ML19312C970

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Radwaste Disposal:Reactor Bldg,Plan Elevation 305 Ft
ML19312C970
Person / Time
Site: Crane Constellation icon.png
Issue date: 03/13/1978
From:
BURNS & ROE CO.
To:
Shared Package
ML19312C956 List:
References
TASK-TF, TASK-TMR 2403, NUDOCS 8001170598
Download: ML19312C970 (1)


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Nuclear Safety Evaluation Does the attached pinceihite change:

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  • (b) create the possibility for an acciilent or nialfunction of a thflerent type than any evaluated previously in the safety analysis report?.

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' (c) reduce the margin of safety as defined in the basis for any technical specification?

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' (h) have a significant adverse effcct on the environment?..

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Nuclear Safety Evaluation Does the attached procedure change:

  • (a) increase the probability of occurrence or the consequences of an accident or malfunction of equipment important to safety?........

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  • (b) create the possibility for an accident or malfunction of a different type than any evaluated previously in the safety analysis report?....

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  • (c) reduce the margin of.afety as delined in the basis for any technical specification?..... yesO noR Details of Evaluation u.pi..n on,.n..

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  • (b) have a significant adverse effect on the environment?...................... yesO noO
  • (c) involve a significant environmental matter or question not previously reviewed and evalua ted b y t he N.R.C........................................ yes O no D Details of Evaluation ( Attach additlunal page.If required)

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  • k Table of Effective Pages

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hp Pat pl hRedisio_rv f I Page, Date Revision Page Date Revision a

1.0 05/17/77 0

26.0 05/17/77 0

51.0 2.0 05/17/77 0

27.0 05/17/77 0

52.0 3.0 01/31/78 1

28.0 05/17/77 0

53.0 4.0 05/17/77 0

20.0 05/17/77 0

54.0 5.0 01/31/78 1

30.0 05/17/77 0

55.0 6.0 01/31/78 1

31.0 05/17/77 0

56.0 7.0 05/17/77 0

32.0 05/17/77 0

57.0 8.0 05/17/77 0

33.0 58.0 9.0 05/17/77 0

34.0 50.0 10.0 01/31/78 1

35.0 60.0 11.0 01/31/78 1

36.0 61.0 12.0 01/31/78 1

37.0 62.0 13.0 05/17/77 0

3a.0 63.0 14.0 01/31/78 1

30.0 64.0 15.0 01/31/78 1

40.0 65.0 16.0 01/31/78 1

41.0 66.0 17.0 01/31/73 1

42.0 67.0 18.0 01/31/73 1

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44.0 60.0 20.0 05/17/77 0

45.0 70.0 21.0 05/17/77 0

46.0 71.0 22.0 05/17/77 0

47.0 72.0 23.0 01/31/78 1

48.0 73.0 24.0 05/17/77 0

40.0 74.0 25.0 05/17/77 0

50.0 75.0 Unit 1 Staf f Recommends Approval Unit 2 Staff Recommends Approval Approval

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I Date Approval Date 7

Cogn;/3nt Def t. Head /1 Cognirant Dept. Head

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., ' '.,l 2104-4.3

'. t Revision 0 05/17/77 THREE MILE ISLAND flVCLEAR STATION UNIT #2 OPERATING PROCEDURE 2104-4.3 WASTE GAS DISPOSAL SYSTEM Ta' ole of Contents SECTION PAGE

1.0 REFERENCES

3.0 1.1 Drawings Applicable for Operation 3.0 1.2 Operating Procedures Applicable for Operation 3.0 1.3 Manufacturers' Instruction Mantals 3.0 1.4 Applicable System Description 4.0 2.0 LIMITS AND PRECAUTIONS 4.0 2.1 Equipment 4.0 2.2 Administrative 5.0 3.0 PREREQUISITES 6.0 4.0 PROCEDURES 7.0 4.1 f ' art-Up 7.0 4.2 Normal Operation 8.0 4.3 Shutdown 9.0 4.4 'Special or Infrequent Operations 10.0 4.4.1 Decay Tank Discharge to the Station Vent 10.0 l

4.4.2 Shift of On-Line Decay Tank 12.0 4.4.3 Reuse of Haste Gas 13.0 4.4.4 Decay Tank to Decay Tank Transfer 15.0 4.4.5 Reactor Building Vent Header Start-Up 16.0 4.4.6 Reactor Building Vent Header Shutdo',fn 16.0 l

l 4.4.7 Vent Header to Station Vent Bypass 16.0 1.0 1

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2104-4.3

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Revision 0 05/17/77 Table of Contents (cont'd)_

SECTI0ri PAGE '

4.4.8 Compressor - Decay Tank Train Shutdown and Purge 18.0 4.4.9 Emergency Operations 21.0 APPEllDICES TITLE tj0.

Valve Line-Up A

22.0 Valve Line-Up Signature Sheet B

31.0 Waste Gas Release Data Sheet C

32.0 4

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2104-4.3 Revision 1 t.

1

/ 1/78 THREE MILE ISLAND NUCLEAR STATION UNIT #2 OPERATING PROCEDURE 2104-4.3 WASTE GAS DISPOSAL SYSTEM

1.0 REFERENCES

l.1 Drawings Applicable for Operation.

1.1.1 Radwaste Gas Disposal, B&R Flow Diagram 2028.

1.1.2 Demineralized Service Water, B&R Flow Diagram 2007, 1.1.3 Instrument Air, B&R Flow Diagram 2012.

i 1.1.4 Nuclear Services Closed Cooling Water, B&R Diagram 2030.

1.1.5 Reactor Coolant Liquid Waste Disposal, B&R Diagram 2027.

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1.1.6 Miscellaneous Liquid Waste' Disposal, B&R Diagram 2045.

1.1.7 Nuclear Sampling, B&R Diagram 2031.

1.1.8 Nuclear and Radwaste Nitrogen Supply, B&R Diagram 2036.

1.2 Operating Procedures Applicable for Operation.

1.2.1 2104-1.10, Nuclear and Radwaste Nitrogen Supply.

1.2.2 2104-1.11, Nuclear Plant Sampling.

1.2.3 2104-2.3, Instrument Air.

1.2.4 2104-2.2, Demineralized Service Water.

1.2.5 2104-3.2, Nuclear Services Closed Cooling Water.

1.2.5 2104-4.1, Miscellaneous Liquid Waste Disposal.

1.2.7 2104-4.2, Reactor Coolant liquid Waste Disposal.

1.2.8 2105-1.8, Radiation Monitoring.

1.2.9 2107-l.1, B0P Auxiliary Electrical.

1.2.10 HPP-1622.2, Releasing Radioactive Gaseous Waste from Unit 2.

1.3 Manufacturers' Instruction Manuals.

1.3.1 Nash Engineering Company, Waste Gas Compressors (55-00),

4 Bulletin No. 475-A.

3.0

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2104-4.3

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Revision 0 05/17/77 1.3.2 Victoreen Instrument Division, Radiation Monitoring (65.00).

1.3.3 Mine Safety Appliance, Waste Gas Filter (63.00).

1. 3. 4 Armstrong Float Type Liquid Drainer (999.22), Bulletin flo.

401-A, Model flo.21-312.

1.4 Applicable System Descriptions.

1. 4.1 Demineralized Service Water System, Index flo. 5.

1.4.2 Instrument and Service Air System, Index tio.10.

1.4.3 Radwaste Disposal, Reactor Coolant Liquid System, Index flo. 21.

1.4.4 Radwaste Disposal, Gas System, Index flo 22.

1.4.5 fluclear Services Closed Cooling Wate.- System, Index flo. 24.

1.4.6 tiuclear Sampling System, Index fio. 25.

1.4.7 tiitrogen for fluclear and Radwaste System, Index No. 30.

1. 4. 8 Radwaste Disposal, Misc. Liquid Systeri, Index flo. 44.

2.0 LIMITS Ario PRECAUTI0t15 2.1 Equipment 2.1.1 The maximum number of compressor starts must not exceed ten (10) per hour to avoid damage to the compressor and associated controls.

2.1.2 flever run a compres.,or without demineralized water - even when checking motor rotation.

flormal water prime in one-third to one-half a casing.

2.1.3 ilever start a compressor when the water level is above the casing centerline.

This can lead to rotor blade failure.

2.1.4 The compressor requires grease lubrication of the pedestal and motor ball bearings.

Do not over grease as this will cause

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the bearings to run hot and possible cause trouble.

4.0

2104-4.3 Rev' sion 1 01/3' / 78 2.1.5 During compressor operation the stuffing box gland should be adjusted to permit a slight outward leakage of water.

2.1.6 The separators should be blown down daily to avoid scale and sludge formation.

2.1.7 The isolation valves for the unloader valves of the compressors must be open prior to starting the compressors.

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2.1.8 Observe precaution when operating normally vented equipment which has been isolated from the vent header.

Care needs to be taken not to overpressurize nor to depressurize the equipment.

2.2 Adminis tra tive.

2.2.1 Comply with Unit 2 Administrative Procedure 1003, the Radiation Protection Manual.

2.2.2 No gas shall be released to the atmosphere without a Waste Gas Release Permit per HPP-1622.2.

2.2.3 The gas release rate shall never exceed 100 scfm as indicated by WDG-FI-3652 on Panel 3028.

2.2.4 The filter assembly shall be replaced when the radioactivity level in the filter becomes excessive or when the differential pressure drop reaches 10 inches of water at 100 scfm.

The clean filter has a pressure drop of 3 inches of water at 100 scfm.

2.2.5 Hydrogen concentration must he maintained at less than 3%

concentration in the waste gas header and the waste gas decay tanks.

If the concentration exceeds 3% hydrogen then nitrogen must be bled into the waste gas header and/or decay tank (s) to dilute the gas to less than 3% hydrogen 4

5.0

2104-4.3 Revision 1

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01/31/78 2.2.6 Observe precaution to minimize the possibility of suffocating personnel working on or near the Waste Gas System.

2.2.7 Do not pressurize a Waste Gas Decay Tank above 110 psig. The alarm setpoint is 115 psig.

The relief valve is sht at 120 psig relieving to the Station Vent by-passing the Waste Gas Filter.

3.0 PREREQUISITES Initial Each Step Upon Satisfactory Completion.

3.1 The iluclear and Radwaste flitrogen System is in operation per 2104-1.10.

3.2 The fluclear Plant Sampling System is in operation per 2104-1.11.

3.3 The Instrumert Air System is in operation per 2104-2.3.

3.4 The Demineralized Service Water System is in operation per 2104-2.2.

3.5 The fluclear Service Closed Cooling Water System is in operation per 2104-3.2.

3.6 The Miscellaneous Liquid Waste System is in operation per 2104-4.1.

3.7 The Radiation Monitoring System is in operation per 210S-1.8.

3.8 Power is available to the 480V MCC 2-32A and breaker 7CF for WDG-P-1A is closed.

Power is available to the 480V MCC 2-42A and breaker 7BR for WDG-P-1B is closed.

1 3.9 The Waste Gas System is lined-up per the Start-up Valve Line-up which is APPEllDIX A to these procedures.

3.10 The control switches on panel 302B for the Waste Gas Compressors are in the 0FF position.

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4.0 PROCEDURES i

Initial Each Step Upon Satisfactory Completion.

4.1 Start-up.

4.1.1 CilECK OPEN WDG-V172, the Waste Gas Compressors discharge CROSS-CONNECT. valve.

CAUTION: This valve must be open to enable both compressors to charge to a single decay tank.

4.1.2 OPEN WDG-V26A (B), the Decay Tank inlet valve, for the tank, WDG-T-1A (B) to be charged.

4.1.2

' CHECK the compressor moisture separators water levels per precautions 2.1.2 and 2.1.3.

Adjust the water level as required.

CAUTION: Comply with Unit 2 Administrative Procedure 1003, the Radiation Protection Manual.

The compressors are in a Radiation Zone VII.

_jt.l.3 PLACE the compressor control switches in RUN and monitor for abnormal noise and vibration.

CAUTION: Comply with Unit 2 Administrative Procedure 1003, the Radiation Protection Manual.

The compressors are in a Radiation Zone VII.

4.1.4 PLACE the compressor control switches in the desired made of operation.

NOTE:

For normal operation put one compressor in AUTO-HI and the other compressor in AUTO-LO.

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05/17/77 WUG-P-1A WDG-P-1B RUti RUti 0FF 0FF AUTO-L0 AUTO-LO AUT0-III AUT0-III 4.2 flormal Operation.

CAUTIO!!: Comply with Unit 2 Admi11strative Procedure 1003, the Radiation Protection fialual.

4.2.1 The following components are normally line-up to the vent header:

4.2.1.1 Miscellaneous Waste llold-up Tank, WDL-T-2.

4.2.1.2 Auxiliary Cuilding Sump Tank, WDL-T-5.

4.2.1.3 Spent Resin Storage Tanks, WDS-T-1 A,18.

4.2.1.4 Concentrated Waste Tank, WDS-T-2.

4.2.1.5 Reclaimed Boric Acid Tank, WDS-T-3.

4. 2.1. 6 Reactor Coolant Bleed floid-up Tanks, WDL-T-1A, 1B, 1C.

4.2.1.6.1 Reactor Coolant Drain Tank, WDL-T-3 (via WDL-T-1 A,18, IC).

4. 2.1. 7 Reactor Coolant Evaporator, WDL-Z-1 (when shutdown with' the vacuum broken).

4.2.2 The Vent lleader and Decay Tanks are periodically sampled for excessive hydrogen.

4.2.3 Pressure regulator, WDG-V59, throttles to control the compressor inlet pressure at 1.0 psig.

4.2.4 The Waste Gas System will operate automatically to maintain the Vent licader pressure ' etween 2.5 and 5.0 psig when the b

compressors are in the AUTO LOW modes' and at 1.0 psig when the compressors are in the RUrl mode.

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a 2104-4.3 Revision 0 05/17/77 4.2.5 Both compressors are normally lined-up to a single Decay Tank.

A Decay Tank can be pressurized to 110 psig.

After sufficient decay time the waste gas is either released to the environment via t'he Station Vent or reused via the Reactor Coolant Bleed Hold-up Tanks.

4.2.6 The system shall be periodically monitored:

4.2.6.1 Monitor the compressors for abnormal noises and vibrations.

4.2.6.2 Monitor the compressor sight glass for proper water level control.

The level should remain essentially at the mid-plane of the compressors.

4.2.7 The Moisture Separator of an operated compressor should be blown down daily.

4.2.7.1 OPEN WDG-V76A (B), the manual drain valve, while observing the water level in the sight glass.

CAUTION:

Insure that the water level does not decrease sign-ificantly.

4.2.7.2 CLOSE WDG-V76A (B) when the blowdown is complete.

4.3 Shutdown.

4.3.1 CLOSE the normally open valves that supply Waste Gas to the Vent Header:

Initial Valve Component WDG-V256 WDL-T-2 WDG-Vl6 WDL-T5 WDG-V17A WDS-T-1A 4

WDG-V100A WDS-T-1A WDG-V178 WDS-T-1B 9.0 L

2101-y.3 Revision 1 01/31/78 Initial Valve Component WDG-V1000 WDS-T-1B WDG-V65 WDS-T2

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WDG-V90 DS-T-3 WDL-V26A WDL-T-1A UDL-V26B WDL-T-1B WDL-V26C WDL-T-lC 4.3.2 CLOSE all normally closed valves that had been opened to vent a component to the Vent Header.

4.3.3 PLACE the compressor control switches in the 0FF position.

4.3.4 OPEN breaker 7CF on MCC 2-32A for WDG-P-1A.

4.3.5 OPEN breaker 78R on MCC 2-42A for WDG-P-18.

4.4 Special or Infrequent Operations.

4.4.1 Decay Tank Dischage to the Station Vent.

The release of waste gas is done by the manual controlled venting of the Waste Gas Decay Tank to the Station Vent.

o.a.l.1 The Waste Gas Decay Tank, kDG-T-1A (B), selected to be released in _not being charged.

4.4.1.2 ilANG a "D0 00T OPERATE" tag on WDL-V26A-(0) control suitch.

4. 4.1. 3 The followin) interfacing has been completed with the Health Physics Department:

4.4.1.3.1 The llP/ Chem Department has been notified that-the Operations Department wants to release a Waste Gas Decay Tank.

_4.4.1.3.2 The llP/ Chem Department has taken a sample of the tank to be released.

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2104-4.3 Revision 1 01/31/78 4.4.1.3.3 The HP/ Chem Department has issued a Waste Gas Release Permit per llPP-1622.2 that has been signed by the llealth Physics / Chemistry Foreman, Supervisor of HP/ Chem and the Shift Supervisor.

The permit as been received by the Control Room Operator.

4.4.1.4 The Waste Gas Discharge Monitor, WDG-R-1480 is operating and has been verified by 2322-Q1 within the last quarter to close WDG-V30A and WDG-V30B on a high radiation signal.

4.4.1.5 The Waste Grs Decay Tank monitor, WDG-R-1485 (1486), for tar,k WDG-T-1A (B) to be released, is operating and hu been verified by 2322-Q1 within the last quarter to close WDG-V30A (B) on a high radiatioa signal.

4.4.1.6 Unit 2 Exhaust Vent Gas Discahrge Monitor, HP-R-219, is operating and has been verified by 2322-Q3 within the last quarter to close WDG-V30A and WDG-V30B on a high radiation signal.

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4. 4.1. 7 The following Meteorological Data is availa'cle:

4.4.1.7.1 The wind speed and direction at the 100 ft level of the meteorological monitoring tower.

4.4.1.7.2 The temparature difference between the 150 ft and 33 l

l ft levels of the tower.

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__ _4. 4.1. 8 Obtain key from Shift foreman for WDG-V54A(B).

I 4.4.1.9 IIAUG a " GAS REl. EASE IN PROGRESS" sign on the Waste Gas l

Disposal Panel.

_4.4.1.10 The Waste Gas Release Permit, issued by the llP Department,

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2104-4.3 Revision 1 l

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4.4.1.10.1 Initial data.

01/31/78 4.4.1.10.2 Subsequent data.

4.4.1.10.3 Shift Supervisor verification.

4.4.1.10.4 Returned to the HP Lab.

1 4.4.1.11 The Waste Gas Release Data Sheet, Appendix C of these procedures, shall be completed as required:

4.4.1.11.1 Initial data.

4.4.1.11.2 Subsequent data, hourly.

4.4.1.11.3 Signed by the operator, f

4.4.1.11.4 Returned to the Supervisor of Operation, Unit 2.

l 4.4.1.12 OPEft WDG-V60, the Station Vent isolation valve.

l 4.4.1.13 Ut1 LOCK and OPEN WDG-54A(B) the manual outlet valve of the

]

tank WDL-TlA(B) to be released.

t 4.4.1.14 UPE!! WDG-V30A (B) the outlet valve of the tank' WDG-T-1 A i

(B) to be released.

4.4.1.15 CRACK OPEfl and THROTTLE WDG-V188A (B), the outlet flow throttle valve.

Control flow to less than 100 SCFM as read on WDG-FI-3652.

j CAUTION:

Do not discharge above 100 SCFM during waste f

gas release.

~ 4.4.1.16' CLOSE WDG-V188A (B) when the gas release has been completed.

4.4.1.17 CLOSE WDG-V60.

_ 4.4.1.18 CLOSE WDG-V30A (B).

4.4.1.19 CLOSE and LOCK WDG-V54A(B).

4.4.1.20 REMOVE the tag hung in step 4.4.1.2.

t 4.4.1.21 REMOVE the tag hung in step 4.4.1.8.

I fl0T_E,:

The procedure is not complete until steps-4.4.1.10 and 4.4.1.11 have been completed.

4. 4.1. 2.2 Return key for WDG-V54A(B) to Shift Foreman.

4.4.2 Shi ft of On-Line Decay Tank.

j 1E.0 w as._

l

w- ~ -e-4,;

2104-4.3 a.-

Revision 0 05/17/77 4.4.2.1 CHECV, to insure that the Vent Header pressure is near the low end of the operating band and that no large pressure surge is anticipated.

4.4.2.2 PLACE the control switches in the 0FF position for both compressors.

4.4.2.3 CLOSE WDG-V26A (B), the inlet valve for the tank, WDG'-T-1A (B) being charged.

4.4.2.4 COMPLETE Section 4.1, Start-up.

The shift of the On-Line Decay Tank occurs in step 4.1.2 when WDG-V268 (A) is opened.

4.4.3 Reuse of Waste Gas The Waste Gas System allows for gas to be directed to the Reactor Coolant Bleed Hold-up Tanks.

However, as presently designed, the transfer must be completed by manual control only.

CAUTI0ft: Special care must be taken not to overpressurize a R.C. Bleed Hold-up Tank which has a design pressure of 20 psig.

4.4.3.1 The Waste Gas Decay Tank, WDG-T-1A (B) selected for reuse is not being charged.

4.4.3.2 HAtlG a "D0 ?!0T OPERATE" tag on the tank inlet isolation valve, WDL-V26A (B), control switch.

4.4.3.3 The following interfacing has been completed with the Health Physics Department.

4.4.3.3.1 The HP/ Chem Department has been n,otifihd that the Operations Department wants to reuse the Waste Gas in a Decay Tank.

l l

13.0 L

2104-4.3 4

_.4.3.3.2 The lip / Chem Department has taken Revision 1 01/31 be reused.

4 4.4.3.3.3 The llP/ Chem Department has verbally stated that the gas conforms to the following specificat' ions for' reuse a.

}Iydrogen 13% by volume b.

Oxygen 5 0.1% by volume, The concentration of radioactive gas isotopes i c.

s less than the restricted MPC values in 10 Appendix B.

4.4.3.4 CilECK CLOSE WDG-V60, the Station Vent isolati 4.4.3.5 on valve.

OPEtt WDG-V61, the Waste Gas Reuse lleader isola 4.4.3.6 on valve.

OPEtt WDG-V62A (B)(C) the isolation valv

-T-1A (B)(C).

4.4.3.7 Obtain key from Shift Foreman and UtlLOCK and OP DG-V54A(B).

4.4.3.8 OPEN WDG-V30A (B) the outlet. valve of

\\

t

-T-1A l

(B) to be reused.

_ 4.4.3.9 Monitor the RC Bleed Hold-up Tank pressure d uring this p rocedure, l

k i

CAUTIO_ti: Do not overpressurize the tank, the design pressure is 20 psig.

4.4.3.10 CRACKOPEliandTilROTTLEWDG-V188A(B)

, the outlet throttle valve.

l Control flow to less than 100 SCFM as rea WDG-FI-3652.

n CAUTION:

Do not exceed 100 SCFM during this procedur 4.4.3.11 CLOSE WDG-V188A (B) when the desired R e.

o -up l

Tank pressure is obtain.

t Must be less than 20 psig.

4.4.3.12 CLOSE WDG-V30A (B).

4.4.3.13 CLOSE and LOCK WDG-V54A(B).

l W. t l

gi.O.'

ma

- m

~

YhW 14.0

.a

.s v,

w_

j

'fp ** # "

U+- i

. ~,, - - --

~~

w,

2104-4.3 4

Revision 1 i

4.4.3.14 CLOSE WDG-V62A (B)(C).

01/31/78 I

4.4.3.15 CLOSE WDG-V61.

4.4.3.16 REMOVE the tag hung in step 4.4.3.P..

l l

4.4.3.17 Return WDG-V54A(B) key to Shift Foreman.

4.4.4

lecay Tank to Decay Tank Transfer.

4.4.4.1 The sum of the gauge pressures of the two tanks total 110 l

1 psig or less.

l CAUTION:

If this condition is not met the transfer i

cannot be complete without the possibility of a i

relief valve lifting and discharging to the Station Vent.

The transfer must be observed b

with special caution and stopped when the tank pressure reaches 110 psig.

i

_4.4.4.2 The Waste Gas System is in operation per Section 4.2, Ilormal Operation.

i l

4.4.4.3 CHECK OPEli WDG-V172, the Waste Gas Compressors discharge j

cross-connect valve.

4.4.4.4 OPEli or CHECK OPEi! WDG-V26A and WDG-V268, the Decay Tank

(

inlet isolation valves, to equalize the pressure in the tanks.

1 4.4.4.5 CLOSE WDG-V26A (B) the inlet valve of the tank, WDG-T-1A I

(B), to be emptied after the pressure has equalized in

{

the tanks.

4 I

,4.4.4.6 CllECK CLOSE WDG-V60 and WDG-V61, the release valves.

_4.4.4.7 OPEli WDG-V170 and UDG-Vl96, the isolation valves to i

regulating valve WDG-V171.

4.4.4.8 OPEli WDG-V30A (B) the outlet valve of the tank to be t

emptied.

i 4.4.4.9 Obtain key from Shift Foreman and Unlock and OPEli WDG-V54A(B).

i l

15 0

'4-

3 -.

2104 a.3 Revision 1

__4.4.4.10 OPEN WDG-V188A (B) the outlet throttle valve.

01/31/78 l

4.4.4.11 MONITOR the compressors suction pressure to ensure that l,

the regulating valve, WDG-V171 is controlling the pressure.

4.4.4.11 CLOSE WDG-V188A (B) when the transfer is complete.

4.4.4.12 CLOSE and LOCK WDG-V54A(B).

j 4.4.4.13 CLOSE WDG-V170 and WDG-Vl96.

4.4.4.14 CLOSE WDG-V30A(B).

4.4.4.15 Return WDG-V,54A(B) key to Shift Foreman.

j CAUTION: The empty tank still will be pressurized and i

must be treated as such.

4.4.5 Reactor Building Vent Header Start-up.

4.4.5.1 The Reactor is shutdown for maintenance and/or refueling.

4.4.5.2 OPEN WDG-V2, the inside containment isolation valve.

4.4.5.3 OPEN WDG-Vl99, the outside containment isolation valve.

4.4.5.4 OPEN WDG-V6, the Reactor Building Vent Header isolation valve.

4.4.6 Reactor Building Vent Header Shutdown.

4.4.6.1 CLOSE W3G-V6, the Reactor Building Vent Header isolation valve.

4.4.6.2 CLOSE WDG-Vl99, the outside containment isolation valve.

4.4.6.3 CLOSE WDG-V2, the inside containment isolation valve.

4.4.7 Vent Header to Station Vent By-Pass.

~

CAUTION: This operation is only performed if there is a large volume of gas to be released which is at or below the allowable discharge limits.

4.4.7.1 The following interfacing has been completed with the Health Physics Department:

4.4.7.1.1 The llP/ Chem Department has been notified that the Operations 4

Department wants to release waste gas.

16.0 J

A*

.,+=e4,

+

~ _.. _.,. +,

_=

2104-4.3 Revision 1 4.4.7.1.2 The llP/ Chem Department has taken a sample of the gas /31/78 01 to be released.

3

._._.___4.1. 7.1.3 The llP/ Chem Department has issued a Waste Gas Release

]

Permit per llPP-1622.2 that has been 'igned by'the llealth s

Physics / Chemistry Foreman, Supervisor of IIP / Chem and the Shift Supervisor.

The permit has been received by the Control Room Operation.

4.4.7.2 The Waste Gas Discharge Monitor, WDG-R-1480 is operating.

I 4.4.7.3 Unit 2 Exhaust Vent Gas Discahrge Monitor HP-R-219 is i

operating.

)

_C_AUTI0f t: There is no automatic action that will secure i

the discharge on a high radiation signal.

The i

operator must secure the flow by closing WDG-V60, the station vent isolation valve.

2 4.4.7.4 The following Meteorological Data is available:

1

_4.4.7.4.1 The wind speed and direction at the 100 ft level of the meteorological monitoring tower.

4.4.7.4.2 The temperature difference between the 150 ft and 33 ft levels of the tower.

i 2.4.7.5 HAf'G a " GAS REl. EASE Ill PROGRESS" sign on the Waste Disposal Panel.

h 4.4.7.6 The Waste Gas Release Permit, issued by the llP/ Chem Department, shall be completed as required.

4.4.7.6.1 Initial data.

I 4.4.7.6.2 Subsequent Data.

4.4.7.6.3 Shif t Supervisor verification.

4 a

1 17.0 l-i

2104-4.3 Revision 1 01/31/78 4.4.7.6.4 Returned to the H.P. Lab.

4.4.7.7 The \\laste Gas Release Data Sheet, Appendix C of these procedures, shall be completed as required.

4.4.7. 7.1 Ini tial data.

4.4.7.7.2 Subsequent data, hourly.

4.4.7.7.3 Signed by the Operator.

4.4.7.7.4 Returned to the Supervisor of Operations, Unit 2.

4.4.7.8 Obtain key and OPEN WDG-V24, the locked closed bypass valve of WDG-V171.

4.4.7.9 OPEf1 WDG-V60, the Station Vent isolation valve.

4.4.7.10 CRACK L. t.N and THROTTLE the valve at the source of the j

gas.

CAUTIOH:

Do not discharge above 100 SCFM during waste gas release as read on WDG-FI-3652.

4.4.7.11 CLOSE the valve at the source of the gas when the release is complete.

]

4.4.7.12 CLOSE WDG-V60.

4 4.4.7.13 CLOSE WDG-V24 and Lock Closed.

I d.4.7.14 REMOVE the sign hung in step 4.4.7.5.

d.4.7.15 Return WOG-V24 key to Shift Foreman.

NOTE:

The procedure is not complete until steps j

4.4.7.6 and 4.4.7.7 have been completed.

4.4.8 Compressor - Decay Tank Train Shutdown and Purge.

The Waste Gas System is not normally shutdown with the exception of the Reactor Building Vent Header. _The

~

following procedure secures one Waste Gas Compressor and the associated Decay Tank and purggs the tank to allow 4

maintenance in the compartment.

In order to shutdown.

18.0 i

i

I 2104-4.3 Revision 0 05/17/77 both trains, complete the following procedure for each train. All other system shutdowns with purge should be evaluated individually to determine the best procedure.

4.4.8.1 EMPTY and PURGE WDG-T-1A (B) by ONE OF the following four methods.

4.4.8.1.1 Alternative Method I, Release and Purge to Station Vent.

4.4.8.1.1.1 COMPLETE Section 4.4.1, Decay Tank Discharge to the Station Vent, through step 4.4.1.13.

4.4.8.1.1.2 SLOWLY OPEN WDG-V69A (B), the nitrogen make-up valve of the tank to be purged.

CAUTION:

Do no exceed 100 SCFf t release rate.

4.4.8.1.1.3 CLOSE WDG-V69A (B) when the purge is completed.

4.4.8.1.1.4 FINISH Section 4.4.1 starting with step 4.4.1.14.

4.4.8.1.1.5 CONTINUE this procedure with step 4.4.8.2.

4.4.8.1.2 Alternative Method II, Release to Station Vent and Purge to Other Tank.

4.4.8.1.2.1 COMPLETE Section 4.4.1, Decay Tank Discharge to the Station Vent.

4.4.8.1.2.2 COMPLETE Section 4.4.4, Decay Tank to Decay Tank Transfer, through step 4.4.4.10, 4.4.8.1.2.3 SLOWLY OPEll WDG-V69A (B), the nitrogen make-up valve of the tank to be purged.

_4.4.8.1.2.4 CLOSE WDG-V69A (B) when the purge is completed.

4.4.8.1.2.5 FINISil Section 4.4.4 starting with step 4.4.4.11.

4.4.8.1.2.6 CONTINUEthisprocedurewithstep4.4.8.2.

4.4.8.1.3 Alternative Method III, Transfer'and Purge to Other Tank.

19.0 l

2104-4.3 Revision 0 l.

05/17/77

~

4.4.8.1.3.1 COMPLETE Section 4.4.4, Decay Tank to Decay Tank Transfer, through step 4.4.4.10.

4.4.8.1.3.2 SLOWLY OPEf1 WDG-V69A (B), the nitrogen make-up valve of the tank to be purged.

4.4.8.1.3.3 CLOSE WDG-V69A (B) when the purge is completed.

4.4.8.1.3.4 FIllISH Section 4.4.4 starting with step 4.4.4.11.

4.4.8.1.3.5 C0flTIftVE this procedure with step 4.4.8.2.

4.4.8.1.4 Alternate fiethod IV, Transfer to Other Tank and Purge to Station Vent.

4.4.8.1.4.1 COMPLETE Section 4.4.4, Decay Tank to Decay Tank Transfer.

4.4.8.1.4.2 SLOWLY OPEfl WDG-V69A (B), the nitrogen make-up valve to dilute the residue waste gas in tank WDG-T-1A (B).

4.4.8.1.4.3 CLOSE WDG-V69A (B) when the desired pressure is re;ched.

4.4.8.1.4.4 COMPLETE step 4.4.8.1.1, Alternative Method I, j

Release and Purge to Station Vent.

CAUTI0ft:

If the sample indicates that the diluted gas still cannot be released, then go to step 4.4.8.1.3, Alternative Method III, Transfer and Purge to Other Tank.

4.4.8.2

-PLACE the Control Switch in the 0FF position for the 1

compressor, WDG-P-1A (B) associated with the purged tank, WDG-T-1A (8).

4.4.8.3 OPEf1 the breaker for the compressor stopped in step l

4.4.8.2.

Of1E of the following:

i t

20.0

2104-4.3

,i Revision 0 i

05/17/77

?

t Initial Breaker Compressor 7CF on flCC 2-32A WDG-P-1A 7BF on fiCC 2-42A WDD P-1B 4.4.8.4 CLOSE WDG-V172, the compressors distnarge cross-connect valve.

4.4.8.5 CLOSE WDG-V124A (B), WDG-V57A (B), and WDG-V129A (B) to

{,

isolate the compressor, WDG-P-1A (B).

4.4.9 Emergency Operations.

I In an emergency the Waste Gas System functions as in the i

j flormal Operations.

i I

i I

i t

d a

4 4

(

f 21.0

~ _ _ _.. -

\\

~"

/

2104-4.3 Revision 0 05/17/77 APPEllDIX A Start-Up Valve Line-up Valve fiumber Description Position Initial

~

WDG-VIA CRDM Vent Isolation CL d'

WDG-VlB CRDM Vent Isolation.

CL 8/lf)

WDG-V2 Inside Containment Isolation CL Y MI WDG-V6 R.B. Vent Hdr Isolation CL Id_

WDG-V16 Aux Bldg Sump Tk Vent Isolation

[;bt50P WDG-V17A Spent Resin Star Tk - 1A Vent Isolation OP

-7KL WDG-Vl7B Spent Resin Stor Tk - 1B Vent Isolation OP

[F(_.

WDG-V24 Vent Hdr to Waste Gas Flt By-Pass L.CL WDG-V26A Decay Tk - 1A Inlet Flow Control CL OPNC c[DecayTk-1BInletFlowControl CL

~)k WDG-V26B WDG-V28A Decay Tk - 1A Drain Control CL

~)b WDG-V28B Decay Tk - 1B Drain Control CL WDG-V29A Decay Tk - 1A Sample CL 26 WDG-V29B Decay Tk - 1B Sample CL IL WDG-V30A Decay Tk - lA Outlet Control CL WDG-V308 Decay Tk - IB Outlet Control CL M

WDG-V32 F1t Inlet Isol.

OP WDG-V33 F1t Upstream Line Drain CL WDG-V34 F1t Downstream Line drain CL WDG-V35 Fit Outlet Isol OP WDG-V39 PX - Test Connection Isolation Y

E GE WDG-V40 Vent Hdr Press Inst Root OP WDG-V47A Decay Tk - 1 A Press Instr Root OP WDG-V478 Decay Tk - IB Press Instr Root OP

)

22.0

,1

2104-4.3 s;

APPENDIX.A biNIN8 Start-Up Valve Line-up Valve ilumber Description Position Initial

((

! -V49 Fit DPT Instr. Upstream Root OP WDG-V54A Decay Tk - 1 A Outlet Isolation L. CL WDG-V54B Decay Tk - 1B Outlet Isolation L. CL 2fb h

WDG-V55A Decay Tk - 1A Inlet Isolation OP WDG-V55B Decay Tk - 13 Inlet Isolation OP WDG-V57A Compress - 1A Inlet Isolation OP N

AT WDG-V578 Compress - 1B Inlet Isolation OP 27M l

WDG-V59 Vent Header to Compress Press Regulator AUTO WDG-V60 Filter to Station Vent Isolation CL WDG-V61 Filter to RC Bleed llold-Up Tks lidr Isolation CL LN-WDG-V62A Gas to RC Bleed Hold-up Tk - 1A Control CL WDG-V628 Gas to RC Bleed Hold-up Tk - 18 Control CL WDG-V62C Gas to P.C Bleed Hold-up Tk - IC Control CL

]k-WDG-V64 Compress - lA Vent Hdr Press Instr Root OP WDG-V65 Conc Waste Tk Vent Control OP WDG-V66 Compress Inlet Press Instr Root OP W

WDG-V67 Filter d-Press Instr Downstream Root OP WDG-V68' Compress - 1B Vent Hdr Press Instr Root OP 7h WDG-V69A Nitrogen to Decay Tk - 1A Isolation CL N

WDG-V69B Nitrogen to Decay Tk - 1B Isolation CL WDG-V70 Nitrogen to Vent Ildr Isolation CL

$_h WDG-V71 Filter Drain lidr Drain CL WDG-V72A Compress - 1A Unloader AUTO

-)/d WDG-V72B Compress - IB Unloader AUTO 23.0

~

2104-4.3

/

(-

Revision 0 05/17/77 APPEllDIX A Start-Up Valve Line-up Valve ilumber Description Position '

Initial WDG-V74A Compress - 1A Auto Ili-Level Drain AUTO N r WDG-V748 Compress - 1B Auto Hi-Level Drain AUTO N

WDG-V76A Compress - 1A Manual Drain CL N

WDG-V76B Compress - IB Manual Drain CL M -

WDG-V83A Compress - 1A Inlet Regulator AUTO WDG-V83B Compress - 1B Inlet Regulator AUTO WDG-V84A Compress - 1A Inlet Control Regulator AUTO N

WDG-V84B Compress - IB Inlet Control Regulator AUT0 WDG-V85A Compress - 1A Auto Lo-Level Makeup AUTO N

WDG-V85B Compress - IB Auto Lo-Level Makeup AUTO Y

WDG-V90 Rec Boric Acid Tk Vent Control OP WDG-V100A Spent Resin Stor Tk - lA Vent Isolation OP 7K(

WDG-V1003 Spent Resin Stor Tk - 1B Vent Isolation OP

[k WDG-Vil4 Conc Waste Tk Vent Isolation OP WDG-Vll6A RC Bleed Holdup Tk - 1A Vent Isolation OP 3/_.,

WDG-Vil68 RC Bleed Holdup Tk - IB Vent Isolation OP

[b I--

WDG-V116C RC Bleed Holdup Tk - IC Vent Isolation OP WDG-Vil7 Rec Boric Acid Tk Vent Isolation OP Y )Q' _.

WDG-V118 Liquid Drainer - UllA Inlet Isolation '

OP IC WDG-V119 flitrogen to RC Bleed Holdup Tks Isolation CL WDG-V121 Liquid Drainer - Ul2A Inlet Isolation OP sk/.-

Liquid Drainer - U12B Outlet Isolation []( OP s1 'k-WDG-V122 r

WDG-V123 Compress Combine Inlet Isolation OP WDG-V124A Compress - 1 A Inlet Isolation OP 24.0

2104-4.3 Revision 0

[.

05/I7/77 APPEt! DIX A Start-Up Valve Line-up blve ilumber Description Position

, Initial WDG-V124B Compress - 1B Inlet Isolation OP WDG-V127 flitrogen to Decay Tk 18 Sample Line CL

%[

WDG-V128A Compress - 1A Unloader Valve Isolation OP WDG-V128B Compress - 1B Unloader Valve Isolation OP N

WDG-V129A Compress - 1A Inlet Control Regulator Isol 0P JM WDG-V1298 Compress - IB Inlet Control Regulator Isol OP

]k WDG-V134A Compress - 1A Makeup Water Isolation OP

[AI WDG-V1348 Compress - 1B Makeup Water Isolation OP

[d8 WDG-V135A Dncay Tk - 1A Press Instr Drain CL WDG-V135B Decay Tk - 1B Press Instr Drain Jh CL WDG-Vl36 Filter Drain Isolation CL i

WDG-V138 Liquid Drainer - U8A Inlet Isolation A

OP W

t WDG-V139 Liquid Drainer - U8A Outlet Isolation OP b

WDG-V140 Liquid Orainer - U9A Inlet Isolation OP WDG-V141 Liquid Drainer - U9A Outlet Isolation OP WDG-V142A Decay Tk - M Outlet Rad Instr Root gr4Atr OP WDG-V1428

. Decay Tk - 18 Outlet Rad Instr Root OP WDG-Vl43A Decay Tk - 1A Outlet Rad Instr Root OP tr 44 W WDG-V143B Decay Tk - IB Outlet Rad Instr Root OP

  1. ^*'

WDG-V145 Station Vent Discharge Rad Instr Root OP 8If WDG-V146 Station Vent Discharge Rad Instr Root OP gM_

WDG-V147 Nitrogen to Decay Tk - 1A Sample Line CL

~~JM WDG-V149 Filter d-Press Instr Upstream Root OP WDG-V150 Filter d-Press Instr Downstream Root OP 25.0

~

2104-4.3

/-

Revision 0

' l ',,.t 05/17/77 APPEllDIX A Start-Up Valve Line-up Valve Number

. Description Position

' Initial WDG-V151 RC Evap Vent Isolation OP v7 b-kb, llDG-V152 RC Evap Vent Isolation OP

-(l.[,/

llDG-V154 RC Evap Vent Isolation OP L

WDG-V157 flitrogen to RB Vent Ildr CL

[# 3 WDG-V159 Liquid Drainer - U10A Inlet Isolation OP WDG-V160 Liquid Deciner - U10A Outlet Isolation OP WD3-V162A Compress - 1 A Outlet Press Instr Root OP 7h WDG-s'1628 Compress - 1B Outlet Press Instr Root OP WDG-V164 Liquid Drainer - Ull A Outlet Isolation OP WDG-V165 Pressurizer Vent Isolation CL

[kf WDG-V166A Steam Gen - 1A Pri-side Vent Isolation CL 8[

llDG-V166B Steam Gen - IB Pri-side Vent Isolation CL 6d

[M WDG-V167A Steam Gen - 1 A Sec-side Vent Isolation L.CL

[M WDG-V1678 Steam Gen - 18 Sec-side Vent Isolation L.CL z[k WDG-V170 Decay Tk to Vent Ildr Regulator Isolation CL WDG-V171 Decay Tk to Vent Ildr Regulator AUTO WDG-V172 Compress Discharge Cross-Connect OP h -

WDG-V174 Decay Tk - 1A Level Instr Top Isolation OP WDG-V175 Decay Tk - l A Level Instr Top Root OP N

WDG-V176 Decay Tk - l A Level Instr Bot Root OP WDG-V177 Decay Tk - 1A Level Instr Bot Isolation OP llDG-V178 Decay Tk - 1B Level Instr Top Isolation t OP WDG-V179 Decay Tk - IB Level Instr Top Root OP Nr llDG-V180 Decay Tk - IB Level Instr Bot Root OP 26.0

2104-4.3 Revision 0

(? ' '.

05/17/77

_ APPENDIX A Start-Up Valve Line-up Valve Number Description Position Initial WDG-Vibl Decay Tk - IB Level Instr Bot Isolation OP 3h UDG-V182 Decay Tk - 1A Level Instr Bot Root OP WDG-V183 Decay Tk - 1A Level' Instr Top Root OP

~]k WDG-V184 Decay Tk - IB Level Instr Bot Root OP

~)([.

WDG-V185 Decay Tk - 1B Level Instr Top Root OP

(([

WDG-V186 Containment Isolation Test Isolation CL WDG-V187 Containment Isolation Test Isolation CL Oh WDG-V188A Decay Tk - lA Outlet Throttle CL WDG-V188B Decay Tk - 18 Outlet Throttle CL

)4 WDG-V189 Vent Hde to Sample Isolation CL

-)

WDG-Vl91 Containment Isolation Test Isolation CL

[M WDG-V192 Containment Isolation Test Isolation CL

[b

')h WDG-Vl93 Vent Hdr Regulator Downstream Isolation OP UDG-Vl94 Vent Ildr Regulator Upstream Isolation OP N

WDG-V195 Vent Hdr Regulator Bypass CL WDG-Vl96 Decay Tk to Vent Hdr Regulator Isolation CL WDG-Vl97 Vent Hdr Regulator Root OP

~)M

[/[

UDG-Vl99 Outside Containment Isolation CL WDG-V200 Liquid Drainer - U24 Inlet Isolation OP JK UDG-V201 Liquid Drainer - U24 Outlet Isolation OP J/U_.

,h.

)-

WDG-V202 Liquid Drainer - U25 Inlet Isolation OP 7

WDG-V203 Liquid Drainer - U25 Outlet Isolation

, OP

_b HDG-V204 Liquid Drainer - U26 Inlet Isolation OP WDG-V205 Liquid Drainer - U26 Outlet Isolation OP 7

27.0

m z.

m_

2104-4.3 Revision 0 I '*' '

APPEf1 DIX A 05/17/77 Start-Up Valve Line-up Valve fiumber Description Position Initial h[

WDG-V206 Rad Sampling Rack Isolation CL WDG-V207 Rad Sampling Rack Isolation CL C#<.I WDG-V208.

Rad Sampling Rack Bypass OP

<f 8 [

WDL-V126 RC Drain Tk Vent Isolation CL WDL-V127 RC Drain Tk Vent Isolation CL CF-V3A Core Flood Tk - 1A Vent Isolation CL

  1. [/2 C CF-V3B Core Flood Tk - 1B Vent Isolation CL

[// f CF-Vil7A Core Flood Tk - 1A Vent Isolation CL

/jd /

CF-Vil7B Core Flood Tk - IB Vent Isolation CL J,T7/b MU-V234A Seal Return Cooler - 2A Vent Isolation CL k

l10-V234B Seal Return Cooler - 2B Vent Isolation CL MU-V358A Seal Return Cooler - 2A Vent Isolation CL s

I(

ilu-V358B Seal Return Cooler - 2B Vent Isolation CL

@b MU-Vil6A Makeup and Purif Demin - 1A Vent Isolation CL MU-Vil6B flakeup and Purif Demin - 2A Vent Isolation CL 2 [_

MU-V217A Makeup and Purif Demin - lA Vent Isolation CL JPL MU-V2178 '

Makeup and Purif Demin - 2A Vent Isolation CL

[tf[-.

MU-V13 Makeup Tk Vent Isolation CL Ab MU-V136 flakeup Tk Vent Isolation CL

[.

MU-V227A Makeup & Purif Demin Fit - 5A Vent Isol CL

</T[

f10-V227B Makeup & Purif Demin F1t - 5B Vent Isol CL N

~

MU-V228A flakeup & Purif Demin Fit - 5A Vent Isol CL MU-V228B Makeup & Purif Demin Fit - 5B Vent Isol CL I[

SF-V187 Spent Fuel Demin Vent Isolation CL Md -

28.0 l

__ =

7

-. _. -.-,. 1

~

2104-4.3 Revision 0 o

05/17/77 APPEllDIX A Start-Up Valve Line-up Valve ilumber Description Position

' Initial jd, SF-Vl97 Spent Fuel Demin Vent Isolation CL 5'-V119A Spent Fuel F1t - 1A Vent Isolation CL M/

SF-V119B Spent Fuel Flt - 1B Vent Isolation CL di///

SF-Vl96A Spent Fuel Fit - lA Vent Isolation CL

[

!!U-V131 A flakeup F1t - 2A Vent Isolation CL dIb d

flu-V131B

!!akeup Fit - 2B Vent Isolation CL k,

SF-Vl963 Spent Fuel Fit - 18 Vent Isolation CL WDL-V355A RB Sump Pump Fit - 8A Vent Isolation CL (N.'[,

WDL-V355B RB Sump Pump Flt - 83 Vent Isolation CL N/,

WDL-V356A RB Sump Pump F1t - 8A Vent Isolation CL MI WDL-V3568 RB Sump Pump Fit - 8B Vent Isolation CL WDL-V256 11isc Waste Tk "ent Isolation OP D [.

WDL-V68A Deborating Demin - lA Vent Isolation CL

/_

hl WDL-V6BB Deborating Demin - 1B Vent Isolation CL WDL-V532A Deborating Demin - lA Vent Isolation CL TO

/

WDL-V532B Deborating Demin - 1B Vent Isolation CL WDL-V378A Aux Bldg Sump Tk Fit - 3A Vent Isolation CL 37dC WDL-V378B Aux Bldg Sump Tk Fit - 3B Vent Isolation, CL ICl-WDL-V379A Aux Bldg Sump Tk Fit - 3A Vent Isolation CL M

WDL-V379B Aux Bldg Sump Tk F1t - 3B Vent Isolation.

CL g/

.fDL-V375A tieutr Tk Flt - 4A Vent Isolation CL

[

WDL-V3750 fleutr Tk Fit - 4B Vent Isolation

' CL

(..-

WDL-V26A RC Bleed Holdup Tk - 1A Vent Isolation OP T[--

I_

WDL-V26B RC Bleed Holdup Tk - 1B Vent Isolatiu.

OP 29.0

2104-4.3

  • j' Revision 0 05/17/77
e 1

j APPEfIDIX A Start-Up Valve Line-up 4

l Valve ilumber Description Position Initial WDL-V2bC RC Bleed flo1 dup Tk - 1C Vent Isolation OP TY[/

i WDL-V57A Cleanup Demin - 2A Verit Isolation CL db

(

1 l

WDL-V578 Cleanup Demin - 2B Vent Isolation CL hd ilDL-V514A Cleanup Demin - 2A Vent Isolation CL db UDL-V5148 1

Cleanup Demin - 2B Vent Isolation CL

_df[L

,i WDL-V201A Cleanup F1t - 9A Vent Isolation CL

$L, ilDL-V201B Cleanup F1t - 98 Vent Isolation CL Mb j

WDL-V202A Cleanup F1t - 9A Vent Isolation CL

@b i

1 l

WDL-V2028 Cleanup Fit - 9B Vent Isolation CL h /_-

i I

4 4

0 t

l 30.0 l

v-

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2104-4.3 Revisian 0

.3 i '

05/Vil77 APPEfIDIX 8 Signatures of those performing / supervising valve Ifne-up Valve Line-up Signature Sheet Operator Opera tor Initials Signature Shift Foreman or Shift Date Supervisor Sig.

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k(

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2104-4.3 Revision 0 05/11/77

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APPEliDIX C Waste Gas Release Data Sheet Radiation ffonitors Time Release Rate 1480 1485 1486 Tank Pressure t

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