BVY 09-009, Technical Specifications Proposed Change No. 273, Supplement 7 Response to Request for Additional Information

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Technical Specifications Proposed Change No. 273, Supplement 7 Response to Request for Additional Information
ML091110498
Person / Time
Site: Vermont Yankee Entergy icon.png
Issue date: 04/09/2009
From: Michael Colomb
Entergy Nuclear Operations
To:
Document Control Desk, Office of Nuclear Reactor Regulation
References
BVY 09-009
Download: ML091110498 (109)


Text

Entergy Nuclear Operations, Inc.

Vermont Yankee P.O. Box 0250 En tergy 320 Governor Hunt Road Vernon, VT 05354 Tel 802 257 7711 Michael J. Colomb Site Vice President April 9, 2009 BVY 09-009 ATTN: Document Control Desk U.S. Nuclear Regulatory Commission Washington, DC 20555-0001

Subject:

Technical Specifications Proposed Change No. 273, Supplement 7 Response to Request for Additional Information Vermont Yankee Nuclear Power Station Docket No. 50-271 License No. DPR-28

References:

(1) Letter, VYNPS to USNRC, "Technical Specification Proposed Change No. 273 Instrumentation Technical Specifications," BVY 08-001, dated February 12, 2008

Dear Sir or Madam,

In Reference (a), Entergy Nuclear Operations Inc. (ENO) submitted a proposed change to the instrumentation sections of the Vermont Yankee Operating License Technical Specifications. Attachment 1 to this submittal provides ENO's response to questions provided by NRC Staff and discussed with the NRC on a telecoms held on January 27, 2009, February 24, 2009 and March 3, 2009. Attachment 2 provides corresponding proposed changes to the TS and TS Bases. The TS Bases is provided for information only. Attachment 3 provides applicable portions of the related High Pressure Coolant Injection (HPCI) setpoint calculation. Attachment 4 provides applicable portions of the associated station procedures governing calibration of the HPCI setpoint.

'I This supplement to the original license amendment request does not change the scope or conclusions in the original application, nor does it change ENO's determination of no significant hazards consideration.

This letter contains no new regulatory commitments.

Should you have any questions or require additional information concerning this submittal, please contact Mr. David J. Mannai at (802) 451-3304.

BVY 09-009 / Page 2 of 2 I declare under penalty of perjury, that the foregoing is true and accurate. Executed on April 9, 2009.

Sincerely, MJC/JMD Attachments: 1. Response to Request for Additional Information

2. Proposed Technical Specification Changes
3. Applicable Portions of High Pressure Coolant Injection Setpoint Calculation
4. Applicable Portions of Station Procedures cc: Mr. Samuel J. Collins (w/o Attachments)

Regional Administrator, Region 1 U.S. Nuclear Regulatory Commission 475 Allendale Road King of Prussia, PA 19406-1415 Mr. James S. Kim, Project Manager Division of Operating Reactor Licensing Office of Nuclear Reactor Regulation U.S. Nuclear Regulatory Commission Mail Stop 0 8 C2A Washington, DC 20555 USNRC Resident Inspector (w/o Attachment 2)

Entergy Nuclear Vermont Yankee, LLC 320 Governor Hunt Road Vernon, Vermont 05354 Mr. David O'Brien, Commissioner (w/o Attachment 2)

VT Department of Public Service 112 State Street - Drawer 20 Montpelier, Vermont 05620-2601

Docket 50-271 BVY 09-009 Attachment 1 Technical Specification Proposed Change No. 273, Supplement 7 Vermont Yankee Nuclear Power Station Response to Request for Additional Information

BVY 09-009 / Attachment I/page I of 5 Technical Specification Proposed Change No.273, Supplement 7 Vermont Yankee Nuclear Power Station Response to Request for Additional Information RAI No.1 The licensee should docket the correction of the reference from the Instrumentation Uncertainty and Setpoint Design Guide, Revision 2, submitted July 21, 2003 (ADAMS Accession No. ML032130568), to Revision 3, submitted December 11, 2003 (ADAMS Accession No. ML033510764).

Response to RAI No. 1 The appropriate version of the Setpoint Design Guide, that is applicable to this proposed change, is Revision 3 which was submitted to the NRC on December 11, 2003 in Entergy Nuclear Operations Letter BVY 03-115.

RAI No.2 The licensee should confirm that with the changes proposed in the letter dated February 12, 2008 the CTS setpoint philosophy, as depicted in Figure 5, on pages 47 of 75, in the Instrumentation Uncertainty and Setpoint Design Guide, Revision 3 is still maintained for all setpoint changes in this amendment request.

Response to RAI No. 2 For the set-point changes provided in the letter dated February 12,2008 (BVY 08-001), the CTS setpoint philosophy, as depicted in Figure 5, on pages 47 of 75, in the Instrumentation Uncertainty and Setpoint Design Guide, Revision 3 is still maintained for all setpoint changes in this amendment request.

RAI No.3 For each setpoint change identified in Response to RAI No. 1, in the letter dated December 18, 2008, the licensee should identify the setpoint class (as defined on pages 2 thru 5 of 75 in the Instrumentation Uncertainty and Setpoint Design Guide, Revision 3).

Response to RAI No. 3 All setpoints identified in the letter dated December 18, 2008 (BVY 08-087) are Class 1 setpoints.

BVY 09-009 / Attachment I/ page 2 of 5 Technical Specification Proposed Change No.273, Supplement 7 Vermont Yankee Nuclear Power Station Response to Request for Additional Information RAI No.4 In Response to RAI No. 2, in the letter dated December 18, 2008, the licensee stated, "None of the setpoints proposed to be modified by this submittal are LSSS setpoints."

Included in the setpoints to be modified is TS Table 3.2.1, Emergency Core Cooling System (ECCS), Trip Setpoint 3.b, "High Pressure Coolant Injection (HPCI) System Low Condensate Storage Tank Water Level." The staff has a concern that this setpoint should be considered Limited Safety System Setting (LSSS) Safety Limit (SL)-related.

Part of the basis for this concern is that the Vermont Yankee UFSAR 1.6.2.11.1 states, "The HPCIS provides and maintains an adequate coolant inventory inside the reactor vessel to prevent fuel clad conditions from exceeding 10 CFR 50.46 criteria as a result of postulated small breaks in the nuclear system process barrier." UFSAR 6.4.1 states, "The HPCI System is provided to assure that the reactor core is adequately cooled in the event of a small break in the nuclear system and loss of coolant which does not result in rapid depressurization of the reactor vessel simultaneous with a loss of normal auxiliary power." UFSAR 7.4.3.2.1 states, "When actuated, the HPCI System pumps water from either the Condensate Storage Tank (CST) or the Suppression Chamber to the reactor vessel via the feedwater pipelines."

Paragraph 50.36(d)(1)(ii)(A) of 10 CFR Part 50 states that where an LSSS is specified for a variable on which a safety limit has been placed, the setting must be so chosen that the automatic protective action will correct the abnormal situation before an SL is exceeded.

These SLs are designated SL-related LSSSs. Appendix A to 10 CFR Part 50 defines AOOs as those conditions of normal operation that are expected to occur one or more times during the life of a nuclear power unit.

Vermont Yankee TS 1.0 specifies the SLs for the plant. The NRC staff evaluated the Condensate Storage Tank level-low setpoint for HPCI to determine if it should be considered as SL-related. The SL of concern is TS 1.1 .D which requires that the reactor vessel water level shall not be less than 12 inches above the top of the enriched fuel.

The licensee should describe how the Condensate Storage Tank, HPCI System, and other systems are used to assure that the reactor vessel water level is above the top of the enriched fuel.

The licensee should also detail any components in these systems that are not safety grade and what safety grade systems are credited to ensure the SL.

Does the Condensate Storage Tank contain sufficient volume to ensure that the reactor water level SL is not exceeded without the switchover to the suppression pool?

Based on the March 3, 2009 conference call with Entergy to discuss the Vermont Yankee instrumentation setpoint issues, the licensee was going to review the Technical Specifications Task Force (TSTF) letter to the NRC, dated February 23, 2009, "Industry Plan to Resolve TSTF-493, Clarify Application of Setpoint Methodology for LSSS

BVY 09-009 / Attachment I/page 3 of 5 Technical Specification Proposed Change No.273, Supplement 7 Vermont Yankee Nuclear Power Station Response to Request for Additional Information Functions," (ML090540849). Upon review of the TSTF letter, the licensee will determine how they want to approach resolution of the staff's concern about LSSS SL-related setpoint changes.

If the licensee intends to add footnotes based on adoption of Strategy 2, on page 3 of the TSTF letter (the addition of footnotes for functions identified in the TSTF letter) the licensee should provide the proposed footnotes, a summary calculation, and a copy of the surveillance/calibration procedure, for the proposed revised setpoint for Vermont Yankee TS Table 3.2.1, "Emergency Core Cooling System (ECCS)," Function 3.b, "High Pressure Coolant Injection (HPCI) System Low Condensate Storage Tank Water Level."

This function is included in Attachment A, of the TSTF letter, on page A-9, Specification 3.3.5.1, "Emergency Core Cooling System Instrumentation," Function 3.d, "HPCI System Condensate Storage Tank Level - Low."

A sample setpoint calculation for RCIC System High Steam Line Space Temperature Isolation setpoint was submitted with the licensee's December 18, 2008 letter (ML083650007). However, this sample calculation is not applicable for the HPCI System Low Condensate Storage Tank Water Level setpoint.

Therefore, the licensee should submit a summary calculation for HPCI System Low Condensate Storage Tank Water Level that includes the Analytical Limit, Total Loop Uncertainty, how the Nominal Trip Setpoint was calculated, how the acceptable As-Left value was calculated, and how the acceptable As-Found value was calculated. The entire calculation is not needed, only a summary calculation.

The licensee provided a description of their surveillance/calibration procedures in the December 18, 2008 letter. The staff's understanding of the description is: The surveillance/calibration procedures list the as-left and as-found calibration tolerances. If the as-found value is within the as-left tolerance, the technician documents that no action is required and the equipment is returned to service. If the as-found value is outside the as-left tolerance, but within the as-found tolerance, the condition is documented, a general conditions inspection is performed, and the equipment is calibrated and returned to service. If the technician does not identify any degradation during the calibration, the equipment is considered operable and returned to service. If the as-found value is outside the as-found tolerance, the equipment is entered into the Corrective Action Program.

However, the licensee's description of their surveillance/calibration procedures did not include a discussion of the plant corrective action process for declaring a channel inoperable when the as-found value is outside the as-found tolerance and for restoring a channel to operable status when the channel has been determined to be inoperable.

Therefore, the licensee should provide a description of the surveillance/calibration procedures that (1) includes a discussion of the plant corrective action process for restoring a channel to operable status when the channel is determined to be inoperable and (2) address investigations of why an as-found value drifted outside the as-left tolerance. The licensee should also describe what the general conditions inspection includes.

BVY 09-009 / Attachment I/ page 4 of 5 Technical Specification Proposed Change No.273, Supplement 7 Vermont Yankee Nuclear Power Station Response to Request for Additional Information For each setpoint change in which footnotes are being added to the TS (HPCI System Low Condensate Storage Tank Level), a copy of the surveillance/calibration procedure should be submitted for information purposes.

Response to RAI No. 4 Based on a telecom held on March 3, 2009, Vermont Yankee (VY) proposes to add the footnotes provided in industry TSTF-493, Revision 3, "Clarify Application of Setpoint Methodology for LSSS" to proposed Technical Specification (TS) Table 3.2.1 "Emergency Core Cooling System Instrumentation" for function 3.b, the High Pressure Coolant Injection (HPCI)

System Low Condensate Storage Tank (CST) Water Level setpoint.

The HPCI system works in conjunction with the other Emergency Core Cooling Systems to ensure that 10CFR50.46 requirements are satisfied. The HPCI system and CST components that support this function are safety related. The HPCI system relies on both the CST and the suppression pool to perform required safety functions. provides the proposed changes to the TS and an associated TS Bases change.

The TS Bases change is provided for information only.

As requested, Attachment 3 provides the applicable portions of the related setpoint calculation.

As requested, copies of the related calibration procedure (OP 43*63) and the plant procedure governing surveillance and calibration activities (AP 0310) are included as Attachment 4. A summary of how these procedures interface with the corrective action program and operability is provided below.

VY TS provide a six hour window for the performance of instrument calibrations without entry into the associated TS Limiting Condition for Operation (LCO). Prior to performing an instrument functional test or calibration, the Operations Department Shift Manager is informed of the activity and grants permission to proceed. Upon completion the Shift Manager is notified of the test results and any discrepancies. This ensures that the Shift Manager is aware of any issues that could impact operability and result in the need to be entered into the Corrective Action Program (CAP).

During the instrument calibration if a component is found outside the prescribed as-found range the result is "circled in RED" and brought to the attention of the technician's supervisor and Shift Manager as discussed above. An evaluation of the as-found condition on operability is performed and, if necessary, an LCO is entered. Once entered, the LCO would not be exited until corrective actions are taken that restore operability. This evaluation is documented in the related CAP report which is initiated to trend the occurrence and further investigate and determine if additional corrective actions are required. The evaluation would include an assessment of the as-found condition on the instruments ability to properly perform its intended function and a general condition inspection of the instrument for obvious material conditions that could impact component functionality.

BVY 09-009 / Attachment I/ page 5 of 5 Technical Specification Proposed Change No.273, Supplement 7 Vermont Yankee Nuclear Power Station Response to Request for Additional Information Following approval of the proposed change, Entergy will enhance procedures to incorporate the specific wording associated with the proposed footnotes and to define expectations for performance and documentation of the required evaluation.

Docket 50-271 BVY 09-009 Attachment 2 Technical Specification Proposed Change No. 273, Supplement 7 Vermont Yankee Nuclear Power Station Proposed Technical Specification Changes

VYNPS Table 3.2.1 (page 3 of 4)

Emergency Core Cooling System Instrumentation ACTIONS WHEN REQUIRED REQUIRED APPLICABLE MODES OR CHANNELS' CHANNELS OTHER SPECIFIED PER TRIP ARE TRIP FUNCTION CONDITIONS SYSTEM INOPERABLE TRIP SETTING

2. LPCI System (Continued)
i. Auxiliary RUN, STARTUP/HOT 1 Note 2 NA Power Monitor STANDBY, HOT SHUTDOWN, Refuel (a) (b)
j. Pump Bus RUN, STARTUP/HOT 1 Note 2 NA Power Monitor STANDBY, HOT SHUTDOWN, Refuel (a) (b)
3. High Pressure Coolant Injection (HPCI)

System

a. Low-Low RUN, STARTUP/HOT 2 Note 4 Ž 82.5 inches Reactor STANDBY(c) HOT Vessel Water SHUTDOWN(c), Refuel(c)

Level

b. Low RUN, STARTUP/HOT 2 Notes 4.24% d)

Condensate STANDBY(c), HOT 5,9,10 Storage Tank SHUTDOWN(c), Refuel(c)

Water Level

c. High Drywell RUN, STARTUP/HOT 2 Note 4
  • 2.5 psig Pressure STANDBY(c), HOT SHUTDOWN(c), Refuel(c)
d. High Reactor RUN, STARTUP/HOT 2 Note 6
  • 177 inches Vessel Water STANDBY(c), HOT Level SHUTDOWN(c), Refuel(c)

(a) With reactor coolant temperature > 212 'F.

(b) When associated ECCS subsystem is required to be operable per specification 3.5.

(c) With reactor steam pressure > 150 psig.

(a) Percent of instrument span.

Amendment No.1-64 37

VYNPS Table 3.2.1 ACTION Notes (Continued)

6. With one or more channels inoperable for ECCS instrumentation Trip Function 3.d:
a. Restore any inoperable channel to operable status within 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />.

If the Action and associated completion time of Note 6.a is not met, immediately declare the HPCI System inoperable.

7. With one or more channels inoperable for ECCS instrumentation Trip Functions 4.a and 4.b:
a. Declare ADS inoperable within 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br /> from discovery of loss of ADS initiation capability in both trip systems; and
b. Place any inoperable channel in trip within 96 hours0.00111 days <br />0.0267 hours <br />1.587302e-4 weeks <br />3.6528e-5 months <br /> from discovery of the inoperable channel concurrent with HPCI System or RCIC System inoperable, and
c. Place any inoperable channel in trip within 8 days.

If any applicable Action and associated completion time of Note 7.a, 7.b or 7.c is not met, immediately declare ADS inoperable.

8. With one or more channels inoperable for ECCS instrumentation Trip Functions l.f, 2.f, 4.c and 4.d:
a. Declare ADS inoperable within 1 hour1.157407e-5 days <br />2.777778e-4 hours <br />1.653439e-6 weeks <br />3.805e-7 months <br /> from discovery of loss of ADS initiation capability in both trip systems; and
b. Restore any inoperable channel to operable status within 96 hours0.00111 days <br />0.0267 hours <br />1.587302e-4 weeks <br />3.6528e-5 months <br /> from discovery of the inoperable channel concurrent with HPCI System or RCIC System inoperable, and
c. Restore any inoperable channel to operable status within 8 days.

If any applicable Action and associated completion time of Note 8.a, 8.b or 8.c is not met, immediately declare ADS inoperable.

9. If the as-found channel setpoint is outside its predefined as-found tolerance, then the channel shall be evaluated to verify that it is functioning as required before returning the channel to service.
10. The instrument channel setpoint shall be reset to a value that is within the as-left tolerance around the Nominal Trip Setpoint at the completion of the surveillance; otherwise, the channel shall be declared inoperable.

Setpoints more conservative than the Limiting Trip Setpoint are acceptable provided that as-found and as-left tolerances apply to the actual setpoint implemented in the surveillance procedures to confirm channel performance.

The methodologies used to determine the as-found and the as-left tolerances are specified in the Vermont Yankee Setpoint Program Manual.

Amendment No. 4-4 40

BASES 3.2A/4.2A Emergencv Core Cooling System (ECCS)

Table 3.2.1 ACTION Notes 9 and 10 The Emergency Core Cooling System Instrumentation, High Pressure Coolant Injection, Low Condensate Storage Tank Water Level function is modified by Notes 9 and 10 as identified in Table 3.2.1. Note 9 requires evaluation of channel performance for the condition where the as-found setting for the channel setpoint is outside its as-found tolerance. Evaluation of channel performance will verify that the channel will continue to behave in accordance with safety analysis assumptions and the channel performance assumptions in the setpoint methodology.

The ability to reset the setpoint represents continued confidence that the channel can perform its intended safety function. The performance of this channel will be evaluated under the Corrective Action Program. This will ensure required review and documentation of the condition for continued operability. Note 10 requires that the as-left setting for the channel be returned to within the as-left tolerance of the Nominal Trip Setpoint. Where a setpoint more conservative than the Limiting Trip Setpoint is used in the plant surveillance procedures, the as-left and as-found tolerances, as applicable, will be applied to the surveillance procedure setpoint. This will ensure that sufficient margin to the Safety Limit and/or Analytical Limit is maintained. If the as-left channel setting cannot be returned to a setting within the as-left tolerance of the Nominal Trip Setpoint, then the channel shall be declared inoperable. The methodologies for calculating the Nominal Trip Setpoint and the as-left and the as-found tolerances are located in the Vermont Yankee Setpoint Program Manual which is included by reference in the UFSAR. This ensures changes are evaluated under IOCFR50.59.

Docket 50-271 BVY 09-009 Attachment 3 Technical Specification Proposed Change No. 273, Supplement 7 Vermont Yankee Nuclear Power Station Applicable Portions of High Pressure Coolant Injection Setpoint Calculation

VYC-0723, Rev. 3 CCN-03 VY CALCULATION CHANGE NOTICE (CCN) Page 1 of CCN Number. 03 Calculation Number VYC-0723 Rev. No. 3 Calculation

Title:

CONDENSATE STORAGE TANK LEVEL (HPCI) MONITORING Initiating Document: ER-2000-1575 01 VYDC/MM!TM/Spec. No./ other Safety Evaluat ion Number: N/A UNCONT"OL For inforx*Y *y Superseded Document: N /A Implementation Required: [] Yes 0 No Reason for Change:

0 To increase the assumed normal area temperature in the CST valve room enclosure from 55-85 F to 45-100°F.

Description of Change:

Revise appropriate pages as required to incorporate additional instrument uncertainty (temperature affect) associated with increasing the ambient temperature range for the CST level transmitter to 45-100lF Technical Justification for Change:

The basis for the temperature range of 45-100lF is contained in ER 2000-1575. The temperature affect uncertainty is based'on the vendor's specifications associated with the CST level transmitter.

==

Conclusions:==

1. The increase in instrument uncertainty due to the increase in ambient temperature has been incorporated into the uncertainty analysis..
2. This Calculation or CCN is not an implementing document. Therefore, this CCN does not require a safety evaluation.

Installation Verification/Final Turnover to DCC:

Open Items Associated with CCN 13 Yes 0l No 03 Closed (Section 2.3.2)

Installation Verification (Section 2.3.4)

"] Calculation accurately reflects plant as-built configuration, OR

" N/A, calculation does not,affect plant configuration Resolution of documents identified in the Design Output Documents Section of VYAPF 0017.07 (Section 2.3.6)

I Print Name Signature Date Total number of pages in package including all attachments Note: VYAPF 0017.07 should be included immediately following this form. VYAPF 0017.08 AP 0017 Rev. 7 Page I of 1

VY CALCULATION DATABASE INPUT FORM VYC-0723, Rev. 3 CCN-03 Page 2__ of VYC-0723 CCN-03 3 VY Calculation/CCN Number Revision Number Vendor Calculation Number Revision Number Vendor Name: PO Number:

Originating Department:

Critical References Impacted: 0 FSAR 0 DBD 03 Reload. "Check" the appropriate box if any critical document is identified in the tables below.

EMPAC AsseLfEquipment ID Number(s):

EMPAC Asset/System ID Number(s):

Keywords:

For Revision/CCN only: Are deletions to General References, Design Input Documents or Design Output Documents required? 0 Yest R1 No General References Critical

  • Reference # II ****DOC#
  • Reference# DOC # I REVE REV# Reference Title (including
  • Reference Title Date, if applicable) (See App. A, Section 3.2.7 for Guidance)

(ineluding Date, if applPcable) (See App. A, Section 3.2.7 for Guidance)

~ Affected

        • Affected Critical Program IReference (_)

.1.

i.

1~

4.

4-

______________ t __ __

VYAPF 0017.07 AP 0017 Rev. 7 Page 1 of 2

VYC-0723, Rev. 3 CCN-03 I Page 3 of I Design Input Documents - The following documents provide design input to this calculation. (Refer to Appendix A, section 4)

  • Reference # ** DOC # REV Document Title (including Date, if applicable) **** Affected Critical I Program Reference U

/ ,.3qZao-/ "77-75_

Design Output Documents - This calculation provides output to the following documents. (Refer to Appendix A, section 5)

Date, Document Title (including

  • Reference
  • Reference # # ** DOC # REV # REV # Document Title (including Date,
    • DOC #
  • Reference # - Assigned by preparer to identify the reference in the body of the calculation.
    • Doc # - Identifying number on the document, if any (e.g., 5920-0264, G191172, VY6-1286)
  • Reference Title - List the specific documentation in this column. "See attached list" is not acceptable. Design Input/Output Documents should identify the specific design input document used in the calculation or the specific document affected by the calculation and not simply reference the document (e.g.,

VYDC, MM) that the calculation was written to support.

        • Affected Program - List the affected program or the program that reference is related to or part of. If the reference is FSAR, DBD or Reload (IASD or OPL), check Critical Reference column and check FSAR, DBD or Reload, as appropriate, on this form (above).

f If "yes," attach a copy of "VY Calculation Data" marked-up to reflect deletion (See Section 3.1.8 for Revision and 5.2.3.18 for CCNs).

VYAPF 0017.07 AP 0017 Rev. 7 Page 2 of 2

PA6 q OF Condensate Storage Tank Level (HPCI) Monitoring VYC-723 Rev. 3 CC. A)--o '

and the level transmitters are located on rack RK-25-66 inside an insulated and un-heated room attached to the side of the CST.. Th te e re mperatures Plant Area Minimum Maximum Condensate Storage Tank - t Instrument Rack 25-66 15eF Control Room - All areas 60 OF 80 OF 2.3.2. CST water minimum temperature is maintained Ž_50 OF (as read on Ti-1 07-3) per VY Procedure AP-0150, Auxiliary Operator Round Sheet TB/OUT, page 5 of 7 (Attachment M). The tank is heated by auxiliary steam heating coils. As a

  • conservative value for minimum temperature, the assumed value of 40°F froimn FSAR section 14.5.2 will be used [Ref. 6.2].

CST water maximum temperature is assumed equal to the maximum ambient temperature of 100 'F as identified in FSAR section 2.3.5 and on HPCI Process Diagram 5920-0784 [Ref. 6.29.1].

2.3.3. The calibration interval is assumed to occur once every quarter or 114 days (91.2 days + 25%).

2.3.4. The transmitter loops are calibrated quarterly and the test equipment temperatures will be bounded by the ambient temperatures extremes listed in Table 2 above. For the test equipment uncertainty evaluations performed under VYC-1 758 [Ref. 6.9, Attachment K], the RB RHR Cmr Rm 232' environment conservatively bounds the environment to be expected at the CST instrument room, and will therefore be used as representative of the CST instrument room.

2.3.5. The temperature variation within a cabinet is the same as the variation of the room in which it is located. The temperature difference between the room and the cabinet is therefore constant. Calibration data are assumed collected with the equipment at the operating temperature of the cabinet.

2.3.6. Review of the Vermont Yankee Environmental Qualification Program Manual (Ref. 6.7] indicates that none of the loop components covered by this calculation is environmentally qualified and are therefore only expected to operate under mild conditions, and negligible radiation exposure. Other than the pressure transmitters located at the tank enclosure, all loop components are located in the control room.

2.3.7. Calibration Tolerance is an output of this calculation, and will be based on the accuracy of the devices. The existing calibration tolerances shown in Tables 5 through 10 are for information only.

Vermont Yankee Design Engineering Page 10 of 28

Condensate Storage Tank Level (HPCI) Monitoring VYC-723 Rev. 3 considerations: t "

a) The analyzed drift data shows the 50% point to be the largest value at 1.2237% with the 0% value at 1.0625%, and the 100% point at 1.0604%.

The 50% analyzed drift value.is largest, and will be used as a conservative ddft value.

b) From review of this drift analysis and the histograms, the data exhibits a near-normal distribution for all points. As indicated in the time dependency discussion for the OP-4363 CST Level Computer Point Loop (Attachment L), some time dependency is exhibited at the 100% point However, the Significance F at all points is much greater than 0.05, indicating no correlation between drift magnitude and time interval. Since there is no indication of a drift to time relationship, the 114-day Analyzed Drift Term will be derived directly from the 82-day ADR term.

c) The average drift value for this group is -0.2293% at the 100% point, -

0.2163% at the 50% point, and --0.1580% at the 0% point. Since these values are all more than 0.08% (N *<40 and STDEV k 0.25%), this term must be considered as a significant bias term [REF. 6.11].

ADRv. = -0.2293%

d) The ERFIS loop ADR value for the operating cycle is calculated directly as follows:

1ADRll,4oys = ADRa2.oD = L 1.2237%

2.3.18. Given that Analyzed Drift (ADR) data is available for each of the loops and components evaluated under this calculation, and given that these loops and 7components will be evaluated for mild environmental conditions for the Control

'Room and CST (i.e. normal conditions), then it is assumed that the Analyzed 1Drift (ADR) term for each includes the Temperature Effect (TE), Readability.

(RD), M&TE Uncertainty (MTE), Barometric Pressure Effect (PB), Power Supply Voltage Effect (VE). Humidity Effect (HE), and Radiation Effect (RE) for ach of the associated loop components [Ref. 6.1 section 3.6.5] under both rmaal and accident conditions.

3. INPUT DATA used to calculate loop uncertainties, process corrections, setpoints, and decision points are tabulated below with the applicable reference or basis noted.
1. Process and Loop Data c dat ed to evaluate process corrections, decision points, and setpoint I.mitations are tabu a ed be I ap V/ItY e Design niiir 04o5ofA2 Pageo

-r. d.7= /I V-Vermont Yankee Design Eng'ineedng Page 14 of 28

vYc--723 g6V3 (f1C/o-o 3 PInse6rt

Condensate Storage Tank Level (HPCI) Monitoring VYC-723 Rev. 3 Table 3 PA- 7oF Process/Loop Inputs Basis Description Data Ref. 6.2 Section 14.5.2.3 & CST Water Temperature Minimum 40 OF Assumpt. 2.3.2 Ref. 6.2 section 2.3.5 & CST Water Temperature Maximum 100 OF Ref. 6.29.1 Ref. 6.10 (Attachment C) Process Limit (ITS/CTS) - 2!28.2" above CST1 bottom Critical height submergence (Vortexing) 20.0" above CST bottom 10,000 gallon reserve 8.2" above critical height TS 3.2.A & Table 3.2.1 Technical Specification Limit (CTS) Low CST Water Level Trip (HPCI auto suction transfer)

Ref. 6.10 (Attachment C) >_3% CST Volume VYC-723 Rev. 2 Attach. IX Lowest point credited for HPCI Suction 11.25" above CST bottom (Attachment B)

Ref. 6.30.2 Reference Elevation; floor at rack 25-66 El. 252' 6" VYC-723 Rev. 2 (Attach. B)' Transmitter Center Line El. 253'8' Ref. 6.30.2 Transmitter Sensing Tap Elevation El. 254' Ref. 6.3 Table 4.2.1 Calibration Test Interval Every 3 months (114 days) 3.2. Environmental Conditions The following information provides the environmental conditions expected for the components located at the Condensate Storage Tank and in the Main Control Room.

Table 4 Environmental Input Data Basis Description Data Ref. 6.2 Table 2.3.2 CST Area Ambient Temperature Extremes OF Assumption 2.3.1 CST Rack 25-66 Normal Ambient Temperatur - I85OF

ý"to Assumption 2.3.6 CST Rack 25-66 Accident Ambient Temp. o 00*-F Assumption 2.2.1 Control Room Normal Temperature 60 to 80°F Assumption 2.2.1 Control Room Accident Temperature 60 to 80°F 1 This limit includes consideration for the 10,000 gallon inventory requirements and the TS Limit of >_3%.

Critical height of submergence prevents introduction of air into HPCI suction prior to completion of transfer to suppression pool; includes consideration for CST Vortexing based on HPCI flow [See Attachment C].

Vermont Yankee Design Engineering. Page 15 of 28

Condensate Storage Tank Level (HPCI) Monitoring VYC-723 Rev. 3 C_.CA' -C*3 3.3. Transmitter LT-107-SA and LT-107-5B Data 1044 la Table 5 Transmitter Input Data Basis Description Data Ref. 6.21 & Minimum span 0 to 170 inches water Attachment E Maximum span (URL) 0 to 850 inches water Zero Suppr./Elevation 0% to 80% of range (URL)

Pressure Rating 2000 psig Over-Pressure Protect. Either direction to full pressure rating Output signal 10 to 50 mAdc into 0 to 5000 load Power Supply 52.5 (+/- 5%) volts DC Test Jacks Built in (10 to 50 mV full scale, lmV per mA)

Damping Adjustable - 4 positions Ref. 6.21 & Ambient temperature -20°F to +1 85 0 F Attachment E 'Maximum fluid temp. 250oF Vibration Up to I G in any direction for 25 to 120 Hz Sc Up to 0.03 inches peak-to-peak amplitude for 0-25 Hz Shock Will not be damaged by shocks up to 1O0G, any direction Humidity Not affected by MIL-F-5272 test (24-hour cycle, 680 F to 158°F at 100% relative humidity)

Ref. 6*2 Accuracy +/- 0.4% span (incl. Linearity, hysteresis, and repeatability)

Attach nt E Temperature effect + 1% span/100 0 F AT at 100% to 50% span

_ 1% to +/-_2% sparil00°F at 49% to 20% n K c1 .- Static Pressure effect Rated drift

+/- 0.4% span/500 psi at 100% to 50% spa.

+/- 0.4% to +/- 1% spanr1O00°Fn None given -7o Z

0 MIA) 0-1,17 S Ptk, n

/

Assump. 2.3.10 Power Supply Effect 0.1% span for 20 volt variati Assump. 2.3.10 Deadband Negligible Ref. 6.12 Existing Input Span 4.0 to 394.0 inches water Existing Output span 10.00 to 50.00 madc Ref. 6.12, Existing Cal Tolerance +/- 0.2 mV Assump. 2.3.6 Radiation effect N/A Assump. 2.3.10 Seismic Effect +/- 0.5% span Assump. 2.3.10 Analyzed Drift (DA) 0.649%

p Page 16 of 28 Vermont Yankee Veftont Engineering Design Engineering Yankee Design Page 16 of 28

Condensate Storage Tank Level (HPCI) Monitoring VYG-723 Rev. 3 CCA) -0 3 3.9. Calibration M&TE Input Data A46 9W.,p

) Table 11 Calibration M&TE Input Data Basis Description Range Resolution, Accuracy Accuracy

(% Rdg or Span) (Calibr. Units)

Attachment K HP 34401A 100 mVdc 0.0001 mVdc 0.0216% rdg 0.010817 DMM @ 50 mVdc mVdc Attachment K HP 3466 200 mVdc 0.01 mVdc 0.1095% rdg 0.0547 DMM @ 50 mVdc mVdc Attachment K Heise 901 B 0 - 400" H20 0.01 -H20 0.1449% span 0.5797" H20 Attach. K & M Heise 901B 0 - 1000" H20 0.1 -H20 0.1452% span 1.4524- H20 Attach. K & M Heise CMM. 0 - 800" H20 1.0 'H20 0.1616% span 1.2925" H20 Attach. K & M Heise CMM 0 - 830" H20 1.0 "H2 0 0.1613% span 1.3391" H20 Attach. K & M Heise -100- 860" H20 0.1 "H20 0.1691% span 1.6236" H20 730A-03

4. CALCULATION DETAIL The detailed calculation of loop uncertainties, setpoints, testing tolerances, and margins have been performed using MathCad and are documented as Attachment D.
5. RESULTS AND CONCLUSIONS 5.1. Total Loop Uncertainty Total Loop Uncertainties (FLU) have been evaluated for the HPCI CST Level indication, trip, recorder, and ERFIS Loops and the results are presented in Table 12 below.

Table 12 Total Loop Uncertainty Loop TLU TLU TLU TLU Normal Normal Accident Accident CQat1 it s .A + Cal Unit.

Irs LT-107-5A/B / LSL-1 07-5A/B Trip A3-0-.M-Vdc -J/ GUA FnVdc,ý LT-107-5A / LI-107-5 Indicator ,/  % 1 A

LT-107-5 / LR-23-73 I7 Recorder 1 .. Ka, LT-107-SA /ERFIS F004 '!--...---.* I ag,%'Kgal-' /.,-NN/-X"-

Vermont Yankee Design Engineering Page 21 of 28

Condensate Storage Tank Level (HPCI) Monitoring VYC-723 Rev. 3 cc$J0ý3 5.2. Setpoint Evaluation /0A(c 10 O~F I

5.2.1. Current Low Level Suction Transfer setpoint As evaluated in Attachment D, section 5.2. the existing Low Level suction transfer setpoint of 12.1 mVdc cannot be supported based on the new requirements for critical height of submergence of the HPCI suction. The revised Process Limit of 2_28.2" from CST bottom [Ref. 6.10 and Attachment C]

includes consideration for the TS requirement that the setpoint be > 3% and that there be 10,000 gallons reserve at the suction transfer point See Table 13 below.

5.2.2. Revised Low Level Suction Transfer setpoint A revised setpoint is evaluated in Attachment D, section 5.3; the proposed setpoint of 12.2 mVdc decreasing supports the requirements for critical height of submergence of the HPCI suction + 10,000 gallon reserve and has adequate margin from LSP to SP. See Table 13 below.

Table 13 Setpoint Results

/

5.3. Calibration and Test Results In order to support and implement the results of this calculation, the loop instruments are to be calibrated at nine points based on the following ranges:

10 Referenced to tank bottom.

1 As sensed by transmitter, level above transmitter tap (0") plus 4' static head.

Vermont Yankee Design Engineering Page 22 of 28

Condensate Storage Tank Level (HPCI) Monitoring VYC-723 Rev. 3 Table 14 10,466 /1 oF Module Calibration Ranges Description Value Units Transmitter input range 4 to 394 Inches H20 Transmitter output range 10.0 to 50.0 mVdc12 Indicator input range 10.0 to 50.0 rmAdc Indicator output range 0 to 100  %

Alarm Unit input range 1.0 to 5.0 Vdc Alarm Unit Lo Setpoint (CST LEVEL LO) 12.2 decrV mVdc Alarm Unit Lo-Lo Setpoint (INST PWR TRBL) 10.2 decr mVdc Recorder input range I to 5 Vdc Recorder output indication range 0 to 100  %

',Computer input range 16 to 80 mVdc1 3 Computer output indication range 0 to 477.1 Kgal Test as-found tolerances (FT) and as-left tolerances (CT) are shown below.

Table 15 Module Calibration Tolerances Device Tag No. , 14 As Left (CT) ký% +/- al Units ++/-%CS +/-Cal Units Transmitter LT-107-5A, B 05 0."mVdc 0.20 mVdc Alarm Unit LSL-107-SA &B 0.60

"- 0. rndc 0.50 ,,' 0.20 mVdc Indicator LI-107-5 N/A N/A 2.0 / 2.0 %

Recorder LR-23-73 N/A N/A 1.0 ' 1.0 %

Computer F004 N/A N/A 0.545./ 2.6 Kgal Point 12 10-50 mAdc through a 1Q transmitter test resistor.

13 10-50 mAdc through a precision 160Q resistor.

14 Module As-Found values provided for alarm unit and transmitter because all other components are Cali-bration Checked as loops per Ref. 6.12; LSL-107-5A & B tested as modules only per Ref. 6.12 (Attach. M).

15 'As-found and As-left tolerances appty to both setpoints of each alarm unit.

Vermont Yankee Design Engineering Page 23 of 28

Condensate Storage Tank Level (HPCI) Monitoring VYC-723 Rev. 3 c C..- a 3 6.30.2. Drawing G-191261 Sheet 65B, "Tank Level Instrument Hookups," Rev. 6.

6.30.3.Drawing B-191260, Sheets 107.1, 111.6, 111.19. and 112.26, Vermont Yankee Instrument List, (Superseded by MPAC).

6.31. International Instruments Test Report #SBI-3, "Seismic Qualification Test Report for Indicating Control Instrument Model 9270 and Meter Models 1122, 1136, 1151," Rev.

1, -February 10, 1976, (Excerpts - Attachment G).

6.32. "ASME Steam Tables," Thermodynamic and Transport Properties of Steam, Sixth Edition, 1993.

6.33. VYI 92/97, "Application of CT, CE and A for Single Point Devices, Rev. 1," Memo from Vermont Yankee Design Engineering Page 28 of 28

eA&t C_C.AN -1so'5or-VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Page 6 of 43 Transmitters MTE uncertainty is included in the MTE I-:= 0.O.inWC MTE 1= 0.Oo-inWC / Loop or Module Drift term (Assumption 2.3.18).

3.2.1.5 Drift (DA)

DA . 0.649% CS DA 1 = 2.531 oinWC . Transmitter analyzed drift (Assumption 2.3.10 and Attachment P).

Temperature effect during normal and accident conditions are the same and included in the Loop or Module Drift term (Assumption 2.3.18). Normal AT of 30oF is included in Loop or module ADR since uart_ e" al a 3.2.1.7 Barometric Pressure Effect (PB)

The GE 555 is a differential pressure transmitter Barometric pressure effect is either the effecton the vented side of gage pressure monitoring a tank vented to atmosphere, therefore this effect is negligible per Ref. 6.1 section 3.6.8.

transmitters, or the error associated with calibration of,an absolute pressure transmitter using gauge pressure test instruments.

PB 1 := 0.inWC 3.2.1.8 Humidity Effect (HE)

Humidity effect during normal and accident HE I := 0.inWO conditions are the same and included in the Loop or Module Drift term (Assumption 2.3.18)

VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Page 7 of 43 3.2.1.9 Radiation Effect (RE)

RE31 = REn1 = 0.0 inWC Radiation effect during normal and accident conditions are the same and included in the Loop RE 1 := 0.OInWC RE 1 = 0.000 -inWC / or Module Drift term (Assumption 2.3.18) 3.2.1.10 Seismic Effect (SE)

SE I := 0.5.%.CS SE I = 1.950 oinWC / Assum pti on 2.3.10 3.2.1.11 Process Pressure Effects (SP)

SP 1 := 0.0.inWC SP I = 0,000 inWC / Since the maximum pressure felt by the transmitter is 394 inWC+ ambient pressure, static pressure and over- pressure effects and corrections for this application are not applicable Power Supply Voltage Effect during normal and 3.2.1.12 Power Supply Voltage Effect (VE) accident conditions are the same and included In the Loop or Module Drift term (Assumption 2.3,18)

VE I := 0.0 inWC VE I = 0.00Oo InWC /

3.2.2 Transmitter Total Module Uncertainty 3.2.2.1 Normal Conditions CE I = 1.$50 ,inWC DB 1 = 0.000 cinWC Since MT , HE, RE and VE are all 2 included in'tAnalyzed Drift term (Assumption enlR CEE 1 +E 2.3.18) and SP = 0.

Normal transmitter module uncertainty (8,1 R)for e nIR 4-9WinWC calibration every 3 months (114 days)

P,466- 4Sc~

VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Page 8 of 43 3.2.2.2 Testing Conditions r, I'Since MTE, P ,P*P E, RE and VE are all included In the'A<-fyzed Drift term (Assumption e tIR ý= 2.3.18) and SP = 0.

Testing transmitter module uncertainty (et1R) for

-tiR = - inW calibration every 3 months (114 days) 3.2.2.3 Accident - LOCA (small break) with Seismic &

CE 1 = 1.950oainWC DB 1 = 0.000 ,inWC SE i =

)Since MTE, P, E, RE and VE are all included in the-k llyzed Drift term (Assumption a al R := GCE 2 t C 2.3.18), SP = 0, and mild environments.

1 Accident transmitter module uncertainty (ealR) for calibration every 3 months (114 days)

VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Page 26 of 43 4.0 Total Loop Uncertainty 4.1 CST Alarm Unit Auto Suction Transfer Trip TLU ( LT-107-5A.& B, LSL- 07-5A & B) 4.1.1 Normal Conditions 4.1.1.1 Random DA 1 ;= 0.649.%,CS DA j = 2.531 ,inWC O/ Transmitter Analyzed Drift Term (Assumption 2.3.10 and Attachment P) e ni j9 7 C Transmitter normal uncertainty from section 3.2L2.1 e n2R 2,412 °JnWC Alarm Unit normal uncertainty from section 3.3.2.1 includes Analyzed Drift UnR12:= eniR2.1-en2R2+ .DA 12 / UnRI2t4--in C V/ Normal Random Uncertainty for alarm unit loop with quarterly calibration.

4.1.1.2 Bias

%Level, PM negn PMPMpos n From section 2.0. magnitude of bias depends on

.n inWC point of interest inWC inWC 0LI -0.020 / S4.0 !0.-007

-0.506 / 1101.5 0.19-'0 ,

-0.9921, 0,372 ,-/

1'--]/ PM bias := 0.190,inWC For alarm unit actuation on decreasing level, A-1.478-- 0.554- positive bias is limiting (sensed level higher 975.01 - 1.9641/ R296.5 10.0 than actual). The process temperature bias is U nB12,.pos := PM bias conservatively chosen at the 25% span point with the setpoint expected to be less than 10%

(25 inWC setpoint/390 inWC span).

U nB12.pos = 0.190=inWC 4.1.1.3 Normal Total Loop Uncertainty U n12 U nR12 + U nB12_pos Unl 4.493-in r Normal TLU in inWC

C....C,* -A)

VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Page 27 of 43 4.1.2 Testing Conditions e t2R = 2.412oinWC Alarm Unit test uncertainty from section 3.3.2.2 includes Analyzed Drift U tR2 := e t2R U tR2 = 2.412°1nWC / Testing Random Uncertainty for alarm unit with quarterly calibration. Alarm unit is calibrated as a module rather than as loop. Transmitter output is varied until trip and mV Input to trip unit is measured and recorded at trip point.

4.1.2.1 Testing Total Loop Uncertainty U t2 " U tR2 U t2 = 2.412°inWC / Testing TLU in inWC, There are no bias terms associated with testing conditions.

4.1.3 Accident - Small Break LOCA with Seismic 4.1.3.1 Random DA 1...2.a4 On= Transmitter Analyzed Drift Term (Section Assumption 2.3.14) eal C Transmitter accident uncertainty from section 3.2.2.3 e a2R 2.412 ,inWC Alarm Unit accident uncertainty from section 3.3.2.3 includes Analyzed Drift U aR12 := ,JealR2 + e a2R2 + DA 12 / U aRl2 -4.45 in 7 Accident Random Uncertainty for alarm unit loop with quarterly calibration.

Pd-+'4d 19 0F VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level LHPCI) Monitoring IPage 28 of 43 O.

C. ..- Bas 4.1.3.2 Sias

%Level, PM neg, Ln PM pose From section 2.0. magnitude of bias depends on point of interest 0 0/] inWC inWC 4.0 inWC 0.007 0.t9-0

-0.5061

-0.9921 ./ 199.0 Iý-=

0,372 1, 0554 PM bias ;= 0.190inWC For alarm unit actuation on decreasing level, positive bias is limiting (sensed level higher 175.0 N0.

-1.478

- 1.964J S394.01 z.3 than actual). The process temperature bias is q===.,m U aB12..pos :=PM bias conservatively chosen at the 25% span point with the setpoint expected to be less than 10%

U aB12_pos = 0.190einWC (25 inWC setpointl390 inWC span).

4.1.3.3 Accident Total Loop-Uncertainty Ua12 := U aR12 + U aB12_pos U V Accident TLU in inWC 4.2 CST Indication Loop TLU ( LT-107-SA, LU-107-5) 4.2.1 Normal Conditions 4.2.1.1 Random DA 13 1,32.%-CS DA 13 777 Indicator Loop Analyzed Drift Term (Assumption 2.3.15) eniR Transmitter normal uncertainty from section 3.2.2.1 e n3R 7.800 oinWC Indicator normal uncertainty from section 3.4.2.1 2 2 U nR13 :2Je nlR i-e n3R + DA 132 Z UnR 1 Normal Random Uncertainty for indicator loop with quarterly calibration.

VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Page 29 of 43 4.2.1.2 Bias

%Level n PM neg Ln PM posn From section 2.0. magnitude of bias depends on InWC point of interest

% inWC inWC 4.0 0.007 25.0 - 0.5061.

-0.992 /

50.0 0.372 129160.50 U nB13._neg: PMneg, For the indication function, both positive and 75.0 T5/

1T0700 -1.9641 394.0 Lo.731 U nB13_.pos, negative bias at all points are considered.

PM posn 4.2.1.3 Normal Total Loop Uncertainty U nR13n:= U nR13 Normal Random uncertainty term Un13-pos :=U' nRI3nt-UnB13.._posn I " Normal positive TLU with bias Un13..neg (U nR13 n)(1) +U nB13.neg, Normal negative TLU with bias U nB13_pos U n13.negq U n13_posn n inWC "02 14 0.3 ,

0.554/

/ U n13 The bounding normal TLU d4 4j C is conservatively chosen for all ph64e*

PACDA.

r- N "ZOoF I - O'sb VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Page 30 of 43 4.2.2 Loop Testing Conditions DA 3 =7.0 oinWC Indicator Loop Analyzed Drift Term (Assumption 2.3.15)

Transmitter test uncertainty from section 3.2.2.2 sat3R 7.800 ainWC Indicator test uncertainty from section 3.4.2.2 U tR13:= e1R2t3 o oA 2 UtR Testing Random Uncertainty, for indicator loop with -quarterly calibration.

4.2,2.1 Testing Total Loop Uncertainty (

U t13 := U tR13 7 Testing TLU in inWC. There are no bias terms associated with testing conditions.

4.2.3 Accident - Small Break LOCA with Seismic 4.2.3.1 Random DA1 3 73 oInWC Indicator Loop Analyzed Drift Term (Assumption 2.3.15) ealR* Transmitter accident uncertainty from section 3.2.2.3 e a3R 7.800 =inWC Indicator accident uncertainty from section 3.4.2.3 U aR13 : je alR2 + e a3R2 i DA 1 3' U aR13 I WC Accident Random Uncertainty for indicator loop 11.618 with quarterly calibration.

MCGt 24 oP C- C /N- 0'!

VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Page 31 of 43 4.2.3.2 Bias

%Level PM negn L PM posn From section 2.0, magnitude of bias depends on inWC point of interest inWC inWC -i 0 -0020 0.007 76 F10o]

5 0. 0 34.01 1-1 1-1.478!. U aB13.negn: PM negn For the indication function, both positive and n;75.0 -1.9649,' negative bias at all points are considered.

E0.73 U aBI3 posn PM posn 4.2.3.3 Accident Total Loop Uncertainty U aR13 U aR13 Accident Random uncertainty term Ua13_posn :=UaR13 n U aB13_posn / Accident positive TLU with bias U a13_neg,:= (U aR13n)'(-1) t U aB13..negn " Accident negative TLU with bias

%Level, U aR13 U aB13...neg,, U a13_.pos U a13_-negn U a13_-posn In n 0 inWC. bnWCo"ainT fa C

-0.020 T 25.-0 -0.50

-j~

0.9 0.736 1424 i

-147

/ U a1L3 13.3ýnWC The ar bounding accident TL.for servatively chosen for all is

cc, . - <o5 VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Page 32 of 43 4.3 CST Recorder Loop TLU ( LT-107-5B, LR-23-73) 4,3.1 Normal Conditions 4.3.1.1 Random DA 14:= 0.9709,%,CS DA 14 = 3.787 -InWC Recorder Loop Analyzed Drift Term (Assumption 2.3.16) e nIR Transmitter normal uncertainty from section 3.2.2.1 e n4R = 3.900 'InWC Recorder normal uncertainty from section 3.5.2.1 U nR14 je nlR2 +e n4R2 + DA 142 '/ U nR14 6-7761CC Normal Random Uncertainty for recorder loop G OC( with quarterly calibration.

4.3.1.2 Bias

%Leveln PM negn Ln PM posn From section 2.0. magnitude of bias depends on point of interest inWC inWC inWC 0 4.o /

0.00 25.0 79-9.0 0.372 o, R750 U nB14._negn:= PM neg, For the recorder indication function, both 1478 o, positive and negative bias at all points are

.1 -/ 3t94.00 90.55,4, considered.

U nB14_posn :- PM posn 4.3.1.3 Normal Total Loop Uncertainty U nR14 '2 U nR14 Normal Random uncertainty term U nl 4_pOSn:= U nR14 1 U n1t4..pos / Normal positive TLU with bias

VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Paqe 33 of 43 U n14_negn: (U nR14n)'(-1) + U nB14_negn Normal negative TLU with bias U nR14n U nBt4_posn n inWC /

0.0 T

U The bounding normal TLU aj-l9-ind is conservatively chosen for alt .n&-

4.3.2 Loop Testing Conditions DA j oinWC Recorder Loop Analyzed Drift Term (Assumption 2.3.16) e tIRAC Transmitter test uncertainty from section 3.2.2.2 eGt4R = 3.9OinWC Recorder test uncertainty from section 3.5.2.2 UtR14 je tlR 2 + e t4R2 + DA 142 / UtRI4 S'oi Testing Random Uncertainty for recorder loop with quarterly calibration.

4.3.2.1 Testing Total Loop Uncertainty U t14 := U tR14 Testing TL.U in inWC. There are no bias terms associated with testing conditions.

PA&6 ?# oF VYC-723 Rev. 3 ATTACHMENT D . Calculagion Detail

.Page 34 of 43 CST Level (HPCI) Monitoring 4.3.3 Accident - Small Break LOCA with Seismic 4.3.3.1 Random DA 14A 3.787 4inWC Recorder Loop Analyzed Drift Term

.(Assumption 2.3.16)

Transmitter accident uncertainty from section 3.2.2.3 e a4R = 4.875 'inWC Recorder accident uncertainty from section 3.5.2.3 U aR`14j.e aiR1a4R +DA 4 ~ UaRI .8 8IDWC, Accident Random Uncertainty for recorder loop with quarterly calibration.

4.3.3.2 Bias

%Leveln PM negn Ln PM posn From section 2.0, magnitude of bias depends on point of interest

% inWC InWC in-C 250 0.00 2.__T5

-65o 7-0.o06201.

66 oo1.

.195 50.0 / 99 9

T9-0 0 V U aB14.negn= PM nagn For the indication function, both positive and 75."-0 -1478 ./ 29.5 0.5 negative bias at all points are considered.

oo.-'

ýn [64 1 3-94/ 7- U aB14_pos: PM posn 4.3.3.3 Accident Total Loop Uncertainty U aR14 n U aR14 Accident Random uncertainty term U aI4_ppos n U aR14n +U aBI4_pos n Accident positive TLU with bias U a14..negn (UaR14,)'(-) + U aB14..neg~ Accident negative TLU with bias

VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Page 35 of 43

%Leveln UaR14n UaB14_.neg n UaBi4...pos, U a14...neg, U a14_posn n %Win 0 250 6.76f a -0.5020.

2 50.0 671 -. 9 in14 C.o The bounding accident TLU '-&-TM25 iC is conservatively chosen for all pi i4 4.4 CST ERFIS Loop TLU ( LT-107-5A, F004) 4.4.1 Normal Conditions 4.4.1.1 Random DA 15:= 1.2237'%'CS DA 15 442Z2 -nWC ERFIS Loop Analyzed Drift Term (Assumption 2.3.17)

Transmitter normal uncertainty from section 3.2.2.1 en5 2,125 ainWC ERFIS normal uncertainty from section 3.6.2,1 U nRI5S::2 enlR 2 +e nR2+ DA 155 / UnRI = &6?frcin C Normal Random Uncertainty for ERFIS loop with quarterly calibration.

PA, F.7.& Or-VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Page 37 of 43

%Level, U nRI5 U nBl5_nega U nB15S_pos, U n15ineg, Y nI5-.pos n n

0

-T The bounding normal TL 2.419 Cs conservatively chosen for all'poits.

4.4.2 Loop Testing Conditions DA 1 5 72i-nWC ERFIS Loop Analyzed Drift Term (Assumption 2.3.17) e tliC Transmitter test uncertainty from section 3.2.2.2 e t5R 2.125 oinWC ERFIS test uncertainty from section 3.6.2.2 UtR15 :=,4e t1 R2 e t5R2- DA 152 / Testing Random Uncertainty for ERFS loop with quarterly calibration.

4.4.2.1 Testing Total Loop Uncertainty DA bias 0-.2293 %.CS DAbia . 4 inWC Bias associated with Analyzed Drift (Assumption 2.3.17) 4u -.inWJ U ti5:= UtR1 5 Testing TLU in inWC. DAblas term is applicable for testing conditions, however, DAbrS term is omitted from Ut,, equation for conservatism.

4.4.3 Accident - Small Break LOCA with Seismic Accident conditions are N/A for ERF'IS

PA-.,PP 7 O2 VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Page 38 of 43 4.5 Summary of Results 4.5.1 Module As-Found (FT)I As-Left (CT) Calibration Tolerances DA =2.531 *!nWC Transmitter Analyzed Drift Term (Assumption 2.3.10) e ti -M- Transmitter test uncertainty from section 3.2.2.2 U ti -= etlR + DA 1 2 2

/ ~Ut.j C~es Testing Random Uncertainty for transmitter module with quarterly calibration.

Component FTinWC) FT (Calibr. Units_ CT (inWC) CT (Calibration Units)

Transmitter 3 /CT-. 1 40.mV = 0.200 -mV ut,-40.

CS mV* CT 1.950 oinW CS LT-1 07-SA & B

,/

40mV0.47.m

/ r2 mV=

Alarm Unit U t2 = 2.412 'inWC CT 2 =1.950 -inWC 0.200,mV LSL-107-5A & B CS CS CT 3 Indicator CT 3 = 7.800 -inWC / 2.000.% /

N/A NIA CS U-107-5 CT=

CT 4 Recorder N/A N/A CT 4 = 3.900 oinWC /

CS 1.000-% Z LR-23-73 (Green)

ERFIS F004 N/A NIA CT =2.13 inWC CT. 4 7 7 .1.K.gal = 2.600oK, gal /

CS Note: The Transmitters and Alarm Units are the only devices calibration checked as modules rather than as a loop under OP-4383 (Attachment M).

rA&c Z9 or-CC-) -OS ATTACHMENT D Calculation Detail VYC-723 Rev. 3 Page 39 of 43 CST Level (HPCI) Monitoring 4.5.2 Loop As-Found Calibration Tolerances (FT)

Loop FT (inWC) FT (Calibration Units)

N/A Alarm Unit is calibrated as a module rather than as Alarm Unit Trip a loop (See section 4A1.2 and Attach. M page 6)

(LSL-107-5A & B) N/

1. 3S2.

Indicator U t13 U-+e3inWC (LI-107-5)

Recorder Indication U ti =-5.M inWC (LR-27-73 Green Pen) 6_4 76 ERFIS Indication U t1 C'55 oinWC (F004) 4.5.3 Loop As-Left Calibration Tolerances (CT)

Transmitter CT from section 3.2 CT 1 = 1.950 oInWC Indicator CT from section 3.4 CT 3 = 7.800 oinWC Recorder CT from section 3.5 CT 4 = 3.900 oinWC ERFIS CT from section 3.6 CT 5 = 2.125 °inWC 2 2 CT loop13 = 8.040 ,inWC Indicator Loop CT in inWC CT 1oop 13 := ýCT 1 1-CT 3 2 CT loop14 = 4.360 °inWC Recorder Loop CT in inWC OT loo1 4 :2 JCT 12 t*CT 4

ýCT 1 2 +CT f)/2 CT loopiS = 2.884 -inWC ERFIS Loop CT in InWC OT 1oo` 5 :t

C.c./'- o3 VYC-723 Rev. 3 ATTACHMENT D Calculation Detail CST Level (HPCI) Monitoring Page 40 of 43 4.5.3.1 Loop As-Left Calibration Tolerances (CT)

Loop CT (inWC) CT (Calibration Units)

Alarm Unit is calibrated as a module rather than Alarm Unit Trip N/A N/A as a loop (See section 4.1.2 and Attach. M page (LSL-1 07-SA & B) 6)

CT loop13 2.062-%0/

Indicator CT loop13= 8.040 .inWC (LI-I07-5) CS CT loopl4 - 1.1184%

Recorder Indication CT loop14 = 4.360 oinWC (LR-27-73 Green Pen) CS 1 CT= oP .118 .29K ga ERFIS Indication CT loop15 = 2.884.inWC ,S .1 .Kgal =3.529 ,K*gal 47 (F004) 4.5.4 Normal/Accident Total Loop Uncertainty (TLU)

Loopi Alarm Unit Trip (LSL-107-5A & B)

Indicator (L-4 07-5)

Recorder Indication (LR-27-73 Green Pen) 8.745- Un15 U 'O0".1 ERFIS Indication 9484al-nWC .~477.1-K gal = 49.84 -K -galv (F004) Cs

'3 VYC-723 Rev. 3 ATTACHMENT D Calculation Deta il CST Level (HPCI) Monitoring Page 42 of 4 3 SP 10mV)390.,rin t L 2 SP 32.475 -in Current setpoint referenced to tank bottom.

40.mV It should be noted that the previously calculated setpolnt did not consider the requirement for minimum-height of submergence due to the effects of potential vortexing within the CST; in addition, the calculated TLU used in the setpoint determination was +1-8".

5.2 Evaluation of Current Setpoint (12.1mV = 32.475 InWC above tank bottom) 5.2.1 Current Tech Specs (CTS)I Improved Tech Specs (ITS) - Quarterly Testing LSP = Process limit + TLU (accident) L5 + U0 12 M1 SP - LSP SP = 32.475 min U 2 4.648 lnW9 LSP:= Li Ua12 LS + -- in

.=L5 SP3.W-n inWC M 1 :=SP-LSP ,/ -a'n 5.2.12

Conclusion:

The current setpolnt of 12.1 mV is not acceptable because it does not support the minimum level requirement of> 28.2" above tank bottom [Ref. 6.10 & Attachment C] plus alarm Unit TLU with positive margin from the SP to the LSP.

Requirement, Required Level LSP Current-Setpoint MarM:L- P Process Limit > 28.2" above bottom / LS~ 32-048--in2¶ L SP = 32.475 -in 7.3a M/tr~8in\

c cA)-c 3 VYC-723 Rev. 3 ATTACHMENT D Calculation De tail CST Level (HPCI) Monitoring Page 43 ol 43 5.3 Evaluation of Revised Setpoint 5.3.1 Current Tech Specs (CTS)l Improved Tech Specs (ITS) - Quarterly Testing An value of 33.45" (equal to 12.2 mV) is chosen as a proposed new setpoint such that it is larger than the minimum level requirement (with uncertainties).

LSP = Process limit + TLU (accident) = L5 + U,12 M1 = SP - LSP SP 33.45.in SP 33.450 tin Proposed new setpoint referenced to tank bottom Process Limit referenced to bottom of L 5 =2O-t~

tank Accident Alarm Unit TLU from section Ual ~4-f64-fln C 4.1.3.3 Ua 12 /5 inWC M1 :=SP-LSP/ M Setpoint Margin for proposed setpoint 5.3.2 Determination of calibration setpoint value SD cat := In. SP cal = 25.450 ,inWC / New calibration setpoint In inWC as sensed by the transmitter SID m-: I 240.mVY t 10mV SP mv = 12.200 omV New calibration setpoint in mV as 390- in , measure transmitter output 5.3.3

Conclusion:

The revised setpoint of 12.2 mV is acceptable because it is higher than the Limiting Setpoint by a Margi f Reguirement, Required Level S New Setpoint 61r3]tE"P, Process Limit > 28.2" above bottom (LJ) /'2L-64In SP= 33.450, o / MA-in

"11-23-98 01:09PM I UL VYC-7Z3 £Ev3 eC-,O-0 A4CF6 '3tZor-VERMONT YANKEE SETFOINT CONTROL PROGRAM INTERDEPARTMVENTAL REVIEW OF CALCULATION:

Anc--

VYC- 723 Revision 3 VYC-723 Revision 3. has been prepared and independently reviewed. The Departments impacted by this calculation are requested to review the results of this calculation, concur with the results and/or recommendations, ezd document the department's acceptance prior to the calculation being approved.

1. Summary! This calculation evaluates the uncertainty for the Kigh Pressure Coolant Injection (1-lPCf) System Auto Suction Transfor on Low CST Level as well as CST Leval Indication Loon frnrormal and PkiAccident.CSTLevel Recorder Lo2 and CST ERFIS Indication Loop. The loop components evaluated are as follows:

'LT-107-SA & B, LSL- 107-5A & B, LI-1 07-5, LR-23-73, and ERFIS PTID F004

2. Q1,2WP&n oen ItMs.'! AP-0028 to be Asslead 2.1. Approval of Dlrft Calculation Memo for GE 555 Transmitters LT.107-SA & B:-,

used as design input for Assumptlon 2.3.10 and Included as Attach. P. o.Zt.,3Yvq j 7

3. Department Review - contact the Setpoint Program Manager (G.Ifrngzrn if not In agreement with the eonclusions/statemcnts.

3.1. Vcrmont Yankee E&C 3.1.a. The Calibration Sections rofP-4363 for LT-107-SA & B-. LSI.l07-SA & B. UL-07-5. LR-23-73. and ElBISIPTa F004 will require the following changes based on CTS/ITS and quarterly calibrations:

3.1,a. Procedure OP-4363 Revision 24 will require the following changes (changes based on Custom Technical Spclflcatlon/standard suryelliance cycle):

I. Add the folloWing In the procedure discussion.

a. LjmitingSspoint (LSP): . 1 - 80 LSL-107-SA & B Low Level Suction Transfer ..--J iVDC (3*-2.6 inche LSL-107-SA & B Low-Lo vet N IA Referenced to Tank BotI 244 inches ap a r)
b. Module As Found values: E'mr 11122 Transmitter LT-107-5A & B d: 0.2mVDC.

Alarm Unit LSL-I07-SA & B (Lo & Lo-Lo) & 0.2mVDC In dicator Il-107-5 Ara No Chane Recorder LR-23-73 No Change ERFIS PTID F004 *26ka

e. Loop As Found values: Erom "NoChann-Indicator LT-107-SA to LI-107-S Recorder LT-107-SB to LR-23-73 A:2,S-G ERFIS LT-107-SA to ERFIS F004
d. Head correction to remain at:
e. Revise the M&Th requirements of OP-4363 to remove the Heise 730A-03.

The following test equipment (or equivalent) is recommended fbr use:

Gauge Heise 901B (0-400 inwc)

DMM HP 34401A (0-100mV Range)

2. In the body of the procedure and the data sheet revise as follows!

Page __ of VY CALCULATION REVIEW FORM Calculation Number- VYC-0723 Revision Number. 3 CCN Number: 03

Title:

CONDENSATE STORAGE TANK LEVEL (TPCI) MONITORING Reviewer Assigned:J6fc.k.4 Required Date:

C Interdiscipline Review 2ldependent Review. VYC-0723, Rev. 3 CCN-03 Page 33 of Comments* Resolution I

jlethodReviewer Signature - dLate of Review: 13 Calculation/Analysis Review Calculation Preparer (Comments Resolved). Date o Alternative Calculation /

ol Qualification Testing Reviewer Signature (Comments Resolved) Date

  • Comments shall be specific, not general. Do not list questions or suggestions unless suggesting wording to ensure the correct interpretation of issues. Questions should be asked of the preparer directly.

VYAPF 0017.04 AP 0017 Rev. 7 Page 1 of 1

Docket 50-271 BVY 09-009 Attachment 4 Technical Specification Proposed Change No. 273, Supplement 7 Vermont Yankee Nuclear Power Station Applicable Portions of Station Procedures

VERMONT YANKEE NUCLEAR POWER STATION

~w..4'rnttrflr,.,%rrnr~rnr9 ~ ~

y ~

OP 4363 REVISION 27 HPCI SUCTION TRANSFER ON CONDENSATE STORAGE TANK (CST)

LOW LEVEL FUNCTIONAL TEST AND CST LEVEL INSTRUMENTATION CALIBRATION USE CLASSIFICATION: CONTINUOUS LPC Effective No. Date Affected Pages T TN C0 N,'"ROLLE, K D.

For lnf0rmRtl0U C'gy-IImplementation Statement: N/A I Issue Date: 09/30/03 OP 4363 Rev. 27 Page 1 of 21

TABLE OF CONTENTS PURPOSE ............................................................... 3 DISCUSSION ............................................................. 3 ATTACHMENTS .......................................................... 5 QA REQUIREM ENTS CROSS REFERENCE ............................................................................................... 5 REFERENCES AND COMMITMENTS 5.........................

PRECAUTIONS/LIMITATIONS ................................................ 6 PRE RE QUISITES .............................. . . . ........................................................................................................... 6 PROCEDURE.... ................................................. 7 A. Functional ..................................................... 7 B. Calibration 12 A CC EPTAN C E CR ITE RIA ......................................................................................................................... 21 FINAL CONDITIONS ........ .............................................................................................................. 21 OP 4363 Rev. 27 Page 2 of 21

PURPOSE To provide Instrument and Control Department personnel with approved methods of functionally testing the HIPCI suction valves auto transfer, calibrating the CST level transmitter loops and calibrating other associated CST level instruments.

Performance of the Functional section of this procedure satisfies the Functional Test requirements as specified by the following Technical Specifications:

Table 4.2.1 for the HPCI Low Condensate Storage Tank Water Level.

Performance of the Calibration section of this procedure satisfies the Calibration and Functional Test requirements as specified by the following Technical Specifications:

Table 4.2.1 for the HIPCI Low Condensate Storage Tank Water Level.

DISCUSSION The CST level transmitters and associated loop instruments provide information on water level in the CST. This level information is used to automatically shift the HPCI suction valves from the CST to the torus in the event of a low CST level signal, provide level indication in the Control Room and provide CST low level and instrument loop trouble annunciation in the Control Room.

Additionally, CST Hi and Low level pressure switches and a local indicator are also tapped off of the sensing lines to the transmitters and are calibrated per this procedure.

Calibration of these instruments do not satisfy any T.S related surveillance.

This procedure shall be accomplished by using Measuring and Test Equipment to inject pressure signals as required for the instrument(s) being tested.

The CST water level instruments tested by this procedure are listed in Table 1 below.

Calibration of LSH-107-6, LSL-107-7 and LI-107-6 is not being performed as part of any Technical Specification requirements.

The level transmitter has a positive 4" H2 0 head applied at all times due to the transmitter being located below the instrument tap. The tap is located at an elevation of 254' and the transmitter centerline is located at 253'8".

OP 4363 Rev. 27 Page 3 of 21

SURVEILLANCE SETPOINT CRITERIA Instrument Measured Tech S1ec VY Trip Number Parameter Action Setting . SettinLg LSL-107-5A/B CST Level Transfer HPCI Suction Valves >3% 11.2mV

  • 12.2 -0.2mV Auto Transfer & Annun 9-3-S-4 LSL-107-5A/B CST Level Annun 9-3-T-9 NA 10.2 +/-0.2mV LSH-107-6 CST Level Annun 9-6-H-7 NA 359 +/-3 in.,

LSL-107-7 CST Level Annun 9-6-H-7 NA 105 +/-3 in.

Out of specification analog data may affect setpoint data, and will require additional evaluation.

  • VYC-723 provides a limiting setpoint of 12.180mV (33.252 inches referenced to tank bottom or 21.252 inches applied at transmitter) for the Auto Transfer of the HPCI Suction Valves.

SURVEILLANCE AS FOUND/AS LEFT TOLERANCES '

VYC-723 VYC-723 Component Component Loop Loop Instrument Calibration Calibration Calibration Calibration Number. As Found As Left Loop Components As Found As Left LSL-107-5A, B +/-0.24mV -0.2OmV N/A N/A N/A LT-107-5A/B +/- 0.38mV +/-0.20mV N/A N/A N/A LI-107-5 - 2.0% +/-2.0% LT-107-5A to LI-107-5 +/-2.5% +/-2.0%

LR-23-73(Gm) _ 1.0% +/-1.0% LT-107-5B to +/-1.5% +/-1.0%

_LR-23-73(Grn)

PTID F004 +/-2.6 KGAL +/-2.6 KGAL LT-107-5A to PTID F004, +/-7.23 KGAL +/-3.53 KGAL LSH-107-6 +/-3" H20 +/-3" H20 N/A N/A N/A LSL-107-7 +/- 3" H20 +/-3" H20 N/A N/A N/A LI-107-6 +/-2% +/-2% N/A N/A N/A TABLE 1 - CST LEVEL INSTRUMENTS Loop Sensor Indicator/Recorder Level Alarm Annunciator/Computer Pt A LT-107-5A LI-107-5 LSL-107-5A Annun 9-3-S-4, 9-3-T-9/Comp Pt F004 B LT-107-5B LR-23-73(GRN) LSL-107-5B Annun 9-3-S-4, 9-3-T-9 N/A LSH-107-6 N/A N/A Annun 9-6-H-7 N/A LSL-107-7 N/A N/A Annun 9-6-H-7' N/A LI- 107-6 Local N/A N/A OP 4363 Rev. 27 Page 4' of 21

ATTACHMENTS

1. VYOPF 4363.01 Deleted
2. VYOPF 4363.02 Deleted
3. VYOPF 4363.03 HPCI Suction Transfer on Condensate Storage Tank (CST) Low Level Functional Data Sheets
4. VYOPF 4363.04 HPCI Suction Transfer on Condensate Storage Tank (CST) Low Level Instrumentation Calibration Data Sheets QA REQUIREMENTS CROSS REFERENCE
1. None REFERENCES AND COMMITMENTS
1. Technical Specifications and Site Documents
a. Tables 3.2.1 and 4.2.1
b. UFSAR Sections 6.4 and 7.4
2. Codes, Standards, and Regulations I a. None
3. Commitments
a. 1NF96022_00, Improper Equipment Settings Due to the Use of Non-Temperature-Compensated Test Equipment
4. Supplemental References
a. Ashcroft 6480 Bulletin
b. CWDs 1229a, 528
  • C. GEK27805, Tab 1 and 3
d. P/IDs G191176 Sh.,1, G191169 Sh. 1
e. VYEM-0018, E27R Series Recorder
f. VYC-723, Condensate Storage Tank Level (HPCI) Monitoring I g. AP 0047, Work Request
h. AP 0310, Surveillance, Preventive and Corrective Maintenance Program
i. OP 4120, High Pressure Coolant Injection System Surveillance
j. AP 6807, Collection, Temporary Storage and Retrieval of QA Records OP 4363 Rev. 27 Page 5 of 21

PRECAUTIONS/LIMITATIONS

1. Only one (1) level instrument loop will be tested at a time.-
2. If this procedure cannot be completed as written, hold at the most secure point, notify the Shift Manager and discuss the problem and possible resolution with an I/C Supervisor.
3. If the need for corrective maintenance is determined during the performance of this procedure, initiate a Work Request (WR) per AP 0047.
4. Valves HPCI-17, 57, and 58 are restricted to 3,valve strokes (e.g., closed to open or open to closed) within one hour per OP 4120.

PREREQUISITES

1. Measurement and Test Equipment:
a. Pressure Gauge, Section B (calibration only) (1NF96022_00)
1) Heise 901B with a range not to exceed 1000" H20 or
2) Heise temperature compensated with a range not to exceed 830" H20
b. DMM HP-34401A (0-100mV Range)
2. HPCI-17, HPCI-57 and HPCI-58 must be fully operational to perform this test.
3. The CST level must be above the CST low level auto swap setpoint to perform this test.'

OP 4363 Rev. 27 Page 6 of 21

PROCEDURE A. Functional (VYOPF 4363.03)

1. The Shift Manager is fully knowledgeable of the scope of this procedure and by initialing the data sheet, grants his permission to perform the work.
2. Verify that HPCI-17 is OPEN, HPCI-57 and HPCI-58 are CLOSED.
3. Establish communications between the local instruments at the CST and the Control Room.
4. Record the reading of LI-,107-5 (CRP 9-6).
5. Prepare level transmitter LT-107-5A for testing as follows:
a. Record start time and date.
b. SHUT the isolation valve.
c. Second party verify Step 5.b.
d. Remove the span access cover for access to the transmitter test jacks.
e. Connect the DMM to the transmitter test jacks.

NOTE The test tubing cap can be manipulated as needed by the performer to obtain the most precise pressure control. Use of the cap will allow the rising action of the test valve stem to more slowly and accurately decrease pressure to the alarm setpoint.

f. Remove test tubing cap, as needed, to perform testing.

OP 4363 Rev. 27 Page 7 of 21

NOTE The high side test valve is a NEEDLE VALVE, DO NOT OVERTORQUE. This valve will be used to reduce pressure for two trip points.

6. Slowly decrease the pressure using the transmitters Hi side test valve until the first trip point is achieved as indicated by Relay 23A-K15 DE-ENERGIZING and verify the following:
a. Relay 23A-K15 (CRP 9-39) DE-ENERGIZES.
b. Annun 9-3-S-4 HPCI CST LEVEL LO - ALARM.
c. Valve HPCI 17 - CLOSES.
d. Valve HPCI 57 - OPENS.
e. Valve HPCI 58 - OPENS.
f. Record the As-Found DMM trip level indication. (12.2 +/-0.2 mV)
g. Record the As-Found LI-107-5 (CRP 9-6) trip level indication.

(5.50 +/-2.0%)

7. Slowly decrease the pressure using the transmitters Hi side test valve until the second trip point is achieved as indicated by Annun 9-3-T-9 CST/TORUS LVL PWR TRBL - ALARM and verify the following:
a. Annun 9-3-T-9 CST/TORUS LVL INST PWR TRBL - ALARM.
b. Record the As-Found DMM Trip indication. (10.2 +/-0.2 mV)
8. If the As-Found data in Steps 6 or 7 are NOT in tolerance, mark "N/A" on data sheet for Steps 10 through 12, then proceed to Section B and complete Steps 7 through 13 for loop calibration check.
9. If the As-Found data in Steps 6 and 7 are in tolerance, proceed to Step 10.

OP 4363 Rev. 27 Page 8 of 21

10. At the CST Instrument Rack perform the following:
a. SHUT the Hi side test valve and replace the tubing cap.
b. Slowly OPEN the Hi side isolation valve.
c. Perform Steps c. 1 and c.2, if needed, to remove any air from the sensor that may have been introduced during testing. If no 'air is introduced, N/A Steps c.1 and c.2 and continue with Step d.
1) Ensure that no air is left in the sensor by opening the vent plug and bleeding off all trapped air.
2) SHUT the vent.
d. Remove the DMM and replace the span access cover.
e. Second party verify that Steps 10.a-d have been performed.
11. At the Control Room, verify the following:
a. LI-107-5 reads same as in Step 4.
b. Relay 23A-K15 is ENERGIZED.
c. Annun 9-3-S-4 HPCI CST LEVEL LO - CLEAR.
d. Annun 9-3-T-9 CST/TORUS LVL INST PWR TRBL - CLEAR.
e. Record stop time and date, calculate'OOS time. Notify SM if OOS time

>6 hours.

12. Record the reading of LR-23-73 (CRP 9-3).
13. Prepare level transmitter LT-107-5B for testing as follows:
a. Record start time and date.
b. SHUT the isolation valve.
c. Second party verify Step 13.b.
d. Remove the span access cover for access to the transmitters test jacks.
e. Connect the DMM to the transmitters test jacks.

OP 4363 Rev. 27 Page 9 of 21

NOTE The test tubing cap can be manipulated as needed by the performer to obtain the most precise pressure control. Use of the cap will allow the rising action of the test valve stem to more slowly and accurately decrease pressure to the alarm setpoint.

f. Remove test tubing cap, as needed, to perform testing.

NOTE The high side test valve is a NEEDLE VALVE, DO NOT OVERTORQUE. This valve will be used to reduce pressure for two trip points.

14. Slowly decrease the pressure using the transmitters Hi side test valve until the first trip point is achieved as indicated by Relay 23A-K15 DE-ENERGIZING and verify the following:
a. Relay 23A-K15 (CRP 9-39) DE-ENERGIZES.
b. Annun 9-3-S-4 HPCI CST LEVEL LO - ALARM.
c. Record the As-Found DMM trip level indication. (12.2 +/-0.2 mV)
d. Record the As-Found LR-23-73 (CRP 9-3) trip level indication.

(5.50 +/-1.0%)

15. Slowly decrease the pressure using the transmitters Hi side test valve until the second trip point is achieved as indicated by Annun 9-3-T-9 CST/TORUS LVL INST PWR TRBL - ALARM and verify the following:
a. Annun 9-3-T-9 CST/TORUS LVL INST PWR TRBL - ALARM.
b. Record the As-Found DMM Trip indication. Required 10.2 +/-0.2 mV.
16. If the As-Found data in Steps 14 or 15 are NOT in tolerance, mark "N/A" on data sheet Steps 18 through 19, then proceed to Section B and complete Steps 17 through 23 for loop calibration check.
17. If the As-Found data in Steps 14 and 15 are in tolerance, proceed to Step 18.

OP 4363 Rev. 27 Page 10 of 21,

18. At the CST Instrument Rack perform the following:
a. SHUT the Hi side test valve and replace the tubing cap.
b. Slowly OPEN the Hi side isolation valve.
c. Perform Steps c. 1 and c.2, if needed, to remove any air from the sensor that may have been introduced during testing. If no air is introduced, N/A Steps c. 1 and c.2 and continue with Step d.
1) Ensure that no air is left in the sensor by opening the vent plug and bleeding off all trapped air.
2) SH1UT the vent.
d. Remove the DMM and replace the span access cover.
e. Second party verify that Steps 18.a-d have been performed.
19. At the Control Room, verify the following:
a. LR-23-73 reads same as Step 12.
b. Relay 23A-K15 is ENERGIZED.
c. Annun 9-3-S-4 HPCI CST LEVEL LO - CLEAR.
d. Annun 9-3-T-9 CST/TORUS LVL INST PWR TRBL - CLEAR.
e. Record stop time and date, calculate OOS time. Notify SM if OOS time

>6 hours.

20. Request the Control Room Operator fully CLOSE V23-57 and V23-58.
21. Request the Control Room Operator fully OPEN V23-17.
22. Proceed to Final Conditions.

OP 4363 Rev. 27 Page 11 of 21

B. Calibration (VYOPF 4363,04)

1. The Shift Manager is fully knowledgeable of the scope of this procedure and by I

initialing the data sheet, grants his permission to perform the work.

2. Verify that HPCI-17 is open, BPCI-57 and HiPCI-58 are closed.
3. Establish communications between the local instruments at the CST and the Control Room.
4. Prepare level transmitter LT-107-5A for testing as follows:
a. Record start time and date.
b. SHUT the isolation valve.
c. Second party verify Step 4.b.
d. Remove the span access cover for access to the transmitter test jacks.*
e. Connect the DMM to the transmitter test jacks.

NOTE The test tubing cap can be manipulated as needed by the performer to obtain the most precise pressure control. Use of the cap will allow the rising action of the test valve stem to more slowly and accurately decrease pressure to the alarm setpoint.

f. Remove test tubing cap, as needed, to perform testing.

OP 4363 Rev. 27 Page 12of 21

NOTE The high side test valve is a NEEDLE VALVE, DO NOT OVERTOROUE. This valve will be used to reduce pressure for two trip points.

5'. Slowly decrease the pressure using the transmitters Hi side test valve until the first trip point is achieved as indicated by Relay 23A-K15 DE-ENERGIZING and verify the following:

a. Relay 23A-K15 (CRP 9-39) DE-ENERGIZES.
b. Annun 9-3-S-4 HPCI CST LEVEL LO - ALARM.
c. Valve HPCI 17 - CLOSES.
d. Valve HPCI 57 - OPENS.
e. Valve HPCI 58 - OPENS.
f. Record the As-Found DMM trip level indication. (12.2 W0.2 mV)
g. Record the As-Found LI-107-5 (CRP 9-6) trip level indication. (5.50

+/-2.0%)

6. Slowly decrease the pressure using the transmitters Hi side tes't valve until the second trip point is achieved as indicated by Annun 9-3-T-9 CST/TORUS LVL INST PWR TRBL - ALARM and verify the following:
a. Annun 9-3-T-9 CST/TORUS LVL INST PWR TRBL - ALARM.
b. Record the As-Found DMM Trip indication. (10.2 +/-0.2 mV)
7. Loop A (LT-107-5A) Calibration Check
a. Remove the test tubing cap if not previously removed and fully OPEN the test valve.
b. Drain all water from the Hi side sensor by opening the transmitter Hi side vent plug.
c. Connect the pressure source to the test connection.
d. SHUT the Hi side vent plug.

OP 4363 Rev. 27 Page 13 of 21

I S8. Applying the values specified in Table B-1 below:

TABLE B LOOP A CALIBRATION TABLE TRANSMITTER VALUES INDICATIONS I Input Pressures Output Level Indicator ERFIS Point LT- 107-5A LT-107-5A LI-107-5 F004 43.0"H20 Increasing 14.0 mV (+/-0.2mV) 10% (+/-2.0%) 47.7 KGAL (+/-3.53 KGAL) 101.5"H 2 0 Increasing 20.0 mV (+/-0.2mV) 25% (+/-2.0%)

199.0"H20 Increasing 30.0 mV (+-0.2mV) 50% (+/-2.0%) 238.6 KGAL (+/-3.53 KGAL) 296.5"H 20 Increasing 40.0 mV (+/--O.2mV) 75% (+/-2.0%)

355.0"H 20 Increasing 46.0 mV (+/--0.2mV) 90% (+/-2.0%) 429.4 KGAL (+/-3.53 KGAL) 296.5"H20 Decreasing 40.0 mV (_-0.2mV) 75% (+/-2.0%)

199.0"H20 Decreasing 30.0 mV (-+0.2mV) 50% (+/-2.0%) 238.6 KGAL (-3.53 KGAL) 101.5"H20 Decreasing 20.0 mV (+/-+0.2mV) 25% (++/-2.0%)

43.0"H 2 0 Decreasing 14.0 mV (_+0.2mV) 10% (+/-2.0%) 47.7 KGAL (+/-3.53 KGAL)

a. Record the As-Found CRP 9-6 indicator, ERFIS point, and transmitter output values, as applicable at each specified pressure.
9. If the As-Found data in Steps 5, 6 or 8 are NOT in tolerance, proceed to Step 11.
10. If the As-Found data in Steps 5, 6 and 8 are in tolerance, record "As-Found" data as "As-Left" on data sheet Step 11, then proceed to Step 12.
11. Component Calibration
a. Transmitter (LT-107-5A)
1) Apply pressures to LT-107-5A as specified in Table B-1 above.
2) Adjust the transmitter zero, span, and linearity adjustments as necessary to bring the mV indication within the allowable tolerance.
3) Record the transmitter As-Left data.
b. Indicator (LI-107-5) and ERFIS point (F004):
1) Apply pressure to LT-107-5A as specified in Table B-1 above.
2) Adjust the LI-107-5 zero as necessary for specified values above.

OP 4363 Rev. 27 Page 14 of 21

NOTE If ERFIS point As-Found data is out of tolerance, initiate WR.

3). Record the As-Left data.

c. Alarm Unit (CRP 9-20)

NOTE LSL- 107-5A has two alarm points which are set in the decreasing direction.

1) Adjust the alarm unit to obtain the following trip points:

12.2 mV +/-0.2 mV (Decreasing) CKT 1 (upper pot) 10.2 mV +/-0.2 mV (Decreasing) CKT 2 (lower pot)

2) Record As-Left value on the data sheet.
12. At the CST Instrument Rack perform the following:
a. Remove the pressure source.
b. SHUT the Hi side test valve and replace the tubing cap.
c. Slowly OPEN the Hi side isolation valve.
d. Ensure that no air is left in the sensor by Opening the vent plug and bleeding off all trapped air.
e. SHUT the vent, remove the DMM and replace the span access cover.
f. Second party verify that Steps 12.b-e have been performed.
13. At the Control Room, verify the following:
a. Relay 23A-K15 is ENERGIZED.
b. Annun 9-3-S-4 -PCI CST LEVEL LO - CLEAR.
c. Annun 9-3-T-9 CST/TORUS LVL INST PWR TRBL - CLEAR.
d. Record stop time and date, calculate OOS time. Notify SM if OOS time

>6 hours. N OP 4363 Rev. 27 Page 15 of 21

14. Prepare level transmitter LT-107-5B for testing as follows:
a. Record start time'and date.
b. SHUT the isolation valve.
c. Second party verify Step 14.a.
d. Remove the span access cover for access to the transmitters test jacks.

e.* Connect the DMM to the transmitters test jacks.,

NOTE The test tubing cap can be manipulated as needed by the performer to obtain the most precise pressure control. Use of the cap will allow the rising action of the test valve stem to more slowly and accurately decrease. pressure to the alarm setpoint.

f. Remove test tubing cap, as needed, to perform testing.

NOTE The high side test valve is a NEEDLE VALVE, DO NOT OVERTOROUE. This valve will be used to reduce pressure for two trip points.

15. Slowly decrease the pressure using the transmitters Hi side test valve until the first trip point is achieved as indicated by Relay 23A-K15 DE-ENERGIZING and verify the following:
a. Relay 23A-K15 (CRP 9-39) DE-ENERGIZES.
b. Annuri 9-3-S-4 -PCI CST LEVEL LO - ALARM.
c. Record the As-Found DMM trip level lindication. (12.2 +/-0.2 mV)
d. Record the As-Found LR-23-73 (CRP 9-3 trip level indication.

(5.50 +/-1%)

OP 4363 Rev. 27 Page 16 of 21

16. Slowly decrease the pressure using the transmitters Hi side test valve until the second trip point is achieved as indicated by Annun 9-3-T-9 CST/TORUS LVL INST PWR TRBL - ALARM and verify the following:
a. Annun 9-3-T-9 CST/TORUS LVL INST PWR TRBL - ALARM.
b. Record the As-Found DMM Trip indication. Required 10.2 +/-0.2 mV.
17. Loop B (LT-107-5B) Calibration Check
a. Remove the test tubing cap if not previously removed and fully OPEN the test valve.
b. Drain all water from the Hi side sensor by opening the transmitter Hi side vent plug.
c. Connect the pressure source to the test connection.
d. SHUT the Hi side vent plug.
18. Applying the values specified in Table B-2 below:

TABLE B LOOP B CALIBRATION TABLE TRANSMITTER VALUES INDICATIONS Input Pressures Output Level Recorder LT-107-5B LT-107-5B LR-23-73 Gm 43.0"H20 Increasing 14.0 mV (+/-0.2mV) 10% (+/-1.0%)

101.5"H20 Increasing 20.0 mV (+/-0.2mV) 25% (+/-1.0%)

199.0"H20 Increasing 30.0 mV (+/-0.2mV) 50% (+/-1.0%)

296.5"H20 Increasing 40.0 rmV (_+0.2mV) 75% (+/-1.0%)

355.0"H 20 Increasing 46.0 mV (+/-0.2mV) 90% (+/-1.0%)

296.5"H 20 Decreasing 40.0 mV (-+0.2mV) 75% (+/-1.0%)

199.0"H20 Decreasing 30.0 mV (+/-0.2mV) 50% (+/-1.0%)

101.5"H20 Decreasing 20.0 mV (+/-0.2mV) 25% (+/-1.0%)

43.0"H 20 Decreasing 14.0 mV (+/--0.2mV) 10% (+/-1.0%)

a. Record the As-Found CRP 9-3 recorder and transmitter output valves as applicable at each specified pressure.

OP 4363 Rev. 27 Page 17 of 21

19. If the As-Found data in Steps 15, 16, or 18 are NOT in tolerance, proceed to Step 21.
20. If the As-Found data in Steps 15, 16 and 18 are in tolerance, record "As-Found" data as "As-Left" on data sheet Step 21, then proceed to Step 22.
21. Component Calibration
a. Transmitter (LT-107-5B)
1) Apply pressures to LT-107-5B as specified in Table B-2 above.
2) Adjust the transmitter zero, span, and linearity adjustments as necessary to bring the mV indication within the allowable tolerance. /
3) Record the transmitter As-Left data.
b. Recorder (LR-23-73)
1) Apply pressures to LT-107-5B as specified in Table B-2 above.
2) Adjust the LR-23-73 zero and span adjustments as necessary for specified values above.
3) Record the As-Left data.
c. Alarm Unit (CRP 9-20)

NOTE LSL-107-5B has two alarm points which are set in the decreasing direction.

1) Adjust the alarm unit to obtain the following trip points:

12.2 mV _+0.2 mV (Decreasing) CKT 1 (upper pot) 10.2 mV +/-0.2 mV (Decreasing) CKT 2 (lower pot)

2) Record As-Left value on the data sheet.

OP 4363 Rev. 27 Page 18 of 21

22. At the CST Instrument Rack perform the following:
a. Remove the pressure source.
b. SHUT the Hi side test valve and replace the tubing cap.
c. Slowly OPEN the Hi side isolation valve.
d. Ensure that no air is left in the sensor by opening the vent plug and bleeding off all trapped air.
e. SHUT the vent, remove the DMM and replace the span access cover.
f. Second party verify that Steps 22.b-e have been performed.
23. At the Control Room, verify the following:
a. Relay 23A-K15 is ENERGIZED.
b. Annun 9-3-S-4 HPCI CST LEVEL LO - CLEAR.
c. Anntin 9-3-T-9 CST/TORUS LVL INST PWR TRBL - CLEAR.
d. Record stop time and date, calculate OOS time. Notify SM if OOS time

>6 hours.

24. Request the Control Room Operator fully CLOSE V23-57 and V23-58.
25. Request the Control Room Operator fully OPEN V23-17.
26. At the CST Instrument Rack calibrate Level switches LSH-107-6 and LSL-107-7 by performing the following:
a. Isolate the Level switch to be tested by SHUTTING its respective isolation valve. Remove the test tubing cap.
b. Second party verify Step 26.a has been performed.
c. OPEN test valve and connect the pressure source to the test connection.
d. Apply pressure as specified on the data sheet.
e. Have the specialist in the Control Room provide a mark at Annun 9-6-H-7 COND XFER SYS TROUBLE - ALARM.
f. Record the As-Found pressure applied.

OP 4363 Rev. 27 Page 19 of 21

g. Adjust the pressure switch as required to maintain the acceptance criteria as specified on the data sheet.
h. Record the As-Left trip pressure.
i. Remove the pressure source, SHUT the test valve and replace the test tubing cap.
j. Return the instrument to service by OPENING the isolation valve.
k. Second party verify that Steps 26.1 and j have been performed.
1. Verify that Annun 9-6-H-7 COND XFER SYS TROUBLE - CLEAR.
m. Repeat Steps'26.a through I for the remaining instrument.
27. At the CST Instrument Rack perform the following:
a. SHUT the isolation valve and depressurize LI-107-6.
b. Second party verify that Step 27.a has been performed.
c. Connect the pressure source to the testconnection.
d. Apply the pressures to the LI-107-6 as specified in Table B-3 below:

TABLE B-3 INPUT PRESSURE REQUIRED OUTPUT 0 in HzO 0% (+2/-0%)

195 in H20 50% (+/-2%)

390 in H20 100% (+0/-2%)

e. Record the As-Found data values.
f. If the As-Found data is in tolerance, skip Step 27.g and record the As-Found" data as "As-Left" data on data sheet Step 27.h, then proceed to Step 27.i.
g. Adjust the gauge as required to meet the acceptance criteria of applied pressure +/-2%.
h. Record the As-Left data.

OP 4363 Rev. 27 Page 20 of 21

i. Remove the pressure source and SHUT the test valve.
j. Return the instrument to service by OPENING the isolation valve.
k. Second party verify that Steps 27.i and j have been performed.
28. Proceed to Final Conditions.

ACCEPTANCE CRITERIA

1. Successful operation of all instruments, relays, alarms and annunciators.
2. Calibration values shall be within the tolerance as specified on the data sheets:

Comparative Data:

PRESSURE TRANSMITTER FUNCTION ELEVATION LEVEL OUTPUT TANK ZERO Inst. Zero 254 ft. 0 in. 4.0 in. H20 10.0 mV 0 in.

Inst. Pwr.

Trbl. Alarm 254 ft. 2 in. 6.0 in. H20 (dec.) 10.2 mV (dec.) 2.0 in.

LSL 107-5A/B Vlv.

lSH Motion Motion 25.5 in. 1-20 (dec.)

256 ft. 1.5 in. 2. in. 12.2 mV (dec.) 21.5 in.

LSH 107-5AfB Lo LvlIII Alarm 263 ft. 9 in. 105 in. H20 (dec.) 1in.

Inst. Mid 270 ft. 3 in. 199 in. H20 30.0 mV 195 in.

Hi Lvl Alarm 284 ft. 11 in. 359 in. H20 in.

Overflow 286 ft. 6 in. 394 in. H120 50.0 mV 32 ft. in.

FINAL CONDITIONS I 1. Notify the Shift Manager on completion of the test and of any discrepancies.

2. Return completed forms, VYOPF 4363.03 or .04 to an I/C S'upervisor for review (AP 0310) and filing in accordance with AP 6807.

OP 4363 Rev. 27 Page 21 of 21

HPCI SUCTION TRANSFER ON CONDENSATE STORAGE TANK (CST) LOW LEVEL FUNCTIONAL TEST DATA SHEETS:

LOCATION: CONTROL ROOM/CST INSTRUMENT RACK STEP REQUIRED A.1 I SM Permission By his signature, the Shift Manager acknowledges that performance of this procedure affects instruments contained in TS Table 3.2.1. Entry into the associated LCO and required ACTIONS may be delayed for up to 6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br /> when a channel is placed in an inoperable status solely for the performance of a required surveillance provided the associated Trip Function or Redundant Trip Function maintains ECCS initiation capability or Recirculation Pump Trip capability.

HPCI 57/58 CLOSED A.2 HPCI-17 OPEN INSTRUMENT NUMBER LI-107-5 Indicator A.4 Normal Reading _

INSTRUMENT NUMBER LT-107-5A

'A.5 Record, Start Time Time:

a and Date Date:

b Perf. By c Verf. By A.6 Relay 23A-K15 a DE-ENERGIZED Annun 9-3-S-4 b ALARM c HPCI-17 CLOSES d HPCI-57 OPENS e HPCI-58 OPENS As-Found Trip Value f 12.0-12.4 mV As-Found Trip Value

__ 3.5-7.5%

Annun 9-3-T-9 A.7 a ALARM, As-Found Trip Value b 10.0-10.4 mV VYOPF 4363.03 OP 4363 Rev. 27 Page I of 3

HPCI SUCTION TRANSFER ON CONDENSATE STORAGE TANK (CST) LOW LEVEL FUNCTIONAL TEST DATA SHEETS (Continued)

LOCATION: CONTROL ROOM/CST INSTRUMENT RACK STEP REQUIRED INSTRUMENT NUMBER LT-107-5A A. 10 a Perf. By b Perf. By c.1 Perf. By c.2 Perf. By e Verf. By Ind.

A.11 a Normal Relay 23A-K15 b ENERGIZED Annun 9-3-S-4 c CLEAR Annun 9-3-T-9 d CLEAR e Record Stop Time and Time:

Date Date:

Calculate OOS Time OOS:

INSTRUMENT NUMBER LR-23-73 Recorder A. 12 Normal Reading INSTRUMENT NUMBER LT-107-5B a Record Start Time Time:_

A. 13 and Date Date:

b Perf. By, c Verf. By Relay 23A-K15 A.14 a DE-ENERGIZED Annun 9-3-S-4 b ALARM As-Found Trip Value c 12.0-12.4 mV As-Found Trip Value d 4.5-6.5%

VYOPF 4363.03 OP 4363 Rev. 27 Page 2 of 3 rý

HPCI SUCTION TRANSFER ON CONDENSATE STORAGE TANK (CST) LOW LEVEL FUNCTIONAL TEST DATA SHEETS (Continued)

LOCATION: CONTROL ROOM/CST INSTRUMENT RACK STEP REQUIRED INSTRUMENT NUMBER LT-107-5B A.15 Annun 9-3-T-9 a ALARM As-Found Trip Value b 10.0-10.4 mV _

a Perf. By A.18 b Perf. By

c. I Perf.1By . ...

c.2 Perf. By .... .....

e Verf. By .

Ind.

A.19 a Normal Relay 23A-K15o b ENERGIZED Annun 9-3-S-4 c CLEAR Annun 9-3-T-9 d CLEAR e Record Stop Time and Time:

Date Date:__

Calculate OOS Time OOS:

V23-57 and V23-58 A.20 Fully CLOSED A.21 V23-17 Fully OPEN MITE Used (VY SN/Due Date):

Discrepancies/Remarks:

Tested By: Date:

(Print/Sign)

Shift Manager: "Date:

(Print/Sign)

I/C Supervisor Review: Date:

(Print/Sign)

VYOPF 4363.03 OP 4363 Rev. 27 Page 3 of 3

HPCI SUCTION TRANSFER ON CONDENSATE STORAGE TANK (CST)

LOW LEVEL INSTRUMENTATION CALIBRATION DATA SHEETS LOCATION: CONTROL ROOM/CST INSTRUMENT RACK STEP I REQUIRED IB.1 I SM Permission 1 i By his signature, the Shift Manager acknowledges that performance of this procedure affects instruments contained in TS Table 3.2.1. Entry into the associated LCO and required ACTIONS may be delayed for up to 6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br /> when a channel is placed in an inoperable status solely for the performance of a required surveillance provided the associated Trip Function or Redundant Trip Function maintains ECCS initiation capability or Recirculation Pump Trip capability.

B.2 HPCI 57/58 CLOSED.,

HIPCI-17 OPEN INSTRUMENT NUMBER LT-107-5A Record Start Time Time:

B.4 a and Date Date:

b Perf. By c Verf. By Relay 23A-K15 B.5 a DE-ENERGIZED Annun 9-3-S-4 b ALARM HPCI-17 c CLOSES BPCI-57 d OPENS HPCI-58 e OPENS As-Found Trip Value f .12.0-12.4 mV As-Found Trip Value g 3.5-7.5%

Annun 9-3-T-9 B.6 a ALARM As-Found Trip Value b 10.0-10.4.mV VYOPF 4363.04 OP 4363 Rev. 27 Page 1 of 7

HPCI SUCTION TRANSFER ON CONDENSATE STORAGE TANK (CST) LOW LEVEL INSTRUMENTATION CALIBRATION DATA SHEETS (Continued)

LOCATION: CONTROL ROOMICST INSTRUMENT RACK STEP IREQUIRED .

LOOP A (LT-107-5A)

INSTRUMENT NUMBER AS-FOUND LI-107-5 F004 (KGAL) LT-107-5A

@43.0" H20 Inc. 8-12% 144.14-51.23 13.8-14.2mV B.8 a @101.5"H 2 0 Inc. 23-27% __ 19.8-20.2mV

@199.0"H 2 0 Inc. 48-52% 235.07-242.13 29.8-30.2mV

@296.5"H 20 Inc. 73-77% ____39.8-40.2mV

@355.0"H20 Inc. 88-92% 425.87-432.93 45.8-46.2mV

@296.5"H20 Dec. 73-77% 39.8-40.2mV

@199.0"H20 Dec. 48-52% 1235.07-242.13 29.8-30.2mV

@101.5"H20 Dec. 23-27% __ 19.8-20.2mV

@43.0"H20 Dec. 8-12% 144.14-51.23 13.8-14.2mV LOOP A (LT-107-5A)

INSTRUMENT NUMBER LT-107-5A AS-LEFT OUTPUT

@43.0"H20 Inc. 13.8 - 14.2mV B.11 a.3 @101.5"H2OInc. 19.8-20.2mV

@ 199.0"H20 Inc. 29.8 - 30.2mV

@296.5"H 20 Inc. 39.8 - 40.2mV

@355.0"H 20 Inc. 45.8 - 46.2mV

@296.5"H 20 Dec. 39.8 - 40.2mV

@199.0"H 20 Dec. 29.8 - 30.2mV

@101.5"H20 Dec. 19.8 - 20.2mV

@43.0"H 20 Dec. 13.8 - 14.2mV LOOP A (LT-107-5A)

INSTRUMENT NUMBER AS-LEFF LI-107-5(%) F004 (KGAL)

@43.0"H20 Inc. 8-12% 144.14-51.23 B.11 b.3 101.5"H 20 Inc. 23-27% _

199.0"H20 Inc. 48-52% 1235.07-242.13 296.5"H 20 Inc. 73-77% _

355.0"H 20 Inc. 88-92% 1425.87-432.93 296.5"H 20 Dec. 73-77% _

199.0"H20 Dec. 48-52% 235.07-242.13 101.5"H 20 Dec. 23-27%

43.0"H 20 Dec. 8-12% E 44.14-51.23 4 !0 VYOPF 4363.04 OP 4363 Rev. 27 Page 2 of 7

HPCI SUCTION TRANSFER ON CONDENSATE STORAGE TANK (CST) LOW LEVEL INSTRUMENTATION CALIBRATION DATA SHEETS (Continued)

LOCATION: CONTROL ROOM/CST INSTRUMENT RACK STEP IREQUIRED INSTRUMENT NUMBER LOOP A (LT-107-5A)

AS-LEFT Trip Value B.11 C. 12.0-12.4 mV i 2 Trip Value 10.0-10.4 mV b Perf. By tB.12 c Perf. By d Perf. By e Pef. By f Verf. By Relay 23A-K15 B. 13 a ENERGIZED Annun 9-3-S-4 b CLEAR Annun 9-3-T-9 c CLEAR Record Stop Time Time:

d and Date Date:

Calculate OOS OOS:

Time INSTRUMENT NUMBER LT-107-5B Record Start Time Time:

B.14 a and Date Date:

b Perf. By c Verf. By Relay 23A-K151 B.15 a DE-ENERGIZED Annun 9-3-S-4 b ALARM As-Found Trip Value c 12.0-12.4 mV As-Found Trip Value d 4.5-6.5 Annun 9-3-T-9 B.16a ALARM As-Found Trip Value b 10.0-10.4 mV VYOPF 4363.04 OP 4363 Rev. 27 Page 3 of 7

HPCI SUCTION TRANSFER ON CONDENSATE STORAGE TANK (CST) LOW LEVEL INSTRUMENTATION CALIBRATION DATA SHEETS (Continued)

LOCATION: CONTROL ROOM/CST INSTRUMENT RACK STEP 'IREQUIRED LOOP B (LT-107-5B)

INSTRUMENT NUMBER AS-FOUND AS-FOUND LR-23-73 LT-107-5B Output

@43.0"H 20 Inc. 9-11% 13.8 - 14.2mV B,18 a @101.5"H2OInc. 24-26% 19.8- 20.2mV

@199.0"H 20 Inc. 49-51% 29.8 - 30.2mV

@296.5"H20 Inc. 74-76% 39.8 - 40.2mV

@355.0"H 20 Inc. 89-91% 45.8 - 46.2mV

@296.5"H 20 Dec. 74-76% 39.8 - 40.2mV

@199.0"H20 Dec. 49-51% _29.8 - 30.2mV

@101.5"H 20 Dec. 24-26% 19.8- 20.2mV

@43.0"H 2 0 Dec. 9-11% 13.8- 14.2mV INSTRUMENT NUMBER LT-107-51 AS-LEFT OUTPUT

@43.0"H 20 Inc. 13.8 - 14.2mV B.21 a.3 101.5"H 20 Inc. 19.8 - 20.2mV 199.0"H 20 Inc. 29.8 - 30.2mV 296.5"H20 Inc. 39.8 - 40.2mV 355.0"H20 Inc. 45.8 - 46.2mV, 296.5"HZO Dec. 39.8 - 40.2mV _

199.0"H 20 Dec. 29.8 - 30.2mV 101.5"H 20 Dec. 19.8 - 20.2mV 43.0"H20 Dec. 13.8 - 14.2mV INSTRUMENT NUMBER LR-23-73 AS-LEFF

@43.0"H20 Inc. 9-11%

B.21 b.3 101.5"H20 Inc. 24-26%

199.0"H20 Inc. 49-51%

296.5"H 20 Inc. 74-76%

355.0"H 20 Inc. 89-91%

296.5"H 20 Dec. 74-76%

199.0"H 20 Dec. 49-51%

101.5"H20 Dec. 24-26%

43.0"H20 Dec. 9-11%

VYOPF 4363.04 OP 4363 Rev. 27 Page 4 of 7

UPCI SUCTION TRANSFER ON CONDENSATE STORAGE TANK (CST) LOW LEVEL INSTRUMENTATION CALIBRATION DATA SHEETS (Continued)

LOCATION: CONTROL ROOMICST INSTRUMENT RACK STEP IREQUIRED I LT- 107-5B INSTRUMENT NUMBER Trip Value B.21 c.2 12.0-12.4 mV Trip Value 0AFOAS-LE r 10.0-10.4 mV LT-107-5B INSTRUMENT NUMBER AS-FOUND I AS-LEFF b Perf. By B .22 c Perf. By d Perf. By ......

e Perf. By Sf Verf. By Relay 23A-K15 B.23 a ENERGIZED Annun 9-3-S-4 b CLEAR Annun 9-3-T-9 c CLEAR d Record Stop Time Time:

and Date Date:

Calculate OOS OOS:

Time V23-57 and B.24 V23-58 Fully CLOSED B.25 OPEN__ _ _ _ _ _ _

VYOPF 4363.04 OP 4363 Rev. 27 Page 5 of 7

HPCI SUCTION TRANSFER ON CONDENSATE STORAGE TANK (CST) LOW LEVEL INSTRUMENTATION CALIBRATION DATA SHEETS (Continued)

LOCATION: CONTROL ROOM/CST INSTRUMENT RACK STEP IREQUIRED INSTRUMENT NUMBER LSH-107-6 LSL-107-7 a Perf. By B.26 b Verf. By Approx. Trip d Press. 359.0 in. H2 0 inc. 105.0 in. H20 dec.

Annun 9-6-H-7 e ALARM As-Found Trip 356 to 362 102 to 108 f Press. in. H20 inc. in. H20 dec.

Acceptance 356 to 362 g Criteria in.H20 inc. 102 to 108 in. H 20 dec.

As-Left 356 to 362 102 to 108 h Trip Press. in. H20 inc. in. H20 dec.

i Perf. By k Perf. By By k Verf.

Annun 9-6-H-7 1 CLEAR_

INSTRUMENT NUMBER LI- 107-6 a IPerf. By B.27 b IVerf. Bv

-I AS-FOUND I I

AS-LEFT A-LEFF eh 10-2.0% I h

P 8-752%

198- 100%

I______ ________

I i.Perf. By _ _ _ _ _ _

jj Perf. By _ _ _ _ _ _

k IVerf. By VYOPF 4363.04 OP 4363 Rev. 27 Page 6 of 7

HIPCI SUCTION TRANSFER ON CONDENSATE STORAGE TANK (CST) LOW LEVEL INSTRUMENTATION CALIBRATION DATA SHEETS (Continued)

LOCATION: CONTROL ROOMICST INSTRUMENT RACK M/TE Used (VY SN/Due Date):

Discrepancies/Remarks:

Tested By: Date:

(Print/Sign)

Shift Manager: Date:

(Print/Sign)

I/C Supervisor Review: Date:

(Print/Sign)

VYOPF 4363.04 OP 4363 Rev. 27 Page 7 of 7

VERMONT YANKEE NUCLEAR POWER STATION A*MINISTRATIVE,UPROCE -

AP 0310 REVISION 20 I&C SURVEILLANCE, PREVENTIVE AND CORRECTIVE MAINTENANCE PROGRAM USE CLASSIFICATION: INFORMATION LPC Effective No. Date Affected Pages UNCONTROLLBD Implementation Statement: N/A Issue Date: 12/02/03 AP 0310 Rev. 20 Page 1 of 24

TABLE OF CONTENTS 1.0 PURPOSE, SCOPE, AND DISCUSSION ...................................................................................... 3 2.0 DEFINITIONS ........................................ 3 3.0 PRIMARY RESPONSIBILITIES ............................................................................................ 3 4 .0 PR O C EDURE ................................................................................................................................. 4 4.1. Surveillance Testing ............................................................................................................ 4 4.2. Preventive Maintenance (PM) ........................................ 5 4.3. Corrective Maintenance 6 4.4. Methods of Conducting Maintenance/Surveillance Activities ................................................ 6 4.5. Work Review and Responsibilities ................................................................................... 13 4.6. Administrative Controls .................................................................................................... 20

5.0 REFERENCES

AND COMMITMENTS ... 23 6.0 FINAL CONDITIONS 24 7.0 ATTACHMENTS 24 8.0 QA REQUIREMENTS CROSS REFERENCE ............................................................... .. 24 AP 0310 Rev. 20 Page 2 of 24

1.0 PURPOSE, SCOPE, AND DISCUSSION 1.1. PURPOSE This procedure serves as a guideline for properly completing the Surveillance, Preventive and Corrective Maintenance responsibilities assigned to the IGC Department.

1.2. SCOPE This procedure provides Department Superintendents and Designated Representatives/Supervisors with guidance to assure the I/C personnel, maintain the surveillance, preventive and corrective maintenance program.

1.3. DISCUSSION The performance of surveillance, preventive and corrective maintenance on installed plant equipment requires that a specific work process be followed. This process is covered by procedures, which control the removal and return to service, performance and quality of the work done, in a manner that will ensure that the operational requirements are fulfilled.

This procedure will serve to provide an overall work process guideline, that when used by department personnel, will ensure that steps in the work process have been accomplished in a complete and correct manner and that the work process is thoroughly documented. Additionally job aids are included to provide department personnel with the information needed to properly perform the task assigned.

This procedure is not intended to supplement or short cut the existing work process procedures, but to act as an overview of the existing work process to ensure that all relevant controls are followed.

2.0 DEFINITIONS 2.1. None 3.0 PRIMARY RESPONSIBILITIES 3.1. None AP 0310 Rev. 20 Page 3 of 24

4.0 PROCEDURE 4.1. Surveillance Testing Periodic testing/inspection of safety-related and other installed plant equipment is required to ensure continued operability within accepted licensing or administrative limits. Procedure AP 4000 provides the mechanism for scheduling, independent verification and documenting completion of surveillance tests through Curator Work List.

The I/C department is responsible for the content of the Curator Surveillance Database for their tests, completion of tests within allotted time, development and maintenance of test procedures, and the collection, review, approval, and retention of test data sheets.

4.1.1. The I&C Department Testing Coordinator (IIC DTC) is a member of the I&C Maintenance Support Group. The TIC DTC will:

NOTE See Appendix H for surveillance schedule information and Outage Surveillance Basis.

4.1.1.1. Review the Master Test List annually for accuracy and submit corrections in accordance with AP 4000.

4.1.1.2. Be responsible for listing on VYAPF 0310.01, all tests scheduled to be completed each Friday as they appear on the weekly Surveillance Test Requirements List compiled by the Surveillance Test Coordinator (STC) in accordance with AP 4000.

4.1.1.3. Generate a new Shop List by either using the Surveillance Schedule Report (pre-Friday), or using the Friday morning printout of "Alert Report" and "Surveillance Test Report".

4.1.1.4. On the old list, note all carryovers.

4.1.1.5. Perform the Work List item completion forevery test completed associated with a completed procedure by entering 1IC specialist initials in the Work List item notes.

4.1.1.6. Provide a copy to the I/C Secretary.

4.1.1.7. Place the original Shop List in the completed surveillance section of the I/C Groups I/C DTCs surveillance log.

AP 0310 Rev. 20 Page 4 of,24

4.2. Preventive Maintenance (PM)

Preventive Maintenance consists of two types.

  • Auto generated time or cycle based.
    • Condition based as a result of observation, prediction, OE, etc.

Also, the PM program is designed to detect equipment and performance problems before significant degradation occurs. Through proper implementation this will allow prompt correction, improved outage and maintenance planning, and increased plant power output with improved plant safety and reliability.

4.2.1. Work Orders will be auto generated and scheduled to be performed in accordance with the plant scheduling guideline."

4.2.2. The Department Supervisor will review the WO or Procedure to be used to perform the PM and assure that sufficient qualified personnel are assigned to the task.

4.2.3. Prior to starting the task the assigned individual will:

4.2.3.1. Ensure the procedure is the current revision.

4.2.31.2. Obtain a sufficient number of copies to cover all work locations. Reference procedure section 4.6 for field use of controlled documents.

4.2.3.3. Review the procedure or work order to become familiar with the requirements and get answers to any questions before starting Work.

4.2.3.4. Obtain any Measuring and Test Equipment (M&TE) needed in accordance with DP 0301.

4.2.3.5. Obtain any parts required and assure they are the correct ones (safety class, EQ, etc.). Reference ENN-MP- 115.

4.2.3.6. Request a Radiation Work Permit in accordance with AP 0502 if required.

4.2.3.7. Review the Safety Requirements and establish any postings and/or obtain any safety equipment as needed.

4.2.4. The assigned individual will perform the task in accordance with the procedure or work order. Reference procedure section 4.4. for methods of conducting maintenance.

4.2.5. The Department Supervisor will review the completed work order or procedure in accordance with section 4.5 of this procedure.

4.2.6. The Program and Component Engineering Department (for assigned components) will trend the PM results for analyzing the component performance history.

AP 0310 Rev. 20 Page 5 of 24

..I 4.2.7. Any suggested PM changes will be processed in accordance with AP 0214.

4.3. Corrective Maintenance Corrective maintenance includes any maintenance activity performed on a piece of plant equipment to correct a malfunction or other nonconforming condition. This section will outline the process from generation to closure as defined in existing procedures and any department specific actions.

4.3.1. Work Requests (WRs) are generated in accordance with AP 0047.

4.3.2. The Department Representatives will review the WR's with the Operations Planning Coordinator (OPC) to assess the validity and assign a priority level in accordance with AP 0047.

4.3.2.1. This review will also consider Whether the task meets the Minor Maintenance definition, reference AP 0049, may be performed as Troubleshooting, reference AP 0050, or processed as FIN Team Work, reference AP 0053.

4.3.3. WR's are scheduled/planned per AP 0168 and AP 0048.

4.3.4. The Department Supervisor will review the scheduled WO for any special requirements and assign qualified individuals to perform the work.

4.3.5. Upon assignment of a work order the repair crew shall review all applicable documentation and perform the task in compliance with AP 0021 and applicable sections of this procedure.

4.3.6. Upon completion the Department Supervisor will close out the WO in accordance with AP'0021 and the applicable sections of this procedure.

4.3.7. Work Orders that can not be completed as scheduled due to parts unavailability, the need for engineering assistance, or other reasons will be returned to Planning for resolution through the AP 0168 Work Management process.

4.3.7.1. An explanation of why the WO could not be completed shall be recorded on the WO notes.

4.4. Methods of Conducting Maintenance/Surveillance Activities During the performance of maintenance and/or surveillance activities specific actions must be performed to ensure the safe and reliable completion of work and the ability of equipment to function properly. To assure consistent performance of work activities the referenced procedures are to be used as applicable and the proceeding processes are to be followed when appropriate.

Safety requirements will be complied with during all work activities.

AP 0310 Rev. 20 Page.6 of 24

4.4.1. Surveillance Test Time Monitoring During performance of Tech. Spec. surveillances which have a 6-hour allowance for performance of the surveillance without entering the LCO actions, it is the I&C Specialist's responsibility to monitor the performance time and to notify the Shift Manager as soon as it is identified that the 6-hour allowance may be exceeded.

When recording elapsed time (stop-start), rounding up to the next hour is acceptable for times up to 5 hours5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br />. For example, 43 minutes can be recorded as <1 hour.

4.4.2. Independent Verifications When independent verification of a component or condition is required and circumstances require two individuals to work together, the act of independent verification must be completely separate and independent. The verifier must not rely on the observed action (except in Steps 4.4.2.1 and 4.4.2.2 below) of a co-worker to determine component identification, position, or condition. Actual separation of workers is not required, but is recommended when practical. The key element is independent assurance of the described condition.

4.4.2.1. When checking the position of a throttled valve or torquing of a component (for example), it is unreasonable to expect a second manipulation, In these cases, the independent verifier would clearly observe the first checker's manipulation of the device.

4.4.2.2. In cases involving significant radiation exposure, the department supervisor may determine the appropriate form of verification and so note it on the documentation.

4.4.3. Second party verification Second party verification is when the second individual verifies that the original performer is accomplishing/performing the activity correctly. The normal process for this is as follows.

4.4.3.1. The second party verifier will observe the performer identify the component, position, or condition.

4.4.3.2. If the second party verifier does not agree with the component, position, or condition, this discrepancy will be pointed out for clarification and resolution. No activity should be performed until both parties are in agreement.

4.4.3.3. The second party verifier will actively observe the performer complete the activity.

4.4.3.4. After the activity has been performed, the second party verifier will sign off indicating acceptability.

AP 0310 Rev. 20 Page 7 of 24

4.4.4. Procedure Signoffs When performing a surveillance or calibration it is not always practical to have all persons involved sign one procedure during the activity. In these situations the following protocol shall be followed.

4.4.4.1. All individuals involved with the activity will have a copy of the procedure.

4.4.4.2. Communications will be maintained during the activity.

4.4.4.3. Individuals performing a step will sign the copy in hand.

4.4.4.4. Verification through communication will be made of step completion before proceeding to the next step.

4.4.4.5. Upon completion all signatures will be transferred to one master copy of the procedure.

4.4.5. When performing a multi-component procedure for only one component the person performing test shall place a N/A next to the remaining component numbers with an explanation in the Remarks/Discrepancy section of the Data Sheet.

4.4.6. If during the work activity a problem is encountered with the procedure the requirements of AP 0095 shall be complied with to stop work at a safe point and notify department supervision for assistance to correct the problem. Procedures will always be used in concert with data sheets.

4.4.6.1. At times during the performance of procedures, plant conditions will prevent or mask a response expected in the procedure. When this occurs, the department supervisor is to be contacted. The department supervisor, with concurrence from the Maintenance Support group, may authorize the procedure to continue with an exception taken for the specific response. All exceptions taken and the reason for the exception shall be noted in the Discrepancies/Remarks section of the procedure. An ER shall be generated per AP 0009 for any procedure that can not be completed as written.

4.4.7. When surveillance procedures are to be performed over a number of days the date of actual component completion will be documented in the procedure and the shop surveillance list.

4.4.8. Environmentally Qualified Equipment When work is performed on EQ equipment it is essential that any changes be documented or that the component is returned to its original qualified condition. The following procedures are established to ensure compliance with the code requirements and must be referenced as applicable.

4.4.8.1. AP 0092, used for changes or supplemental clarification to EQ program manual.

AP 0310 Rev. 20 Page 8 of 24

4.418.2. AP 0021, describes the process of WO review and actions to take as necessary.

4.4.8.3. AP 0305, provides guidance and establishes a mechanism for the maintenance of I equipment qualification files.

4.4.9. Adjustments/Alterations Tolerances are established based on balancing the necessity to prevent violations of design limits and the reduction of adjustments required. At times it may be prudent to optimize the calibration prior to the instrument exceeding the specified tolerance.

4.4.9.1. Functional Calibrations If during a functional calibration it is identified that the instrument is in tolerance but may need to be adjusted the supervisor shall be informed. Based on available information the calibration section of the procedure may be entered to optimize the readings. The following shall be used to identify test results.

AS-FOUND data which is out of tolerance or adjustments made per the above supervisors determination are to be circled in RED.

AS-LEFT data which is out of tolerance is to be circled in RED and documented in the discrepancy section of the data sheet or on the data page of the PM work order and brought to the attention of the supervisor.

  • IC Supervisor will evaluate As-Left condition and advise the Department Superintendent and Shift Manager of any Out of Service condition.

AP 0310 Rev. 20 Page 9 of 24

4.4.9.2. Other Calibrations NOTE It is preferred that all instruments are returned to the cardinal point if the adjustment is easily done. Instruments within thetolerance range are considered to meet the minimum requirements. Concerns should be brought to the supervisor's attention.

If not delineated in the procedure or WO, when performing calibrations if the as-found values are near the extremes of their acceptable range they should be adjusted. The following example shall be used to determine if adjustments will be made.

Example:

Input = 10 psig Output = 10 mA Tolerance = +.5 Accuracy Range 9.5 to 10.5 Required Calibration = 1 mA x 10% = .1 mA Values between 9.5 to 9.6 and 10.4 to 10.5 require recalibration.

4.4.9.3. Temporary electrical jumpers and lifter leads.

NOTE The instructions contained in AP 0315 are not provided to circumvent the requirements of AP 0140, Vermont Yankee Local Control Switching Rules, or AP 0020, Control of Temporary Modifications. Prior to utilizing AP 0315, it must be determined that these procedures do not apply.

To assure the proper administration and documentation of all temporary electrical jumpers and lifted leads AP 0315 must be used, unless the necessary controls are in the procedure being implemented.

4.4.10. Measuring and Test Equipment (M&TE)

I In accordance with the Entergy QA Program controls will be established to assure the I proper use and accuracy of M&TE. The I/C Department has established procedure DP 0301 for this purpose.

AP 0310 Rev. 20 Page 10 of 24

4.4.11, General Condition Inspections 4.4.11.1. During the performance of all surveillance procedures and maintenance activities, an inspection of the general condition of equipment being tested or worked on is to be accomplished. Also a determination of failure cause must be considered.

Discrepancies will be noted on Data Sheets and Work Orders. This inspection is to include but not be restricted to the following:

  • Evidence of moisture or oxidation,
  • Evidence of overheating,
  • Evidence of wear,
  • Evidence of leaking (manual instrument valve stem leaks may be adjusted),
  • Loose or poorly made connections (process or wiring),
  • External damage,
  • Security of mounting.

4.4.11.2. The requirements of AP 6024 including Appendix C, "Work Area and Adjacent Equipment Inspection Guideline" shall also be complied with.

4.4.12. Documentation In addition to the requirements established in the referenced procedures discussing the documentation of WO closeout, Identification of M&TE, Issuance of Event Reports, etc; the following information will be required when performing maintenance or surveillance activities.

4.4.12. 1. If not already covered by specific procedure step, WO data sheet, or a tagging order, all plant equipment "removed from" and "returned to" service will have "Performed By" and "Verified By" Sign-Offs in the WO notes.

(AUD1TRPIT96O6....1) 4.4.12.2. In the recommendation section of the WO all opportunities for improvement, recommendations to prevent recurrence and/or need for further action shall be documented. To ensure review of recommendations use the 00 (Further Evaluation Recommended) failure code.

4.4.12.3. Complete the Probable Cause portion of the WO by providing what is felt to be the most probable cause of the failure based on observations made during the repair effort.

AP 0310 Rev. 20 Page I11 of 24

4.4.12.4. If during the performance of a procedure it is discovered that a Corrective Maintenance WO is needed, the following steps are to be taken:'

  • If the corrective maintenance WO does not interfere with the completion of the procedure, complete the activity and initiate a WR and note the number in the Discrepancy Section of the Data Sheet.
  • If the corrective maintenance WO will interfere with the completion of the procedure, contact the Supervisor and determine the best method of restoring the system to it's pretest condition, notify the Shift Manager of the condition and act upon the recommendations. Initiate a WR and note the number in the Discrepancy Section of the Data Sheet.

4.4.13. Test Equipment Hook-Up To Contaminated Systems During the performnance of routine calibrations of plant instrumentation, JIG Specialists are required to connect test equipment to various potentially contaminated plant systems.

4.4.13.1. Prior to work on instrument racks that are posted as contaminated, RP shall be contacted to determine if any special controls are required.

4.4.13.2. For work on instrument racks or individual instruments which are not posted as contaminated, the following bulleted items can be used to accomplish the connections. In lieu of bulleted items below, RP may be contacted for specific direction and the RP directed actions followed.

  • Obtain and wear rubber gloves (except when handling isolation/test valves).
  • Place a containment device or absorbent material under the test fitting and open slowly.
  • Make connections and perform testing as required.
  • After testing, remove connections and wipe all fittings and tools with a cloth.. Consider all items to be contaminated and place in a bucket, or other suitable container appropriately marked identifying the contents as potentially contaminated.
  • Remove and dispose of gloves as contaminated.
  • Perform any required valve manipulations without rubber gloves.
  • Return unused or extra tools to the JIG Hot Shop. Treat buck *etand contents as contaminated, dispose of unwanted material and wipe down tools and inside of bucket.

AP 03 10 Rev. 20 Page 12 of 24

At the end of the day bring all potentially contaminated equipment to the' RP Checkpoint for survey. After survey by RP, tools may be stored in the Checkpoint M&TE locker for use the next day.

4.4.14. Permanent and Temporary Labels (INS9705020216)

Dymotape labels are permissible for use in lighting panels to identify breaker position, but should not be used for general equipment identification. The following process must be complied with regarding equipment labeling.

4.4.14.1. A WO will be generated when it is identified that a new or replacement label is needed.

4.4.14.2. If a temporary label is required, with the Department Superintendent's permission, make a Dymotape label. Prior to installing the label verify component identification then install it.

4.4.14.3. Upon receipt of the permanent Bakelite label, one individual will affix the tag with appropriate fasteners in accordance with the WO, ensure the component identification and the label contents match. (If required the temporary label may be removed to install the permanent label.)

4.4.14.4. Independent verification will be.required to assure component identification, label contents and proper installation.

4.4.14.5. After proper application of the label and independent verification the temporary label shall be removed if one exists. (If not previously removed) 4.4.15. If during the performance of work activities it is required to leave tools or equipment unattended for a period of time, an I/C "Work in Progress" tag shall be hung at the job site with the appropriate information on it, (WO#, Name, Date).

4.5. Work Review and Responsibilities At the start of any task a preparation review is required and upon completion of all work activities such as corrective/preventive maintenance, surveillance tests or calibration the work performed and results generated must be reviewed and properly addressed. The following are responsibilities assigned to I/C personnel.

AP 0310 Rev. 20 Page 13 of 24

4.5.1. Specialist 4.5.1.1. Before starting work Review the WO for Permit requirements and obtain any as necessary.

(AP 0042, ENN-DC-161, AP 0140, AP 0077, or AP 0502, etc.)

  • Review the WO scope and ensure a thorough understanding of the job and boundaries. The scope shall not be exceeded with out compliance to AP 0021, AP 0049, and AP 0050.

0 Review documents for any required notifications and make them as necessary.

Review the Safety Manual for any requirements and take appropriate actions.

If parts are required, review the WO Safety Classification to assure the "P" tag info is correct for the application.

Review Procedures including prerequisites and precautions.

Determine if any housekeeping requirements are necessary in accordance with AP 6024 or AP 6026.

  • Review EQ file and obtain any walk down sheets if needed.

Review Equipment Manuals.

Review drawings and stamp as necessary for field use, see Section 4.6.

Review BOP cal data sheets (If Applicable).

  • Review M&TE requirements and sign out tools.

AP 0310 Rev. 20 Page 14 of 24

4.5.1.2. Upon completing work.

  • Review Procedure for completion including all data sheets. Ensure all out of spec data is red circled.
  • Review WO to assure scope was met and completed.
  • Review WO completion notes to assure description of work is accurate, complete and housekeeping closeout inspection is done.
  • Review revision submittals to assure they are accurate as needed.
  • Issue Event Reports as necessary.

NOTE An Event Report will be initiated whenever a component's as-left condition is such that operability has been challenged.

0 Return material as required by ENN-MP- 116.

  • Request a Job Order File if required per AP 6022.

Enter information to the Work Order Approvers section indicating work completion.

  • Perform required steps of AP 0021 for WO closeout.
  • Ensure all computer/chart recorder printouts, vendor reports, marked up drawings , copies of stock issue tickets and "P" tags, calibration data sheets and/or any QC reports are turned in with the completed work package.

AP 0310 Rev. 20 Page 15 of 24

4.5.2. Supervisor 4.5.2.1., Before assigning work

  • Review work activity and personnel training and assign qualified personnel to perform the job,
  • Review Work scope for tests or evolutions which may degrade the plant's safety margins. Consideration should be given to notifying the Department Superintendent for the need of additional management oversight (SOER 9101) and implementing AP 6100, Infrequently Performed Tests or Evolutions.

0 Review the work scope to determine if temporary electrical jumper and/or lifted leads require implementation of AP 0020, AP 0140, or AP 0315.

0 Review the work scope to determine if the activity may create a significant fire hazard or degrade any portion of the fire protection system. Implement AP 0042 and ENN-DC-161 if necessary, 0 If work is Minor Maintenance or Troubleshooting (AP 0049 and AP 0050),

review scope to ensure the work will not exceed the Minor Maintenance or Troubleshooting definition per AP 0049 or AP 0050.

  • Perform a pre-job briefing in accordance with AP 0052 to insure the individual assigned has an understanding of the work scope, 0 Review any Safety and Housekeeping AP 6024 or AP 6026 requirement,

. Review the work order for the need to perform Peer Inspections (AP 6025),

assign individuals as required, 4.5.2.2. Upon completion of work, review the following:

4.5.2.2.1. Procedures and/or Work Orders 0 Review all data sheets for completion and readability.

  • Review all data sheet blocks and assure they are filled in or N/A'd with an explanation.

Ensure all signoffs and dates are entered including housekeeping inspection closeout.

Ensure the M&TE used has been recorded.

AP 0310 Rev. 20 Page 16 of 24

  • Ensure all AS-Found/AS-left data out of spec is circled in red. Any surveillance with out-of-spec data will be routed to the applicable Maintenance Support Individual for review.
  • Ensure all acceptance criteria had been met.
  • Ensure the Surveillance List had been signed off.

0* Ensure the I/C Calibration Data Sheet form is complete if applicable.

  • Ensure there is documentation of equipment returned to service.

(AUDlTRPT9606_01)

  • Review attached records, graphs, etc. for QA records and note on the WO.
  • ' Assign reconciliation code and failure codes Per AP 0021. If in the recommendation section of the WO there are opportunities for improvement, recommendations to prevent reoccurrence and/or a need for further action identified ensure that a "00" (Further Evaluation Recommended) Failure Code is assigned.
  • Disposition all remarks in the WO/Procedure notes. If immediate Maintenance Support review for disposition of technical issued is necessary, contact the appropriate Support group to resolve. If there are opportunities for improvement, recommendations to prevent reoccurrence and/or a need for further action identified ensure that a "00" (Further Evaluation Recommendation) Failure Code is assigned.
  • Review all WO feedback forms, add notes to form as necessary and forward to Work Control Department.

4.5.2.2.2. Review for out of tolerance data and noted discrepancies to determine if

  • Tech Spec Administrative Limits were exceeded,
  • Tech Spec, TRM, or ODCM Limits were exceeded,
  • Environmental Qualifications limits expired.

4.5.2.2.3. Initiate an Event Report if:

  • The requirements of Step 4.5.2.2.2. above are not met.
  • The component's as-left condition is such that operability is challenged (if not previously initiated).

AP 0310 Rev. 20 Page 17 of 24

4.5.2.2.4. Review the Post Maintenance Test assuring proper component operation.

The PMT shall verify that the work activity corrected the identified discrepancies and did not create any new unresolved issues.

4.5.2.2.5. Determine whether a Failure Cause Analysis is required, reference Appendix C. Failure Code "00"must be assigned to Work Orders.

4.5.2.2.6. All applicable documents are updated such as VYEM's, EQ Files, Equipment History and Procedures, initiate AP 6022 if necessary.

4.5.2.2.7. Peer Inspection Reports are complete and problems addressed.

4.5.2.2.8. If WO involves maintenance on an AOV (Air Operated Valve) forward entire package to the Program/Component AOV Engineer for review.

4.5.3. Department Support Individual/Maintenance Coordinator 4.5.3.1. Department Support Individual/ Maintenance Coordinator review of Work Orders and Surveillance Data will be performed in accordance with the following:

4.5.3.1.1. If in the recommendation section of the WO there are opportunities for improvement, recommendations to prevent recurrence and/or a need for further action identified the following shall be performed:

  • Provide an explanation on the WO whether you agree or disagree.

Identify any action that was or will be taken. If no action will be taken on the recommendation this should be discussed with the individual who made the suggestion so that he will be aware of the reasons.

Consult the Department Superintendent if a recommendation can not be achieved.

4.5.3.1.2. Review Minor Maintenance WO's to ensure adequate documentation of the work performed.

4.5.3.1.3. Ensure the PMT addresses the WO problem description.

4.5.3.1.4. Review any calibration data associated with the Work Order's or procedures to ensure the:

  • As-left data is acceptable and that there is no evidence of a negative trend developing.

As-found data does not indicate a programmatic problem with past calibrations.

AP 0310 Rev. 20 Page 18 of 24

An Event Report (AP 0009) will be initiated for any negative trend identified, as-left condition where equipment operability is challenged or programmatic problem identified with past calibrations. (If not previously initiated).

4.5.3.1.5. Ensure that calibration data is input into the instrument calibration history.

4.5.3.1.6. Review the reconciliation code and failure code. If any changes are required discuss it with the Supervisor.

4.5.3.1.7. Review the parts list and ensure that the parts were the appropriate safety classification.

4.5.3.1.8. Verify that any special P-Tag requirements have been addressed in the WO notes.

4.5.3.1.9. Ensure all maintenance items have final closure review i.e., if the failure is end of life, should a PM be put in place to preclude failure in the future; 4.5.3.1.10. Maintenance Support individual will assist in developing QC Peer inspections with the Work Control Peer Inspection Coordinator..

4.5.3.1.11. Maintenance Support individual will evaluate unacceptable Peer Inspection results and provide resolution to the Department Supervisor.

4.5.4. I/C Secretary 4.5.4.1. Ensure that the most recent procedure revision is contained in the procedure file and that sufficient quantities of procedure data sheets are available.

4.5.4.2. Transfer all M&TE data to the M&TE tracking forms perDP 0301.

4.5.4.3. Transfer all Calibration Data Sheet Information to the I&C Cal Database.

(ER 99-0755,02) 4.5.4.3.1. Obtain and independent verification ofdata entry.

4.5.4.4. File all required forms and attached QA records per AP 6807.

4.5.4,5. Ensure that all data and other pertinent information is properly maintained'per procedures AP 0021, DP 0305, AP 6807.

AP 0310 Rev. 20 Page 19 of 24

4.6. Administrative Controls 4.6.1. Field use of Controlled Documents The use of controlled documents such as P&ID's, CWD's, other Controlled Prints, VYEM's in the field is highly desirable and necessary when performing troubleshooting and repairs. The following process is designed to ensure that the necessary documents are available for use while ensuring that no work is performed with outdated or uncontrolled documents.

This instruction has been developed with the realization that there are differing situations in regard to the use of controlled documents and provides differing directions as to the control of this information.

4.6.1.1. Use of Documents in Clean Non-Contaminated Areas.

The original document may be used in this situation by signing out the document and inserting the card in the storage location.

  • The document must be returned to its storage location upon completion of work in its original condition.

4.6.1.2. Use of Documents in Contaminated Areas or where it couldbe destroyed or is to be marked-up.

  • Make a copy of the document and stamp it with the information below.

WORKING COPY OF: (P&ID,CWD,VYEM,OTHER)

TO BE USED FOR (WO # / OTHER)

VALID UNTIL (DATE):

The "VALID UNTIL" date shall not be more then 14 days from the date of the copy being produced.

Upon completion of work or expiration of valid date any mark-ups will be addressed and the copy destroyed.

4.6.2. Review and Control of Procedure Change Recommendations.

This section describes the internal review and change process. AP 0096 is the controlling document. The process described below is considered to be an enhancement to the parent document. This process is meant to provide good information to the procedure developers, effect a working communication link between commentor and resolver, and provide a method of resolving any difference.

AP 0310 Rev. 20 Page 20 of 24

4.6.2.1. Inter-Department Review and Comment Process The "Procedure Change Recommendation Form" (VYAPF 0096.05) will be available to all members of the department for communicating procedure enhancement opportunities.

This form with comments filled out by the initiator will be forwarded to the Support individual.

The Maint. Support Manager will assign a member of the Support Group the responsibility for reviewing the suggested change and resolving the comments.

The individual assigned to review and resolve the comments will meet with the initiator to further clarify the comments and discuss resolutions.

    • Unresolved comments may be pursued by the initiator through the management organization.

Upon resolution of the comments, the individual performing this task will review the results with the Support individual. If procedure changes are required, a plan for making these changes within a proper time frame shall be established.

I

  • The disposition is approved by the Department Superintendent.

A copy of the completed VYAPF 0096.05 form will be sent to the originator.

For long term corrective action, a copy of this form will be placed in the shop procedure file for information.

AP 0310 Rev. 20 Page 21 of 24

4.6.3. Incorporation of Instrument Uncertainty Calculations into I&C Surveillance Procedures.

4.6.3.1. Instrument Uncertainty Calculations will be incorporated in the discussion section in a table format as follows:

  • Channel being monitored ,(optional).
  • Instruments that are being checked by the procedure.
  • List the measured parameters.
  • List the action that will occur at the setpoint.
  • List the required Limiting setpoint/Tech. Spec. value.
  • List the setting established as the VY administrative limit.
  • Include all factors used in this determination (i.e. Head correction).
  • List the allowable As-Found tolerance from the Uncertainty calculation.

AP 0310 Rev. 20 Page 22 of 24

5.0 REFERENCES

AND COMMITM[ENTS 5.1. Technical Specifications and Site Documents 5.1.1. Section 1.0 5.1.2. VOQAM, Vermont Yankee Operational Quality Assurance Manual 5.2. Administrative Limits 5.2.1. None 5.3. Codes, Standards, and Regulations 5.3.1. None 5.4. Commitments 5.4.1. AUDITRPT 9606_01 5.4.2. :INS 970502-02_16 5.4.3. ER 990755_02, Control of I&C Cal Program 5.5. Supplemental References 5.5.1. SOER 91-01, Conduct of Infrequently Performed Tests or Evolutions Plant Controlled Drawings 5.5.2. VY E&C Preventive Maintenance System Analyzed Maintenance Project (SAM) 5.5.3. Reliability Based Maintenance (RBM) 5.5.4. ENN-LI-102, Corrective Action Process 5.5.5. ENN-MP-1 15, Material Issues and Staging 5.5.6. ENN-MP-116, Material Receiving and Returns 5.5.7. ENN-DC-161, Transient Combustible Program-5.5.8. ENVY Safety Manual 5.5.9. AP 0009, Event Reports 5.5.10. AP 0020, Control of Temporary and Minor Modifications 5.5.11. AP 0021, WorkOrders 5.5.12. AP 0042, Plant Fire Prevention and Fire Protection 5.5.13. AP 0047, Work Request 5.5.14. AP 0048, Work Planning 5.5.15. AP 0049, Minor Maintenance 5.5.16. AP 0050, Trouble Shooting 5.5.17. AP 0052,Pre-Job Brief 5.5.18. AP 0053, Fix It Now (FIN) Process 5.5.19. AP 0092,Environmental Qualification (EQ) Document Change Notification 5.5.20. AP 0095, Plant Procedures 5.5.21, AP 0096, Procedure Development, Review, Issuance and Cancellation 5.5.22. AP 0140, Vermont Yankee Local Control Switching Rules 5.5.23. DP 0210, Tracking and Trending Program 5.5.24. AP 0214, Preventive Maintenance Program AP 0310 Rev. 20 Page 23 of 24

5.5.25. AP 0305, I/C Department Environmental Qualification (EQ) Maintenance and Surveillance (M/S) Program 5.5.26. AP 0315, Equipment Alterations 5.5.27. AP 0502, Radiation Work Permits 5.5.28. AP 4000, Surveillance Testing Program 5.5.29. AP 6022, Job Order Files 5.5.30. AP 6024, Plant Housekeeping and Foreign Material Exclusion/Cleanliness Control 5.5.3 1. AP 6025, Independent Inspection 5.5.32. AP 6026, Refuel Floor Foreign Material Control Procedure 5.5.33. AP 6100, Infrequently Performed Tests or Evolutions 5.5.34. AP 6807, Collection, Temporary Storage and Retrieval of QA Records 6.0 FINAL CONDITIONS 6.1. None 7.0 ATTACHMENTS 7.1. VYAPF 0310.01 I/C Surveillance 7.2. VYAPF 0310.02 Deleted 7.3. VYAPF 0310.03 Deleted 7.4. Appendix A Deleted 7.5. Appendix B Deleted 7.6. Appendix C Failure Cause Analysis 7.7. Appendix D Use of Thread Sealant for Fluid/Systems 7.8. Appendix E Deleted 7.9. Appendix F Lubricant Quick Reference 7.10. Appendix G Deleted 7.11. Appendix H Surveillance Schedule Information 7.12. Appendix I Deleted i8.0 QA REQUIREMENTS CROSS REFERENCE 8.1. None AP 0310 Rev. 20 Page 24 of 24

I/C SURVEILLANCE Week Beginning DATE TEST TS EQ QC DUE PROC NUMBER DESCRIPTION Y/N Y/N Y/N DATE(S) INITIALS VYAPF 0310.01 AP 03 tO Rev. 20 Page 1 of 1

APPENDIX C FAILURE CAUSE ANALYSIS A failure cause analysis should be considered as an adjunct to a corrective maintenance repair when the component that failed is safety or capacity related and any of the following apply:

The cause of the failure was not identified during the repair process.

The failure resulted in an LCO condition or degraded safety system performance.

The failure cannot be attributed to "end of life" with any degree of certainty.

Doubt exists in the mind of the Specialist or Maintenance Support individual that the replaced/repaired component won't fail in the same mode due to installation, design inadequacies.

Past history indicates similar failures of an unacceptable frequency.

The failure resulted in degraded plant system performance.

A cause analysis could be cost beneficial based upon gaining information that might decrease maintenance frequencies, or down time on the equipment.

Appendix C AP 03 10 Rev. 20 Page 1 of 1

APPENDIX D USE OF THREAD SEALANT FOR FLU[D/SYSTEMS MEMORANDUM TO: DISTRIBUTION . XVERNON DATE: 6/8/94 FROM: D.C. GIRROI>4 VERNON FILE: 3.1

SUBJECT:

THREAD SEALANT FOR FLUID/AIR SYSTEMS

References:

a) Memo, J.E. Gardner to T.A. Watson, dated 1/17/86, Use of teflon on primary system fittings b) Memo, H. Heilman to P.B. Corbett/G. Cappuccio, dated 4/27/94, Use of liquid thread sealants .......

c) General Electric RICSIL No. 67, dated 4/1/94, Use of thread sealants on scram solenoid pilot valves The above references provides guidance for sealing threads on swagelok fittings and small pipe fittings for both liquid and air applications.

The use of teflon tape and liquid sealants provide potential problems for safety related equipment and instrument components.

If teflon tape is not correctly applied to connections it can be dislodged and adversely affect valves, instruments and other vital equipment. This has occurred at least once at Vermont Yankee resulting in the leak rate testing failure of valves CRD-413A and 413B (see LER 92-10).

If liquid, thread sealant is not cautiously applied to connections intrusion into the process system is possible and may degrade certain components. Air systems with installed pilot valves using Buna-N and Dupont Viton elastomers are particularly susceptible to degradation when in contact with certain thread sealants. Neolube 100, Locktite PST 580, and Locktite 242 are specifically identified as inappropriate for use in air systems. Vermont Yankee has experienced specific problems with certain transmitter installations due to the use of liquid sealant.

Based upon the above discussion and consideration of the references, ME&C agrees that new guidance for sealing fluid/air systems is warranted.

Therefore:

1) Liquid thread sealant shall not be used in Service Air or Instrument Air system installations. When liquid thread sealant is used, great care shall be taken to insure that no liquid is applied to the first thread that enters the female thread. This practice will help to mitigate migration.
2) Teflon Tape thread sealant shall be used for all Service Air and Instrument Air Installations. Great / care shall be taken in using Appendix D AP Page0310 I ofRev.

2 20

APPENDIX D (Continued) teflon. A minimum of at least one full end thread on the NPT fitting shall be left uncovered to absolutely assure that no tape is left in contact with the process fluid.

3) Teflon tape thread sealant is also the preferred material for fluid connections which involve instruments. For other fluid system applications, the selection of thread sealing material will be decided on a case by case basis and will consider the fluid medium, pressure, temperature and any other environmental affects.
4) Training should be provided to all appropriate plant and contractor personnel in the proper application of teflon tape thread sealant and the prohibition of use of liquid thread sealant. The training shall also caution personnel to carefully clean both male and female fittings during all repairs or reinstallations.
5) Training should also be provided for all appropriate plant and contractor personnel in the proper installation procedure for swagelok tube fittings. Experience warrants' such training and this memo will serve to provide this recommendation.

Approved:

Approved: ;4--

,4/e: 7.4 77, USER Department Manager or designee Date distribution:

Bernie Buteau Greg Maret Mike Watson Terry Watson Mike Trombley Larry Wood.

a~~ae - C 9, I,,? C977r.

Appendix D AP 0310 Rev. 20 Page 2 of 2 3

APPENDIX F LUBRIJCANT OUICK REFERENCE Name / Type Application [VY Stock # Reference # Equivalent NOTES Dow Coming 55M Gen Plant Use 2000069022 For General plant use - except HCUs.

Except HCUs _ OQA.

Dow Coming High Vacuum HCU/CRD 2000058757 GEK-9582C GE 351 This should be used for all HCU O-rings.

Grease _ SIL 395 (not 55M). GE# 209A6805P002. OQA.

Dow Coming 33 IRMISRMs 4000058902 OP 5302/5333 GE# 213A7170P001 Dow Coming C-20057 LPRMs See Equivalent OP 5370 Dow Coming Equivalent per GE letter DH to TAW 2/14/89.

GEK-32384 33 Additional Reference GEK-83439.

Gear Oil, AGMA #8 IRM/SRM Drives 45OB048509 OP 5333 GE# 176A1777P001 (Rev 5 or 6)

GEK- 13962G Texaco Aircraft Feed Rate 40SU156166 OP 5353 Use in Feed Rate Valve Snubber Hydraulic Oil 15 Valves Thread Lubricant Gen Plant Use 2000049014 Various D50YP5B Equivalent per PEGIKRS.0028.

FELPRO N5000 HCUs GEK-9582C D50YP5A OQA Silver Goop 2000078647 D50YP3 Superseded GEK uses Dow Coming 41 2000069025 Dow Coming 111. Rosemount Xmtr 50GE182985 Rosemount Dow Coming

  • Equivalent for Rosemount xntrs only, per
  • letter TJL to RAC of 11/30/92.

Vulcanlube NLGI, Scoop Tube 40LU152265 OP 5322 Location: I/C hot shop.

Grade I Positioner GE Silicone Compound 640 46GE060724 GE# 175A8251P001 (Dielectric)

Hydraulic Sealant IRIMSRMs GEK-32384 GE# 225A4819P001/2 Locktite # 56931 Lubriplate, Fiske Brothers Eagle Timers

  • Per vendor to FPL, any good silicone grease is adequate.

Dow Coming 44 DeZurik Valves Vendor Dow Corning Per D. Kohl of DeZurik, 55M is equal to 44 for

._ -_ Literature 55M cylinder and rubber good applications.

This is not intended as an all-inclusive list. Provide feedback for additions to Maintenance Support.

Appendix F AP 0310 Rev. 20 Page 1 of I N

APPENDIX H SURVEILLANCE SCHEDULE INFORMATION PRE-STARTUP OP 4300, 4301, and 43108 are performed within 7 days of a startup.

All I/C operating procedures are performed prior to startup unless plant requirements must be established in order to perform (see below).

OP 0105 STARTUP The following procedures are tested during startup when plant conditions permit:

Procedure Function Requirement OP 5371 LT-2-3-70 Hot Cal >212°F OP 4386 SRV Bellow Venting Normal Operating Temp OP 4308 APRM Cal RMSS in Run OP 43104 MSIV Isolation RMSS in Run OP 4379 Drywell Torus D/P After D/P Established OP 43105 TSV Logic >30% 1st Stage Press OP 4304 RBM Functional >30% Power POST STARTUP Additionally, logic procedures OP 4332, OP 4343 and OP 4306 are performed within a week after startup.

SYSTEM VS. OPERABILITY CONDITION RPS: Need >212°F or critical. If <212°F and (3.1.1 Note 1) subcritical only need 1) Mode switch in S/D,

2) Manual Scram, 3) High Flux IRM, and 4)

High SDV.

RMCS: Need when RMCS is not in S/D.

ADS: Need >100 psi and irr fuel in vessel. (3.5.F)

RCIC: Need >150 psi and irr fuel in vessel. (3.5.G)

HPCI: Need >150 psi and irr fuel in vessel and prior (3.5.E)

S/U from cold S/D.

CS and LPCI: Need when irr fuel in vessel and prior Rx S/U (3.5.A, 3.5.H) from cold S/D. If cold S/D and no work that could drain vessel, all may be relaxed.

Containment Spray: Need >2120 F. (3.5.B)

Post Accident: Power operation. (3.2.G)

Primary Containment: Need Rx critical or >2120F with fuel in vessel. (3.7.C)

Secondary Containment: RMSS in run, S/U or hot S/D; movement of irr (3.7.C) fuel or fuel cask; core alts; or OPS which could drain vessel.

SGTS: RMSS in run, S/U or hot S/D with Secondary (3.7.B.1)

Containment required.

Drywell/Torus D/P: Need within 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> of reaching NOT/NOP. (3.7.A.9)

Rx Bldg/Torus and Drywell/ Torus Need when Primary Containment required. (3.7.A.5/6)

VAC Breakers:

Appendix H AP 0310 Rev. 20 Page 1 of 2

APPENDIX H (Continued)

Test Numbers I xxx = weekly 2xxx = monthly 3xxx = quarterly 4xxx = semiannual 5xxx = annual 7xxx = 18 month operation (end of outage to end of outage) 8xxx = 18 month refuel outage Schedule events are from base date (not last performed).

Drop dead dates are from last performed.

Any surveillance can be done late up to drop dead date with no (future or past) effects.

Surveillance done early must be cautious of time till next scheduled surveillance. If 5 weeks lapse until next monthly, you can only perform 3 days earlier than scheduled.

Tech Spec +/-25%

Non-Tech Spec +/-50%

Weeklies: 8.75 days (8 days rounded) max Monthlies: 38 days max SHUTDOWN The following surveillances should be maintained current during refueling outages to ensure shutdown requirements for NIs, CS, LPCI, and Secondary Containment are satisfied. (SDV required for both RPS and RMCS, but is quarterly.)

NEUTRON MONITORING (Every 7 days when not in S/D) 4300 SRM (for RMCS) 4301 IRM (for RPS and RMCS)

CORE SPRAY & LPCI (Every 30/38 days) 4337 Rx Level (only low needed) 4338 Drywell Press (needed?)

4340 Rx Low Press Permissive 4342 Rx Low Press Permissive 4348 Core Spray Power Monitor 4351 Rx Low Press - RHR S/D Cooling 4353 RHR Power. Monitor SECONDARY CONTAINMENT (Every 30/38 days) 4313 Rx Level 4326 RBV/Refuel Floor Rad 4335 RBV/SGTS Power Monitor 4311 Drywell Press (needed?)

Appendix H AP 0310 Rev. 20 Page 2 of 2