.006-3 IA2 N/A N/A N/A N/A 0.75 N/A PB2 FT-04037 4037 N 21CP-04.006-3 lA2 N/A N/A N/A N/A 0.75 N/A i PHO LI-04038 4038 N ICP-13.009-2 IA2 N/A N/A 21FT N/A 1.5 1.750 PHO LM-04038- 1 4038 N ICP-13.009-2 IA2 N/A N/A N/A N/A 0.5 N/A PHO LT-04038 4038 N ICP-13.009- 1 IA2 N/A N/A N/A N/A 0.75 N/A ;

PB0 1.1-04039 4039 N ICP-13.009-2 IA2 N/A N/A 21FT N/A 1.5 1.750 l PHO l.M-04039- 1 4039 N ICP-13.009-2 IA2 N/A N/A N/A N/A 0.5 N/A !

PB0 1,T-04039 4039 N ICP-13.009-1 lA2 N/A N/A N/A N/A 0.75 N/A Pill PI-00420A 420 Y ICP 13.4 IA2 N/A N/A 3000 PSIG 2.0 ( L) 1.5 1.871 [

Pil2 PI-00420A 420 Y ICP 13.4 IA2 N/A N/A 3000 PSIG 2.0 (L) 1.5 1.871 [

FBI PM-00420A-I 420 Y ICP 13.4 IA2 N/A N/A N/A N/A 0.5 N/A !

Pill PM-00420A-1 420 Y ICP 13.4 IA2 N/A N/A N/A N/A 0.5 N/A PHI PT-00420A 420 Y IICP-04.004-I IA2 N/A N/A N/A N/A 1.0 N/A Pil2 PT-00420A 420 Y 2iCP-04.004-1 IA2 N/A N/A N/A N/A 1.0 N/A PHO FI-04459A 4459A Y ICP 6.57 IA2 6000 GPM 18000 GPM 10000 GPM 2.0 ( L) 0.1 0.269 PHO FI-04459H 4459A Y ICP 6.57 IA2 6000 GPM 18000 GPM 10000 GPM 2.0 (L) 0.1 0.269 PHO FIT-04459A 4459A Y ICP 6.57 IA2 N/A N/A N/A N/A 0.25 N/A Pil0 FIT-04459H 4459H Y ICP 6.57 IA2 N/A N/A N/A N/A 0.25 N/A

PHI PI-00468 468 N ICP 4.Ili IA2 N/A N/A 1400 PSIG N/A 1.5 1.732

PB2 PI-00468 468 N ICP 4. lli IA2 N/A N/A 1400 PSIG N/A 1.5 1732 Pill PM-00468A 468 N ICP 4.lli 1A2 N/A N/A N/A N/A 0.5 N/A i

4

PB2 PM-00468A 468 N ICP 4.l E lA2 W/A N/A N/A N/A 0.5 N/A !

PBl PM-00468B 468 N ICP 4.l E lA2 N/A N/A N/A N/A 0.5 N/A ,

PB2 PM-0046811 468 N ICP 4.lE IA2 N/A N/A N/A N/A 0.5 N/A PBI PT-00468 468 N I ICP-04.004-2 IA2 N/A N/A N/A N/A 0.5 N/A PB2 PT-00468 468 N 2lCP-04.004-2 IA2 N/A N/A N/A N/A 0.5 N/A Pill PI-00478 478 N ICP 4.l E lA2 N/A N/A 1400 PSIG N/A 1.5 1.732 .

PB2 PI-00478 478 N ICP 4.1 E lA2 N/A N/A I400 PSIG N/A 1.5 1.732 l PBl PM-00478A 478 N t ICP 4.l E IA2 N/A N/A N/A N/A 0.5 N/A i

PB2 PM-00478A 478 N ICP 4.lE lA2 N/A N/A N/A N/A 0.5 N/A PHI PM-00478B 478 N ICP 4.l E IA2 N/A N/A N/A N/A 0.5 N/A PB2. PM-00478B 478 N ICP 4.l E lA2 N/A N/A N/A N/A 0.5 N/A ,

Pill PT-00478 478 N llCP-04.004-2 1A2 N/A N/A N/A N/A 0.5 N/A PB2 PT-00478 478 N 21CP-04.004-2 IA2 N/A N/A N/A N/A 0.5 N/A PHI F619 (PPCS) 619 Y I ICP-06.068 IA2 2583 GPM 7749 GPM 8000 GPM 2.0 (L) 0.025 0.501 [

PH2 F619 (PPCS) 619 Y 2ICP-06.068 IA2 2600 GPM 7800 GPM 8000 GPM 2.0 ( L) 0.025 0.501 PSI FI-00619 619 Y IICP-06.068 IA2 2583 GPM 7749 GPM 8000 GPM 2.0(L) 1.5 I.581 ,

PH2 FI-00619 619 Y 2iCP-06.068 IA2 2600 GPM 7800 G PM 8000 GPM 2.0 (L) 1.5 1.581 -

PHI FT-00619 619 Y llCP-06.068 IA2 N/A N/A N/A N/A 0.5 N/A PB2 FT-00619 619 Y 2ICP-06.068 IA2 N/A N/A N/A N/A 0.5 N/A l Pill TE-00622 622 N N/A N/A N/A N/A N/A N/A UNK N/A Pil2 TE-00622 622 N N/A N/A N/A N/A N/A N/A UNK N/A Pill TI-00622A 622 N ICP-06.050 IA2 N/A N/A 350 F N/A 1.5 UNK l PB2 TI-00622A 622 N ICP-06.050 IA2 N/A N/A 350 F N/A I.5 UNK l PBI TM-00622 622 N ICP-06.050 IA2 N/A .N /A N/A N/A 0.5 N/A PB2 TM-00622 622 N ICP-06.050 IA2 N/A N/A N/A N/A 0.5 N/A PBI TM-00622-2 622 N ICP-06.050 IA2 N/A N/A N/A N/A 0.5 N/A PB2 TM-00622-2 622 N ICP-06.050 IA2 N/A N/A N/A N/A 0.5 N/A PB1 TE-00623 623 N ICP-06.050 IA2 N/A N/A N/A N/A UNK N/A PB2 TE-00623 623 N ICP-06.050 1A2 N/A N/A N/A N/A UNK N/A PB1 TI-00623A 623 N ICP-06.050 IA2 N/A N/A 350 F N/A 1.5 UNK !

PB2 TI-00623A 623 N ICP-06.050 IA2 N/A N/A 350 F N/A 1.5 UNK Pill TM-00623 623 N ICP-06.050 IA2 N/A N/A N/A N/A 0.5 N/A PB2 TM-00623 623 N ICP-06.050 1A2 N/A N/A N/A N/A 0.5 N/A Pill TM-00623-2 623 N ICP-06.050 IA2 N/A N/A N/A N/A 0.5 N/A PB2 TM-00623-2 623 N ICP-06.050 IA2 N/A N/A N/A N/A 0.5 N/A

, Pill FI-00626 626 N ICP 4.19 IA2 N/A N/A 4000 GPM N/A 1.5 1.658 PB2 F1-00626 626 N ICP 4.19 IA2 N/A N/A 4000 GPM N/A 1.5 1.658 PHI FM-00626 626 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N'A I PB2 FM-00626 626 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A Pill FT-00626 626 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A Pil2 FT-00626 626 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A I 5

[

I

i PBl PI-00628 628 N ibP 4.19 IA2 N/A N/A 600 PSIG N/A 1.5 1.581 ,

Pil2 PI-00628 628 N ICP 4.19 1A2 N/A N/A 600 PSIG N/A. l.5 1.581 PBI PT-00628 628 N ICP 4.19 IA2 N/A N/A N/A N/A- 0.5 N/A i PB2 PT-00628 628 N ICP 4.19 IA2 N/A N/A- N/A N/A 0.5 N/A ,

PBI PI-00629 629 N ICP 4.19 IA2 N/A N/A 600 PSIG - N/A 1.5 1.581 Pil2 PI-00629 629 N ICP 4.19 1A2 N/A N/A 600 PSIG N/A 1.5 1.581 PBI PT-00629 629 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A i PB2 PT-00629 629 N t ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A i PBl PI-00922 922 N ICP 4.19 1A2 N/A N/A 2000 PSIG N/A 1.5 1.581 l PB2 PI-00922 922 N ICP 4.19 IA2 N/A N/A 2000 PSIG N/A 1.5 1.581 PBI P T-00922 922 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A PB2 PT-00922 922 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A PBI PI-00923 923 N ICP 4.19 IA2 N/A N/A 2000 PSIG N/A -1.5 1.581 PB2 PI-00923 923 N ICP 4.19 IA2 N/A N/A 2000 PSIG N/A 1.5 1.581 ;

Pill PT-00923 923 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 - N/A ,

PB2 PT-00923 923 N ICP 4.19 IA2 N/A N/A N/A N/A- 0.5 N/A PBI F1-00924 924 N ICP 4.19 IA2 N/A N/A 1500 GPM N/A 1.5 1.732 :

Pil2 F1-00924 924 N ICP 4.19 IA2 N/A N/A 1500 GPM N/A 1.5 1.732 l PBI FM-00924-2 924 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A Pil2 FM-00924-2 924 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A t PBI FT-00924 924 N ICP 4.19 1A2 N/A N/A N/A N/A- 0.25 N/A l PB2 FT-00924 924 N ICP 4.19 IA2 N/A N/A N/A N/A 0.25 N/A '

Pill FI-00925 925 N ICP 4.19 lA2 N/A N/A 1500 GPM N/A 15 1.732 PB2 FI-00925 925 N ICP 4.19 IA2 N/A N/A 1500 GPM N/A 1.5 1.732 i PB1 FM-00925-2 925 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A !

PB2 FM-00925-2 925 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A I PBI FT-00925 925 N ICP 4.19 IA2 N/A N/A N/A N/A 0.25 N/A- I PB2 FT-00925 925 N ICP 4.19 1A2 N/A N/A N/A N/A 0.25 N/A ;

PBI F1-00928 928 N ICP 4.19 IA2 N/A N/A 2500 GPM N/A 1.5 1.835 Pil2 FI-00928 928 N ICP 4.19 I A2. N/A N/A 2500 GPM N/A I.5 1.835 ,

PB1 FM-00928-2 928 N ICP 4.19 1A2 N/A N/A N/A N/A 0.5 N/A t PB2 FM-00928-2 928 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A i PBI FT-00928 928 N ICP 4.19 1A2 N/A N/A N/A N/A 0.75 N/A [

PB2 FT-00928 928 N ICP 4.19 1A2 N/A N/A N/A N/A 0.75 N/A PHI FI-00930 930 N ICP 6.17 IA2 N/A N/A 50 GPM N/A 1.5 1.803 PB2 FI-00930 930 N ICP 6.17 IA2 N/A N/A 50 GPM N/A 1.5 1.803 !

PBI FIT-00930 930 N ICP 6.17 IA2 N/A N/A N/A N/A l.0 N/A PB2 FIT-00930 930 N ICP 6.17 IA2 N/A N/A N/A N/A 1.0 N/A PHI I.I-00934 934 N ICP 4.13 IA2 N/A N/A 100 *h N/A 1.5 I.803 PB2 LI-00934 934 N ICP 4.13 IA2 N/A N/A 100*L N/A 1.5 1.803 l PBI l.T/LC-00934 934 N ICP 4.13 1A2 N/A N/A N/A N/A 1.0 N/A

. 6 i

i

Pil2 LT/LC-00934 934 N ICP 4.13 IA2 N/A N/A N/A N/A 1.0 N/A Pill LI-00935A 935 N ICP 4.13 1A2 N/A N/A 100 */. N/A l.5 1.803 Pil2 L1-00935A 935 N ICP 4.13 IA2 N/A N/A 100 % N/A 1.5 1.803 PBI LT/LC-00935 935 N ICP 4.13 IA2 N/A N/A N/A N/A 1.0 N/A PB7 LT/LC-00935 935 N ICP 4.13 1A2 N/A N/A N/A N/A I.0 N/A Pill Li-00938 938 N ICP 4.13 1A2 N/A N/A 100 % N/A 1.5 1.803 PB2 LI-00938 938 N ICP 4.13 iA2 N/A N/A 100 % N/A 1.5 1.803 PBt LT/LC-00938 938 N t ICP 4.13 IA2 N/A N/A N/A N/A 1.0 N/A Pil2 LT/LC-00938 938 N ICP 4.13 1A2 N/A N/A N/A N/A 1.0 N/A Pill LI-00939A 939 N ICP 4.13 1A2 N/A N/A 100 % N/A 1.5 1.803 Pil2 LI-00939A 939 N ICP 4.13 IA2 N/A N/A 100 % N/A I.5 1.803 311 LT/LC-00939 939 N ICP 4.13 IA2 N/A N/A N/A N/A 1.0 N/A Pil2 LT/LC-00939 939 N ICP 4.13 IA2 N/A N/A N/A N/A l.S N/A Pill LI-00972 972 N ICP 4.13 iA2 N/A N/A 100 % N/A 1.5 1.058 Pil2 LI-00972 972 N ICP 4.13 1A2 N/A N/A 100 % N/A 1.5 1.658 Pill LM-00972-1 972 N ICP 4.13 1A2 N/A N/A N/A N/A 0.5 N/A PB2 LM-00972-1 972 N ICP 4.13 1A2 N/A N/A N/A N/A 0.5 N/A PRI LT-00972 972 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A Pil2 LT-00972 972 N ICP 4.19 IA2 N/A N/A N/A N/A 0.5 N/A PHO I P-032 A-M N/A N NONE N/A N/A N/A 600 Amps N/A UNK N/A Ammeter Pilo I P-032 B-M N/A N NONE N/A N/A N/A 600 Amps N/A UNK N/A Ammeter P110 I P.032C-M N/A N NONE N/A N/A N/A 600 Amps N/A UNK N/A Ammeter P110 I P-032 D-M N/A N NONE N/A N/A N/A 600 Amps N/A UNK N/A Ammeter PHO I P-032 E-M N/A N NONE N/A N/A N/A 600 Amps N/A UNK N/A Ammeter PHO I P-032 F-M N/A N NONE N/A N/A N/A 600 Amps N/A UNK N/A Ammeter PHO DPIS-02936 N/A N ICP 6.6 IM2 N/A N/A IS PSID N/A 0.5 N/A PRO DPIS-02937 N/A N ICP 6.6 IM2 N/A N/A 15 PSID N/A 0.5 N/A PRO DPIS-02938 N/A N ICP 6.6 IM2 N/A N/A 15 PSID N/A 0.5 N/A PBI FI-00II5 N/A Y IICP-04.003-7 IA2 N/A N/A 20 GPM 2.0 0.5 N/A Pil2 F1-00ll5 N/A Y 2iCP-04.003-7 IA2 N/A N/A 20 GPM 2.0 0.5 N/A Pill F1-00lI6 N/A Y I ICP-04.003-7 IA2 N/A N/A 20GPM 2.0 0.5 N/A PB2 FI-00lI6 N/A Y 2iCP-04.003-7 IA2 N/A N/A 20GPM 2.0 0.5 N/A P110 FI-00636 N/A N ICP 6.15 IM2 N/A N/A 100 GPM N/A 0.5 N/A Pilo F1-00652 N/A Y ICP 4.19 IA2 1250 GPM 3750 GPM 2700 GPM 2.0 0.5 N/A Pill F1-03087 N/A N NONE N/A N/A N/A UNK N/A UNK N/A 7

PB2 F1-03087 N/A N NONE N/A N/A N/A UNK N/A UNK N/A PHO FI-03905 N/A Y NONE N/A 43.5 GPM 130.5 GPM 60GPM 2.0 0.5 N/A PHO FI-03928 N/A Y NONE N/A 37 GPM iiIGPM 60GPM 2.0 0.5 N/A PHO F1-03929 N/A Y NONE N/A 41.5 GPM I24.5 GPM 60 GPM 2.0 0.5 N/A PHO FI-04666 N/A Y ICP-06.062 1A2 II7.5 GPM 352.5 GPM i40 GPM 2.0 0.5 N/A PHO FI-04667 N/A Y ICP-06.062 IA2 101 GPM 303 GPM IID GPM 2.0 0.5 N/A PHI FIT-00659 N/A Y ICP 6.17 IA2 400 GPM 1200 GPM 1071 GPM 2.0 0.25 N/A PB2 FIT-00659 N/A Y g ICP 6.17 IA2 400 GPM 1200 GPM 1971 GPM 2.0 0.25 N/A PHI FIT-00660 N/A Y ICP 6.17 IA2 1560 GPM 4680 GPM 2086 GPM 2.0 0.25 N/A PH2 FIT-00660 N/A Y ICP 6.17 IA2 1560 GPM 4680 GPM 2086 GPM 2.0 0.25 N/A PHI FIT-00661 N/A Y ICP 6.17 iA2 1200 GPM 3600 GPM 1674 GPM 2.0 0.25 N/A PH2 FIT-00661 N/A Y ICP 6.17 IA2 1200 GPM 3600 GPM - 1674 GPM 2.0 0.25 N/A PHI FIT-04049 N/A Y llCP-04.003-5 IA2 126 GPM 378 GPM 120GPM 2.0 0.25 N/A PH2 FIT-04049 N/A Y 21CP-04.003-5 IA2 125.5 GPM 376.5 GPM 120 GPM 2.0 0.25 N/A PHO FIT-04050A N/A Y ICP 13.8 IA2 86.5 GPM 259.5 GPM 120 GPM 2.0 0.25 N/A PHO FIT-04050H N/A Y ICP 13.8 IA2 88.3 GPM 264.9 GPM 120 GPM 2.0 0.25 N/A' PHI lT-00185 N/A Y N/A N/A 40 GPM 120 GPM 100 GPM 2.0 0.5 N/A Pil2 FT-00185 N/A Y N/A N/A 40 GPM 120 G PM 100 GPM 2.0 0.5 N/A PB0 G A Pl-1 N/A N ICP-13.007A-1 2A2 N/A N/A 300 PSIG N/A UNK N/A ,

PB0 G A PI-2 N/A N ICP-13.007 A- 1 2A2 N/A N/A 300 PSIG N/A UNK N/A PB0 G A PI-l N/A N ICP- 13.007 A-1 2A2 N/A N/A 300 PSIG N/A UNK N/A Pllo G A PI-2 N/A N ICP-13.007A-I 2A2 N/A N/A 300 PSIG N/A UNK N/A !

Pil2 P-002A Oil Press N/A N NONE N/A N/A N/A 60 PSIG N/A 1.0 N/A Gauge Pill P-002A Oil Press N/A N NONE N/A N/A N/A 60 PSIG N/A UNK N/A Gauge r PB2 P-00213 Oil Press N/A N NONE N/A N/A N/A 60 PSIG N/A 1.0 N/A Gauge Pill P-002B Oil Press N/A N NONE N/A N/A N/A 60 PSIG N/A UNK N% ;

Gauge j Pill P-002C Oil Press N/A N NONE N/A N/A N/A 60 PSIG N/A UNK N/A i Gauge , j Pil2 P-002C Oil Press N/A N NONE N/A N/A N/A 100 PSIG N/A UNK N/A f Gauge i Pill P-015 A-M- AM I N/A N NONE N/A N/A N/A UNK N/A 1.5 N/A ,

PB2 P-015 A-M- AM I N/A N NONE N/A N/A N/A UNK N/A 1.5 N/A Pill P-015 B-M-A M I N/A N NONE N/A N/A N/A UNK N/A 1.5 N/A PB2 P-01511-M- A M I N/A N NONE N/A N/A N/A UNK N/A 1.5 N/A Pil2 PI-00108 N/A Y ICP 6.41 3A2 N/A N/A 160 PSIG 2.0 0.5 N/A PHI PI-00108 N/A Y I C P 6.4I 3A2 N/A N/A 160 PSIG 2.0 0.5 N/A :

PHI PI-00184 N/A Y ICP 6.41 JA2 N/A N/A 160 PSIG 2.0 0.33 N/A s

Pil2 PI-00184 N/A Y ICP 6.41 3A2 N/A N/A 160 PSIG 2.0 0.5 N/A PHI Pl.00617A N/A Y ICP 6.15 IM2 N/A N/A 200 PSIG 2.0 0.5 N/A PH2 PI-00617A - N/A Y ICP 6.15 iM2 N/A N/A 200 PSIG 2.0 0.5 N/A t PHI ~ s-00617H N/A Y ICP 6.15 IM2 N/A N/A 200 PSIG 2.0 0.5 N/A P32 PI-00617H N/A Y ICP 6.15 IM2 N/A N/A 200 PSIG 2.0 0.5 N/A PHO PI-00631 A N/A Y ICP 4.19 IA2 N/A N/A 60 PSIG 2.0 0.5 N/A PRO Pl.0063111 N/A Y ICP 4.19 1A2 N/A N/A- 60 PSIG 2.0 0.5 N/A PB0 PI-00651 N/A N t ICP 6.15 IM2 N/A N/A 160 PSIG N/A 0.5 N/A

, PHI PI-00653A N/A Y ICP 4.19 IA2 N/A N/A 60 PSIG 2.0 UNK N/A ;

PH2 PI-00653A N/A Y ICP 4.19 IA2 N/A N/A 60 PSIG 2.0 UNK N/A :

PHI PI-00653H N/A Y ICP 4.19 IA2 N/A N/A 60 PSIG 2.0 UNK N/A f' PH2 PI-0 % 53 H N/A Y ICP 4.19 IA2 N/A N/A 60 PSIG 2.0 UNK N/A PHI PI-00655A N/A Y ICP 4.19 IA2 N/A N/A 400 PSIG 2.0 0.25 N/A [

PH2 PI-00655A N/A Y ICP 4.19 IA2 N/A N/A 400 PSIG 2.0 0.25 N/A t Pill PI-0%55H N/A Y ICP 4.19 IA2 N/A N/A 400 PSIG 2.0 0.25 N/A [

PH2 PI-00655H N/A Y ICP 4.19 IA2 N/A N/A 400 PSIG 2.0 0.25 N/A j PHO PI-00658A N/A Y ICP 4.19 IA2 N/A N/A IS PSIG 2.0 0.5 N/A PHO PI-00658H N/A Y ICP 4.19 IA2 N/A N/A 15 PSIG 2.0 0.5 N/A f PHI PI-00692A N/A Y ICP 6.15 IM2 N/A N/A 60 PSIG 2.0 0.25 N/A I

! PH2 PI-0%92A N/A Y ICP 6.15 1M2 N/A N/A 60 PSIG 2.0 0.25 N/A !

PHI PI-006928 N/A Y ICP 6.15 IM2 N/A N/A 60 PSIG 2.0 0.25 N/A t PH2 PI-00692 H N/A Y ICP 6.15 IM2 N/A N/A 60 PSIG 2.0 0.25 N/A PHI PI-00913A N/A Y ICP 4.19 IA2 N/A N/A 1500 PSIG 2.0 0.5 N/A [

PH2 PI-00913A N/A Y ICP 4.19 IA2 N/A N/A 1500 PSIG 2.0 0.5 N/A !

I

PHI PI-00913H N/A Y ICP 4.19 IA2 N/A N/A 1500 PSIG 2.0 0.5 N/A PH2 PI-00913H N/A Y ICP 4.19 IA2 N/A N/A 1500 PSIG 2.0 0.5 N/A PHI PI-00933A N/A Y ICP 6.17 IA2 N/A N/A 600 PSIG 2.0 0.5 N/A PH2 PI-Od933A N/A Y ICP 6.17 IA2 N/A N/A 600 PSIG 2.0 0.5 N/A PHI PI-00933B N/A Y ICP 6.17 IA2 N/A N/A 600 PSIG - 2.0 0.5 N/A l PH2 PI-00933H N/A Y ICP 6.17 IA2 N/A N/A 600 PSIG 2.0 0.5 N/A PHI PI-00933C N/A Y ICP 6.17 IA2 N/A N/A 60 PSIG 2.0 0.25 N/A PB2 PI-00933C N/A Y ICP 6.17 IA2 N/A N/A 60 PSIG 2.0 0.25 N/A [

PHI PI-00933D N/A Y ICP 6.17 IA2 N/A N/A 60 PSIG 2.0 0.25 N/A j PH2 PI-00933D N/A Y ICP 6.17 IA2 N/A N/A 60 PSIG 2.0 0.25 N/A i PHI PI-00974 N/A i ICP 4.19 1A2 N/A N/A 60 PSIG 2.0 0.25 N/A [

PH2 PI-00974 N/A Y ICP 4.19 IA2 N/A N/A 60 PSIG 2.0 0.25 N/A !

PHO PI-02815 N/A Y ICP 6.6 IM2 N/A N/A 160 PSIG 2.0 0.5 N/A PHO PI-02846 N/A Y ICP 6.6 IM2 N/A N/A 160 PSIG 2.0 0.5 N/A PHO PI-02847 N/A Y ICP 6.6 IM2 N/A N/A 160 PSIG 2.0 0.5 N/A PHO PI-02848 N/A Y ICP 6.6 IM2 N/A N/A 160 PSIG 2.0 0.5 N/A I PHO PI-02849 N/A Y ICP 6.6 IM2 N/A N/A I60 PSIG 2.0 0.5 N/A !

9

?

. . . . _ . . . . _ _ - _ - _ _ ..__________________________________________.____.__._________m.___ _ _ _ _ _ _ _ _ _ _ . _ _ _ _ . _ . _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ . _ _ _ _ _ _ _ _ _ _ _ _ . _ _ _ _

PB0 PI-02850 N/A Y ICP(W IM2 N/A l N/A . l 160 PSIG 2.0 0.5 N/A PHO PI-03973A N/A Y NONE N/A N/A N/A 160 PSIG 2.0 0.5 N/A PB0- PI-03973B N/A Y NONE N/A N/A N/A 160 PSIG 2.0 0.5 N/A PB0 PI-03974A N/A Y NONE N/A N/A N/A 160 PSIG 2.0 0.5 N/A PB0 PI-039748 N/A Y NONE N/A N/A N/A 160 PSIG 2.0 0.5 N/A PBI PI-04004 N/A N llCP-04.010-2 IA2 N/A N/A 1500 PSIG N/A 0.5 N/A PB2 PI-04004 N/A N 21CP-04.010-2 iA2 N/A N/A 1500 PSIG N/A 0.5 N/A PB0 PI-04010A N/A Y o ICP 13.8 IA2 N/A N/A 30 PSIG 2.0 0.5 N/A PRO PI-040ll N/A Y ICP 13.8 IA2 N/A N/A 1500 PSIG 2.0 0.5 N/A PRI Pl.04013A N/A Y IICP-04.006-3 1A2 N/A N/A 30 PSIG 2.0 0.5 N/A PB2 PI-04013A N/A Y 2lCP-04.006-3 IA2 N/A N/A 30 PSIG 2.0 0.5 N/A-PB0 PI-0401'/A N/A Y ICP 13.8 lA2 N/A N/A 30 PSIG 2.0 0.5 N/A PB0 PI-04018 N/A N ICP 13.8 IA2 N/A N/A 1500 PSIG N/A 0.5 N/A PBI PI-04458 N/A N ICP 6.6 IM2 N/A N/A 100 PSI N/A 0.5 N/A PB2 PI-04458 N/A N ICP 6.6 IM2 N/A N/A 100 PSI N/A 0.5 N/A PB0 PI-04741 N/A Y ICP-06.062 IA2 N/A N/A 30 PSIG 2.0 1.0 N/A PB0 PI-04742 N/A Y ICP-06.062 IA2 N/A N/A 60 PSIG 2.0 0.5 N/A PRO PI-04743 N/A Y ICP-06.062 IA2 N/A N/A 30 PSIG 2.0 1.0 N/A PRO PI-04744 N/A Y ICP-06.062 IA2 N/A N/A 60 PSIG 2.0 0.5 N/A PB0 PI-04745 N/A Y ICP-06.062 IA2 N/A N/A 15 PSIG 2.0 0.5 N/A PB0 PI-04746 N/A Y ICP-06.062 1A2 N/A N/A 60 PSIG 2.0 0.5 N/A PB0 PI-04747 N/A Y ICP-06.062 IA2 N/A N/A 15 PSIG 2.0 0.5 N/A PB0 PI-04748 N/A Y ICP-06.062 IA2 N/A N/A 60 PSIG 2.0 1.0 N/A PBI PI-05976 N/A N NONE N/A N/A N/A 160 PSIG N/A UNK N/A PB2 PI-05976 N/A N NONE N/A N/A N/A 160 PSIG N/A UNK N/A Pill PI-05977 N/A N NONE N/A N/A N/A 160 PSIG N/A UNK N/A PB2 PI-05977 N/A N NONE N/A N/A N/A 160 PSIG N/A UNK N/A PB0 PI-06354B N/A N NONE N/A N/A N/A 400 PSIG N/A 0.5 N/A PB0 PI-06354D N/A N NONE N/A N/A N/A 400 PSIG N/A 0.5 N/A PB0 PI-06355B N/A N NONE N/A N/A N/A 400 PSIG N/A 0.5 N/A PB0 PI-06355D N/A N NONE N/A- N/A N/A 400 PSIG N/A 0.5 N/A PB0 TI-00633A N/A N ICP 6.41 3A2 N/A N/A 200 F N/A I.0 N/A PHO TI-0%33B N/A N ICP 6.41 3A2 N/A N/A 200 F N/A 1.0 N/A PB0 TI-00665 N/A N NONE N/A N/A N/A UNK N/A UNK N/A PBI TI-00960 N/A N ICP 4.19 IA2 N/A N/A 130 F- N/A 1.0 N/A PB2 TI-00960 N/A N ICP 4.19 IA2 N/A N/A 130 F N/A I.0 N/A PIl0 TI-04045 N/A N ICP 13.8 IA2 N/A N/A 250 F N/A I.0 N/A PHO TI-04046 N/A N ICP 13.8 IA2 N/A N/A 250 F N/A 1.0 N/A 10

- i ATTACHMENT 3 ;

Portable Eauipment Used in ASME Section XI Testinn '

CompID. 3 Cal Procedure - (Freq~ Required : Actual

, .A ccuracy. Accuracy - ,

l

- (%)' L(%) '

ICTI-210 - ICP 8.77 1A2 5.0 UNK ICTI-211 ICP 8.77 lA2 5.0 UNK ICTI-212 ICP 8.77 IA2 5.0 UNK MCDT-001 N/A N/A 2.0 0.035 MCDT-002 N/A N/A 2.0 0.035 MCST-001 ICP 8.32 1A2 2.0 +/- 1 RPM OPSDT-001 N/A N/A 2.0 0.035 OPSDT-002 N/A N/A 2.0 0.035 OPSML-001 ICP 8.77 1A2 5.0 1.0 OPSSW-001 ICP-08.001 IA2 N/A UNK OPSSW-002 ICP-08.001 lA2 N/A UNK OPSSW-003 ICP-08.001 IA2 N/A UNK OPSSW-004 ICP-08.001 IA2 N/A UNK OPSSW-005 ICP-08.001 1A2 N/A UNK OPSSW-006 ICP-08.001 1A2 N/A- UNK OPSSW-007 ICP-08.001 IA2 N/A UNK OPSSW-008 ICP-08.001 lA2 N/A UNK OPSSW-009 ICP-08.001 1A2 N/A UNK OPSSW-010 ICP-08.001 IA2 N/A UNK OPSSW-O l t ICP-08.001 1A2 N/A UNK l

l 1

l

ATTACIIMENT 4 .

Installed IST Instrumentation

' Uxit - - CompID; , ASME Req Y/N Mfr Model # . Inst ; increments .. .; Headability .

Accuracy ; (1) .-

' Accuracy in -

(%)i %:

(.51/FSR)

P110 IP-032A-M Ammeter N WEST TYPE KA-241 UNK N/A N/A ;

PB0 IP-03211-M Ammeter N WEET TYPE KA-241 UNK N/A N/A Pil0 IP-032C-M Ammeter N WEST TYPE KA-241 UNK N/A N/A P110 IP-032D-M Ammeter N WEST TYPE KA-241 UNK N/A N/A P110 IP-032E-M Ammeter N WES T TYPE KA-241 UNK N/A N/A P110 IP-032F-M Ammeter N WEST TYPE KA-241 UNK N/A N/A PHO DPIS-02936 N llAltTON 277 0.5 N/A N/A P110 DPIS-02937 N llARTON 289A 0.5 N/A N/A i P110 DPIS-02938 N HARTON 277 0.5 N/A N/A ,

Pilo E/l-03510 Y FOXIlOR M!693A 0.5 N/A N/A Pill E/I-03598 Y FOXilOR M/693A 0.5 N/A N/A ;

Pil2 E/I-03598' Y FOXilOR M/693A 0.5 N/A N/A Pill F619 (PPCS) Y N/A N/A 0.025 N/A N/A Pil2 F619 (PPCS) Y N/A N/A 0.025 N/A N/A Pill FI-00115 Y llA RTON 200 0.5 0.2 GPM (0 - 0.5/0.25 IO GPM)/0.1 GPM (10 - 20 GPM)

Pil2 FI-00115 Y llARTON 200 0.5 0.2 GPM (0 - 0.5/0.25 ,

10 GPM)/0.I l GPM (10 - 20 GPM)

Pill FI-00l I6 Y llARTON 200 0.5 0.2 GPM (0 - 0.5/0.25 10 GPM)/0.I GPM (10 - 20 GPM)

I'll2 F1-00116 Y llARTON 200 0.5 0.2 GPM (0 - 0.5/0.25 10 GPM)/0.1 GPM (10 - 20 GPM)

Pill FI-00128 Y WEST 252 1.5 2GPM 0.7 PIl2 FI-00128 Y WEST 252 1.5 2GPM 0.7 Pill FI-00619 Y WEST 252 1.5 200 GPM I.25 [

Pil2 FI-00619 Y WEST 252 I.5 200 GPM 1.25 I

f

- - , . - - - - - - -.u-,- . - - . - - - - - , . - - _ _ _ --_---_-,------s-.------ _ . - - _ - .,--,----,-,a-,-,.---s - - - - - - - - - _ - - - - - - . - - - - - - - - - - _ _ _ -------___-_-----.---------------_-:------_------___----____---_--------__-_---,----.-

. _ . . _ . - = _ _ _ . _ , _ . ~ .- - - -_. . _ _ . . - _ _ _ - _ _ _ _ _

r PBI FI-00626 M WEST llX-252 1.5 N/A N/A PB2 Fl.00626 N WEST IIX-252 1.5 N/A N/A t

PB0 FI-00636 N BARTON 200 0.5 N/A N/A Pl10 F1-00652 Y llARTON 200 0.5 UNK UNK Pill FI-00924 N WEST llX-252 1.5 N/A N/A Pil2 FI-00924 N WEST llX-252 1.5 N/A N/A PB1 F1-00925 N WEST llX-252 1.5 N/A N/A PB2 FI-00925 N n WEST llX-252 1.5 N/A N/A PB2 F1-00928 N SIGMA 1151 1.5 N/A N/A PBI F1-00928 N WEST IIX-252 1.5 N/A N/A Pill F1-00930 N WEST llX-252 1.5 N/A N/A PB2 F1-00930 N WEST IIX-252 1.5 N/A N/A PBI F1-03087 N UNK UNK UNK N/A N/A I

PB2 F1-03087 N UNK UNK UNK N/A N/A Pil0 FI-03905 Y HARTON 226 0.5 0.5 PSI 0.4 !

Pilo FI-03928 Y HARTON 226 0.5 0.5 PSI 0.4 P110 FI-03929 Y HARTON 226 0.5 0.5 PSI 0.4 PB1 FI-04002 N WEST 252 1.5 N/A N/A PB2 F1-04002 N WEST 252 1.5 N/A N/A PHO F1-04007 N WEST 252 1.5 N/A N/A j Pil0 FI-04014 N WEST 252 1.5 N/A N/A PBt FI-04036 N WEST llX-252 1.5 N/A N/A PB2 F1-04036 N WEST IIX-252 1.5 N/A N/A Pill FI-04037 N WEST IIX-252 1.5 N/A N/A >

PB2 F1-04037 N WEST llX-252 1.5 N/A N/A PB0 FI-04459A Y NEWPRT 558A 0.1 1GPM N/A Pilo FI-0445911 Y NEWPRT 558A 0.1 iGPM N/A PB0 11-04666 Y I!ARTON 227A 0.5 4.0 GPM (0 - I.4/0.7 4

60 CPM)/2.0 GPM (60 - 140 GPM) '

Pit'l F1-04667 Y HARTON 227A 0.5 2.0 GPM (0 - 0.9/0.45

., 50 GPM)/1.0 GPM (50 - 100 GPM)

Pill FIT-00659 Y ROSEMT I151 0.25 N/A N/A Pil2 FIT-00659 Y ROSEMT IISI 0.25 N/A N/A Pill FIT-00660 Y ROSEMT I151 0.25 N/A N/A .

Pil2 FIT-00660 Y ROSEMT IISI 0.25 N/A N/A Pill FIT-00661 Y ROSEMT IISI 0.25 N/A N/A Pil2 FIT-00661 Y ROSEMT 1851 0.25 N/A N/A 2

t PB1 FIT-00930 W FISitP 1401 l 1.0 - N/A N/A PB2 FIT-00930 N FISilP 1401 1.0 N/A N/A PHI FIT-04049 Y ROSEMT IISI 0.25 N/A N/A PH2 FIT-04049 Y ROSEMT IISI 0.25 N/A N/A I PHO FIT-04050A Y ROSEMT 1151 0.25 N/A N/A PHO FIT-04050H Y ROSEMT I151 0.25 N/A N/A PHO FIT-04459A Y ROSEMT IISI 0.25 N/A N/A PHO FIT-04459H Y u ROSEMT 1151 0.25 N/A N/A PHI FM-00128 Y FOXHOR 66AC 0.5 N/A N/A {

PH2 FM-00128 Y FOXllOR 66AC 0.5 N/A N/A PBl FM-00626 N FOXilOR 66AC 0.5 N/A N/A PB2 FM-00626 N FOXBOR 66AC 05 N/A N/A PB1 FM-00924-2 N FOX 110R N-2 AO-V Al 0.5 N/A N/A PB2 FM-00924-2 N FOXBOR N-2AO-val 0.5 N/A N/A PBI FM-00925-2 N FOXBOR N-2AO-val 0.5 N/A N/A Pil2 FM-00925-2 N FOXilOR N-2AO-val 0.5 N/A N/A PBI FM-00928-2 N FOXilOR N-2 AO-val 0.5 N/A N/A PB2 FM-00928-2 N FOXilOR N-2 AO-val 0.5 N/A N/A PBI FM-04002A N FOXBOR M!66AC 0.5 N/A N/A Pil2 FM-04002A N FOXilOR M/66AC 0.5 N/A N/A Pill FM-04002B N FOXilOR M'66BC 0.5 N '5 N/A Pil2 FM-0400211 N FOXBOR M/66BC 0.5 N/A N/A !

PRO FM-04007A N FOXBOR M/66A 0.5 N/A N/A P110 FM-040078 N FOXBOR M/6611 0.5 N/A N/A PB0 FM-04014 A N FOXilOR M/66A 0.5 N/A N/A ,

P110 FM-04014B N FOXBOR M/6611 0.5 N/A N/A PBI FM-04036A N FOXBOR M!66AC 0.5 N/A N/A PB2 FM-04036A N FOXBOR M/66AC 0.5 N/A N/A PBI FM-04036B N FOXilOR Mf66BC 0.5 N/A N/A Pil2 FM-0403611 N FOXBOR M/66BC 05 N/A N/A Pill FM-04037A N FOXBOR M/66AC 0.5 N/A N/A '

PB2 FM-04037A N FOXBOR M/66AC 0.5 N/A N/A PRI FM-04037B N FOXBOR M/6611C 0.5 N/A N/A Pil2 l FM-04037B N FOXBOR M/66BC 0.5 N/A N/A Pill FT-00128 Y ROSEMT I151 0.25 N/A N/A

Pil2 FT-00128 Y ROSEMT 1151 0.25 N/A N/A Pill FT-00185 Y ROSEMT 8712 0.5 N/A N/A Pil2 FT-00185 Y ROSEMT 8712 0.5 N/A N/A i Pill FT-00619 Y FOXilOR N-E13DM 0.5 N/A N/A ,

Pil2 FT-00619 Y FOXIROR N-EI3DM 0.5 N/A N/A Pill FT-00626 N FOXIlOR N-El3DM 0.5 N/A N/A 3 i t

Pil2 FT-00626 N FOXBOR W-El 3 DM 0.5 N/A N/A Pill FT-00924 N ROSEMT I154 0.25 M/A N/A PB2 FT-00924 N ROSEMT I154 0.25 N/A N/A PBI FT-00925 N ROSEMT 1154 0.25 N/A N/A PB2 FT-00925 N ROSEMT I154 0.25 N/A N/A PB1 FT-00928 N FOXBOR N-EI3 DM 0.75 N/A N/A Pil2 FT-00928 N FOXilOR N-El3DM 0.75 N/A N/A Pill FT-04002 N n FOXIlOR N-E13DM 0.5 N/A N/A PB2 FT-04002 N FOXHOR N-E 13DM 0.5 N/A N/A P110 FT-04007 N FOXBOR N-E13DM 0.75 N/A N/A P110 FT-04014 N FOXBOR N-E13DM 0.75 N/A N/A Pill FT-04036 N FOXllOR N-El3DM 0.75 N/A N/A PB2 FT-04036 N FOXBOR N-EI3DM 0.75 N/A N/A PBI FT-04037 N FOXBOR N-El3DM 0.75 N/A N/A Pil2 FT-04037 N FOXBOR N-E13 DM 0.75 N/A N/A PB0 G-01-A PI-I N USGAGE 2941 UNK N/A N/A PB0 G-01-A PI-2 N USGAGE 2941 UNK N/A N/A PB0 G-02-API-I N USGAGE l'941 UNK N/A N/A P110 G-02-API-2 N USGAGE 2941 UNK N/A N/A PHI L3598 (PPCS) Y N/A N/A 0.025 N/A N/A Pil2 L3598 (PPCS) Y N/A N/A 0.025 N/A N/A PB0 LE-03992A N DREXEL 700-1-24 UNK N/A N/A PHO LE-0399211 N DREXEL 700-1-24 UNK N/A N/A PB0 LI-00171 N WEST 252 1.5 N/A N/A

~Pil2 LI-00172 N WEST 252 1.5 N/A N/A PRI LI-00172 N WEST VX-252 1.5 N/A N/A PB2 LI-00934 N SIGMA 1251 1.5 N/A N/A Pill LI-00934 N WEST VX-252 L5 N/A N/A PBI LI-00935A N SIGMA 1251 1.5 N/A N/A PB2 LI-00935A N SIGMA 1251 1.5 N/A N/A PB2 LI-00938 N SIGMA 1251 1.5 N/A N/A Pill LI-00938 N WEST VX-252 1.5 N/A N/A PBI LI-00939A N SIGMA 1251 1.5 N/A N/A PB2 LI-00939A N SIGMA 1251 1.5 N/A N/A Pill L1-00972 N SIGMA 1251 1.5 N/A N/A PB2 L1-00972 N SIGMA 1251 1.5 N/A N/A PHO LI-04038 N SIGMA 1251 1.5 N/A N/A P110 LI-04039 N SIGMA 1251 1.5 N/A N/A Pilo LIT-03992A N DREXEL 508-47-6 0.1 N/A N/A -

PB0 LIT-0399211 N DREXEL 508-47-6 0.1 N/A N/A Pilo LM-00171 N FOXBOR 66 tlc 0.5 N/A N/A 4

I

& t i~

PBI LM-00172 N FOXBOR 6611C 0.5 N/A- N/A PB2 LM-00172 N FOXBOR 66BC 0.5 N/A N/A Pill LM-00972-1 N FOXBOR N-2AO-VAI -- 0.5 N/A N/A [

PB2 LM-00972-1 N FOXilOR N-2AO-val 0.5 N/A N/A PB0 LM-04038-1 N FOXilOR N-2AO-val 0.5 N/A N/A }

PB0 LM-04039-1 N FOXBOR N-2AO-VAX 0.5 N/A N/A !

PB0 1.T-00171 N FOXBOR N-El 3DM 0.5 N/A N/A I PBI LT-00172 N u FOXIlOR N-El 3DM 0.5 N/A N/A ;

PB2 LT-00172 N FOXilOR N-E13DM 0.5 N/A N/A .

PBI LT-00972 N FOXBOR N-El l DM 0.5 N/A N/A I PB2 LT-00972 N FOXBOR N-El l DM 0.5 N/A N/A i PHI LT-03598 Y FJII UNK I.0 N/A N/A ;

PH2 LT-03598 Y Elll UNK l.0 N/A N/A !

PB0 LT-04038 N FOXBOR N-E13DM 0.75 N/A N/A :

PHO LT-04039 N FOXBOR N-E13DM 0.75 N/A N/A PB2 LT/LC-00934 N MAGNET 82-4021 1.0 N/A N/A >

PHI LT/LC-00934 N MAGNET 82-4021-313 1.0 N/A N/A ;

Pil2 LT/LC-00935 ~

N MAGNET 82-4021 1.0 N/A N/A !

PB1 LT/LC-00935 N MAGNET 82-4021-313 1.0 N/A N/A ['

PB2 LT/LC-00938 N MAGNET 82-4021 1.0 N/A N/A PB1 LT/LC-00938 N MAGNET 82-4021-313 1.0 N/A N/A l Pil2 LT/LC-00939 N MAGNET 82-4021 1.0 N/A N/A ;

Pill LT/LC-00939 N MAGNET 82-4021-313 1.0 N/A N/A PBi P-002A Oil Press Gauge N ASIICT UNK UNK N/A N/A Pil2 P-002A Oil Press Gauge N MCDANIEL CONTROI.S Model T 1.0 N/A N/A [

Pill P-002B Oil Press Gauge N ASilCT UNK UNK N/A N/A Pil2 P-002B Oil Press Gauge N MCDANIEL CONTROLS Model T l.0 N/A N/A i PBI P-002C Oil Press Gauge N ASilCT UNK UNK N/A N/A i PB2 P-002C Oil Press Gauge N ASilCT UNK UNK N/A N/A !

PHI P-015 A-M- A M I N WEST 252 1.5 N/A N/A I PB2 P-015 A-M- AM I N WEST 252 1.5 N/A N/A I PBl P-0158-M- A M I N WEST 252 1.5 N/A N/A f PB2 P-0 I S B-M- A M I N WEST 252 1.5 N/A N/A !

Pill P-020 Inboard Pump Bearing N UNK UNK UNK N/A N/A Temp TC ;

PB2 P-029 Inboard Pump Bearing N UNK UNK UNK N/A N/A l Temp TC i PBt P-029 Inboard Turbine Bearing N UNK UNK UNK N/A N'A l Temp TC !

Pil2 P-029 Inboard Turbine Bearing N UNK UNK UNK N/A N/A Temp TC .

5 l

l r

_ ___ -. . ~ . . , _. , _ . - . _ , . .

. _ . _ . . . _ _ . . -_.._.m _

i Pill P-029 Outboard Pump Bearing N UNK UNK UNK N/A N/A i Temp TC l PB2 P-029 Outboard Pump Bea;ing N UNK UNK UNK N/A N/A !

Temp TC Pill P-029 Outboard Turbine llearing N UNK UNK UNK N/A N/A Temp TC l PB2_ P-029 Outboard Turbine Bearing N UNK UNK UNK N/A N/A Temp TC I PB0 P-038A Inboard Pump ilearing N UNK UNK UNK N/A N/A Temp TC P110 P-038A Outboard Pump Bearing N UNK UNK UNK N/A N/A ;

Temp TC 1 PB0 P-038B Inboard Pump Bearing N UNK UNK UNK N/A N/A l Temp TC l PB0 P-038B Outboard Pump Bearing N UNK UNK UNK N/A N/A !

Temp TC !

Pill P2289 (PPCS) N N/A N/A 0.025 N/A N/A Pil2 P2289 (PPCS) N N/A N/A 0.025 N/A N/A Pill P2290 (PPCS) N N/A N/A 0.025 N/A N/A I PB2 P2290 (PPCS) N N/A N/A 0.025 N/A N/A j PB2 PI-00108 Y ASIICT 1379SS 0.5 2 PSI 0.6 t PBI PI-00108 Y PRMCAl, III 0.5 2 PSI 0.6 Pill PI-00139 N WiiST 252 1.5 N/A N/A !

PB2 PI-00139 N WEST 252 I.5 N/A N/A Pill PI-00184 Y ASilCT 45 0.33 i PSI 0.3 i Pil2 PI-00184 Y ASilCT 50-200SS 0.5 I PSI 0.3 i Pill PI-00420A Y SIGMA I151 1.5 50 PSI 0.8 [

PB2 PI-00420A Y SIGMA I151 1.5 50 PSI 0.8 ;

PB1 PI-00468 N WEST 252 1.5 N/A N/A !

Pil2 PI-00468 N WEST 252 1.5 N/A N/A i PBI PI-00478 N WEST 252 1.5 N/A N/A l PB2 PI-00478 N WEST 252 1.5 N/A N/A l Pill PI-00617A Y ASIICT 1379SS 0.5 2 PSI 0.5 PB2 1 I-00617A Y ASilCT 1379SS 0.5 2 PSI 0.5 Pill PI-0061711 Y ASIICT I3795S 0.5 2 PSI 0.5 PB2 PI-00617B Y ASIICI' 1379SS 0.5 2 PSI 0.5 Pill PI-00628 N WEST llX-252 1.5 N/A N/A Pil2 PI-00628 N WEST llX-252 1.5 N/A N/A PB1 PI-00629 N WEST llX-252 1.5 N/A N/A l PB2 PI-00629 N WEST llX-252 1.5 N/A N/A l Pilo PI-00631 A Y ASilCT DURAGAUGE 0.5 0.5 PSI 0.4 6

l

. a PHO PI-0063 t li Y ASilCT DURAGAUGE 0.5 0.5 PSI 0.4 PIl0 PI-00651 N ASitCT 1379SS 0.5 N/A N/A '

PHI PI-00653A Y locked Ili Rad UNK UNK UNK UNK PB2 PI-00653A Y tecked Ili Rad UNK UNK UNK UNK !

PHI PI-00653H Y locked Ili Rad UNK UNK UNK UNK PH2 PI-00653H Y lecked Ili Rad UNK UNK UNK UNK PHI PI-00655A Y PRMCAL 101 0.25 2 PSI 0.3 PH2 PI-00655A Y u PRMCAL 101 0.25 2 PSI 0.3 !

Pill PI-00655H Y ASilCT DURAGAUGE 0.5 5 PSI 0.6 f PH2 PI-00655H Y PRMCAL 101 0.25 2 PSI 0.3 i PHO PI-00658A Y ASitCT DURAGAUGE 0.5 0.1 PSI 0.3 PHO PI-00658H Y ASilCT DURAGAUGE 0.5 0.1 PSI 0.3 PHI PI-00692A Y PRMCAL 101 0.25 0.2 PSI 0.2 i PH2 PI-00692A Y PRMCAL 101 0.25 0.2 PSI 0.2 :

PHI PI-00692H Y PRMCAL 101 0.25 0.2 PSI 0.2 PH2 PI-0069211 Y PRMCAL IOI 0.25 0.2 PSI - 0.2 [

PHI Pl4H)913A Y ASitCT 1379SS 0.5 10 PSI 0.3 j PH2 PI-00913 A Y ASitCT 13795S 0.5 10 PSI 0.3 l PHI PI-00913H Y ASIICT 1379SS 0.5 10 PSI 0.3 i PH2 PI-00913Il Y ASIICT 1379SS 0.5 10 PSI 0.3 Pill PI-00922 N WEST llX-252 1.5 N/A N/A Pil2 PI4)0922 N WEST llX-252 1.5 N/A N/A

. PHI PI-00923 N WEST llX-252 1.5 N/A N/A ;

PH2 PI-00923 N WEST llX-252 1.5 N/A N/A 5 Pill PI-00933A Y ASIICT 1379SS 0.5 5 PSI 0.4 ;

PH2 PI-00933A Y ASilCT 1379SS 0.5 5 PSI 0.4 i Pill PI-00933H Y ASilCT 1379SS 0.5 5 PSI 0.4 j PH2 PI-0093311 Y ASilCT 1379SS 0.5 5 PSI 0.4 PHI PI-00933C Y PRMCAL 101 0.25 0.2 PSI 0.2 PH2 PI-00933C Y PRMCAL 101 0.25 0.2 PSI 0.2 Pill PI-00933D Y PRMCAL 101 0.25 0.2 PSI 0.2 ;

PH2 PI4H)933D Y PRMCAL 101 0.25 0.2 PSI 0.2

, Pill Pl.00974 Y PRMCAL 101 0.25 0.2 PSI 0.2 PH2 PI-00974 Y PRMCAL 101 0.25 0.2 PSI 0.2 !

PHO PI-02815 Y ASilCT DURAGAUGE 0.5 2 PSI 0.6 l PHO Pl.02844 N SIGMA IISI 1.5 N/A N/A .

PHO Pl 02845 N SIGMA 1151 1.5 N/A N/A !

Pilo PI-02H46 Y ASilCT DURAGAUGE 0.5 2 PSI 0.6 PHO PI-02M47 Y ASilCT DURAGAUGE 0.5 i PSI 0.3 ,

Pilo PI-02M4N Y ASIICT DURAGAUGE 0.5 2 PSI 0.6 Pil0 PI-02849 Y ASilCT DURAGAUGE 0.5 2 PSI 0.6 7

-- - - - - , a . . - . - . ~ - - . - - - _ _ . - - - . _ _ . _ _ . _ _ . _ . - _ . - - - - . - . _ . _ _ _ _ . _ _ _ _ _ - - _ _ . . - - - . - - . _ . - _ _ _ _ - . - - - - . .

_ _ _ _ . _ _ _ ._ _ . - . ~ . - . _ _ = - _ . . . - . _ . . _ _ . . _ 1 .. _ _ . m

. . L I

PHO PI-02850 Y ASilCT DURAGAUGE 0.5 2 PSI 0.6 i Pilo PI-03973A Y PRMCAL 11I 0.5 2 PSI 0.3 PHO PI-03973 B Y PRMCAL Ill 0.5 2 PSI 0.3 12 H0 PI-03974A Y PRMCAL III 0.5 2 PSI 0.3 F110 PI-039748 Y PRMCAL 11I 0.5 2 PSI 0.3 +

Pill PI-04004 N ASilCT DURAGAUGE 0.5 N/A N/A PIl2 PI-04004 N ASilCT DURAGAUGE 0.5 N/A N/A PHI PI-04005 Y t WEST 252 1.5 50 1.6 PH2 PI-04005 Y WEST 252 1.5 50 1.6 PHO PI-04010A Y ASilCT DURAGAUGE 0.5 0.2 PSI 0.3 ;

PHO PI-040ll Y PRMCAL 111 0.5 10 PSI 0.3 PHO PI-04012 Y WEST 252 1.5 50 1.6 i PHI PI-04013 A Y ASIICT DURAGAUGE 0.5 0.2 PSI 0.3 PH2 PI-04013 A Y ASilCT DURAGAUGE 0.5 0.5 PSI 0.8 Pilo PI-04017A Y ASilCT DURAGAUGE 0.5 0.2 PSI 0.3 Pilo PI-040l 8 N ASilCT DURAGAUGE 0.5 N/A N/A 4 Pilo PI-04019 Y WEST 252 1.5 50 1.6 I PB1 PI-0445R N ASHCT DURAGAUGE 0.5 N/A N/A !

PB2 PI-04458 N ASilCT DURAGAUGE 0.5 N/A N/A Pilo PI-04741 Y ASilCT DA1009 1.0 0.5 0.8 Pilo PI-04742 Y MCDANIEL CONTROLS Model T 1.0 1.0 0.8 Pilo PI-04743 Y ASIICT D A 1009 1.0 0.5 0.8 Pilo PI-04744 Y MCDANIEL CONTROLS Model T 1.0 1.0 0.8 l Pilo PI-04745 Y MCDANIEL CONTROLS Model T I.0 0.25 0.8 !

Pilo PI-04746 Y MCDANIEL CONTROLS Model T I.0 1.0 0.8 Pilo PI-04747 Y MCDANIEL CONTROLS Model T 1.0 0.25 0.8 PHO PI-04748 Y ASilCT DA1009 1.0 1.0 0.3 PB2 PI-05976 N ASIICT UNK UNK N/A N/A Pill PI-05976 N UNK UNK UNK N/A N/A !

P132 PI-05977 N ASilCT UNK UNK N/A N/A !

PHI Pi-05977 N UNK UNK UNK N/A N/A P110 PI-06354 B N PRMCAL 111 0.5 N/A N/A Pilo PI-06354D N PRMCAL 111 0.5 N/A N/A Pl30 PI-06355B N PRMCAL Ii1 0.5 N/A N/A P130 PI-06355D N PRMCAL Ii1 0.5 N/A N/A !

Pill PM-00420A-1 Y FOXHOR N-2 AO-val 0.5 N/A N/A .

PH2 PM-00420A-1 Y FOXHOR N-2 AO-val 0.5 N/A N/A PHI PM-00468A ~

N FOXIlOR 66RC 0.5 N/A N/A PB2 PM-00468A N FOXHOR 66RC 0.5 N/A N/A Pill PM-0046Sil N FOXilOR 6611C 0.5 N/A N/A l Pil2 PM-0046811 N I OXilOR 66 tlc 0.5 N/A N/A 8 i

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PBI TE-03510 N UNK UNK UNK N/A N/A-Pil2 TE-03510 N UNK UNK UNK N/A N/A PBI TI-00I40 N e WEST 252 I.5 N/A N/A PB2 TI-00140 N WEST 252 1.5 N/A N/A PBl TI-00622A N SIGMA 1851 1.5 N/A N/A PB2 TI-00622A N SIGMA 1151 1.5 N/A N/A j Pill TI-00623A N SIGMA 1151 1.5 N/A N/A PB2 TI-00623A N SIGMA 1151 1.5 N/A N/A PB0 TI-00633A N ASilCT UNK 1.0 N/A N/A s P110 TI-006 3B N ASilCT UNK 1.0 N/A N/A PB0 TI-00665 N UNK UNK UNK N/A N/A Pill TI-00960 N ASilCT UNK 1.0 N/A N/A PB2 TI-00960 N ASilCT UNK 1.0 N/A N/A !

PB0 TI-04045 N ASilCT UNK 1.0 N/A N/A P130 TI-04046 N ASilCT UNK 1.0 N/A N/A [

Pill TM-00140 N FOXilOR 694AC 0.5 N/A N/A-PB2 TM-00140 N FOXBOR 694AC 0.5 N/A N/A l N FOXIlOR N-2Al-P2V N/A '

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P-207A - -

PI-03974A FI-03903 PORT -

P-20711 - -

PI-0397411 FI-03929 PORT -

15 P-111 A -

PI-04745 PI-04746 F1-04667 PORT -

P-111 B -

PI-04747 PI-04748 FI-04667 PORT -

P-I I2A -

PI-04741 PI-04742 F1-04666 PORT -

P-11211 -

PI-04743 PI-04744 F1-04666 PORT -

n 17 (18) P-004A - PI-00184 PI-00108 FT-00185 PORT -

P-904B -

PI-00184 PI-00108 FT-00185 PORT -

21 (22) P-002A PORT PI-00139 PI-00420A F1-00128; F1-008 i3; PORT -

Discharge pressure not ASME fi-00116 required P-00211 PORT PI-00139 PI-00420A FI-00128; FI-00115; PORT -

FI-00116 P-002C PORT PI-00139 PI-00420A FI-00128; FI-00115; PORT -

FI-00116 2

~

ATTACIIMENT 6 Previous 36 Month Failure Ilistory for ASME Section XI Required Instrumentation (Shaded Components Indicates Multiple Failure Incidents)

Ulit CampID. 4 Loop # of OOC Work Order! . Date Failure Type ; As-Found Conditions P110 FI-006 2 N/A -

NONE N/A N/A N/A PB0 FI-03905 N/A -

NONE N/A N/A N/A PITO F1-03928 N/A -

NONE N/A N/A N/A PB0 F1-03929 N/A -

NONE N/A N/A N/A Pilo F1-04459A N/A -

NONE N/A N/A N/A PB0 FI-04459B N/A -

NONE N/A N/A N/A PB0 F1-04666 N/A - NONE N/A N/A N/A PB0 F1-04667 N/A 1 9410869 941220 OOC 7 gpm LOW @ 2 points PB0 FIT-04050A - N/A- 2- 9505881 950615 OOC 0.7 gym LOW @ 59.8 gpm PB0 FIT-04050A - N/A 9605321 960517 OOC None identired PHO FIT-0405011 N/A -

9511573 951031 Loose display conn =ctors N/A P110 FIT-04459A N/A -

NONE N/A N/A N/A PB0 FIT-04459B N/A -

NONE N/A N/A N/A PB0 PI-00631 A N/A I 9601939 960328 OOC 0.5 psi LOW @ 20 psi PB0 PI-00631B N/A -

NONE N/A N/A N/A PB0 Pl.00658A N/A 2 -- 9502308 950303 OOC 0.2 - 0.3 psi LOW -

PB0- PI-00658A N/A 9601939 960328 OOC 0.3 - 0.5 psi LOW ra) 5,10 psi PB0 PI-00658B N/A I 9502308 950303 OOC 3.5 psi LOW @ 3 points _

PB0 PI-02815 N/A -

NONE N/A N/A N/A ~

PB0 PI-02846- N/A 1 936045 93IIII Loose needle N/A' PB0 PI-02846 N/A 9606541 960619 OOC 6 psi HIGH -

PB0 PI-02847 N/A -

9509532 950919 Gauge broken N/A Pfl0 PI-02848 N/A -

NONE N/A N/A N/A PHO PI-02849 N/A 1 9608293 960809 OOC Zero shitI PB0 PI-02850 N/A -

NONE N/A N/A N/A PB0 PI-03973A N/A -

NONE N/A N/A N/A PHO PI-03973B N/A -

NONE N/A N/A N/A PB0 PI-03974A N/A -

NONE N/A N/A N/A PHO PI-03974B N/A -

NONE N/A N/A N/A Pfl0 PI-04010A N/A -

NONE N/A N/A N/A PRO PI-0401i N/A- -2 9403152 940721- OOC 40 - 50 psi HIGH G) all points PB0 PI-04011 N/A 9505881- 950615 OOC 45 - 50 psi HIGH @ all points PB0 PI-04012 4012 -

NONE N/A N/A N/A PB0 PI-04017A N/A 2- 9403152 94072i OOC 0.2 psi HIGH G) 15 psi PB0 PI-04017A N/A 960533I 960628- OOC 0.3 - 0.8 psi LOW I

_ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ . ___ _ _ _ _ _ - _ __ . _ _ _ - _ _ _ _ _ _ _ _ _ . _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ - - - _ _ _ _ _ _ - _ _ _ _ _ ___ - _ ___=

. 4 P110 Pl414019 4019 -

NONE N/A l N/A N/A i P110 PI-04741 N/A -

NONE N/A N/A N/A Pil0 PI-04742 N/A -

9409477 941122 Gauge overranged N/A PB0 PI-04743 N/A -

9500650 950120 Needle fell oft N/A PHO PI-04744 N/A 1 9410135 941103 OOC N/A PB0- PI-84745 N/A- 2- 9410869 941220 OOC. 0.3,1.5 psi HIGH @ 2 points ,

PB0 PI-04745 -- N/A- 9508200-- 950308 OOC- 0.3 psi LOW @ 7.5 psi -

' P110 PI-04746 N/A I 3410970 941219 OOC None identified PHO - PI-04747 : N/A: 2- 0052378 931207~ OOC 0.3 psi HIGH @ 14 psi PB0 PI-04747 N/A 9508200 950808 OOC 0.3 - 0.5 psi LOW @ all points -

PHO PI-04748 N/A -

NONE N/A N/A N/A PB0- PT-04012 4012.. 2 9403152 940721 OOC 0.22 - 0.25 ma HIGH @ all points PB0- PT-040l?. .4012 9605331 960628- OOC 0.31 - 0.38 ma HIGH @ all points . i

'PB0 PT-04019 4019 -

NONE N/A N/A N/A i PBl Ell-03598 3598 -

NONE N/A N/A N/A ,

PB1 F619 (PPCS) 619 -

NONE N/A N/A N/A PBl F1-00l l5 N/A -

NONE N/A N/A N/A PBI F1-00l l6 N/A -

NONE N/A N/A N/A Pill F1-00128 128 -

NONE N/A N/A N/A PBI FI-00619 619 -

NONE N/A N/A N/A !

PHI FIT-00659 N/A -

NONE N/A N/A N/A Pill FIT-00660 N/A -

NONE N/A N/A N/A Pill FIT-00661 N/A -

NONE N/A N/A N/A PBI FIT-04049 N/A -

NONE N/A N/A N/A !

Pill FM-00128 128 -

NONE N/A N/A N/A PHI FT-00128 - .128 2 9403771 940607 OOC- None identified I PBl FT-00128 128 9502517 950330 OOC 0.21 -0.29 ma HIGli @ 3 points Pill FT-00185 N/A -

NONE N/A N/A N/A Pill FT-00619 619 I 950l884 950301 OOC 0 4 - 0.5ma LOW j Pill L3598 (PPCS) 3598 -

NONE N/A N/A N/A Pill LT-03598 3598 -

NONE N/A N/A N/A PHI P2289 (PPCS) 2289 -

NONE N/A N!A N/A Pill PI-00108 N/A 1 9604948 960506 OOC None identified Pill PI-00184 N/A -

NONE N/A N/A N/A I Pill PI-00420A 420 -

NONE N/A N/A N/A PBl PI-00617A N/A -

NONE N/A N/A N/A I Pill PI-00617B N/A -

NONE N/A N/A N/A [

PHI PI-00653A N/A -

NCNE N/A N/A N/A I Pill PI-00653 B N/A -

NONE N/A N/A N/A ;

Pill PI-00655A N/A -

NONE N/A N/A N/A l Pill PI-00655 tl N/A -

NONE N/A N/A N/A !

2

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~Pil2 PI-0061711 N/A - NONE N/A N/A N/A Pil2 PI-00653A N/A - NONE N/A N/A N/A PB2 PI-00653B N/A - NONE N/A N/A _

N/A ,

PB2 PI-00655A N/A -

NONE N/A N/A N/A PB2 PI-00655B N/A -

NONE N/A N/A N/A PIl2 PI-00692A N/A - NONE N/A N/A N/A Pil2 PI-0069211 N/A - NONE N/A N/A N/A PS2 PI-009I3A N/A J6 ' Q049632.- 930922 OOC- 90 - 96 psi HIGH @ all points '

PB2 PI-00913A : N/A- 9407525, 940922 OOC 35 45 psi HIGH @ all points Pfl2 PI-00913 A N/A . 9509116:: 950929- OOC 5 psi HIGH @ 5 points PB2 PI-00913 A - N/A- % 02066 960227 OOC. -100 psi LOW PB2 PI-00913A - N/A- 9604543: 960425' OOC 100 psi LOW; Zero shift -

PB2 - PI-00913A - N/A 9606094 960619 OOC- None identified :

PB2 PI-00913A - N/A- % 07297 960712 Gauge failed : N/A PJ2 PI-00913B N/A :- '3 0049632 930922 OOC- 8 - 10 psi HIGil @ all points PB2 PI-00913B -- N/A- 9407525' 940922 OOC 13 - 19 psi LOW @ all points PB2 PI-00913B - N/A- % 05183 960619 - OOC None identified :

Pil2 PI-00933A N/A -

NONE N/A N/A N/A Pil2 PI-00933B N/A - NONE N/A N/A N/A FB2 PI-00933C N/A- 2- 0055326 940506 OOC IIIGH @ all points PB2 PI-00933C N/A 9504793 950530 OOC 0.5 psi HIGH @ all points PB2 PI-00933D N/A -2 9504793 950530 OOC I.9- 2.1 psi HIGH @ all points PB2 PI-00933D N/A 9511502 951024 Gauge broken N/A Pil2 PI-00933D N/A 9512774 951201 OOC; gauge broken Nonc id(ntified Pil2 PI-00974 N/A -

NONE N/A N/A PB2 PI-04005 4005 -

NONE N/A N/A N/A PB2 PI-04013 A N/A -

NONE N/A N/A N/A Pil2 PM-00420A-1 420 -

NONE N/A N/A N/A PB2 PT-00420A ~ 420- ~4 0049643 931007 OOC 0.1 ma HIGH @ 2 points PB2- PT-00420A - 420- 9407536 941001 OOC 0.15 ma LOW to 0.13 ma HIGli -

PB2 PT-00420 A - 420 9505922- 950613 : OOC 80 - 100 psi LOW @ 2 points PB2 PT-00420A 420- 9509218 951012 000 0.1 -0.12 ma HIGH @ 2 points Pil2 PT-04005 4005 -

NONE N/A N/A N/A 4

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PB1 FM-00924-2 924 - NONE N/A N/A N/A PBI FM-00925-2 925 - NONE N/A N/A N/A PBI FM-00928-2 928 -

NONE N/A N/A N/A PBl FM-04002A 4002 - NONE N/A N/A N/A PBI FM-04002B 4002 - NONE N/A N/A N/A Pill FM-04036A 4036 -

NONE N/A N/A N/A PBI FM-04036B 4036 -

NONE N/A N/A N/A PBt ~ FM-04037A 4037- 2 u 9502523. 950328- OOC 0.21 ma HIGH @ 20 ma . ['

PBI FM-04037A 4037 9602053 92109- OOC 0.31 ma LOW @ 30 ma Pill FM-0403711 4037 -

NONE N/A N/A N/A PBI FT-00626 626 I 9601939 960328 OOC None identified PHI FT-00924 924 -

NONE N/A N/A N/A PB1 FT-00925 925 -

NONE N/A N/A N/A PBI FT-00928 928 -

NONE N/A N/A N/A PBl FT-04002 4002 1 9602035 960411 OOC 0.22ma @ loma PB1 FT-04036 4036 I 9502519 950328 OOC 0.37ma lilGil @ 2 points PB1 IT-04037 4037 -

NONE N/A N/A N/A j PB1 LI-00172 172 -

NONE N/A N/A N/A t PB1 Ll-00934 934 1 9601934 960312 OOC 3?& I OW @ 100*h PBl Ll4)D935A 935 -

NONE N/A N/A N/A PB1 LI-00938 938 -

NONE N/A N/A N/A PBI LI-00939A 939 -

NONE N/A N/A N/A PHI LI-00972 972 -

NONE N/A N/A N/A PB1 LM-00172 172 -

NONE N/A N/A N/A Pill LM-00972-1 972 -

NONE N/A N/A N/A PHI LT-00172 172 -

NONE N/A N/A N/A PHI LT-00972 972 -

NONE N/A N/A N/A PHI LT/LC-00934 934 - 9602844 960326 Subcomponent Part Failure N/A ;

PRI LT/LC-00935.' 935 I 9505418' 950515- Subcomponent Part Failure N/A. I PB1 LT/LC-00935 935 9601933 960404 OOC 1.4% HIGH @ 25%-

FHI LT/LC-00938 938- 0 9500887: 950131 Subcomponent Part Failure N/A PB1 LT/LC-00938 938' 9602845 960326 Subcomponent Part Failure N/A ;

PHI LT/LC-00939 939 I 9502435 950405 OOC I.5?& LOW 6tl 0?b; 1.596 lilGil Gil 25?a !

PB1 P-015 A-M-AM I N/A -

NONE N/A N/A N/A PBl P-015 B-M-AM I N/A -

NONE N/A N/A N/A PBI P-029 Inboard Pump 2000 -

NONE N/A N/A N/A i Bearing Temp TC !

PHI P-029 inboard Turbine 2000 -

NONE N/A N /A N/A [

Bearing Temp TC i Pill P-029 Outboard Pump 2000 -

NONE N/A N/A N/A l Ilea ing Temp TC i 3 L e

f

. _ ._. --__ - -~___ _______ - _ _ ___ ____ - - - - - _ _ _ _ _ _ _. - _ . . _ . _ . - _ - -- - - - - - . - . - - .- . . . - . . . ,, .-

PB1 P-029 Outboard Turbine 2000 - NONE N/A N/A N/A Bearing Temp TC Pill P2289(PPCS) 2289 - NONE N/A N/A N/A PBI P2290(PPCS) 2290 -

NONE N/A N/A N/A Pill PI-00139 139 -

NONE N/A N/A N/A PBI PI-00468 468 - NONE N/A N/A N/A PJi- PI-00478 - 478. 2 0054481- 940411 OOCe 20 psi LOW @ I400 psi PB1 PI-00478 '478- ,, 9601925 92405- OOC 20 psi LOW @ 1400 psi; PBI "I-00628 628 -

NONE N/A N/A N/A PBI PI-00629 629 -

NONE N/A N/A N/A Pill PI-00922 922 -

NONE N/A N/A N/A Pill PI-00923 923 - NONE N/A N/A N/A !

PBl PI-04004 N/A -

NONE N/A N/A N/A j Pill PI-04458 N/A - NONE N/A N/A N/A PB1 PI-05976 N/A - NONE N/A N/A N/A ,

PBI PI-05977 N/A -

NONE N/A N/A N/A Pill PM-00468A 468 -

NONE N/A N/A N/A Pill PM-0046811 468 - NONE N/A N/A N/A Pill PM-00478A 478 -

NONE N/A N/A N/A ,

Pill PM-00478B 478 - NONE N/A N/A N/A !

Pill PT-00139 139 2- 0053700 940217' OOC 0.4 ma LOW @ all points PBl PT-00139 - 139 9507866 950821' OOC IllGII @ all points l Pill PT-00468 468 -

NONE N/A N/A N/A i PRI PT-00478 478 0 9602732 960308- Air in sensing line N/A.

PB I ' PT-00478 478 9603305 960322 Subcomponent Part Failure N/A I Pill PT-00628 628 - NONE N/A N/A N/A Pill PT-00922 922 - NONE N/A N/A N/A !

Pill PT-00923 923 -

NONE N/A N/A N/A Pill PT-02289 2289 -

NONE N/A N/A N/A Pill P T-02290 2290 - NONE N/A N/A N/A ,

Pill T2104 (PPCS) 2104 -

NONE N/A N/A N/A !

PBl T2105 (PPCS) 2105 -

NONE N/A N/A N/A l Pill TE-00140 140 -

NONE N/A N/A N/A PB1 TE-00622 622 -

NONE N/A N/A N/A Pill TE-00623 623 -

NONE N/A N/A N/A Pill TE-02104 2104 -

NONE N/A N/A N/A Pill TE-02105 2l05 -

NONE N/A N/A N/A Pill TE-03510 3510 -

NONE N/A N/A N/A Pill TI-00140 140 -

NONE N/A N/A N/A Pill ll-00622A 622 -

NONE N/A N/A N/A i Pill TI-00623A 623 -

NONE N/A N/A N/A f

P._1 TI-00960 N/Ax 2a 9502308~ 950303- OOC: 2 -3 Degrees F HIGH PBl TI-00960 - N/A: 9601939- 960328 OOC- 2 - 2 8 Degrees F LOW @ cli poi 2ts -

PBI TM-00140 140 1 9507866 950821 OOC 0.32 - 0.43ma lilGli @ 4 points ;

PBI TM-00622 622 -

NONE N/A N/A N/A Pill TM-00622-2 622 -

NONE N/A N/A N/A PBI TM-00623 623 - NONE N/A N/A N/A !

PBI TM-00623-2 623 -

NONE N/A N/A N/A PBI TR-2000B 2000 -

u 941092 940509 Subcomponent Part Failure N/A I PB2 IP-002A Oil Press Gauge N/A -

NONE N/A N/A N/A ,

Pil2 IP-00211 Oil Press Gauge N/A -

NONE N/A N/A N/A Pil2 IP-002C Oil Press Gauge N/A -

NONE N/A N/A N/A Pil2 F1-00626 626 -

9408660 941004 Meter internal contamination N/A j Pil2 F1-00924 924 -

NONE N/A N/A N/A PB2 F1-00925 925 -

NONE N/A N/A N/A I PB2 FI-00928 928 -

NONE N/A N/A N/A ;

PB2 FI-00930 930 -

NONE N/A N/A N/A PB2 Fi-03087 N/A -

NONE N/A N/A N/A [

PB2 F1-04002 4002 -

NONE N/A N/A N/A PIl2 F1-04036 4036 -

NONE N/A N/A N/A Pil2 F1-04037 4037 -

NONE N/A N/A N/A <

PB2 FIT-00930 930 - 2 935032 930917 OOC None identified l PB2 FIT-00930 - 930 9504793 950530 OOC I.3ma LOW @ 20ma Pil2 FM-00626 626 -

NONE N/A N/A N/A l Pil2 FM-00924-2 924 -

NONE N/A N/A N/A ;

PB2 FM-00925-2 925 -

NONE N/A N/A N/A Pil2 FM-00928-2 928 -

NONE N/A N/A N/A I PB2 FM-04002A 4002 -

NONE N/A N/A N/A Pil2 FM-0400211 4002 -

NONE N/A N/A N/A I PB2 FM-04036A 4036 -

NONE N/A N/A N/A y PB2 FM-0403611 4036 -

NONE N/A N/A N/A I PB2 FM-04037A 4037 -

NONE N/A N/A N/A !

PB2 FM-0403711 4037 -

NONE N/A N/A N/A !

Pil2 FT-00626 626 1 0049632 930922 OOC 0.25ma I.OW @ 50ma PB2 FF-00924 924 4 935436 931013 OOC Zero shift -

PB2 FT-00924 . 924- 9407525 940922- OOC 0.13 - 0.18 ma LOW @ all points l PB2 FT-00924 924 9509116 950929 OOC 0.09 ma LOW @ 2 upper points Pil2 FT-00924 924' 9512934- 951299 OOC- Zero shift Pil2 FT-00925 925 -

NONE N/A N/A N/A [

PB2 FT-00928 928 1 0049632 930922 OOC 0.14ma I.OW @ 20ma i Pil2 IT-04002 4002 3- 0049642 931014 OOC 0.3 - 0.5 ma LOW @ 4 points !

PB2 FT-04002 4002 9407535 94101i OOC 0.24 - 0.35 ma llIGil @ 3 points ;

5 ;

1

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PB2- FT-04002 4002 9509214: 950124 OOC- 0.25 m2 HIGH O 30 ma PB2 FT-04036 4036 I 9407535 94101I OOC 0.44 - 0.53ma LOW @ all points PB2 FT-04037 4037 1 9407535 941011 OOC 0.6 - 0.7ma LOW @ all points PB2 L1-00172 172 - NONE N/A N/A N/A ,

PB2 LI-00934 934 -

NONE N/A N/A N/A PB2 LI-00935A 935 -

NONE N/A N/A N/A PB2 LI-00938 938 -

NONE N/A N/A N/A I' PS2' L1-00939A : 939 -2 n 0049626 930915 OOC- 3% LOW @ 100%

PB2 L1-00939A' - 939 9406676 940822 OOC 4% LOW @ 100% - .

Pil2 LI-00972 972 - NONE N/A N/A N/A PB2 Lht-00172 172 -

NONE N/A N/A N/A t Pil2 Lht-00972-1 972 -

NONE N/A N/A N/A PB2 LT-00172 172 1 9509113 95092I OOC 0.24 - 0.44 tilGII @ 3 points :

Pil2 LT-00972 972 -

NONE N/A N/A N/A PB2 LT/LC-00934 - 934 1- 932478- 930604- LT/LC failed N/A .

PB2- LT/LC-00934. 934 9509110 951117 OOC 1.3 - 2.5% LOW @ 3 points -

PB7 LT/LC-00934 934c 9513053 951220 Air in sensing line ~ N/A l PB2 LT/LC-00934 - 934 9600811 960I24- Air in Sensing Line N/A . I PB2' LT/LC-00934 - 934 9605868- 960603 Air in sensing line N/A l PB2 LT/LC-00934 : 934: 9606993- 960628- Subcomponent part failure : N/A '

PB2 LT/LC-00934 934 9607050- 960703 Air in sensing line - N/AJ j PR2 LT/LC-00935 935 - i: 9401807 940420: Subcomponent part failure - N/A<

PB2 LT/LC-00935 935. 9408287 941029 Subcomponent part failure N/A.

PB2 LT/LC-00935 935' 9509110 951117' 000 1.9%,2.49% LOW @ 2 upper poinis ;

PB2 LT/LC-00935 935- 9605869 960603- - Air in sensing line - N/A-- [

PB2 LT/LC-00935 - 935- 9607051 960703 Air in sensing line N/A ;

PS2 LT/LC-00938 938 12 935028 931124: Subcomponent part failure - N/A PB2 LT/LC-00938 - 9381 9509110 951117 OOC- 1.1%,2.1% LOW @ 2 mid-points PB2 LT/LC-00938 ' 938 9600253' 960109- Subcomponent part failure N/A PB2 LT/LC-00938 938 9605870 960603 Air in sensing line N/A PB2 LT/LC-00939 939 1: 935007- 930930- LT/LC failed N/A- !

PB2 LT/LC-00939 - 939 9509110 95Ii17 OOC 1.1%,2.8% LOW @ 2 mid-points '

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NONE N/A N/A N/A f' PB2 P-029 Inboard Pump 2000 -

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Pil2 P-029 Inboard Turbine 2000 -

NONE N/A N/A N/A !'

Bearing Temp TC PB2 P-029 Outboard Pump 2000 -

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ATTACilMENT G - PB2 PIMX)5

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ATTACIIMENT 8 - PB0 PI 00631 A, B

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ATTACllMENT 8 - PB1 P14)0108

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. ,, ACTION ITEM' STATUS REPORT DWM MM 75~ PAGE

! ' , 12/26 f96_

l ******************************* Responsible Person: .

l;* Trkid: NRC 96EC

Urgency: NOT DUE / IN CLOSEOUT

N. Action Number: 20

Work Priority: 99 i *******************************

Activity Pending is: ACTION VERIFICATION ASSOCIATED KITH A COMMITMENT

! ----------TITLE AND TASK DESCRIPTION-----------------------------------------

NRC 09/12/96 Enforcement Conference Operations Conduct: Revise the initial and requalification training plans >

to include a review of the administrative procedures identified as l significant to daily operation of the plant during each 2-year Operations training plan.

______----DATES-- -- ---------------------------------------------------------

, Source Record: 11 13 96 ******* Evaluation ********* ****** Correction ******

Commitment: 12 27 96 Eval Due: Corr Act Due: 12 27/96 ;

i Action Create: 11 14 96 Orig Eval Due: Orig CA Due: 12 27/96 '

Action Closed: Eval Done: Corr Act Done:12 26/96

PEOPLE----------------------------------------------------------- -

Responsible for Overall Action: TROPS Responsible for Current Pending Activity: PEI Issue Manager:

Initiator:

Punchlist Administrator: .

UPDATE--------------------------------------------------------------

,(11/22/96 PJS1) Ability to complete this item is dependent upon Operations identifying theInitial operations." " administrative discussionsprocedures with T. significant todailySant that 1 l

is the target date to have the procedures identified. Sheley indicateTRPR 33.0 will nee /6 d

revision to reflect the commitment to review these on a two year basis.

LRTP for 1997 will need to be updated to reflect which procedures will be covered in the various cycles. This NUTRK also refers to an initial i training plan which does not exist. Initial materials can be revised orior 1 to next imolementation but will not be able to be revised by commitmeht i date. I will check with J. Palmer to ensure this is acceptable. J (12/26/96 PJS1) Operations has undertaken an initiative to upgrade and revise the operations manual and associated administrative procedures.

The process is expected to be completed by 4/1/97. O has Befined the following ignificant administrative As such," areas," perations '

vice

" procedures," which affect daily, operation of the plant;k OM expectations, 1 Control Room.condugt, watchstanding, logkeeping, and wor i control / configuration management.

(12/26/96 PJS1) CONTINUING TRAINING: TRPR 33.0 (Licensed Operator Requalification Training Program) has had a revision submitted to add l

" Review administrative areas significant to daily operation of the plant during each 2-year In with commitments.

operations training plan" to the appendix associated addition, the long range training plan has been l revised to include blocks of time devoted to covering significant administrative areas and current issues in cycles 97-1, 97-2, 97-4, 97-5, and 97-6.

,(12/26/96 PJS1) INITIAL TRAINING: To encompass initial training, a NUTRK item has been generated (TWR 96-074) directing operations training to ensure that the significant administrative pr9ceaures affecting, daily ,

plant operations are incorporated into the initial programs administrative training courses (TRCR 61.0, TRCR 68.0, and TRCR 86.0) prior to 5/1/97.

The due date allows for a one month window to make the necessary revisions to the courses and associated lesson plans upon completion of the operations administrative procedure upgrade initiative. Operations manaaement has committed to define the significant administrative proc 6dures upon completion of the upgrade (4 /1/ 97 )

(12 PJS1) Theprgcedures adm/26/96inistrative intent of this that commitment significantly,effectis to ensuredailythat plant operations i

j are incorporated into initial training continuing training, as well as 1 ensuring they are periodically reviewed, in subsequent 2-year plans. The !

actions contained in the previous updates describe the actions taken to ensure this takes place.

(12/26/96 PJS1) Passed to for Verification.

This item is complete. Close.

I

. . _ _ ~ . .. . . . . _ _ __ _ . _ ... _ . _ __..___..___..m. . . _ .

d 1

T

! POINT BEACH NUCLEAR PLANT 4

i. TRAINING PROGRAM COVER SHEET i mu TRP2 33.0 uecuseh opuma atominesma Twan & cum J

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)

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Check if desired Date i .

Reviewed By /2/M 5

Date Training Coordinator' i

Approved By Group Head Date 4

Approved By Training Manager Date l

i TR-7.2.1

i Revision 2 (08/17/94) 4

l

. 1 1

1 OR LONG R ANGl'. TRAINING l'I.AN

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une fi m r.ulded H i t . , , ,

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Limf' If A 13 hegmResni Rauf u.40 r Aderimetraine E UI 4 "'"' '

Fr \n Prwedures "d* * Il ieth rate indded Rii g,,,,,,,.,

l 91 4 Irw e f4 . ms ISemrver N oic : aw UW I A oe n 4+m.44 i s Aot N *lW t H l&4el<IH IN de l s trem I i K A tetw fchae M no eg nr 6 w lms to a 2t e n i l AJ ene f \( % %< W *elt I psiere %( 16 4 5 mp ment supp,rt I...o .I ( T u (\rt tjuan 6 meicte si r 6.hne huem W Hursium i nei out f (IP 4 .og ugi. . MMfurec ts.ms Camdem

Noon Jouti.*' d "f 5 Mgmricani f or i I Admmistrative P'"'*

Pron edures "tlume 6.mrrot u uem 9.,,n. r, r ,

Dihom Anmy p.m e r,peraw n 97-3 l os nr 1.,n oI Power N. mc I DG. AOP lo serw %na bor I cu nt Peooraten ef hv Neteaarv elearn al e'ecoi6 a! p *er 54'eruards Act.ene l' owes P! asp $s seems dish 1 OP P p -e' r '

eet,,ui He ,n M acrea*d < emra 9 . a ro,da,nm Ic4on emer s.mrtes I . 4mio n 4$$s Het er al

Cycle time devoted to reviewing signincant administiatise procedures which effect daily plant operations.

Specifics determined on basis of planned procedure upgrade and awessment based needs (Ops. Mgt.)

l t

j

NUCLEAR POWER BUSINESS UNIT TRPR 33.0 TRAINING PROGRAMS NNSR l Revision 3 j LICENSED OPERATOR REQUALIFICATION TRA!NING October 16,1996 PROGRAM APPENDIX C LONG RANGE TRAINING PLAN l REQUIRED OR COMMITMENT RELATED TOPICS l 4

1 Commitment References Frequencv l l

Complete task P7311 AOT, Wear NUREG 0041 Annual SCBA 10 CFR 20.103 Review and update training, as AM 3-1, Corporate Water Chemistry Annual appropriate, on NP 3.2.2, Primary Policy Chemistry Monitoring Program and NP 3.2.3, Secondary Chemistry Monitoring Program Review Conservative Decision SOER 94-01 (Salem) Annual Making Operating Philosophy NUTRK: SOER 94-01-04A/1 l l

Conduct Operational Examination 10 CFR 55.59 Annual 1 (Dynamics /JPMs)

Conduct Written Examination 10 CFR 55.59 Biennial (Static / Limits & Controis)

Conduct evaluation of shift NUTRK: TAC-OPS-94-06, SOER Biennial management tumover. DSS, DOS. or 94-01-04 Ail Third RO outside of the simulator control room at commencement of the dynamic evaluation knw Joer-*sinnVE AMAS NUTRk; NRC MSL *W 8tWY Swfacaur to Nay oncurW of TNG flAM bMnoA26 lata 2-yent orepww.s 'nt4turale ALAM 1

ACTION ITEM STATUS REPORT PAGE '.

12/26/9A '~

't Trkid: TWR 96-074

-

Responsible Urgency: Person: .DUE IN 121-180 DAYS i l

Action Number: 1

Work Priority: -100 Activity Pending is: ACTION NEEDED l

TITLE AND TASK DESCRIPTION------------------------------------------

Incorporation of Admin Procedures into Training Documents.

Ensure that the significant administrative procedures affecting daily plant operations are incorporated into the initial programs administrative training courses (TRCR 61.0 TRCR 68.0, + TRCR 86.0). Significant a nistrative procedure lis,t to be determined by operations Mgt. by 4 97.

DATES--------------------------------- -----------------------------

Source Record: 12/26/96 ******* Evaluation ********* ****** Correction ******

Commitment: Eval Due: Corr Act Due: 05/01/97 Action Create: 12/26/96 Orig Eval Due:

Eval Done:

Orig CA Due:

Corr Act Done:

05/01/97 Action Closed:

________.-PEOPLE----------------------------------------------------- --------

Responsible for Overall Action: TROPS Responsible for Current Pending Activity: TROPS Issue Manager:

Initiator:

Punchlist Administrator:

UPDATE---------------------------- ---------------------------------

_.--------REFERENCES------------------------------------------------------ ---

NRC 96EC

MISCELLANEOUS------------ ----- ----------------------- - ----------

Originating Agency: System: XX NRC Open Item Numoer. NRC Status:

Related Outages:

Engineering Work Type: Information Person Hours: Original Estimate =

Current Estimate =

Actual Hours =

1 1

I o

Gsrper /iss,o/3 SUNINiARY M

OPERATIONS PROCEDURES REVIEW FOR h1AINTENANCE ACTIVITIES January 21,1997 The Operations Group procedures were reviewed for maintenance activities using the attached document (page 2). This document was developed for this review to aid in flagging maintenance activities. The list of flags developed on this document was only to be a guide and not set the limit to what was finally identified as a maintenance activity.

The following Operations Group series procedures were reviewed:

ORT.. ..with exception to 3. 3a,3b,3c,9,10, and 17 see attached exception table.

01 OP TS IT PC RP. . ..with exception to 7 and 8 see attached exception table.

RF Total number of procedures reviewed for maintenance activities 781 Total number of procedures requiring a revision for PhiT or QC 70 (see attached list of procedures requiring revision)

Total number of procedures requiring a revision for PhiT 67 Total number of procedures requiring a revision for QC 15 Summary prepared by Bill Heinsohn Page1 of9

OPERATIONS PROCEDURES MAINTENANCE ACTIVITY REVIEWS The following is a list of fiags that can be used to help find Maintenance activities during initial reviews of Operations procedures:

NOTE. If any of thefollowing words or descriptions under IS A FLAG appear in the procedure you are reviewing, then the step isflagged by making a rev-bar using a blue highlighter. This willidennh possible procedures needing PMTor QC revisions. Ifyou are not .sure FLAG ITin pink.

IS A FLAG IS NOT A FLAG Flange or test cap removal (test cap only if Flange or test cap removal ifisolation valve there is NO isolation valve. In most cases is used there will be an isolation valve)

Perform packing adjustment or tighten Packing adjustment on a manual valve.

packing on AOV or MOV Lubricate, fill with oil, or grease If grease type is specified in procedure l Filter removal or replacement Resin replacement (eg., boron control) Resin is not used for Safety related system Setpoint adjustment If controlled in procedure Installing / removing jumpers, grounds, or It restoration is described in procedure lifling/ landing leads Breaker racking-in or out Valve manipulations Changing bulbs Hose connections Repair ( anytime the word repair is used flag it)

Any other possible maintenance activities you think are appropriate Page 2 of 9

j- EXAMPLES OF MAINTENANCE ACTIVITIES FOUND DURING REVIEW- <

!~

1.- PMT steps were added following installation of equipment requiring a leak check.

EXAMPLE; 7.3.6 Install following steam traps: i

a. (list of steam traps) l PMT 7.3.7 - Check components listed in step 7.3.6 for leakage when system is at normal operating pressure.

2. Removal and installation erfilter housing covers.

EXAMPLE; Added PMT identification to existing step.

l PMT 4.6 Inspect filter housings listed in step 1.1 for leakage while system is in operation.

3. Preventative maintenance performed on pumps.

EXAMPLE; Added PMT identification to existing step.

l PMT ;

4.7 Cycle pump No. 3 from minimum to maximum (greater than 56 gpm), noting any abnormal noises or conditicas. 1 4.- QC witness points were added following cover installation.

EXAMPLE; Added QC inspector note and step. Added M&TE identification.

l NOTE: QC Inspector must witness performance ofStep 5.2.12.

5.2.12 Ensure access cover properly installed and torqued to 60 ft-lbs.

Torque Wrench No. Cal Date:

5.2.13 Access cover bolts properly torqued. _

QC l

I i

Page 3 of 9

~

EXCEPTION TABLE l

The procedures listed below will recieve an extensive revision prior to use.

ORT 3 series has many issues not related to maintenance steps that require resolution before the procedures will be revised and used. ORT 3 Unit 2 is being reviewed for this outages performance.

ORT 9,10, and 17 (Unit 2) series are in the process of revision for this outage. The current schedule for approval of this procedure series is after Jan 31,1997. Guidance on including PMT/QC for maintenance activities has been provided to the responsible engineer. A review for QC will be required by a QC inspector qualified individual prior to procedure approval.

ORT 9,10, and 17 (Unit 1) series will be based on the Unit 2 procedures when that series is complete. l I

The Unit 1 ILRT is currently scheduled for the spring outage. This series will be required for that performance.

1 RP-7 and RP-8 are for ISFSI. The review of this series of procedutes was previously completed by a l maintenance QC inspector. The procedure series is currently in draft form. It is not expected that this series will be approved by Jan 31,1997. The revisions to this series will be required for loading the next i cask.

i 4

Procedure ID Unit 1 Unit 2 i'

ORT 3 Revisions will ORT 3 will be done Jan 29 i 3A be done prior to 3B next use ORT 3 A and 3B revisions will be done prior to next 3C (ORT 3,3 A,3B,3C) use ORT 9 Prior to next use Prior to completion of 10 (Unit 1 Outage) Unit 2 Outage 17

. RP 7 ISFSI 8 Prior to Cask Load Page 4 of 9

i -

PROCEDURES REOUIRING REVISION

~

l i

ORT UNIT I ORT UNIT 2 l PROCEDURE PROCEDURE TITLE REV TITLE REV <

g NUMBER NUMBER

]

ORT 4 Main Turbine Mechanical 8 ORT 4 Main Turbine Mechanical Overspeed Trip 8 I Overspeed Trip Device Device ORT 31 Nitrogen Supply to the Pressurizer 10

^

f Relief Tank (P14A)

ORT 30 PRT to Gas Analyzer Sample Line 8 ORT 50 PRT to Gas Analyzer, Sampic Linc(P34A) 6 (P34A)

L.~AT 59 Train A Spray System CIV Leakage 16 ORT 59 Train A Spray System CIV Leakage 17 4 Test Test (P54) j ORT 60 Train B Spray System CIV Leakage 18 ORT 60 Train B Spray System CIV Leakage 17 Test Test (P55)

ORT 67 Component Coohng Water to and 14 ORT 67 Component Cooling Water to and from 12

from the Excess Letdown Heat the Excess Letdown Heat Exchanger, Unit Exchanger - Refueling Shutdown 2 - Refueling Shutdown (P19,20)

(P19.20) l

, ORT 71 Electrical Penetration Leak Test 6 ORT 71 Electrical Penetration Leak Test (PE58) 6 l (P58)

ORT 72 Electrical Penetration Leak Test 7 ORT 72 Electrical Penetration Leak Test (PE20, 8

^

(P21,22) E22)

ORT 73 Electrical Penetration Leak Test 7 ORT 73 Electrical Penetration Leak Test (PEl) 6 (P28) i 5

4 Page 5 of 9

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

1-i 01 PROCEDURE TITLE REV TITLE REV NUMBER NUMBER 01-17 Letdown Gas Stripper Operation 9 OI 22G Changing Boric Acid Evaporator 4 Feed Filters (F8)

OI 17A Letdown Gas Stripper Preparation 1 OI 22H Changing Boric Acid Ceacentrates 4 for Maintenance and Recovery, Filters (F-5A&B)

Unit 1 OI-17B Letdown Gas Stripper Preparation 1 01-32 Hydrogen System Operation 16 for Maintenance and Recovery, Unit 2 OI-22A Changing Reactor Coolant Micron 9 01-48B Lube Oil Filter Changcouts 3 Filter (FI)

OI-22B Changmg Seal Water Return Filter 6 OI-48E EH Fluid System 14 (F2)

OI-22C Changing Spent Fuel Pit Filter 5 OI-64A Installation and Removal of Purge 5 (F6) Valve Component Bypass Lines OI-22D Changing Seal Water Injection 8 01-86 Instrument Air K2A/K2B and 5 Filters (F39A&B) Service Air K3A/K3B Compressor Run-in Operating Ins' 'ctions OI-22E Changing Letdown Gas Stripper 6 OI-86A Instrument Air Drycr Z-31 Operating 1

( Filters (F60A&B) Instructions Changing Boric Acid Filters (F3) 2 01-115 SFP Service Water Cooling Isolation i

[ OI-22F for Maintenance i 01-73J Water Treatment Resin Sampling 1 l OP PROCEDURE TITLE REV NUMBER OP-4D Part i Draming the Reactor Coolant System to a CVCS HUT 45 Without Entering Reduced Inventory OP-4D Part 5 Draining the Reactor Coolant System to a CVCS Hut 0 Without Entering Reduced Inventory and Without Draimng Steam Generator Tube OP-9C Containment Venting and Purging 37 Page 6 of 9

TS PROCEDURE TITLE REV NUMBER TS-37 U1 Containment Spray Nozzles Check (Frequency of Less Than or 5 Equal to Five Years)

TS-38 U2 Containment Spray Nozzles Check (Frequency of Less Than or 5 Equal to Five Years)

TS-80 Sampling of Emergency Fuel Oil Tank (T-72), Fuel Oil Storage 8 Tanks (T-175A,B) and EDG Day Tanks (T-31 A,B & T-176A,B) (Quarterly)

IT PROCEDURE TITLE REV NUMBER IT-200 U t Pressurizer Power-Operated Relief Valves and Block Valves 12 (Cold Shutdown)

IT-205 U2 Pressurizer Power-Operated Relief Valves and Block Valves 14 (Cold Shutdown)

IT-380 U1 Purge Valve Air System Check Valve (Quarterly) .5 w IT-385 U2 Purge Valve Air Sy7 tem Check Valve (Quarterly) 6 IT-530 Ul Leakage Reduction and Preventive Maintenance Program Test 11 of the Residual Heat Removal System (Refueling)

IT-530A UI Leakage Reduction and Preventive Maintenance Program Test I of the Train A HHS1 and RHR Systems (Refueling)

IT 530B U1 Leakage Reduction and Preventive Maintenance Program Test 1 of the Train B HHSI and RHR Systems (Refueling)

IT-535 U2 Leakage Reduction and Preventive Maintenance Program Test 11 of the Residual Heat Removal System (Refueling)

IT-535A U2 Leakage Reduction and Preventive Maintenance Program Test 1 of the Train A HHSI and RHR Systems (Refueling)

IT 535B U2 Leakage Reduction and Preventive Maintenance Program Test 2 of the Train B HHSI and RHR Systems (Refueling)

[

l l

Page 7 of 9

i PC PROCEDURE TITLE REV NUMBER PC-1 Monthly Heating and Ventilation System Checks, Unit 2 20 Part 3 Part 2 Monthly Heating and Ventilation System Checks, Unit i 27 Turbine Hall

~

PC-9 Monthly Shifting ofInstrument Air Compressors and Air Dryer 20 ;

Checks Pan 1 PC 23 Charging Pump Preventative Maintenance 1 i

Part 5 PC 24 Containment inspection Checklist (Monthly), Unit 1 42

PC-24 Containment Inspection Checkhst (Monthly), Unit 2 42 PC-43 Service Water Strainers 12 Part 3 PC-77 Refueling Interval Automatic Fire Protection System Valve 8 Trip-Test and Alarm Verification Test, Unit i p 3 Part 2 Refueling Interval Automatic Fire Protection System Valve 10 ;

Trip-Test and Alarm Verification Test Unit 2 Part 4 Annual Automatic Dry-Pipe Fire Protection System Valve Trip- 4 Test and Alarm Verification Test I Part 6 Annual Gas Turbine and Auxiliary Transformer Fire Protection 5 System Valve Trip-Test and Alarm Verification Test l

Page 8 of 9

RP !

i PROCEDURE TITLE REV NUMBER-RP1A Preparation for Refueling 42 ;

RP-1B Recovery from Refueling 32 )

RP-6A Steam Generator Crevice Flush (Vacuum Mode) 8 :

RF PROCEDURE TITLE REV NUMBER RF-190 Condenser Hotwell Inspection, Unit i 3 RF-195 Condenser Hotwell Inspection. Unit 2 2 RF-230.1 EH Filter Changcout and Magnetic Plug Inspection, UI 4 RF-235.1 EH Filter Changeout and Magnetic Plug Inspection. U2 3 l

l l

l i

I Page 9 of 9

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

p______________________________________*

Printed For: BRAD.FROMM * '

i Date: Sunday, 19 Januarv 1007 22:46 CT ,

To: ;

Cc:

From:

Subject:

WO/PMT: Project Plan Topic: rev. O QA PROJECT PLAN !

PBNP Unit 2 Restart Commitment # 15

" Work Order / Post-Maintenance Testing Surveillance" t

Restart Issue # 15 reads as follows:

" Review 20% of the work orders performed since January 1, 1995 on Unit 2 or !

common PSA safety significant systems (AFW, SW, EDG, IA, 4.16 kv, gas turbine, !

-and CCW) to verify adequate PMT was performed to ensure system / component safety function." .,

Clarification of this commitment is as follows:

- it applies to ALL work orders, not just Maintenance work orders (e.g., not i just work performed by the Maintenance group, but all work orders in total). <

- should generic or significant issues be identified, the scope of the review l will be expanded beyond the 20% sample.

i ** the 20% will be selected in a truly random manner, using a random number !

generation.

- documentation will be made and maintained for the selection / sample process, as well as documented evidence of each work order review.

!z** systems will be ordered and reviewed in the expected order of " return to

! service" for U2R22. '

Approach

l

~A QA Surveillance ( # S-P-97-01 ) will be conducted i.a.w. NP 11.2.1 as

, follows:

1 SCOPE: As per this project plan. Also, a full " surveillance checklist" will also be prepared and approved.

i e--

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e

, -Me mW T PBNP UNIT 2 Restart Issue # /6 W wu.A-c Work Order / Post-Maintenance Testing

eem QA Sui veillance # S-P-97-01 Q System: Work Order #: l NATURE OF WORK PERFORMED:

PMT PERFORMED /

REFERENCES:

DISCREPANCIES / DEFICIENCIES NOTED:

I L

7 i

CONCLUSION:

O Adequate O Deficiencies Noted, QCR #

Comments:

Reviewed by: Date: __

QAF-072 Rev. 0

- - , , , . .- .,

ML20134D401

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ML20134D401

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