ML20044D159

Rev 11 to Sys Description 3526-004, Auxiliary Bldg Emergency Cleanup Sys (EPICOR-II)

ML20044D159
Person / Time
Site:	Crane
Issue date:	05/05/1993
From:	GENERAL PUBLIC UTILITIES CORP.
To:
Shared Package
ML20044D157	List: ML20044D154 ML20044D159
References
3526-004, 3526-004-R11, 3526-4, 3526-4-R11, NUDOCS 9305170297
Download: ML20044D159 (78)

Text

I SD 3526-004 REV 11 ISSUE DATE t'.a y 1993 0 ITS U NITS DIVISION S Y S T E fA DESCRIPTI^N FOR Auxiliary Buildin, Enercencv Licuid Clean-un System (EPICOR II) p50 COG ENG DATE 5Y-??

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Tne system Ges:-sption for Aaxiliary Buil:1"5 Pa ge 2 cf 78 Emergen:y Li: ate Clean-up System (EP!OOR : )

Rev.

SUMMARY

OF CMANGE Approval Oate 0

Initial issue per GPU ka:1 ear letter 4410-82-L-0017.

b 2/B2 1

Update: per GPU kw: lear letter 4410-63-L-0078.

N 4/83 2

Upcate per GPU Wu: lear letter &410-84 L-0023.

M 2/84 3

Upcate: see G U Wsclear letter 4410-85-L-0074 N

4/85

n::r,: rate: E;M 3475.6, Revision 6.

4

.pcate: pee GPU ha:1 ear letter 4410-85-L-0069.

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4/86 I

5 Annual secate t: refle:t tee :urrent :pe sti:n Of 5/E7

nfi;;ratien :f the EP 00R II system. Aces further cetati as :: tee ::e-atten :f the Transfer Pats AL -F-5 i n Se: tion 2.1.2.

Revisec the ces:ripti:n f cemineralizer AL: F 1 in Se:11:n 2.1.3.

Revisec Section 2.1.19 :encernia; system isolation v41ves.

A: s new Se: tion 3.4.2 anc 3.4.1.

6 Annsal s::ste t: reflect tne f=11: wing:

6/EB

a. : a-ifi:stien of Se:ti:n 1.0 regarcing appr vec

't:ti vi ng taa.t s f or EP 00R !! pr::essee water an: r:; tine /n:n-reatine operati:ns.

. :nstallati:n :f a stainless steel ALC-P-5 transfer psm: nas :nange: Se:ts:1 2.1.2 an: Ta:1e 2 regar:ing

tal cf.ami: m-

. eela:eeat :f at:-RE-12 ( ALC ventilati:n Rad 3

f "Onit:rI re: sire: m::1fi:a11:n :: Secti:n 2.2. A an:

I

• able 10 an: 12.

l r.. Ia:1e 15 ( ALC Valve List) has been etDanced t: i ncl u fe tw: new valves steed fer MitA 3526 67 0016 ( ALC F 1)

Bypass.

e. Tatie 15 als: n:. in:1uces the ces:rt:ti:n f *W3*

tj valves :: r.senly use: when pre:essing MvHi, RBis, and E,,

heatralizer Tanas thecu;;EP] TOR II. vnen tne

~l "iANKF AR*" 5.*i. 83230-003 =a s can:ellec, these *WG" Ei valves snN1: nave een in:erp: rate: inte 50 3526-0*,*.

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No.

Nuslear 3s2e-004 M8 SYSTEM DESCRIPTION F0P. AUXILIARY BUILDING EMERGEtiCY Page of 3

78 LIQUID CLEAN-UP SYSTEM (EPICOR II)

Rev.

SUMMARY

OF CHANGE Approval Date 7

Annual update to reflect the current operating 7/89 i

continguration of the EPICOR II System and to reflect the out of service (03S) condition of the Submerged Demineralizer System (SDS). Table 12 was deleted for administrative purposes; Table 13 was deleted as being redundant to Table 16; and Table 14 was deleted because SDS is 005.

8 Annual update to reflect the following:

a.

ALC-F-5 filter cartridge is not only 1 micron 8/90 (nominal) and has been as " rough" as 10 micron (nominal).

b.

Radiation monitor ALC-RM-12 is no longer in service.

c.

Numerous other small corrections (e.g., typos,

syntax, labels) were also made.

9 Annual update to reflect the following:

6/91 a.

Air compressors ALC-P-7 and ALC-?-8 were removed.

b.

Changes in the system for Processed Water Disposal System (PWDS) evaporator feed and return pathways to and from CC-T-1, 10 Annual update to reflect the following:

6/92 a.

Use of polyethylene High Integrity Containers (HICs) b.

Use of BWST as feed or effluent storage tank.

c.

Delete MLB pump as end-user of EPICOR effluent.

d.

Delete references to DWCS systen which is out-o f-se rv ice.

e.

tiumerous other small corrections (e.g., typos, syntax) 11 Annual update to reflect the following:

5/93 l

a.

Data is provided on ALC-F-6 resin trap, and new motor for ALC-P-5.

b.

Other miscellaneous small corrections.

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TABLE OF CONTENTS i

I SECTION PAGE

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1.0 INTRODUCTION

6 1.1 System Functions 6

i 1.2 Summary Description of the System 7

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r 1.3 System Design Requirements 9

2.0 DETAILED DESCRIPTION OF THE SYSTEM 14 2.1 Components 14 l

2.2 Instruments, Controls, Alarms, and 31 Protective Devices f

3.0 PRINCIPAL MODES OF OPERATION 35 l

i 3.1 Startup 35 j

3.2 Normal Operatian 36 l

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3.3 Shutdown 37 3.4 Special or Infrequent Operation 38 3.5 Emergency 39 4.0 HAZARDS AND PRECAUTIONS 41 l

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SD 3526-004 TABLE OF CONTENTS (Cont'd) 4 TABLE PAGE I

i 1.

EPICOR II Pumps

.22 l

2.

Transfer Pump 43-3.

Pumps ALC-P-9 and ALC-P-10 44 i

4.

Recirculation Pump ALC-P-11 45 l

5.

Filters 46 t

6.

Demineralizers 47 i

i 7.

Miscellaneous Waste Hold-up Tank 48 8.

Clean Water Receiving Tank 49 l

9.

Off-Spec. Water Receiving / Batch Tank 50 10.

ALC-T-3 51 11.

Sump Pump, Chemical Cleaning Building 52 12.

Monorail Hoist System 53 13.

CCB Ventilation System Nameplate Data 54 14.

Valve List 55 t

15.

EPICOR. II Radwaste Pmcessing System 78 (IHC Polishing Mode) i

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SD 3526-004

1.0 INTRODUCTION

1.1 System Functions The functions of the Auxiliary Building Emergency Liquid Clean-up (EPICOR II)

System are (or have been):

1.1.1 To decontaminate, by filtration and ion exchange, radioactive waste water contained in TM1 Unit 2. In the past, EPICOR II also served as a polishing ion exchanger system for the Submerged Demineralizer System (SDS). SDS has been taken out of service and will no longer process / filter contaminated liquids. Therefom, EPICOR II processes the waste water directly.

1.1.2 To transfer EPICOR II pmcessed water from the Clean Water Receiving Tank (CC-T-2) to the following tanks:

a.

Processed Water Storage Tanks (PWSTs or PW-T-1 and 2).

b. Off-Spec. Water Rece.iving/ Batch Tank (CC-T-1) to be used for decontamination of the Reactor Building and Auxiliary / Fuel Handling Buildings. CC-T-1 is also used for recycle processing when required.

c.

Evaporator Condensate Test Tanks (ECTrs or WDI T-9A and 9B) to be used for various decontamination activities and make-up water / chemical additions via the Boric Acid Mix Tank (BAMT).

NOTE:

The transfer to WDL-T-9A/B passes thmugh Unit I Turbine Building, but is physically isolated from all Unit I systems.

d. On a non-routine basis to either the Condensate Storage Tank (CO-T-1 A), Borated Water Storage Tank (BWST) or the Synt Fuel Storage Pools via the truck fill station.

1.1.3 To provide mmote handling of spent resin containers from their position inside the Chemical Cleaning Building (CCB) to a transport cask or truck. Revision 11

I SD 3526-004 l

l 1.1.4 To limit releases of radioactive material to the environment to "as low I

as is reasonably achievable."

1.1.5 To pmvide for operation and maintenance of the liquid cleanup system in compliance with "as low as is reasonably achievable" radiation doses l

to personnel.

1.1.6 To provide a staging tank (CC-T-1) for the supply of water to, and the collection of distillate from, the Processed Water Disposal System

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(PWD3) evaporator.

t 1.1.7 To accomplish the above independently fmm TMI Unit-1 (for exception see NOTE above).

i 1.2 Summary Description of the System The Auxiliary Building Emergency Liquid Clean-up System, as the name implies, i

was originally designed and constructed for the primary purpose of processing and cleaning up the accident-generated water that collected in the TMI-2 Auxiliary Building. The system is commonly referred to as "EPICOR II."

The system consists of a liquid radwaste processing system which is located in the l

CCB. It is able to decontaminate, by filtration and ion exchange, radioactive l

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waste water contained in the Auxiliary Building, Fuel Handling Building, Service i

Building, and Reactor Building of TMI Unit 2. Contaminated water is pumped fmm a connection located on the Miscellaneous Waste Holdup Tank (MWHT) by i

a pump located in the CCB thmugh the yard and into the pmcess system;

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contaminated wate.r may also be routed from the Monitor Tanks (SDS-T-1 A and IB), the Contaminated Drain Tanks (CDTs), the Reactor Coolant Bleed Tanks (RCBTs), the Neutmlizer Tanks (WDL-T-8A and 8B), or the Borated Water Storage Tank (BWST). Yard piping is shielded and enclosed within a guard pipe, the open end of which terminates inside the CCB.

The primary process system consists of three demineralizers (ALC-F-1, ALC-K-1, I

and ALC-K-2), connected in series. Waste liquid is transferred from the source tank (MWHT, WDL-T-8A/B, RCBT, CDT, BWST, or SDS-T-1 A/B) thmugh the demineralizers, to the CC-T-2. Typical change-out criteria for the various units are indicated in Table 15.

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SD 3526-004 Processed water is typically delivered to CC-T-2 for sampling and analysis. The processed water is then pumped to one of the following, if within specification:

the Liquid Waste Disposal System of Thil Unit 2, the Spent Fuel Storage Pools, the PWSTs, the BWST, CO-T-I A, or WDL-T-9 A/B.

Additionally, the processed water can be transferred to the CC-T-1 for recycling thmugh the process system or use in the decontamination of the Reactor Building, Auxiliary, and Fuel Handling Buildings. Reprocessing under a feed and bleed scheme (via CC-T-2) can be done if the water does not meet the end process criteria; this is not a mutine operation since feed and bleed processing requires a long time to accomplish.

CC-T-1 may also be used to provide tankage for distillate water from the PWDS evaporator. In addition, feed water to the evapomtor may be supplied fru CC-T-1.

The CCB is a low leakage confinement building with an exhaust ventilation system to maintain the building at a negative pressure. hioisture separators, high efficiency paniculate air (HEPA) filters, and charcoal filters have been provided in the exhaust ventilation system in order to filter the building air before it is released to the stack at the roofline of the CCB. All effluent air is monitored for j

mdioactivity at this point. Provisions for gab samples are available.

Normal operation of the ion exchange processing system is by remote means I

except for infrequent operations such as sampling, spent resin container removal j

and new resin container installation. All remote system operations are controlled from the TV Monitor and Contml Building located outside the nonhwest corner of the CCB.

Remote handling of spent resin containers fmm their position inside the CCB to the transpon cask and truck is via a mmotely-operated, twenty-ton monorail hoist system.

t A fire protection system is installed in the HVAC equipment room, the TV Monitor and Control Building, and the CCB. A 4" tie-in to the existing fire main supplies a sprinkler system in the TV Monitor and Control Building and a hose station in the CCB, as well as the sprinkler line to the air filtration unit charcoal filters. The key to the lock on this sprayline valve is kept in the TV Monitor and Control Building. Line and grid pressure indication is provided in the TV Monitor and Contml Buildmg.

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EPICOR II interfaces with the TMI Unit 2 Radwaste Disposal Miscellaneous Liquids System, the Demineralized Water System, the Processed Water Storage l

System, the BOP Electrical System, the Senice Air System, the Unit 1 Liquid j

Waste Disposal System, the Fim Pmtection System, the Unit 2 Radwaste Disposal Reactor Coolant Liquid System, and the PWDS.

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NOTE:

Although them is an interface with the Unit 1 Liquid Waste Disposal System, the Unit 1 System will not be used. In this respect, Unit 2 will l

function independently. Valve ALC-V169 shall remain locked closed (unless transferring water fmm either CC-T-1 or CC-T-2 to the "B" Spent Fuel Pool) and a spectacle flange is installed downstmam of valve ALC-V169 at the transition between Unit I and Unit 2 liquid radwaste systems.

j 1.3 System Design Requirements q

1.3.1 Process System Design Requirements j

l 1.3.1.1 The ion exchange process line pipe size is nominally 2" j

schedule 40, based upon the EPICOR II System flow rate l

of 10-30 gpm.

Other line sizes are based on service l

requirements and

function, such as service air, I

demineralized water, recirculation and sampling.

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j 1.3.1.2 Pumps ALC-P-1 through 4 have hose connections and am

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pmvided with drip trays to collect leakage. Drip trays have nozzles as close to the bottom of the tray as possible and j

are served by flexible tubing which leads to the nearest

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floor or equipment drain using the floor slo,m to induce l

l flow. This tubing is placed well down into the floor drain.

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1.3.1.3 Remote system operations are directed and contmlled fmm i

outside of the CCB from the TV Monitor and Control i

Building. This area is provided with remote closed circuit j

television monitoring of the opemting amas inside and outside the CCB.

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I SD 3526-004 1.3.1.4 Process instmmentation consists of pH and conductivity monitors. Resin bed radiation irxels, pmcess line radiation levels, process flow rates, pmcess totalizers, and tank /demineralizer levels are also monitored.

Accelerometers for pumps ALC-P-1 through 4 are provided for equipment protection and an alternate method to determine processing flowntes.

1.3.1.5 The system tank vents are provided with inline heaters, demister filters, and charcoal filters for adsorption of evolved iodine. These units are sloped to dmin demisted liquids back into the system tanks.

1.3.1.6 Liquid waste feed to the system will be drawn fmm the source tank (MWHT, RCBT, SDS-T-I A/B, CDT, BWST, WDL-T-8A/B, CC-T-2, or CC-T-1) to the first EPICOR II pump (ALC-P-1).

1.3.1.7 The EPICOR II System is contained within the CCB which was originally designed to meet seismic criteria per Zone 1 of the building code. The EPICOR II System and major components when constructed were considered to be non-Quality Control (QC) scope; however, the system has F

since been reclassified Important to Safety (ITS), in QC scope.

i 1.3.1.8 All system piping is welded stainless steel except for air piping which is welded carbon steel or copper tubing.

Instmment tubing systems are 316 SS tubing and are made up using compression fittings. The process system piping l

is rated at 150 lbs. and is designed, installed and inspected in accordance with ANSI B31.1 (Power Piping).

NOTE:

Flanged and screwed connections are used as l

necessary on certain components.

1.3.1.9 Capability is provided to obtain a representative sample of CC-T-1 and CC-T-2, and the effluents of demineralizers i

ALC-F-1, ALC-K-1 and ALC-K-2, while in a low radiation area in accordance with Regulatory Guide 1.21.

• Revision 11 f

SD 3526-004 Representative sampling for either CC-T-1 or CC-T-2 is here defined as "after recirculating the tank contents for three volume changes". Also, the sample line for either CC-T-1 or CC-T-2 is purged to the sample sink for five line volumes prior to drawing the sample, and for demineralizers ALC-F-1, ALC-K-1 and ALC-K-2, the sample lines are flushed for a minimum of three (3) minutes prior to dmwing the sample.

NOTE:

Demineralizer ALC-F-1 is the first demineralizer, followed in series by demineralizers ALC-K-1 and ALC-K-2, respectively.

i 1.3.1.10 The building sump is a covered sump.

i 1.3.1.11 System blowdown air and demineralized water lines are provided with individual check valves ALC-V060 through V079 to minimize contamination of these systems.

1.3.1.12 The demineralized water supply header is provided with demineralized water from TMI Unit 2 in the range of 80-130 psig to meet EPICOR II requirements.

i 1.3.1.13 The system air supply header is provided with a pressure regulator operating in the range of 80-90 psig, and a moisture separator. An air oiler, and an anti-freeze injector are provided for the portion of the system air header servicing the EPICOR II pumps. The Plant Service Air System is the normal air supply.

1.3.1.14 If sampling indicates that the processed water is within limits for usage, the contents of CC-T-2 may be routed to one of the following:

the TMI Unit 2 Liquid Waste i

Disposal System, the Spent Fuel Storage Pools, the PWSTs, the BWST or CC-T-1.

1.3.1.15 All system overflow lines discharge to the CCB sump. All floor drains also discharge to the sump.

The water l

collected in the sump is staged in CC-T-1 by the sump 3

pump for recycle through the cleanup system or it is drawn i

i Revision 11

i SD 3526-004 i

and processed directly through the EPICOR II System via existing valves and piping.

1.3.1.16 Since the elevation of the discharge nozzle of CC-T-2 and the CCB floor were fixed prior to design and construction of EPICOR II, the hydraulic design for draining CC-T-2 is not adequate for complete draining of the tank. However,

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the system was designed to facilitate draining to the maximum extent possible. Final draining of CC-T-2 is accomplished with the manual drain line (valves ALC-V131 and V132).

l.3.1.17 Three resin traps are installed downstmam of the demineralizers.

1 1.3.1.18 A ten micron (nominally mted) or finer canridge filter (ALC-F-5) is installed downstream of the three resin traps.

1.3.1.19 The system has personnel shielding on various components f

to reduce the radiation levels in the operating areas of the i

building.

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I 1.3.1.20 A resin tmp (ALC-F-6) is installed on the outlet from the liners' overflow line to prevent resin carryover into the l

sump.

i 1.3.2 Material Handling Design Requirements j

1.3.2.1 Normal operation of the EPICOR II System is by remote methods.

j 1.3.2.2 Densineralized water and service air connections are i

prmided to flush and blowdown the entire system or j

ponions of it to allow system maintenance.

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1.3.2.3 Four (4) feet high by four (4) feet in diameter (4x4) liners or high integrity container (HIC) demineralizers with an -

adapter lift ring attached may be removed from the building l

by making use of the transfer bell designed for this i

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purpose.

The transfer bell is positioned over the radioactive liner; the shield doors on the bottom of the bell am opened and the liner is drawn up into the bell. The doors are closed and the bell is carried, by the crane, to the i

truck which may have a concrete shield vessel for isolating the bell during transponation to the staging facility.

Monitoring of the area is carried on during these activities to assure the safety of personnel.

Another liner is positioned in the vacated space. Shielding, process lines, l

and level instrumentation are mpositioned and the unit is returned to service.

NOTE: The shielded transfer bell is no longer routinely.

used and will only be used if operation of the i

system results in radiation levels from the demineralizers exceeding limits for unshielded handling.

1.3.2.4 Six (6) feet high by six (6) feet in diameter (6x6) liners and lightly loaded 4x4 liners are handled in and out of the building without shielding. This is accomplished by remote operation and by establishing appmpriate barriers limiting i

the appmach of personnel to the handling operation. Spent resin containers are lifted directly from within substantial shielding barriers in the CCB and deposited directly in the transfer cask on the unmanned truck located immediately outside the building, or loaded unshielded on a transport truck depending on the liner's radiation levels.

1.3.3 Air Handling Design Requirements 1.3.3.1 A ventilation fan is provided to maintain the CCB at a negative pressure.

1.3.3.2 The MSA filtration unit is designed to meet the

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requirements of NRC Regulatory Guide 1.140.

i 1.3.3.3 The moisture separator is provided to remove water vapor

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droplets from the air.

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1.3.3.4 An electric heater is provided within the MSA filtration unit j

to lower relative humidity (RH) to 30% with 100% RH inlet air.

1.3.3.5 The prefiker has an average atmospheric air strain efficiency of 85%.

1.3.3.6 The two HEPA filter banks are DOP tested in place to assure an efficiency of 99.95% for removing 0.3 micron particles.

I 2.0 DETAILED DESCRIPTION OF THE SYSTEM 2.1 Components 2.1.1 EPICOR II Pumps ALC-P-1 through 4 (See Table 1)

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Pumps ALC-P-1 through 4 are air-driven, positive displacement pumps with a capacity of 10 gpm to 120 gpm. Each pump is equipped with a pulsation dampener in the process outlet.

l These pumps are utilized in the system to circulate the liquid through the demineralizers. The hoses furnished for the flexible connections to l

the pumps, filters, demineralizers, and traps have a design pressure of

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100 psi.

j Air supplied to the pumps passes thmugh an air oiler and an anti-freeze injector to a valve manifold. Pump speed and capacity will be varied by the EPICOR II operator to achieve the desired flow through the radwaste process system. Pump speed is controllui by throttling the drive air at the Fava Control Panel. Demineralized water and oil free air connections are provided on the suction and discharge side of each l

pump for flushing and blowdown purposes. Pump noise and vibration monitors are present for pumps.ALC-P-1 through 4 and have a read-out -

on panel ALC-PNL-2 in the TV Monitor and Control Building.

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1 SD 3526-004 2.1.2 Transfer Pump ALC-P-5 (See Table 2)

Transfer pump ALC-P-5 is a single stage horizontal centrifugal pump with a capacity of 200 gpm at 100' head. The pump motor is rated at 10 HP and is powered from AICC 2-33A in the TV hionitor and Control Building.

The pump is controlled by push buttons for START /STOP fmm AICC 2-33A, a hand selector switch for low level j

control of either CC-T-1 or CC-T-2 fmm the panel ALC-PNL-1 in the IV hionitor and Control Building and level switches in panel ALC-PNL-1 for CC-T-1 and CC-T-2. The level switches receive their signals from level transmitters ALC-LT-1 and ALC-LT-2 at CC-T-1 and CC-T-2, mspectively. CC-T-1 and CC-T-2 also have high level cutouts to transfer pump ALC-P-5.

Demineralized water is supplied to the pump mechanical seal from a solenoid operated valve ALC-V136 controlled from the pump motor staning circuit. When the motor stans, the valve opens. The seal water flow rate is maintained at 1-2 gpm by throttling valve ALC-V134 i

when seal water injection is required. Seal water injection is only required if the pump is handling water which contains greater than 7000 ppm boron.

If the pump handles clean water, it is acceptable to allow the mechanical seal to be lubricated through the pump's internal passages.

l As long as the water has passed through filter ALC-F-5, the water is clean enough (from a grit standpoint) to lubricate the mechanical seal.

Thus, as long as filter ALC-F-5 is in use, the demineralized seal water i

can be tumed off with valve ALC-V134 to reduce the total volume of processed water or mdwaste.

This pump is used to transfer water from either CC-T-1 or CC-T-2.

It is also used to transfer water from CC-T-2 to CC-T-1.

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Furthermore, this pump may be used for recirculating and sampling the contents of CC-T-2 or CC-T-1. (Recirculation of CC-T-1 may also be accomplished using ALC-P-il.) The sample connection terminates at l

the sample system sink. The pump is provided with a discharge pressure gauge, and a flow element on the discharge line to Units No.

I 1 and No. 2, the Spent Fuel Pools, the PWSTs and the truck fill station. Remote indication of flow (ALC-FI-2) and a flow totalizer I Revision 11 t

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i SD 3526-004 (ALC-FQ-2) are located on panel ALC-PNL-1.

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To protect the pump from operating at shutoff or low flow, it is provided with a solenoid-operated minimum flow control valve ALC-V291. The minimum flow line branches to both CC-T-1 and

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CC-T-2; the direction of the flow is to the tank from which the water i

originates.

The operation of the minimum flow control valve is automatic, although manual control is provided as well. Automatic

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control is provided by differential pressure switch ALC-DPS-1. The i

switch measures the flow through the pump in terms of AP across the equipment. When the flow is less than 40 gpm, the minimum flow control valve opens and will remain open until the flow has increased l

to approximately 90 gpm, at which time it will close. Manual control permits the opening and closing of the valve at any time.

2.1.3 ALC-P-9 (See Table 3)

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This pump provides water from CC-T-1 to the PWDS evaporator. It is located in the CCB, underneath CC-T-1. Discharge piping from this

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I pump crosses the CCB, the yard, runs down the Unit 1/2 corridor and J

into the Evaporator Building. The design flowrate of this pump is 5 to 7 pm.

I 2.1.4 ALC-P-10 -(See Table 3) i i

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This pump discharges water from the PWDS evaporator to CC-T-1 for l

storage. Normally, this water is distillate water; however, flush water or other water may be transferred. This pump draws its suction from j

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ALC-T-3, a small storage tank in the Unit I/2 corridor. The discharge piping runs down the corridor, across the yard, and into the CCB, l

l where it ties into the ALC-P-5 discharge piping routed to CC-T-1.

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f Normally tnis pump's operation in controlled by a level controller m ALC-T-3. When ALC-T-3 is full, the pump operates; when ALC-T-3 l

reaches low level, the pump stops. A handswitch in the Unit 1/2 i

corridor allows manual operation of the pump as well.

The design flowrate of this pump is 5 to 7 gpm.

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2.1.5 ALC-P-11 (See Table 4) f This single stage centrifugal pump provides the ability to recirculate CC-T-1. (This operation was at one time performed by ALC-P-5. At j

this time, ALC-P-5 recirculates CC-T-2 while ALC-P-11 recirculates CC-T-1. The use of separate pumps and piping to recirculate these f

tanks prevents their contents fmm mixing).

A sample line is provided on the discharge of the pump. This sample j

line is routed to the CCB Sample Sink.

ALC-P-11 is located beneath CC-T-1. It takes its suction on the tank f

discharge pipe at the bottom of the tank and discharges into a f

penetration at the top of the tank.

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2.1.6 Demineralizer ALC-F-1 (See Table 6) i j

This first stage demineralizer (also referred to as a " liner") is generally j

used to remove sodium, other non-radioactive chemicals, and low r

4 concentrations of radioactive isotopes. This demineralizer is either a l

4x4 or 6x6 carbon steel Imer.

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Should conditions require gross cesium and strontium removal, a stainless steel HIC loaded with zeolite resins is placed in the first position to act as a roughing filter. This mode of operation precludes the need for SDS; thus, SDS has been placed out of service. The HIC is similar in size to the carbon steel 4x4 liner; the major difference in l

design being the materials used during fabrication of each type. HIC demineralizers are constmeted of a very high grade stainless steel, l

enabling the container to meet the burial limits of Class B or Class C l

waste.

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In all cases (4x4, 6x6, or HIC liners), the top of the liner has four (4) quick disconnect (QD) fittings: an inlet (pump discharge), an outlet l

(pump suction), a combination vent / overflow, and an air type QD

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fitting for the level bubbler tube.

As a means of backup level j

indicator, a threaded level conductivity probe also penetrates the liner top. (NOTE: Polyethylene HICs do not have operable conductivity

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probes.)

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An additional air connection is pmvMed at the top of the carbon steel 6x6 liners to allow removal of the plug from the top of the false bottom after final dewatering. The false bottom is filled with an approved sorbent to absorb water that may tend to accumulate. The false bottom is not required because the water volume absorbed is less than the 0.5 %

limit for shallow land burial. A manway with approximately a 20" l

diameter opening is installed on top of the liner.

1 The inlet nipple is connected to a full dispersion manifold in the top of the liner. The outlet nipple (pump suction line) connects to a single layer filter manifold which is located at the bottom of the liner.

l The level probe or bubbler system maintains water level between 4" and 6" from the top of the liner by opening and closing solenoid valve ALC-V185 on the air supply to pump ALC-P-1, which is supplying the i

water; starting the pump on low level and stopping the pump and closing valves ALC-V043 or ALC-V242 on high level. On Hi Hilevel 4" from the liner top, an audible alarm is sounded at the EPICOR II I

Monitoring Console, located in the TV Monitor and Control Building, l

valve ALC-V255 closes, and the pump motor opemted valve closes.

i The EPICOR II operator may select either air bubbler or conductivity level contml on the Fava Control Panel located in the TV Monitor and Control Building.

The demineralizer is vented, via hose connections, to a 2" vent header which leads into the top of CC-T-1.

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A tee is provided in this vent line for a hose connection to a ccmmon header which discharges to the CCB sump. The line is provided as a demineralizer overflow line and demineralizer overpressure protection.

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A loop seal is provided to ensure that all liner gases are routed to l

CC-T-1 and its vent filters, rather than directly into the CCB. A level switch (ALC-LS-21) is installed in the loop seal for indication of flow in the header and provides an alarm at panel ALC-PNL-1 in the TV Monitor and Control Building.

The shielding in the ALC-F-1 position consists of a 5 1/8" thick, square lead brick wall (3 1/8" thick on south side) plus a 1/2" of i

shield-supporting steel. Radiation monitors (ALC-RM-1 and 2) are located inside this shield 180 degrees apart at different elevations to

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monitor accumulated radiation levels in the demineralizer. When the HIC is installed, a concrete shield (culven) will provide additional shielding and a place to land the transfer bell while removing the spent HIC.

t To avoid breakthrough of sodium to the second liner when l

demineralizer ALC-F-1 is organically loaded, the batch size through j

demineralizer ALC-F-1 is limited.

If a HIC is in service in the ALC-F-1 position, activity breakthrough i

i will be limited through batch size or by the activity as measured by radiation monitor ALC-RM-7, installed at the influent header of demineralizer ALC-K-1.

The second liner will then normally be i

organically loaded for sodium removal.

l If the water source is very low in cesium and strontium, but still l

mquires further polishing (i.e., ecycle processing of either CC-T-1 or j

CC-T-2), a jumper hose may bypass the HIC demineralizer in the ALC-F-1 position. In this configuration, the first liner in the series -

will be demineralizer ALC-K-1 followed by demineralizer ALC-K-2 (i.e., two liners versus three). Processing relatively clean water will l

rinse cesium and/or strontium activity off of the HIC zeolites on to the 7

downstmam ALC-K-1 demineralizer.

This is the purpose of the l

" BYPASS" mode.

Refer to Section 2.1.23 for details regarding demineralizer level controls.

R.efer to Sections 3.4.2 and 3.4.3 regarding operations and systems that prepare a HIC /demineralizer for shipping and burial.

1 Remote indication is provided on the cleanup panel ALC-PNL-1 for radiation monitors ALC-RM-1 and 2.

During system operation, I

radiation levels as indicated on radiation monitors ALC-RM-1 and 2 should not be allowed to exceed 1 R/hr.

i 2.1.7 Demineralizers ALC-K-1 and ALC-K-2 (See Table 6) t t

Two demineralizers are installed in series with demineralizer ALC-F-1 to funher rtmove radioactivity from the waste liquid and polish the 3

effluent.

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Demineralizer ALC-K-1 is either a 4x4 or 6x6 liner or a polyethylene HIC and is primarily used to reduce the activity level of the process fluid through ion exchange and filtering.

For this reason, the anticipated activity levels are high and the shielding around demineralizer ALC-K-1 is identical to shielding around demineralizer ALC-F-1 when demineralizer ALC-F-1 is a 6x6 liner.

Demineralizer ALC-K-2 is either a 4x4 or 6x6 liner and is primarily

_l used to polish the effluent water from demineralizer ALC-K-1 and to l

act as a guard in the event of a resin breakthmugh from demineralizer ALC-K-1.

For this reason, the anticipated activity levels in demineralizer ALC-K-2 are lower than in deminemlizer ALC-K-1.

Each demineralizer has the same external connections as deminerahzer ALC-F-1. The demineralizer resin composition and quantity will be determined on the basis of system samples and operating data.

4 As with demineralizer ALC-F-1, two radiation detectors are located at different elevations 180 degrees apart inside the lead shield. Remote indication is pmvided in the TV Monitor and Control Building on panel ALC-PNL-1. During system operation, radiation levels on indicators ALC-RMI-3 and 4 for deminemlizer ALC-K-1, should not be allowed to exceed 1 R/hr. Radiation levels on indicators ALC-RMI-5 and 6 for demineralizer ALC-K-2, should not be allowed to exceed IR/hr.

2.1.8 Miscellaneous Waste Hold-up Tank WDL-T-2 (See Table 7) l The MWHT which has a capacity of 19,518 gallons, can receive liquid from the following sources:

a.

Auxiliary Building Sump Tank t

b. Neutmlizer Tanks i

c.

Contaminated Drain Tanks

d. Reactor Building Sump e.

Deborating Demineralizer back wash outlet Revision 11 t

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Fuel Storage Pool Submersible Pump Discharge

g. Demineralized Water System l

h. Condensate Polisher Sump

i. Water Treatment Sump

j. Reactor Coolant Bleed Tanks

k. Concentr2ted Waste Stomge Tank l

The tank also has connections to the MWHT pump suction, recirculation capability, a caustic and sulphuric acid inlet, two nitrogen inlets, two vents, a gas sample connection and a relief valve. The tank is vented to the Radwaste Disposal-Gas OVDG) System and has its own HEPA-filtered vent to the Auxiliary Building atmosphere. To prevent acid splashing on the inner tank walls, the inlet piping extends eight (8) feet into the tank. The diameter of the tank is 10'-91/4". The hnVHT is located in the Auxiliary Building at elevation 305' A tee connection is installed in place of the suction line strainer, 1

WDL-U202B, on the MWHT pump OVDL-P-6B) suction ' line.

l Connected to this tee is a 2" line which may supply the liquid from the hnVHT to the suction side of pump ALC-P-1. An alternate connection from the discharge side of the MWHT pump to EPICOR may also be used to supply EPICOR. A 4" guard pipe with a combination of lead and conemte shielding encloses the piping run from the Auxiliary e

Building corridor to the CCB penetration. The guard pipe is open to the atmosphere of the CCB, which is under a slight negative pressure.

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2.1.9 Clean Water Receiving Tank CC-T-2 (See Table 8) f CC-T-2 is a stainless steel atmospheric pressure tank with a capacity of 133,689 gallons located in the CCB. CC-T-2 receives the processed liquid from the discharge of pump ALC-P-4 via, in order, three resin traps, a filter, conductivity cell, pH meter, and an inlet l

flowmeter / totalizer.

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An overflow line with a loop seal is pmvided near the top of CC-T-2.

A demineralized water supply is pmvided to fill or flush the loop seal.

A suction line from transfer pump ALC-P-5 penetmtes the CC-T-2 skirt i

and connects to the bottom of CC-T-2. A connection on the top of CC-T-2 is also pmvided for the transfer pump recirculation line, a feature that enhances mixing of the contents. Level indication and high level alarm are provided on panel ALC-PNL-1.

A future xenon j

hold-up tank connection is provided on the vent line.

A 2" i

demineralized water line is also pmvided on top of CC-T-2 for l

whenever large quantities of demineralized water are required in i

CC-T-2. This would include preoperational testing or tank cleanup.

A drain line is pmvided off transfer pump ALC-P-5 suction piping to i'

drain the suction piping and the remaining water in CC-T-2 that the transfer pump cannot drain.

CC-T-2 has a 2" vent line exhausting to the CCB thmugh a two-stage j

demister filter. The first stage consists of two moisture separators and

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a HEPA filter. The second stage consists of two charcoal filters and a HEPA filter. A normally energized heater in the common 2" vent line is contmlied from power panel MP 2-33A..

f Processed water is stored in CC-T-2 until a batch is completed. A representative sample of the processed water can be obtained from the l

discharge of the transfer pump at the sample sink after recirculating three volumes of CC-T-2 and purging the sample lines for five line i

i volumes before drawing the sample. If the sample indicates the water quality is unsatisfactory, the water can be pumped to CC-T-1 for temporary storage or routed directly back into the suction line of pump ALC-P-1 for mprocessing thmugh the filter and demineralizers until the quality is acceptable for discharge to the plant or storage tanks. If sampling indicates that the contents of CC-T-2 am satisfactory, the water is pumped normally into one of the following: the TMI Unit 2 Liquid Waste Disposal System, the Spent Fuel Storage Pools, the BWST, or the PWSTs; however, the water may be stored in CC-T-1, 1

if desired. CC-T-1 is flushed clean with demineralized water or clean

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processed water before it is used for clean water storage.

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SD 3526-004 2.1.10 Off-Spec. Water Receiving / Batch Tank CC-T-1 (See Table 9)

CC-T-i.3 a stainless steel tank with a capacity of 85,978 gallons f

designed for full vacuum to 75 psig. For the EPICOR II System, l

CC-T-1 is operated at atmospheric pressure only. CC-T-1 can receive

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the discharge fmm the CC-T-2 transfer pump whenever it is desired to l

either recycle the water for further processing, or store the purified water for future disposition.

CC-T-1 is piped to receive the discharge from the CCB sump pump, if

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desired, but normally the sump is drained by a 2" suction line to pump 3

ALC-P-1 (see Section 2.1.12). A suction line at the bottom of CC-T-1 can be lined up either to pump ALC-P-1 for reprocessing the contents of CC-T-1 through the system, to transfer pump ALC-P-5 for i

recirculation and sampling, or discharge, or to pump ALC-P-1I w.

recirculation and sampling. The recirculation lines connect to the top of CC-T-1.

CC-T-1 is vented to the building in the same manner as CC-T-2. An overflow line with a loop seal is pmvided near the top of CC-T-1. A f

l deminemlized water supply is provided to the loop seal. A connection at the top of CC-T-1 receives vents from the prefilter, the i

demineralizers and the cmd filter. Level indication and high level

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4 alarm are provided on panel ALC-PNL-1. A future xenon hold-up tank connection is provided on the vent line.

a CC-T-1 has a 2" vent line exhausting to the CCB through a two-stage 1

demister filter. The first stage consists of two moisture separators and a HEPA filter. The second stage consists of two charcoal filters and i

a HEPA filter. A normally energized heater in the common 2" vent l

line is controlled from power panel MP 2-33A.

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CC-T-1 is piped to receive water discharged from the PWDS evaporator. In addition, CC-T-1 may be used to provide water to the j

PWDS evaporator by way of ALC-P-9.

2.1.11 ALC-T-3 (See Table 10)

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This stainless steel tank has a capacity of 100 gallons and is designed to receive water fmm the PWDS. The tank is located in the Unit 1/2 i

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i corridor and provides a suction volume for pump ALC-P-10 to forward water to CC-T-1, or pump PW-P-3 to fonvard water to the Processed i

Water Storage Tanks.

A ball-float level-controller installed in this tank normally controls the operation of ALC-P-10 or PW-P-3 (pumping out the tank when level i

is high, stopping the pump when the level is low). The overDow from I

this tank is routed to the Evaporator Building sump. The tank is operated at atmospheric pressure only and is placed in a stainless steel drip tray to capture any tank leakage. A sight glass is provided on the r

side of the tank to allow a visual check of water level.

2.1.12 Chemical Cleaning Building Sump I

The CCB sump is a stainless steel lined pit with a capacity of 4000 gallons located in the nonhwest comer of the CCB. All leakage fmm i

tank overflow, equipment, and floor drains is collected in the sump.

One sump pump (see Table 11) is installed to permit the transfer of the liquid from the sump to CC-T-1, if desired. The pump is a single stage centrifugal pump with a capacity of 100 gpm. The pump motor is rated at 20 HP and is controlled from a selector switch (MAN-OFF-AUTO) located on MCC 2-33A. When in AUTO, the pump is controlled by

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conductivity type level switch ALC-LS-1 which stans and stops the pump automatically.

A High Sump Level Alarm is provided on cleanup panel ALC-PNL-1.

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When in AUTO, the pump is started when the water level in the sump l

reaches a level that is 481/4 inches below the face of the pump mounting. The pump stops when the level of water has been lowered to a level that is 90 3/8 inches below the pump face. The high level r

alarm is actuated when the water level reaches 36 I/4 inches below the face of the pump mounting. The volume of water removed from pump START to pump STOP is approximately 1600 gallons. There is also a volume of nearly 1700 gallons above the High Alarm before the sump overflows.

The sump is normally drained by a 2" line provided from the sump to a 2" flushing line just upstream of its entry into the suction line of l

pump ALC-P-1. This permits the return of the sump water to the l

EPICOR II System directly from the sump without circulating through i

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SD 3526-004 pump CC-P-2A and CC-T-1. A 3/4" branch connection is provided in this line with quick disconnects attached to permit ready access for flushing with demineralized water fmm an outlet downstream of valve l

ALC-V015 with a shon length of hose.

t 2.1.13 20 Ton Monorail Hoist System (See Table 12) l A 20 ton hoist is pmvided for removal and replacement of the i

deminemlizers and other large pieces of ar.xiliary equipment in and out l

of the building. It is mounted on the monorail which extends from the nonh side of the CCB above the resin traps through the south end of the building, extending 18' outside of the building over the cask loading

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area.

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In order to minimize the radiation exposure to personnel during demineralizer removal, the hoist is operated remotely using a remote pendant opemting station in the TV Monitor and Contml Building.

Remote opemtion is aided through the use of a closed cimuit TV (CCTV) system with six cameras. The pendant has six pushbuttons for

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trolley and hoist operation - one START, one STOP, two for nonh/ south movement of the single speed trolley, and two for the hoist j

Quad-Speed Control System which are, a 4-step button for creep, low, medium and high speed RAISE, and a 4-step button for creep, low, medium and high speed LOWER.

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1 There is also a local monorail hoist pendant located on the CCB

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operating floor. This pendant is used for performing operations where j

there is little radiation exposure, such as bringing a new liner of resin into the building.

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-1 To aid positioning of the hoist remotely for demineralizer replacement, I

the monorail has visible target markings above the demineralizers and l

in the cask loading area, all of which can be viewed with the TV cameras.

i 2.1.14 Resin Filters ALC-F-4A, B and C (See Table 5)

Three resin filters (i.e., traps) are pmvided downstream of pump ALC-P-4 to prevent resin fines from entering CC-T-2. If any filter's contact radiation level reaches 250 mR/hr (on any pan of the filter), the

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SD 3526-004 system must be shutdown and the filter replaced. Four sides of the i

filters are shielded by 8" thick solid concrete blocks. The top is shielded with 1/2 inch of lead.

2.1.15 Crud Filter ALC-F-5 (See Table 5)

A ten micron (nominally rated) or finer filter with isolation valves is f

provided between the resin filter and CC-T-2. The primary purpose of this filter is to eliminate most particulates 'pmsent in the processed water. A vent line connected to CC-T-1 and a drain line to the floor i

drain system is pmvided for draining the filter housing prior to i

inserting or removing a filter cartridge. The filter is shielded by 3 1/8" l

lead bricks on three sides, and by a concrete wall on the fourth side.

During removal of the filter, it is handled as radioactive material. The i

filter is replaced whenever the contact radiation level reaches 250 mR/hr or when the pressure drop reduces the process flowrate below an acceptable value. A special lever is provided to aid in removal of l

the filter cartridge, if necessary.

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2.1.16 Ventilation Heating Unit and Moisture Separator i

Heatmg umt ALC-E-H1 (see Table 13) is mounted on the inlet of the i

filtration unit at elevation 304' and consists of a moisture separator j

(ALC-E-F1) and a 60 KW 480 volt, 3 phase heater. The heater is j

powered from MCC 2-33A.

i j-2.1.17 Ventilation Filter Unit The tilter unit consists of a single housing containing, in order: a prefilter (ALC-E-F2), a HEPA filter (ALC-E-F3), charcoal filter beds l

(ALC-E-F4) and a final HEPA filter (ALC-E-F5). A manually actuated fim protection water supply is provided for the charcoal beds.

2.1.18 Ventilation Fan Assembly (See Table 13) f Fan assembly ALC-E-1 is a 30HP,460 volt,3 phase, 60 cycle, radial flow centrifugal unit with a capacity of 8000 cfm. This fan, powered from MCC 2-33A, is mounted on the outlet of the filter unit and discharges the ventilation exhaust through ducting (monitored by a r Revision I1 i

SD 3526-004 radiation detector) and out through the roof.

2.1.19 Ventilation Radiation Monitor ALC-Rh11-18 (See Table 13)

This radiation monitor samples air in the fan discharge line isokinetically at a rate of 4 cfm to provide local (at monitor) and remote indication (on panel ALC-PNL-1) of discharge paniculate and noble gas activity levels. Remote indication of these parameters is recorded on a strip chart recorder. The monitor will provide an alarm at a radiation level of 4.1IE-2 pCi paniculate or 3.81E-4 pCi/cc noble gas activity -

on the panel in the TV Monitor and Control Building. This radiation monitor is powered from MCC 2-33A. A splitter block has been provided in the line to the radiation monitor to provide a means of taking grab samples as may be required.

2.1.20 Ventilation Weatherproof Enclosure The weatherproof enclosure is located at grade level and houses the components discussed in Sections 2.1.16 through 2.1.19.

2.1.21 Chemical Cleaning Building Radiation Monitors Four area radiation monitors (ALC-RM-8 through 11) are provided in the CCB. These radiation rconitors are provided with remote indication on the radiation monitoring panel ALC-PNL-1 in the TV Monitor and Control Building. The monitors provide a common alarm at a high radiation level and monitor failure on panel ALC-PNL-1.

These radiation monitors are provided for operator information.

2.1.22 Closed Circuit TV System A CCTV system is provided to aid in remote handling of the demineralizers and to aid in system surveillance during operation. The system consists of seven TV cameras strategically located in the CCB.

The TV monitors and necessary controls are mounted on the TV Monitor Console located in the TV Monitor and Control Building.

Camera No. I is mounted on the monorail support structure outside the CCB to allow viewing of the prefilter or demineralizer while being loaded into the transfer cask. Camera No. 2 is mounted directly on the Revision 11

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i SD 3526-004 20 ton hoist and provides a direct view of the monorail. Target markings which can be viewed with this camera are provided on the monorail to aid in the positioning of the hoist. Camera No. 3 has a i

PAN-TILT control and is mounted to provide a view of demineralizer ALC-K-2 for remote handling. The PAN-TILT control allows remote movement of the camera to permit scanning a large area of the CCB for

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surveillance during system operation.

Cameras No. 4 and No. 5 provide a view of the top area of demineralizers ALC-F-1 and j

ALC-K-1 to aid in remote handling of these casks and to provide a surveillance capability for these casks during operation of the system.

Camera No. 6 is mounted to provide a view of the pumps ALC-P-1 i

thmugh 4.

This camera provides the operator' with a remote surveillance capacity for viewing this area of the building during system operation. Camera No. 7 has a PAN-TILT control and is mounted on the west wall between demineralizers ALC-K-1 and ALC-K-2 to l

provide remote monitoring of potential leak areas.

2.1.23 Major System Valves l

Inlet Isolation Valve ALC-V043 l

t One stainless steel, 2",120V motor-operated ball valve is installed on i

the inlet line from the source tank to the EPICOR II System. The valve is powered from the 120/208V power panel MP 2-33A and controlled by a handswitch located on MCC 2-33A, Compartment 3D and a prefilter level probe.

Valve position and control power availability indications are provided by red, green and white indicating lights also located on Compartment 3D. The three lights will be on while the valve is in an intermediate position. The valve is provided I

with a manual override for "close" operation only. Valve ALC-V043 is interlocked with valve ALC-V242 to assure that only one of these two valves can be OPEN at a time.

Valve ALC-V043 is also interlocked with the level monitor of demineralizers ALC-F-1 and ALC-K-1. The valve closes automatically when a high level occurs in the controlling demineralizer, to prevent overfilling of the vessel. The choice of the controlling demineralizer is dictated by the configuration of the processing train through selector switch ALC-SS-1 (F-1 ON LINE or F-1 BYPASSED).

If demineralizer ALC-F-1 is in the processing train, its level controller will control valve ALC-V043; if demineralizer ALC-F-1 is bypassed, control of valve ALC-V043 is

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SD 3526-004 transferred to demineralizer ALC-K-1 level controller.

Service Air Reculator Valve ALC-V109 i

One 3" pressure regulating valve with a 150 lb. rating at 120*F is l

installed on the service air header supply to the EPICOR II System to reduce the pmssure to 80 psig.

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Process Supply Line Valve ALC-V255 to Demineralizer ALC-F-1 One 2" solenoid valve (ALC-V255) with a 150 lb. rating at 120*F is installed on the line between pump ALC-P-1 and deminemlizer ALC-F-1 between manual valves ALC-Vl91 and ALC-V207. Valve ALC-V255 is normally closed unless energized and is interlocked to close on high level in demineralizer ALC-F-1. Additionally, it closes on loss of electrical power or when the EPICOR II System is not running.

Off-Spec. Water Supply Isolation Valves ALC-V086 and ALC-V242 to l

4 Pump ALC-P-1 One stainless steel,2", air-operated ball valve, ALC-V242, is installed on the supply line from CC-T-1 to the suction of pump ALC-P-1. The valve allows reprocessing of water from either CC-T-1 or CC-T-2.

The valve is powered from the 120/208V power panel MP 2-33A and controlled by a handswitch located on MCC 2-33A, Compartment 3E.

Valve position and power availability indications function in the same manner as for valve ALC-V043. Valve ALC-V242 is interlocked with i

valve ALC-V043 to assure that only one of these two valves can be OPEN at a time. Valve ALC-V242 is an air-operated ball valve which is energized to open. This valve will close on loss of power thus l

avoiding uncontrolled draining of either CC-T-1 or CC-T-2. The valve 4

is interlocked with valve ALC-V043 such that only one valve can be opened at a time to prevent crossflow. It is also interlocked with the i

level controller of demineralizers ALC-F-1 and ALC-K-1, in the same l

arrangement as valve ALC-V043.

Valve ALC-V086 is a stainless steel, 2",120V motor-operated ball valve which is also installed on the outlet line of CC-T-1.

It is controlled by a manual handswitch mounted in MCC 2-33A, i

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compartment 3E.

By opening valve ALC-V086 and. closing ALC-V242, clean water can be sent from CC-T-1 to the suction of transfer pump ALC-P-5 for transfer to the PWSTs or other transfer points.

2.1.24 Sample System A sample system is provided to obtain a representative sample of CC-T-1, CC-T-2, and the effluents of demineralizers ALC-F-1, ALC-K-1 and ALC-K '

The samples from the demineralizers and the sample obtained from the feed tank are used to determine the isotopic inventory deposited on the l

msin beds. The determination is made by analyzing the influent and effluent isotopic concentrations, the difference of which is deposited on i

the bed.

This information is requirtd for shipment of the spent containers to the waste disposal site.

A common collection station shielded by an 8-inch thick solid block wall is located on the CCB mezzanine, and is provided for contmiled and safe sampling.

The collection station consists of individual sample stations for CC-T-1 and CC-T-2; and for deminemlizers ALC-F-1, ALC-K-1, and ALC-K-2; and a sample sink.

i The sample sink is provided with demineralized water for the sink spray header and bottle washing. The drain from the sink is routed to the CCB sump. The sink is also provided with ventilation which consists of a hood and ductwork tied into the CCB ventilation system.

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Recirculation of the sample lines from demineralizers ALC-F-1, f

ALC-K-1, and ALC-K-2 back to the suction of pump ALC-P-2, and the l

collection of samples is controlled by solenoid valves. The ability to obtain grab samples is pmvided in the recirculation line for flow i

verification. Piping for the sample lines is 1/2" stainless steel tubing with compression type connectors.

NOTE:

See Sections 2.1.9 and 2.1.10 for funher information on obtaining a sample from CC-T-1 and CC-T-2. Revision 11 P

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SD 3526-004 2.1.25 ALC-F-1 Liner Breakthrough Monitor Radiation monitor ALC-RMI-7 is installed on the discharge of demineralizer ALC-F-1 to monitor for activity breakthmugh on the first demineralizer. The monitor has two alarm setpoints. The Alert Alarm setpoint is 68,000 cpm above background, and the High Alarm setpoint is 136,000 cpm above background.

2.2 Instruments, Controls, Alarms, and Pmtective Devices 2.2.1 Cleanup System The EPICOR H System is nonnally operated and monitored from i

control panel ALC-PNL-1 located in the TV Monitor and Contml Building which is a separate prefabricated building. The TV Monitor I

and Control Building is adjacent to the northwest corner of the CCB.

Electrical power is supplied to the EPICOR II System fmm 750 KVA Unit Substation USS 2-33 located on the mezzanine floor at elevation 305' in the southeast corner of the Turbine Building for Unit 2. USS 2-33 was originally the power supply to the Control Rod Drive Motors.

I 480V power from USS 2-33 is supplied to MCC 2-33A located inside the TV Monitor and Contml Building. The HVAC system fan and heaters, the transfer pump, building sump pump, and the 20-ton hoist are powered fmm MCC 2-33A.

A 480-120/208 Vac, 25 KVA l

transformer, supplied from MCC 2-33A, supplies all other system electrical loads from power panel MP 2-33A, except heat traces which are supplied from the control rod breaker MCC 2-43.

The EPICOR II pumps are controlled through an automatic control unit l

which provides AUTO / MANUAL on-off switches and indicating lights for the pumps, deminemlizer high level alarms, and an ON/OFF switch for the unit. Control power is provided for the EPICOR H solenoid l

operated air supply valves through these units. The speed of the pumps is controlled by throttling motor operated valves ALC-V260,261,262 and 263. A turbine flowmeter (ALC-FI-1) is provided to monitor process flow rates.

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SD 3526-004 l

All process instrumentation monitored in the control center is mounted i

on cleanup panel ALC-PNL-1. Audible alarms and indicating lights are pmvided on this panel for CCB Sump High Level, CCB Ventilation l

System Trouble, CCB Charcoal Filter High Temperature, CCB High Exhaust Radiation Level, CCB Radiation hionitor Failed, Building Radiation Level, and demineralizers ALC-F-1, ALC-K-1 and 2 Loop

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Seal Flow.

Remote indication is pmvided for the area radiation monitors and the air sampler on the radiation monitoring panel located l

adjacent to the cleanup panel.

2.2.2 Ventilation System l

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L 2.2.2.1 Heating Unit and hicisture Separator

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r The moisture separator is instrumented with a differential i

pressure indicator and

switch, ALC-DPI-ll and l

ALC-DPS-II, respectively. The heating unit (ALC-E-HI) is pmvided with a tempemture indicating contmller and a i

high temperature switcl.

The temperature indiceting contmiler functions to maintain the heaters energized pmviding a heater outlet air temperature of no more tien 146 F. If the air temperature rises to 160 F, the high temprature switch will automatically deenergize the heaters. 'if the heaters are to be reenergized, the reset button must be. depressed when air temperature at the thermocouple drops below the 160*F temperature switch setpoint.

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Indication of operation of the temperature indicating I

controller and high temperature switches are pmvided on the switches, bc'th of which are located in the heater control i

panel near the beaters on the filtration unit.

l hianual energizing /deenergizing of the heater control panel occurs at AICC 2-33A.

The heater panel is also j

de-energized automatically should the system ventilation fan trip or in any other way fail to maintain minimum flow at the fan discharge flow switch.

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SD 3526-004 A red light on the heater contmiler panel indicates power available to the heater control panel.

2.2.2.2 Filter Unit Differential pmssure indication is provided for the filter unit's prefilter (ALC-E-F2). While a differential pressure l

l indication (ALC-DPI-l1) is provided locally, a differential pressure switch (ALC-DPS-11) will actuate a mmote

" Trouble" alarm at 1.75" w.g. warning the operator of a l

l restricted flow condition existing in the prefilter. (Note:

The prefilter is replaced when it exhibits a pressure drop of 1.5" w.g.)

Two differential pressure switches (one not connected) and a differential pressure indicator (ALC-DPI-13) are located on the first HEPA filter (ALC-E-F3) in the filter unit for indication and alarm. Switch ALC-DPS-13 wams of a high differential pressure condition by actuating the ventilation unit common " Trouble" alarm at 3" w.g.

The charcoal filter is instrumented with a fire detection system. A prealarm (switch ALC-TSH-15 set at 220*F) actuates a local amber light, a remote high temperature alarm and a horn warning ofincreasing temperature in the charcoal bed. At 325"F, remote common " Trouble" and local red light alarms are actuated fmm switch ALC-TSHH-15 indicating a Hi Hi temperature condition exists in the bed. In addition, ALC-TSHH-15 actuation results in an alarm in the Unit 2 Control Room (Alarm

1. 7BP5, " Chem Cleaning Building (EPICOR) Fire").

Indication of operability of the fire detection system is f

provided by an " Abnormal Detection" white light, located on the filtration unit fire detection panel.

Also provided on the charcoal absorber is a differential pressure indicating contmller (ALC-DPI-14). This is not connected.

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l SD 3526-004 i

The final stage of filtration in the filtration unit occurs in the last HEPA filter (ALC-E-F5). In addition to being provided with local differential pressure indication j

(ALC-DPI-16), the remote " Trouble" alarm is actuated on i

a high HEPA filter differential pressure of 3" w.g. by the locally mounted differential pressure switch (ALC-DPS-16).

2.2.2.3 Fan Assembly The fan assembly, as previously noted, is interlocked with the 60 KW heater. A controlinterlock is provided through the fan and heater circuitry such that the heater may not be energized unless the fan is mnning. A flow indicating switch (ALC-FIS-17) on the discharge of the fan pmvides a safety interlock: if the filtation unit is operating and the discharge flow of the fan falls below 4,000 cfm, the heater r

and fan monitor will trip. Switch ALC-FIS-17 is also tied into the common, remote panel mounted " Trouble" alarm.

The fan is started and stopped from MCC 2-33A.

2.2.2.4 Radiation Monitor (Controls)

Radiation monitor ALC-RMI-18 is energized and deenergized locally at the monitor cabinet. Separate contml switches are provided: one on the unit itself and another for the monitor sample pump. (Note: During operation of the CCB Ventilation System, the radiation monitor must be energized at all times).

A " Power Available" light is provided on the unit.

Imcal indication of the ventilation exhaust particulate and/or gaseous activity level is provided on the monitor. At a radiationlevel of 4.11E-2 Ci particulate or3.81E-4 Ci/cc noble gas the High Radiation alarm will sound on the panel i

in the contml shed.

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3.0 PRINCIPAL MODES OF OPERATION 3.1 Startup 3.1.1 Ventilation System Prior to startup of this unit, the manual dampers ALC-E-DI and D2 am checked open and the radiation monitor is energized and opemtional.

When the fan is started (at MCC 2-33A), sufficient air flow will exist (approximately 4000 cfm minimum) thmugh the unit prior to energizing the heaters. After stanup, ventilation unit temperatum, flow, and i

activity indications are verified normal before the unit is left unattended. The system is normally operated at 7000 - 9000 cfm to i

ensure the CCB is maintained under negative pressure.

3.1.2 Cleanup System l

i Initial stanup of the EPICOR II System is with the deminerahzers empty of liquid. The CCB Ventilation System shall be in operation prior to operating the EPICOR II System.

Normal stanup of the EPICOR II System is accomplished by supplying the system with the process feedwater fmm CC-T-1, CC-T-2, or the various source tanks. Except for the MWHT, the pmcess feedwater is delivered to the process stream by the source tank's pumping system.

If MWHT is the feedwater source, the suppiy header is primed initially.

Depending on the source of the process feed, the feed supply valve (e.g., ALC-V043 or ALC-V242) is then opened and pmcess pump ALC-P-1 staned.

Stanup of pump ALC-P-1 is accomplished by opening the air supply valve ALC-V0ll, stop valve ALC-V185 and control valve ALC-V260; the latter is used to control the pump speed.

The water drawn from the feedwater supply header by pump ALC-P-1 is pumped to demineralizer ALC-F-1. When demineralizer ALC-F-1 is full, pump ALC-P-1 will stop automatically on high level. Similarly, pmcess pump ALC-P-2 is operated until demineralizer ALC-K-1 is full, then pump ALC-P-3 is operated until demineralizer Alf-K-2 is full.

As soon as the demineralizers am full, processing is then commenced by staning pump ALC-P-4 and opening discharge valve ALC-V277.

Using the process pumps respective control valves (ALC-V260 through Revision 11

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f SD 3526-004 ALC V263), the pump speed is adjusted to maintain a balanced flow of about 5 to 25 gpm through the demineralizers.

1 NOTE:

Batch quantity and flow rate are calculated / determined by the efficiency of the demineralizer resin charge. Flow rates and batch sizes are adjusted to efficiently pmcess the i

radioactive waste water.

j 3.2 Normal Operation 3.2.1 Ventilation System l

?

During normal operation, the ventilation unit requires little operator action. The unit is periodically checked to ensure that indication is l

opemble and that temperatures, flows and radiation levels are within the normal ranges.

l Increasing differential pressures acmss the moisture separator and i

HEPA filters am an indication that the components are retaining dirt, etc. These components are replaced as required to ensure that flow through the ventilation unit is maximized.

The radiation monitor and recorder are checked periodically and l

f reviewed for evidence of trends indicating that increasing levels of l

activity are being discharged. A trend showing increasing discharge j

activity levels is indicative of carryover from the filter unit and will be treated accordingly.

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1 3.2.2 Cleanup System Once the flow rate is established for the process, the system operates f

automatically by stanting and stopping the pumps (ALC-P-1 through 4) in order to maintain the pmper level in the demineralizers.

Instrumentation is pmvided on the control panel to monitor system i

parameters and to balance the system to minimize pump cycling.

When a desired volume has been reached in CC-T-2, transfer pump ALC-P-5 is started to recirculate at least three tank volumes of water after which a sample is drawn for analysis. Water acceptable for use in the plant will be pumped to the TMI Unit 2 Liquid Waste Disposal

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System, CC-T-1, CO-T-1 A, BWST, or the PWSTs.

Out of specification water may be pumped to CC-T-1 for mprocessing (See Sections 2.1.9 and 2.1.10) or it will be processed directly from CC-T-2

-l under a feed and bleed schem :.

3.3 Shutdown 3.3.1 Ventilation System The purpose of the ventilation system is to ensure that all air leaving the CCB is filtered and monitored for radiation. Shutdown of the ventilation system will preclude filtration and monitoring of the air and I

will not be performed unless dictated by other casualty / operational considerations. To shutdown the ventilation unit, the 60 KW heaters, fan (ALC-E-1) and radiation monitor are de-energized from their respective breakers in MCC 2-33A.

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3.3.2 Clecnup System i

The system is shutdown and flow through the process system stopped by closing the air supply valves to pumps ALC-P-1 through 4.

To j

shutdown the system upon completion of processing a batch, the pumps i

are secured and the liquid supply valve ALC-V043 or ALC-V086 is closed. Valves ALC-V242 and ALC-V255 close automatically as -

power is shutdown. Valve ALC-V277 is closed to prevent syphoning of the third demineralizer to CC-T-2.

s The system is shut down and the affected unit replaced when radiation monitors on any of the demineralizers or system sampling indicate the l

unit has collected a quantity of material which is limited by shipping regulations, or that the resins are exhausted chemically. To replace one l

of the units, the liner is emptied of water, the three hoses, the level probe cable and the bubbler unit disconnected from the liner, and the remotely-operated hoist used to transport the demineralizer to the outside of the CCB to the transfer cask. The replacement unit is then installed, the hoses, the level probe cable and the bubbler line reconnected and the system started as described in Section 3.1. Each liner has its own level probe which is discarded with the liner.

(NOTE: Polyethylene HICs do not have operable conductivity-type level probes.)

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3.4 Special or Infrequent Operation 3.4.1 Filter Change-out When a filter bank require.; changing, the EPICOR II System will be shutdown. The ventilation system will be shutdown during the filter j

change-out.

i 3.4.2 HIC /Demineralizer Dewatering and Drying i

The Zeolite Resin Drying System dries process media (i.e., zeolite l

resin, activated carbon and/or sand) in a 50 cu. ft. stainless steel i

IUC/demineralizer for transportation and disposal at a low level waste disposal facility.

This is accomplished in a three (3) step pmcess. First, the bulk of the free water is mmoved using procedures associated with IEC removal at the EPICOR II System. Second, the drying unit's sandpiper is started and its blower is energized to meirculate air down through the media. The air is heated as it passes through the blower and as this I

warm dry air passes through the media it entmins and vaporizes moisture. This warm air then passes through the entrainment separator, i

enroute to the blower inlet, where refrigeration coils condense the water vapor in the air snd any entrained water is mmoved. Water is removed from the entrainment separator using the dewatering pump. Air is circulated down through the media for four (4) hours. Finally, the drying process shifts from downflow to upflow. This is done in onier to have the driest media at the bottom of the container where they can best absorb any water generated through condensation as the container cools during stomge and shipment. Air is circulated up thmugh zeolite i

resin for 12 hours1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br /> or, in the case of activated carbon, for 20 hours2.314815e-4 days <br />0.00556 hours <br />3.306878e-5 weeks <br />7.61e-6 months <br />. At this point, the relative humidity of the air stream leaving the container should be at or below the required value, indicating that the media is dry. The system is then shut down and the container is ready to be sealed and shipped.

The dewatering pump (sandpiper) not only removes entrained water r

imm the separator tank but, for the most part, maintains the process under a vacuum thereby minimizing the potential spread of l

contamination due to hose / connection leaks. The excess air removed

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SD 3526-004 by the dewatering pump is directed thmugh a filtered drain path / container approved by Radiological Controls personnel.

The drying system is a skid mounted unit. The services required for drying operations am 480 VAC (standard 4 pole welding receptacle),

100 psi service air and deminemlized water or processed water needed to fill and flush the system. Polyethylene HICs are not dried using the Zeolite Resin Drying System.

Rather, they are dewatered using approved procedures to meet the dewatering criteria for their burial.

3.4.3 Remote Closum Device The remote closure device is designed to provide a safe and efficient means of sealing an EPICOR II stainless steel HIC /demineralizer to meet the requirements for disposal at a low level waste disposal facility.

Performing this operation (installing the ENVIROALLOY lid) to a HIC /demineralizer is done remotely in order to minimize exposure of operating personnel to ionizing radiation. This is accomplished by means of a hydraulic skid.

Aligning the closure head with the HIC /demineralizer is performed using the CCTV cameras and monitor.

Maintaining proper alignment is important so that the eight wedges are driven evenly into their respective holes on top of the HIC /demineralizer. This operation pushes down on the lid and seals the container. Once the container is sealed, it can be removed from service for storage and/or shipment to the burial site.

The Remote Closure Device is not used on polyethylene HICs.

3.5 Emergency 3.5.1 Loss of CCB Ventilation System On loss of the CCB Ventilation System, the EPICOR II System will be shutdown.

3.5.2 Loss of Electrical Power On loss of electrical power to the CCB MCC 2-33A, pumps ALC-P-1 through 4 will automatically stop as the solenoid valves on the air Revision 11

SD 3526-004 supply lines fail closed on loss of power. Valves ALC-V043 and V086 l

fail "As Is". Valve ALC-V255 fails closed. Valve ALC-V242 fails closed on loss of power to stop flow from CC-T-1. If flow thmugh the

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system is fmm the MWHT, operator action is required to close valve WDL-V262B. Power will be lost to the CCB Ventilation System -

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60KW heaters, exhaust fan and radiation monitor.

On loss of power to the MCC 2-43 supply, backup air supply and heat

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taces will not be available.

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When electrical power is lost, all automatically controlled equipment will be placed in the manual OFF position. When emergency power is f

available, the system will be restaned.

l 3.5.3 Loss of System Air Loss of system air causes the EPICOR II pumps to stop until the l

Service Air System is retumed to service.

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3.5.4 Fire 3.5.4.1 Ventilation System

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The charcoal absorber beds in the ventilation unit ignite upon high temperatum. Upon verification ofignition of the l

charcoal bed, the manually actuated fire protection sprays l

will be cut in.

j 3.5.4.2 Cleanup System i

If a fire occurs in the TV Monitor and Control Building the l

sprinkler system will automatically initiate. The CCB is pmvided with a hose station on the mezzanine for manual i

firefighting.

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SD 3526-004 I

4.0 HAZARDS AND PRECAUTIONS Since the system is handling radioactivity contaminated fluids, all appropriate health physics precautions will be observed during operation and maintenance. Under no circumstances will discharges be made to the environment without proper authorization.

i The CCB Ventilation System will process potentially contaminated air. As such, any operations or maintenance associated with the system will fully incorpomte appropriate Radiological Controls Depanment guidelines / requirements. Any solid or liquid ventilation system waste will be sampled and cleared by Rad Con before release to the environment.

Positive verification of a charcoal bed fire will exist before manual initiation of fire i

protection spray system since water will damage the charcoal bed.

Flushing connections are provided at various locations in the system and provide a means for reducing the radiation levels in the piping.

Flushing will be exercised when maintenance is performed.

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TABLE 1 l

EPICOR II PUMPS i

Pump Details i

Identification ALC-P-1, 2, 3, 4 l

t Number Installed 4

l Manufacturer Warren Rupp Co.

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Model No.

SA 2-A i

Type Double opposed diaphragm I

Maximum rated capacity at 90 psi air supply 120 gpm at 45 ft of head Operadng point capacity at 90 psi air supply 20 gpm at 170 ft of head i

Max. air pressum 125 psi j

Lubricant Oil t

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TABLE 2 i

TRANSFER PUhfP l

i Pumn Details 5

Identification ALC-P-5 Number Installed 1

I hianufacturer Ingersoll Rand i

hiodel No.

3 x 2 x 10 Type HOC 2, l

l Group 2, ANSI A60 Type Horizontal Centrifugal Standard hiaterial Designation Col. DI Rated Speed 1750 rpm Rated Capacity 200 gpm i

Rated Total Dynamic Head 100' Shutoff Head 121' Design Pressure, Casing 200 psig Design Temperatum Il0'C Lubricant SAE 20 or 30 Oil Impeller Dia.

10.0" installed; 10.75" max.

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i biotor Details i

l hianufacturer Allis-Chalmers l

Type RGZ l

Enclosure TEFC i

Rated Horsepower 10 HP Speed 1750 rpm l

Lubricant / Coolant Grease / air l

Power Requirements 480V AC/13A,3 Phase, 60 Hz Power Source h1CC 2-33A

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i TABLE 3 l

i PUMPS ALC-P-9 and ALC-P-10 f

E Pump Details f

Identification ALC-P-9/ALC-P-10 I

Number Installed 2

Manufacturer Price Pump Company i

Model Number HP-75-150B

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Type Single Stage Close Coupled i

Centrifugal Rated Speed 3600 rpm (nominal) f Rated Capacity 7 gpm i

Rated TDH 148' Shutoff Head 165' l

Motor Details Manufacturer Baldor Type Induction Enclosure ODP Rated Horsepower 1-1/2 HP Speed 3450 rpm Insulation Class B

Service Continuous Service Factor 1.3 Lubricant / Coolant Grease / Air Power Requirements 120 volt, single phase, 60 Hz f

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SD 3526-004 TABLE 4 RECIRCULATION PUMP ALC-P-II Pump Details Identification ALC-P-11 Number Installed I

f Manufacturer Duriron Company, Inc.

Model No.

Durco Mark II (1.5" x 1" x 4-7/8" impeller)

Type Self-priming, recessed impeller Standard Material Designation 316 Stainless i

Rated Speed 3500 rpm Rated Capacity 50 gpm t

Rated Total Dynamic Head 65 ft l

Shutoff Head 100 ft t

Design Pressure, Casing 275 psig Design Temperature 100*F j

Lubricant Modified stuffing box w/

packing F

Motor Details Manufacturer U.S. Electrical Motors Rated Horsepower 3 HP i

Speed 3490 rpm Lubricant / Coolant Grease / Air Power Requirements 230/460V, 3 Phase, 8.2/4.1 3

amps Frame 145 T i

ID No.

F-4606-02-750 i

Coupling T.B. Woods Model SC4J Shaft End Bearing 6205-22-J/C3 Opp. End Bearing 6203-22-J/C3 l

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f TABLE 5 FILTERS Resin Filters (Traps)

Details f

Identification ALC-F-4A, B, C Number Installed 3

Manufacturer GPUN Installation Horizontal Outside diameter and height Approx.10" x 28" l

Shell material PVC

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Design pressure 100 psig Screening 100 Mesh, Stainless i

Identification ALC-F-6

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Number Installed I

Manufacturer FSI Filter Specialists, Inc.

l Installation Vertical Basket Type Strainer i

Orig. P.O.#

065333 Model #

FSI #FSP-35 Filter Bag 150 Micron Nylon Monofilament FSI P/N-l NM0150P4P-A l

Crud Filters Identification ALC-F-5 Number Installed 1

i Manufacturer of Housing Pall Trinity Micro Corp.

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Installation Vertical Outside diameter and height 7" x 34" Shell thickness 0.165" Shell material -

SA-312 TP304

- Design pressure, temperature 150 psi @ 180*F Particle size rating 1 micron, nominal up to 1

10 micron, nominal

-)

Model No.

5EHD-10702-261US48 National Board No.

22223 Year 1979 j

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SD 3526-004 TABLE 6 DEMINERALIZERS Tank Details Identification Alf-F-1, Alf-K-1, Alf-K-2 Number Installed 3 (typically)

Manufactumr (Various)

Installation Vertical i

Outside diameter and height 4'x4' or 6'x6' Shell thickness 1/4" Shell material Carbon Steel Design pmssure 2 psi M

Identification ALC-F-1 (HIC)

Number Installed 1 (typically)

Manufactumr Nuclear Packaging Inc.

Installation Vertical Outside diameter and height 4'0" x 4'3" Shell thickness 3/8" Shell material Ferralium (ASTM A240 UNS Desig S-32550)

Design pressure 10 psi M

Identification ALC-K-1 (Polyethylene HIC)

Number Installed 1 (typically)

Manufacturer SEG Corporation Insts'lation Vertical Outside diameter and height 6' x 6' (Radiok-179)

Shell thickness 0.57" minimum Shell material Cross-linked polyethylene Design pmssure 5 ft. H O (while in senice 2

at EPICOR) Revision 11

i SD 3526-004 TABLE 7 MISCFI I ANEOUS WASTE HOLD-UP TANK

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Tank Details I

i Identification WDL-T-2 j

e Manufacturer Richmond Engineering Co. Inc.

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Capacity 19,518 gal.

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Installation Horizontal

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Outside diameter and length 10'-91/4";32'-45/8" i

Shell material SA-240,304 S/S Shell thickness 3/8" Design temperature 150*F Design pressure 20 psig Corrosion allowanca 0"

l Design code 1968 ASME, Sec. III, Class 3 Code stamp required ASME Code l

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TABLE 8 l

1 CLEAN WATER RECEIVING TANK

• i i

l Tank Details Identification CC-T-2 i

i Number Installed 1

E Manufacturer Chicago Bridge & Iron Co.

Capacity 133,689 gal.

l Installation Vertical Outside diameter and height 25'; 35' Shell material 304 Stainless Steel Shell thickness 3/16" to 3/8" Design pressure Atmospheric j

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Corrosion allowance 0"

i Code stamp required No I

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Formerly designated the Rinse Hold Tank for Once-Through-Steam-Generator (OTSG)

Chemical Cleaning System

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i TABLE 9

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OFF-SPEC. WATER RECEIVING / BATCH TANK

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Tank Details j

Identification CC-T-1 I

Number Installed 1

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Manufacturer Chicago Bridge & Imn Co.

j Capacity 85,978 gal.

Installation Vertical i

i Outside diameter and height 21'-10"; 39'-0" l

P Shell material 304 Stainless Steel

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Shell thickness 13/32" to 11/16" i

Design temperature 250*F 4

Design pressure Full vacuum to 75 psig Cormsion allowance 0"

i Code stamp required Yes i

I Formerly designated the Chemical Cleaning Solution Tank for the OTSG Chemical Cleaning System l

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T TABLE 10 AI.C-T-3 l

Tank Details f

Identification ALC-T-3 Manufacturer B&G Machine, Co., Inc.

Capacity 100 gallons Installation Vertical Shell Material 304 S.S. (ASTM A240-87)

Outside Diameter and Height 30"/53" Design Temperature 212*F Design Pressure Atmospheric L

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TABLE 11 l

I SUMP PUMP CHEMICAL CLEANING BUILDING Pumo Detail l

J Identification CC-P-2A Number Installed 1

Manufacturer Gould i

Model No.

3171 i

Type Venical l

Rated speed 3600 rpm l

Rated capacity 100 gpm i

Rated total head 250' Min. Submergence required l'

i Design pressure, casing 150 psig d

Design temperature 450*F Lubricant Water Motor Details i

i Manufacturer General Electnc Type Vertical Induction Enclosure TEFC Rated Horsepower 20 HP Speed 3600 rpm Lubricant / Coolant Grease / Air Power Require-ments 480V AC,3 Phase,60 Hz Power Source MCC 2-33A i

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SD 3526-004 TABLE 12 MONORAIL HOIST SYSTEM Number Installed 1

1 Manufacturer Harnischfeger, Inc., P&H Model

1. 36CS23E Capacity 20 ton Total Lift 25'-6" Speed Hoist 20 fpm maximum (90% load) 10 fpm medium 5 fpm low I fpm creep Trolley 50 fpm Contml Hoist Quad - Speed I

Trolley Single Speed Power Supply 460 V AC,3 Phase,60 Hz MCC 2-33A Control Voltage 110 V AC Control Station Imcal and Remote six pushbutton l

pendant control; deadman type' l

element contml Reeving Four part single reeved l Revision 1I r

i SD 3526-004 TABLE 13 i

i CHEMICAL CLEANING BUILDING VENTILATION SYSTEM NAMEPLATE DATA MSA Filter Unit Identification No. ALC-E-HI i

60KW Chromalox Heater Unit 480 volts AC,3 Phase,60 Hz Cat. Number SCCP-080-3480 l

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Type J 0-800 F Temperature Controller Type J 0-800*F High Limit with Manual Reset 6

Intemal Industrial Fan t

l Identification No. ALC-E-1 i

8000 cfm Fan Unit l

30 HP i

l 460 volts AC,3 Phase,60 Hz U

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ID Number P28G353G-G7-XD j

Eberline Ping - 2A Off Line Effluent Monitor 3 Channel Readout - gaseous, paniculate, iodine 110 voks AC,1 Phase,60 Hz j

Self contained sample / return pump (4 cfm)

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i TABLE 14 3526-004 AUXILI ARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPICOR 11)

VALVE LIST DESIGN PRESSURE /

SI8E MANUFACTURER /

TEMPERATURE VALVE NO.

(in.)

HEE DESCPIPTION PO NO.

MODEL fusio / 'F1 COMMENTS ALC-V0001 3/4 GLOBE-6000-SW-40S Process Suetion 68817 LADDtSH 150/120 Line Vent CAT.9 7661-2407-07A ALC-V0002 3/4 GLOBE-6000-SW-405 Process suction 68817 LADDISH 150/120 Line Vent CAT.9 7661 2407-07A ALC-Y0003 3/4 GLOBE-6009-SW-405 Process Suetion MANCCCK 150/120 Line Prima and CAT.# 5500W-1 Fill Velve ALC-V0004 1

GLOBE-6000-SW-405 Chemical Addition HANCOCK 150/120 Line for CC-T-1 CAT.8 5500W-1 ALC-V00C5 2

GLOBE-6009-SW-403 Discharge Line HANCOCK 150/120 From CC-T '

CAT.t 5500W-1 ALC-V0006 2

GATE-6009-SW-405 Clean Water Dis-ALOYC0 150/120 charge Line to FIG.8 110 Units 1 & 2 i

ALC-V0007 2

GATE-6005-SW-405 Truck Fill ALOYC0 150/120 Connection FIG.9 110 ALC-V0008 2

GATE-6008-SW-40S Truck Fill ALOTCO 150/120 Connection FIG.0 110 ALC-V9009 3/4 GLOBE-6005-SW-40 Service Air to HANCOCK 150/120

.ALC-P-2 CAT.9 5500W-1 ALC-V0010 3/4 GLOBE-6005-SW-40 Service Air to HANCoCK 150/120 ALC-P-1 CAT.9 5500W-1 ALC-V0011 3/4 GLOBE-6004-SW-40 Oiled Air to HANCoCK 150/120 ALC-P-1 CAT.9 5500W-1 ALC-V9012 3/4 GLOBE-6009-SW-40 Servlee Air to HANCOCK 150/120 ALC-P-1 CAT.9 5500W-1 ALC-V0013 3/4 GLOBE-6000-SW-405 Demsn. Water to 68817 LADDISH 150/120 ALC-P-4 CAT.9 7661=

2407-07A ALC-v0014 3/4 GLOBE-6005-SW-405 Demin. Water to 68817 LADDISH 150/120 ALC-P-4 CAT.0 7661 2407-07A ALC-V0015 3/4 GLOBE-6008-SW-40S Demin. Water to 69001 OBERT 150/120 ALC-P-3 TYPEf 103 -- ~,...,...,. - - -.

....,..._....,.____.,..._.,-......-_...._..m.

-.,....-,,......-.,.m.

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

-==

4 TABLE 14 3526-004 AUXILIARY BUILDING EMERGENCY LIQUID CL!,ANUP SYSTEM (EPICOR II)

VALVE LIST DESIGN PRESSURE /

SISE MANUFACTURER /

TEMPERATURE VALVE NO.

(in.)

M DESCPIPTION PO NO, MODEL fosig / 'F)

COMMENTS ALC-Y9016 3/4 GLOBE-6009-SW-40S Demin. Water to 69001 CBERT 150/120 ALC-P-3 TYPES 103 ALC-V0017 3/4 GLOBE-6005-SW-40S Demin. Water to 69001 08ERT 150/120 ALC-P-2 TYPEt 103 ALC-Y0018 3/4 GLOBE-6000-SW-403

- Demin. Water to 69001 OBERT 150/120 ALC-P-2 TYPE 9 103 ALC-v0019 3/4-GLOBE-6005-SW-405 Demin. Water to 69001 CBERT 150/120 I

ALC-P-1 TYPEf 103 ALC-V0020 3/4 GLOBE-6009-SW-40S Process Line Flush 69001 OBERT 150/120 Connection TYPES 103 ALC-V0021 3/4 GLOBE-6009-SW-40 Service Air to BANCOCK 150/120 ALC-P-4 CAT.9 5500W-1

. ALC-V0022 3/4 GLOBE-6009-SW-40 Oiled Air to RANCOCK 150#120 ALC-P-4 CAT.8 5500W-1 ALC-V0023 3/4 GLOBE-6000-SW-40 Service Air to BANCCCK 150/120 ALC-P-4 CAT.8 5500W-1 ALC-V0024 3/4-GLOBE-6000-SW-40 Service Air to BANCOCK 150/120 ALC-P-3 CAT.9 5500W-1 l

ALC-V0025 3/4 GLOBE-6000-SW-40 Oiled Air to HANCOCK 150/120 ALC-P-3 CAT.9 5500W-1 ALC-V0026 3/4 GLOBE-6005-SW-40 Service Air to HANCOCK 150/120 ALC-P-3 CAT.9 5500W-1 ALC-Y0027 3/4 GLOBE-6004-SW-40 Service Air to BANCOCK 150/120 I

ALC-P-2 CAT.8 5500W-1

'ALC-V0029 3/4 GLOBL-6000-FW-40 Oiled Air to HANCOCK 150/120 ALC-P-2 CAT.t 5500W-1 l

ALC-V0029 3/4 GLOBE-6005-SW-405 Sampled Line From 68917 LADISR 150/120 l

ALC-P-5 CAT,t 7661-2007-07A.

ALC-V0030 3/4 GLOBE-6005-SW-40S Sempled Line From 68917 LADISM 150/120 m

ALC-P-5 CAT.9 7661-l 2407-07A

[

ALC-V0031 3/4 GLOBE-6000-SW-40S Loep Seal Fill 68817 LADISH 150/120 Connection on CAT.9 7661-CC-T-1 2407-07A l

, i' I

l 4

re, e-.

. v...- wo - wd.-

t e w

.e t-m

.~,.5 e re.r v e-w-~.-- w re-we= e-

=es-pr,**-eme.+,.--+eee<w+-,si--

e e-nr-4.-~

w-e, ev - w

-T

+--+-r-en,--

m r

rw-w-+<

w--w-sr -mu--

4

-e en

,--w-w.1.

v e-r-

sw-+-

e-t we e newsew.---m,vesa.~,.c-vw-=-.-r----r

-=

• m.

m.

.m.

4 t

TABLE 14 3526-004 AUXILIARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPICOR II)

VALVE LIST DESIGN PRESSURE /

SilE MANUFACTURER /

TEMPERATVPE VALVE NO.

M M

DESCRIPTICH PO NO.

MODEL 1psic / 'F1 COMMENTS ALC V0032 2

BALCRK-6005-SW-403 Discharge of 69001 OBERT 150/120

(

CC-P-2A TYPE 9 50 ALC-V0033 2

GLOBE-6019-SW-40S Discharge of 69001 OBERT 150/120 ALC-P-5 to CC-T-1 TYPEt 103 ALC-v0034 3/4 GLOBE-6004-SW-40s Pres. Ind. Root 69817 LADISM 150/120 va. On Dischg. of CAT 97661 ALC-P-5 2407-07A ALC-V0035 2

GLOBE-600t*SW-405 Recire. Line From 69001 OBERT 150/120 ALC-P-5 to CC-T-2 TYPEG 103 ALC-Y0036 3

GLOBE-1500-FLCD-40s Suction Line From 69001 NEWC0 150/120 l

CC-T-2 to ALC-P-5 CAT.O 6415R ALC-V0037 2

BALCHK-6005-SW-405 Inlet to CC-T-2 69001 OBERT 150/120 TYPEt 50 ALC-V0038 1/2 GLOBE-CMP FIG Sensin i Line on PARRER FAN-150/120 Control Va.

NIFIN CAT.f-436 ALC-V-109 ALC-v0039 3/4

- GLOBE-600 $-SW-405 Boot Va. For 69001 HANCOCK 150/120 CC-T-2 Level CAT.S 5500W-1 Indicator ALC-V0049 1/2 GLOBE-6009-SW-403

- Root Va On HANCOCK 150/120 l

ALC-P-5 Dischg.

CAT.95500W-1 Flow Transmit i

l ALC-v0041 1/2 GLOBE-6000-SW-40s Root Va. On HANCOCK 150/123 ALC P-5 Dischg.

CAT.9 5500W-1 Flow Transmit ALC-V0042 3/4 GLOBE-6000-SW-40s Loop Seal Fill 68817 LADISH 150/120 Connection on CAT.4 7661-CC-T-2 2407-07A ALC-V0043 2

BALL SW-405 Process Suetion 69000 QUARTROL 150/120 Motor operated.

Line From WDL-T CAT.9 5215530 120 volts

. -2 to ALC-P-1 ALC-V0044 3/4 GLOBE-SW-40 Blowdn. Line From HANCDCK 150/120 Strainer ALC-U-1 CAT.9 5500W-1 ALC-V0045 2

SWGCHK-1509-SW-405 Process System ALOYCO 150/120 Demin. Water Flush supply _,

3 t',ae=s--

4..

--enw

--.e.ew w am me.*+--w%.ve--swe.,-e'-

-w - rv

-e*+

seva-we,-,*-%r+e-w*eme-,.

-weee--me--+er rw-=-v==a,-es.--=-.e.'-w--3meev--=+i-v4-

.,wes, es a+ s-a w w w e 3 -

M---

ein mmw

=.

-.-iww. n e w ww-e e e r-

-r+ e -w-mee=-

• • e--e+-++wew.se *me,,a er uma.--

-w

.m

.m m

m a

}

i a

TABLE 14 3526 104-5 AUXILIAPY BUILDING EMERGENCY L1 QUID CLEANUP SYSTEM (EPICOR 11)

VALVE LIST DESIGN t

PRESSURE /

SIZE MANUFACTURER /

TEMPERATURE i

VALVE No.

fin,1 HPE DESCRIPTION PO NO.

MODEL (Dsis / 'Fl COMMENTS ALC-V0046 2

BALCRK-EW-40S Process System 69001 OBEPT 150/120 Internals oE Valve From CC-T-1 TYPE 050 are Removed ALC.V0047 Deleted ALC-V0048 3/4 CLOBE-S% 40S Demin. Water To 69001 OBERT 150/120 ALC-P-1 TYPE 1103 ALC-v0049 1/2 GLOBE-600$-SW 405 Poot Va. On HANCOCK 150/120 CC T-2 Inlet Flow CAT.tS500W-1 f

Transmit I

ALC-V0050 1/2 GLOBE-6004-BW-40S Root Va. On MANCDCK 150/120 CC-T-2 Inlet Flow CAT.f5500W-1 Transmit ALC-V00$1 Deleted ALC-V00$2 3/4 GLOBE-SW-40S Root Va. On HANCoCK 150/120 CC-T-1 Level CAT.05500W-1 Indicator Line ALC-V0053 2

CLOBE-SW-40S Pecire 7,in*

69001 OBERT 150/120 I

^

From ALC-P-5 to TYPEt 103 CC-T-2 ALC-V0054 2

GLOBE-6005-SW-40S Clean Water ALOYCo 150/120 Discharge to Units FIG.9 110 i

1 & 2 ALC-V0055 2

GLOBE-6005-SW-40S Inlet Line From HANCOCK 150/120 CC-T-2 to ALC-F-2 CAT.9 5500W-1 ALC-V0056 2

GLOPE-6004-SW-405 Future Kenon Hold-

- BANCOCK 150/120 Up connect. On CAT.9 5500W-1 CC-T-2 ALC-V0057 2

GLOBE-6005-SW-40S Inlete Line From HANCoCK 150/120 CC-T-1 to ALC-F 3 CAT. S 5500W-1 ALC-V0058 2

GLOBE-6009-SW-40 Service Air.pdr./

HENRY VOGT 150/120 Unit 92 1 solation

. DWG, f Va.

E-44248-RG ALC V0059 2

BALCHK-6000-SW-40S Process Sys.

69001 OVERT 150/120 Suction Line TYPE #50 ALC-V0060 1

POPCHK-SCRD-40$

Service Air Supply 68819 NUPRO 150/120 to ALC-P-1 CAT.0 B-16C4-1 w%-

u

<.-ww i w w.e-w

- e ww -r -

.s-wv=.

..wmi wrr.

", wem.- r-w, c -e w w ev -rm-v = m - ~ wv e me w-wav e

+ w w w.wwe--+i-,-+=

++-ee e w ve,- twwown* e e,-+w--en te > -w e= v +

w rwer--w ww w e

• -*w--vewww-r---

~

~

TABLE 14 3526-004 AUEILIARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPICOR II)

VALVE LIST DESIGN PRESSURE /

2 S18E MANUPACTURER/

TEMPERATURE V

(in.)

TJfPJ DESCRIPTION PO No.

MODEL 10s11 / *P1 COMMENTS gVE NO.

e ALC-V0' 41 1

POPCHK-SCRD-403 Demin. Water to 68819 NUPRO 150/120 to ALC-P-1 CAT.9 B-16C4-1

.ALC-V0062 1

POPCHK-SCRD-40 Oiled Air to 68819 NUPPO 150/120 ALC-P-1 CAT.t B-16C4-1 i

ALC-V0063 1

POPCHK-SCRD-40 Service Air to 68819 NUPPO 150/120 ALC-P-1 CAT 0 B-16C4-1 ALC-V0064 1

POPCHK-SCRD-40 Demin. Water to 68819 NUPPO 150/120 ALC-P-1 CAT.9 B-16C4-1 ALC-V0065 1

POPCHK-SCRD-40 Demin. Water to 68819 NUPPO 150/120 ALC-P-2 CAT.9 B-16C4-1 ALC-V0066 1

POPCHK-SCRD-403 Service Air to 68819 NUPRO 150/120 ALC "-2 CAT.8 B-16C4-1 ALC-V0067 1

POPCHK-SCRD-40 Oiled Air to 68819 NUPRO 150/120 ALC-P-2 CAT.# B-16C4-1 ALC-V0068 1

POPCHK-SCRD-40S Demin. Water To 68819 NUPRO 150/120 ALC-P-2 CAT.i B-16C4-1 ALC-V0069 1

POPCHK-SCRD-40s service Air To 68819 NUPRO 150/120 ALC-P-2 CAT.9 B-16C4-1 ALC-V0070 1

POPCSK-SCRD-40S Demin. Water To 68819 NUPRO 150/120 ALC-P-3 CAT O B-16C4-1 ALC-YOO71 1

POPCHK-SCRD-40 Service Air To 68819 NUPRO 150/120 ALC+P-3 CAT.O B-16C4-1 ALC-V0072 1

POPCHK-SCRD-40S Oiled Air To 68819 NUPRO 150/12t ALC-P-3 CAT.8 B-16C4-1 ALC-V0073 1

POPCHK-SCRD-40S Demin. Water To 68819 NUPRO 150/120 ALC-P-3 CAT.9 B-16C4-1 ALC-V0074 1

POPCHK-SCRD-40S Service Air To 68819 NUPRO 150/120 ALC-P-3 CAT.5 B-16C4-1 ALC-V0075 1

POPCHK-SQRD-40S Demin. Water To 68819 NUPRO 150/120 ALC-P CAT.S B-16C4-1 ALC-V0076 1

POPCHK-SCRD-40S service Air To 68819 NUPRO 150/120 ALC-P-4 CAT.5 B-16C4-1 ALC-V0077 1

POPCHK-SCRD-40S Diled Air To 68819 NUPRO 150/120 ALC-P-4 CAT.9 B-16C4-1... _ -. _ ~.,.., -,,.., _, _., _.

_-._....-.-.-%.-...~._~._._,.

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

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

m.

m.

6 TABLE 14 3526-004 AUXILIARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPICOR II)

VALVE LIST DESIGN PRESSURE /

SIBE MANUFACTURER /

TEMPERATURE VALVE NO.

M T

DESCRIPTION PO NO.

MODEL fesig / *F1 COMMENTS E

ALC-V0078 1

POPCHK-SCRD-40S Demin. Water To 68819 NUPRO 150/120 ALC-P-4 CAT.9 B-16C4-1 ALC-v0079 1

POPCHK-SCRD-40S

'ervice Air To 68819 NUPRO 150/120

" -P-4 CAT.9 B-16C4-1 ALC-V0080 3/4 GLOBE-6004-SW-40 Root Va. for Pres.

HANCoCK 150/120 Ind. on Demin.

CAT.9 5500W-1 Water Feeder ALC-V0081 3/4 GLOBE-600f-SW-40 Root Va. for Pres.

HENRY VoGT 150/120 Ind, on Service DWG.9 Air Reader E-44244-R7 ALC-V0082 2

GLOBE-SW-40S Future Xenon HANCoCK 150/120 Roldup Connect.

CAT.9 5500W-1 On CC-T-1 ALC-V0083 1 1/4 BALL-SW-40S Root VA. for 68875 ATOLLO 150/120 Conductivity Probe CAT.9 316 on CC-T-2 Inlet ALC-V0084 1 1/4 BALL-SW-403 Root VA. for 68875 APOLLO 150/120 pH Probe On CAT.9 316 CC-T-2 Inlet ALC-V0085 Deleted r

ALC-V0086 2

BALL-SW-40S Discharge from 80322 QUARTROL 150/120 Motor operated.

Tank CC-T-1 CAT.8521SSSO 120 Volts ALC-V0087 1 1/2 BALL-SW-405 Clean Water Dis 80792 QUARTROL 150/120 Motor Operated.

Charge to Unit $2 CAT.8 5218530 120 Volts l

Cond. Test Tks.

WDL-T-9A & B J

ALC-V0088 1 1/2 BALL-SW-40s clean Water Die 80792 QUARTROL 150/120 Motor operated.

Charge to Unit 42 CAT.9 5215530 120 Volts Cond. Test Tks.

WDL-T-9A & B-ALC V0089 2

GLOBE-6000-SW-40s Discharge Line HANCOCK 150/120 From Sump Pu.mp CAT 0 55004-1 CC-P-2A ALC-V0090 Deleted

-60 u < w

,r w e ns--* ** = w em e~s ww

--w--

r+.,-.,.u-

.m

. m *- se-e,w e+w-,m

-*+e ea'w--

r

=

+--e m e+ + m eme t, e- + e-w-es e e- - ~.e e

% ~ w -

• er-*=*-,m=r,e=

em=-w+*

we=-=rw-*.-

--w*we-

-.-=---<=e-v--7 e we--

---.-= -. - - - - = = - -

A.

1 4

e TABLE 14 3526-004 AUKILIARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPICOR II)

VALVE LIST DESIGN PRESSURE /

SISE NANUFACTURER/

TENPERATURE VALVE No.

(in,)

LYIE DESCRIPTION PO NO.

MODEL tosie / 'F)

COMMENTS ALC-V0091 1 1/4 BALL-SW-40s Root Valve for 68875 APOLLO 150/120 cond Probe at CAT.4 316 i

Inlet to Pump ALC-P-1 ALC-v0092 1 1/4 BALL-SW-40s Root valve for 68875 APOLLO 150/120 cond Probe at CAT.8 316 Inlet to Pump ALC-P-3 ALC-v0093 1 1/4 BALL-SW-405 Root Valve for 68875 Apollo 150/120 cond Probe at CAT.O 316 Inlet to Pump

-ALC-P-3 ALC-V0094 3/4 GLOBE 6005-$W-403 Root Valve for 69001 OBERT 150/120 Pres. Ind. On TYPE 9 103 Sump Pump CC-P-2A Discharge ALC-Y0095 2

GLOBE 6000-SW-40S Process System HANCOCK 150/120 Flush Line Near CAT.I 5500W-1 Inlet to ALC-P-1 l

ALC-YOO96 Deleted ALC-v0097 3/4 GLOBE-6004-SW-40 Oiled Air to RANCOCK 150/120 ALC-P-6 CAT.9 5500W-1 ALC-V0098 3/4 GLOBE-6009-SW-40s Demin. Water to VELAN 150/120 ALC-P-6 CAT.5 374B ALC-v0097 3/4 GLOBE-6005-SW-40 Service Air to RANCOCK 150/120 ALC-P-6 CAT. t 5500W-1 i

ALC-V0100 3/4 GLOBE-6004-SW-40 Service Air to BENRY VOGT 150/120 ALC-P-6 DWG.8 l

E-44244-R11 ALC-V0101 3/4 GLOBE *600f-SW-405 Demin. Water to 69001 OBERT 150/120 ALC-P-6 TYPEI 103 ALC-Y0102 1-PCPCHK SCRD-40' Oiled Air to 68919 NUPRO 150/120 ALC-P-6 CAT.5 B-16C4-1 l

l ALC-Y0103 1

BALCR8-6005-SW-40S Filter ALC-F-1 69001 CBERT 150/120 Precoat Supply TYPE 9 50 j

.Line ALC-Y0104' 1

POPCBK-SCRD-40 Service Air'to 68819 NUPRO 150/120 ALC-P-6 CAT.9 B-16C4-1 l t

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

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

... ~.. m........-

m.m.

l l

l

}

TABLE le 3526-004 AUKILI ARY BUILDING EMERGENCY LIQUID CLEANUP l

SYSTEM ( EPICOR II) t VALVE LIST DESIGN FRESSUDE/

S18E MANUFACTURER /

TEMPERATURE i

VALVE NO.

( in,,)

M DESCRIPTION PC NO.

MODEL fosic / 'F)

COMMENTS

[

[

ALC-V0105 Deleted I

ALC-V0106 2

GLOBE-6004-SW-40S Discharge From HANCOCK 150/120 one Micron Filter CAT.6 5500W-1 ALC-VO107 3/4 GLOBE-6009-SW-40s vent en one Micron HANCOC K 150/120 Filter CAT.9 $500W-1 ALC-V0109 3/4 GLOBE-6009-SW-403 Drain on One HANCOCK 150/120 Micron Filter CAT.I $500W-1 ALC-V0109 2

CONTRCL-FLGD-40 Service Air Supply 69005 F1 SHER 150/120 Header TYPE 8 310-32 ALC-V0110 3

GLOBE-FLCD-40$

Suetion Lire From 69001 NEWC0 150/120 CC-T-1 t o ALC-P-5 CAT.9 6415R ALC-V0111 Deleted t

ALC-V0112 2

GLOBE-6005-SW-40S Inlet to One HANCOCK 150/120 Micron Filter CAT.8 5500W-1

+

ALC-V0113 1

POPCHK-SW-40S Chemical Addition 69919 NUFRO 150/120 Line to CC-T-1 CAT.9 B-36C4-1 1

ALC-V0114 2

BALCHK-6000-SW-40$

Discharge From 69001 OBERT 150/120 ALC-P-5 TYFEt 50 ALC-V0115 3/4 GLOBE-SN-40S Drain Line on 150/120 Process Suetion Line ALC-V0116 3/4 GLOBE-SN-405 Drain Line on 150/120 Process Suetion

'Line ALC-V0111 3/4.

GLOBE 6000-SW-40s' Pressure Test HANCOCK 150/120 connection Near CAT.8 5500W-1 d

' Suetion of ALC-P-1 ALC-V0119 No Longer in Use Located in Unit 1

+123

. (Unsecessible)

ALC-V0124 1

GLOBE-6008-SN-403 Filter ALC-r-1 HANCOCK 150/120 Precoat Supply CAT.5 5500W-1 Line ALC-v0125 3/4.

GLOBE-6005-SW-40S' Pressure Test HANCOCK 150/120 Connection On CAT.9 5500W-1 Demin Water Hesder-r a

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

.......ai.

m.- _..,m

._,..m s...-..-..

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

,_,,,.-_,.--.m_.m-.,_,,,,Z

x c

.~

TABLE 14 3526-004 AUKILIARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPICOR II)

VALVE LIST DESIGN PRESSURE /

S18E MANUFACTURER /

TEMPERATURE VALVE NO, (in,1 77 3 DESCRIPTION PO NO.

MODEL (ps11 / *F)

COMMENTS ALC-YO126 3/4 GLOBE-6004-SW-405 Pressure Test HANCOCK 150/120 Connection On CAT.O 5500W-1 Service Air Hender ALC-V0127 3/4 GLOBE-6005-SW-40S Pressure Test RANCOCF 150/120 Connection On CAT.9 5500W-1 Sump Pump Discharge ALC-V0128 3/4 GLOBE-6000-SW-40S Priming Vent 68817 LADISH 150/120 For ALC-P-5 CAT.9 7661-2407 07A ALC V0129 3/4 GLOBE-6005-SW-403 Priming Vent 68817 LADISH 150/120 For ALC-P-5 CAT.9 7661-2407-07A ALC-V0130 3/4 BALCHK-6000-SW-40S Drain on One 69001 OBERT 150/120 Micron Filter TYPE 9 103 ALC-V0131 3/4 BALCHK-6009-SW-40S Drain on Suetion 69001 OBERT 150/120 Line From CC-T-2 TYPE 9 103 to ALC-P-5 ALC-V0132 3/4 GLOBE-6004-SW-405 Drain on Suetion 69001 OBERT 150/120 Line From CC-T-2 TYPES 103 to ALC-P-5 ALC V0133 3/4 GLOBE-6005-SW 405 ALC-DPS-1 LP Leg 69001 OBEPT 150/120 Root valve TYPE 9 103

'ALC-V0134 3/4 GLOBE-6009 SW-405 Demin. Water to HANCOCK 150/120 ALC-P-5 Seals CAT.9 5500W-1 ALC-v0135 1

POPCHK-SCRF-40S Demin. Water to 68819 NUPRO 150/120 ALC-P-5 Seals CAT.I B16C4-1 ALC V0136 3/4 SOLND-SCRD-405 Demin. Water to 92188 ASCO 150/120 2 Way Normally closed ALC-P-5 Seals CAT.9 9210D9 Energized to open ALC-V0137 2

GLOBE-SW-405 Demin. Water to 150/120 Flush Line to CC-T-2 ALC-VS138 2

BALCHK-6004-SW-40S Discharge Line 69001 OBERT 150/120 From CC-P-2A TYPEf 50 ALC-V0139 2

GLOBE-6009 SW-40 Service Air HANCOCK 150/120 Header CAT.9 5500W-1 1 !

.-----.-,J.__,,

- - - _. -., - _ _. - - _. -,.__....- -. _. _..- _.- ---..---.- ~, - --

.4

m _ m m

_ m m

l TA8tE le 3526 004 l

AUXILIARY BUILDING EMERGENCY L1001D CLEANUP l

SYSTEM IEPICOR 11)

VALVE LIST l

DESIGN PRESSURE /

' SIEE MANUFACTURER /

TEMPERATURE VALVE NO.

(in,)

TYPE DESCRIPTION PO NO, MODEL IDsio / *F1 pOMMENTS i

ALC-V0140 2

CLOBE-6000-SW 40S Future waste HANCOCK 150/120 Supply Line CAT. 4 5500W-1 ALC-V0141 2

GLOBE-6000-SW-405 Future Weste HANCoCK 150/120' Supply Line CAT.8 5500W-1 ALC-V0142 2

LIFCHK-SW-40$

Demin. Water VELAN 150/120 Supply Header SERIAL 9 S-50-1 ALC-V0143 1 1/2 REL1EF-SCRD-405 Demin. Water J. E. LONERGAN 150/120 Set Pressure at 150 psig Supply Reader CORP. MODEL LOT 11 1

ALC-V0144 2

_ GLOBE =6005-SW-405 Demin. Water RANCOCK 150/120 Supply Header CAT.4 5500W-1 CC-T-2 ALC.V0145 2

Glob?-600 0 -SW-4 03 Spare Plant Air /

HANCOCK 150/120 EPICOR 11 Air CAT.0 5500W-1 f

Sup. Cale-P-788 Ipslation Va.

t ALC-V0146 1/2 BALL-COM FTG Sample Line 80498 WHITEY 150/120 From ALC-P-2 CAT.4 SS-4558 ALC-V0147 1/2 BALL-CCM FTG Sample Line 80498 WHITEY 150/120 From ALC-P-3 CAT.8 SS-45SS 1

ALC-V0148 1/2 BALL-COM FTG Sample Line 80498 WHITEY 150/120 From ALC-P-4 CAT.8 SS-45S8 ALC-V0149 1/2 GLOBE-COM FTG Grab Sample BOKE 150/120 From ALC-P-2 CAT.9 N281108Y15 ALC-V0150 1/2 GLOBE-COM FTG Grab Sample HOKE 150/120 From ALC-P-3 CAT.4 N2811Q8Y15 ALC-V0151 1/2

- GLOBE-COM FTG Grab Sample soke 150/120 From ALC-P-4 CAT.8

' I N2811Q8Y15 ALC-V0152 1/2 GLOBE COM FTG Grab Sample HOKE 150/120 From ALC-P-5 CAT.9 N281108Y15 ALC-V0153 1

BALL-COM FTG Sample Recire.

80498 WHITEY 150/120 i

Line CAT'.9 SS-65F16 t t

w er--rwr

+,+.--emr,--v,marw,i +m,- w e r wa w w -, ir w mm ww m v e-= w-,a--r-mum

- s w ve -as+-,v w m, w y e ww y-y ww w ww a eg-w=-swwww 4-,ri m,-

++-w w e.

,# e.e e v e.rwv w wwe -v, w w w%

.-4.+s ne z.,+

w erw w.m e i., v

, www we-v -w-e

-m. -. rwis

- w-e-

,,,a..w,,

l TABLE 14 3526-004 AUX 1LIARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPIcom II)

VALVE LIST DESIGN PRESSURE /

SIZE MANUFACTURER /

TEMPERATURE VALVE No.

Iin,)

T_QE DESCRIPTION PO NO.

MODEL fpsla / 'F)

COMMENTS ALC-V0154 1/2 BALL-COM FTC Grab Sample From 80498 WHITEY 150/120 ALC-P-5 CAT.9 SS-4538 ALC-V0155-1/2 BALL-COM FTG Grab sample From 80498 WHITEY 150/120 ALC-P-4 CAT.f SS-45SS ALC-V0156 1/2 BALL-COM FTG Grab Sample From WHITEY 150/120 ALC-P-3 CAT.S SS-4538 ALC-V0157 1/2 BALL-COM FTG Grab Sample From 80498 WHITEY 150/120 ALC-P-2 CAT.8 SS-4558 ALC-V0158 3/4 GLOBE-6005-SW-40S Demin. Water to 68817 LADISH 150/120 Sample sink Spray CAT.9 7661-Header 2407-07A ALC-V0159 3/4 GLOBE-6008-SW-40S Demin. Water to 68817 LADISH 150/120 Sample Bottle CAT.9 7661-Wash Hose 2407-07A ALC-V0160 1/2 LIFCHK-COM FTG Recire. Line From 80498 WHITNEY 150/120 ALC-P CAT.0 55-58S8 ALC-V0161 1/2 LIFCHK-COM FTG Recire. Line From 80498 WHITNEY 150/120 ALC-P-3 CAT.0 5S-5838 ALC-V0162 1/2 LIFCHK-COM FTG Recire. Line From 80498 WHITNEY 150/120

+

ALC-P*4 CAT.9 55-58S8 ALC-v0163 1/2 SOLND SCRD Pecire. Line From 80548 ASCO 150/120 2 Way Normally Closed ALC-P-4 CAT.9 8210C94 Energized to open ALC-Y0164 1/2 SQLND SCRD -

Sample Line From.

80548 ASCO 150/120 2 Way Normally Closed ALC-P-4 CAT.8 8210C94 Energized to Open ALC-v0165 1/2 SOLND SCRD Pecire. Line From 80548 ASCO 150/120 2 May Normally Closed ALC-P-3 CAT.9 8210C94 Energized to Open ALC-v0166 1/2

- SOLND SCRD Sample Line From 80548 ASCO 150/120 2 Way Normally Closed ALC-P-3 CAT.9 8210C94 Energized to Open ALC V0167 1/2

' SOLND SCRD Recire. Line From 80548 ASCO 150/120 2 Way Normally closed ALC-P-2 CAT.f 8210C94 Energized to open 80548 ASCO 150/120 2 Way Normally Closed ALC-V0168 1/2 SOLND SCKD.

Sample Line From ALC-P-2 CAT.4 8210C94 Energized to Open i

ALC-V0169 2

GLOBE-6004-SW-403 Clean Water Dis.

POWEL 150/120 charge to Unit #1 FIG,# 2474

-65

-[

Nwn,

,<-en e-sw - - wn,.~-+~.

ne-+,<-va,-na,,,-..

-n.,we,n,~,-~,-,--an-ra,w....-

- ~... - + +., -,, - ~,

uw

,-,v--.-

v,--

--,-~~rw+,-~,n.,n~+-e

.m,,-~s--

,,,---~a,-..n,,---

A TABLE 14 3526-004 AUXILIARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPICOR II)

VALVE LIST DESIGN PRESSURE /

.SIIE MANUFACTURER /

TEMPER.ATURE VALVE NO.

(in.)

TJPg DESCRIPTION PO No.

MODEL tesie / 'F1 COMMENTS ALC-V0170 2

GLOBE-6000-SW-40s Clean Water Dis-NEWC0 150/120 charge to Unit 92 CAT. 9 287F32 ALC-V0171 3/4

- GLOBE-600 0-SW-405 Clean Water Dis.

68817 LADISH 150/120 charge to Unit St CAT.9 7661 Drain Line 2407-07A ALC-V0172 3/4 GLOBE-SW-40S

. Clean Water Dis-150/120 charge to Unit 92 l.

Vent Line ALC-V0173 3/4 GLOBE-SW-40S Clean Water Dis-150/120 charge to Unit 92 Drain Line ALC-V0174 3/4 GLOBE-6004-SW-408 Cask overflow 68817 LADISH 150/120 Loop Seal Leveling CAT.0 7661-Line 2407-07A ALC-V0175 3/4 GLOBE-6000-SW-40s Cask Overflow 68817 LADISH 150/120 Loop Seal Fill CAT.9 7661-Line 2407-07A ALC-V0176 3/4 GLOBE-6000-SW-40 Oiled Air Line BENRY VCGT 150/120 For ALC-P-6 DWG.O E44244-R11 ALC-V0177 1/2 POPCBK-CCM FTG

. Sample Line From 82033 NUPRO 150/120 ALC-P-2 CAT.9 SS-8C-1/3 ALC-V0178 1/2 POPCHK-COM FTG Sample Line From 82033 NUPRu 150/120 ALC-P-3 CAT.9 SS-8C-1/3 ALC-V0179 1/2 PCPCBR+COM FTG Sample Line From 82033 NUPRO 150/120 ALC-P-4 CAT.8 SS-8C-1/3 ALC V0180 2

BALL SCRD Process Inlet To JAMESBURY Supplied by CAP-GUN Pump ALC-P-1 TYPE 1000 FIG. NO.

11-1100TT ALC-V0181 3/4 BALL SCRD Servlee Air To JAMESBURY Supplied by CAP-GUN Pump ALC-P-1 TYPE 1000 FIG

.MO.

11-1100TT

.. ~. - -

e i

I['

TABLE 14 3$26-004 i

AUXILIARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPICOR 11)

VALVE LIST DFSIGN t

PRESSURE /

S1SE MANUFACTURER /

TEMPERATURE VALVE NO.

lin.)

M DESCRIPTION PO NO.

MODEL tesic / *F1 COMMENTS ALC-V0182

'3/4 BALL SCRD Demin. Water To JAMESBURY Supplied by CAP-GUN Pump ALC-P-1 TYPE 1000 FIC. NO.

11-1100TT ALC-V0183 3/4 BALL SCRD Service Air To JAMESBURY Supplied by CAP-GUN Pump ALC-P-1 TYPE 1000 FIG. NO.

11-1100TT 4

ALC V0184 3/4 BALL SCRD Demin. Water To JAMESBURY Supplied by CAP-GUN Pump ALC-P-1 TYPE 1000 FIG. NO.

11 1100TT ALC-Volts

. 3/4 SOLND SCRD Oiled Air To ASCO.

Supplied by CAP-GUN Pump ALC-P-1 CAT. NO.

8210D95 ALC V0186 3/4 BALL SCRD Oiled Air to JAMESBURY Supplied by CAP-GUN Pump ALC-P-1 TYPE 1000 FIG.. NO.

11-1100TT ALC-V0187 3/4 ANGLE SCRD Oiled Air to NARREN RUPP Supplied by Mfr of Pump ALC-P-1 CO., PART 5 Pump ALC-P-1 (Narren 893-048-162 Rupp)

ALC-V0188 3/4 BALL SCRD Service Air to JAMESBURY Supplied by CAP-GUN Pump ALC-P-1 TYPE 1000 FIG. BO.

11 1100TT ALC-V0189 3/4 BALL SCRD Sample Point vs.

JAMESBURY Supplied by CAP-GUN On Outlet Of Pump TYPE 1000 This Sample Point ALC-P-1 FIG. No.

Not Used 11-1100TT ALC-V0190 3/4 BALL SCRD Demin. Water to JAMESBURY Supplied by CAP GUN Pump ALC-P-1 TYPE 1600

- F1G NO.

11-1100TT ALC-V0191 1

BALL SCRD Process Outlet JAMESBURY-Supplied by CAP-GUN Pump ALC-P TYPE 1000 FIC..NO.

11-1100TT l,

4

,<~ ree

-.,--w e n,,-nn-m,-e v~ < ~ ~, m,w.m ew,m.w w - w me., me m, n w ~., - a e n,e

---

w,m+vew~,w,-

-,.,,-,,w,,-eww-r-ww--.----,------,.,m

,..-,,.n-,ne,,--

w-

.w-,nar-,,,,r,--,,-+,ww.,-,,c,m,v.-,,-

.m m..

m_

m

__m m

i i

TABLE 14 3526-004 AUX 1LIARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPICCR 11)

VALVE LIST I

DESIGN PPESSURE/

SISE MANUFACTURER /

TEMPERATURE I

VALVE NO.

.(it) s )

M DESCPIPTION PO NO.

MODEL ies11 / 'F1 COMMENTS ALC-V0192 3/4 BALL SCRD Service Air to JAMESBURY Supplied by CAP-GUN Pump ALC-P-1 TYPE 1000 FIG. No.

t 11-1100TT ALC-V0193 3/4 BALL SCRD Demin. Water to JAMESBURY Supplied by CAP-GUN Pump ALC-P-1 TYPE 1000 FIG. NO.

4 11-1100TT ALC-V0194 2

BALL SCFD Process Inlet To JAMESBURY Supplied by CAP-GUN Pump ALC-P-2 TYPE 1000 d

FIG. NO.

j 11-1100TT ALC-V0195

. 3/4 BALL SCRD Demin. Neter To JAMESBURY Supplied by CAP-GUN Pump ALC-P-2 TYPE 1000 FIG. No.

11-1100TT ALC-V0196 3/4 BALL SCRD Service Air To JAMESBURY Supplied by CAP-GUN Pump ALC-P-2 TYPE 1000 FIG. No.

11-1100TT i

ALC-V0197 3/4 BALL SCRD service Air To JAMESBURY Supplied by CAP-GUN Pump ALC-P-2 TYPE 1000 FIG. No.

11-1100TT ALC-V0198 J/4 BALL SCRD Service Air To JAMESBURY Supplied by CAP-GUN Pump ALC-P*2 TYPE 1000 FIG. No.

11-1100TT ALC-V0199 3/4 SOLND SCRD' 011ed Air To ASCO Supplied by CAP-GUN Pump ALC-P-2 CAT. NO.

8210D95 ALC-V0200 3/4 ANGLE SCRD oiled Air To NADREM RUPP dopplied by Mfr. of Pump ALC-P-2 Co., PART 9 Pump ALC-P-2 (Narren 893-043-162 Rupp)

ALC-v0201 2

BALL SCRD Process Supply JAMESBURY Supplied by CAP-GUN From Pump ALC-P-2 TYPE 1000 FIG. NO.

11-1100TT

, t

• 2.-_-.mmm.U,.----.-.-*e,._---.4.<%+.U..r.

.w.2-*+-..r--

%=,#w-w.m.-svv-+.

ew-mm-e..,-.,mem**,=.ww*e..

.ns-.--u,+e e.---,,,wm.m..-w.=,wanew<w*

.-w-v-,

-mm--

.m m,

m_

m - -

m.

m..

m m

il TABLE 14 1526-004 AURILIARY BUILDING EMERGENCY LIQUID CLEANUP I

SYSTEM (EPICOR 11)

VALVE LIST DESIGN PRESSURE /

SIZE MANUFACTURER /

TEMPERATURE VALVE No.

fin.)

M DESCRIPTION PO No.

MODEL M ig / 'F)

COMMENTS ALC-V0202 3/4 BALI. SCRD Demin, water To JAMESBURY Supplied by CAP-GUN Puep ALC-P-2 TYPE 1000 FIG. NO.

11-1100TT ALC-V0203 Deleted ALC-V0204 3/4 BALL SCRD Serelee Air To JAMESBURY Supplied by CAP + GUN Pump ALC-P-2 TYPE 1000 FIG. NO.

11-1100TT ALC-v0205 3/4 BALL SCPD Demin. Water To JAMESBURY Supplied by CAP-GUN f

Pump ALC-P-2 TYPE 1000 FIG. No.

11-110077 ALC-V0206 3/4 BALL SCRD Sereice Air To JAMESBURY Supplied by CAP-GUN Pump ALC-P-2 TYPE 1000 TJG. No.

11-1100TT ALC-v0207 2

BALL SCRD Process Supply JAMESBURY Supplied by CAP GUN To ALC-r-1 TYPE 1000 F1G. No.

11-1100TT ALC-V0208 2

BALL SCRD Process Supply JAMESBURY Supplied by CAP-GUN To ALC-r-1 TYPE 1000 FIG. No.

11-1100TT ALC-V0209 2

BALL SCRD Process Supply JAMESBJRY Supplied by CAP-GUN To ALC-K-1 TYPE 1000 FIG. No.

11-1100TT

- ALC-V0210 2

BALL SCRD Process Supply JAMESBURY Supplied by CAP-GUN To ALC-K-1 TYPE 1000 FIG. No.

11-1100TT ALC-V0211 2'

BALL SCRD Process Supply JAMESBURY Supplied by CAP-GUN To ALC-K-2 TYPE 1000 I

FIG. No.

11 1100TT ALC YO212

.2 BALL SCRD Process Supply JAMESBURY Supplied by CAP-GUN To ALC-K-2 TYPE 1000 FIG. No.

11-1100TT l I l

I

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

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

i

i

;!

Li

?'

.i

l.

1 4

0 0

6 2

5 3

n N

N N

N N

N fe N

N N

• N U

U U

U U

U or U

U U

t G

G G

G G

G r

G G.

G G.

.a P

P P

P P

P rW P

P P

P A

A A

A A

A f(

A A

A A

C C

C C

C C

M C

C C

C 3

y y

y y

y y

y-y y

y y

b b

b b

b b

bP b

b b

b S

d d

d d

d d

dC d

d d

d T

e e

e e

e e

eL e

e e

e N

i i

i i

i i

iA i

i i

i E

l l

l l

l l

l

)

l l

l l

M p

p p

p p

p ppp p p

p p

M p

p p

p p

p pm p p p

p p

O u

u u

u u

u uuu u u

u u

C S

S S

S S

S SPR S

S S

S El RP

/U*

ET RA/

NUR GSE1 ISPi SEMs ERED DFTI 5

9 D

/

0 R

1 E

2 P

2 R

8 PS6 UL Y0 T

Y0 T

Y0 T

Y0 T

Y0 T

U 1

Y0 T

Y0 T

Y0.T Y0 T

P TE R0

.T R0

.T R0

.T R0

.T R0

.T RT-R0

.T R0

.T R0 T

R0.T U

CD U0o0 U0O0 U0O0 U0O0 U0O0 O

R8 U0O0 U0O0 U0o0 U0O0 N

AO B1N0 B1N0 B1N0 B1N0 B1N0

.N MA4 B1N0 B1N0 B1N0 B1N0 A

FM S

1 S

1 S

1 S

S 1

EP0 S

1 S

1 S

1 S

1 1

EE

.1 O. R EE 1

EE

.1 EE 1

EE

.1 E

U EE 1

EE

.1 EE 1

EE 1

L N

MPG-MPG-MPG-MPG -

MPG-CT R

3 MPG-MPG-MPG-MPG-C A

AYI1 AYI1 AYI1 AYI1 AYI1 SA AO9 AYI1 AYI1 AYI1 AYI1 M

JTF1 JTF1 JTF1 JTF1 JTF1 AC WC8 JTF1 JTF1 JTF1 JTF1 D

I UQ IL)1 Y1 4

C 1

NRT EOS E

G CI L

IL O.

R P

B E

N 0

EE 7

A M

T E(V O

L P

GMA NEV T

I m

DS LYS I

U B

3 o

o o

o T

o T

o T

o T

Y tr T

T T

R e-r3 3

r3 3

o3 o3 o3 r3 3

r3 A

N lC e-r-

e-r-

T-T-

T-e-

r-e-

I C

nL tP iP tP P

P P

tP iP tP i P.

L 1

IA a-A-

a-A r-r-

r-a-

A-a-

I T

WC C

WC C

iC iC iC WC C

WC K

P sp L

eL

.L eL AL AL AL aA cA

.A L

eL L

U I

sm

.A cA A

cA A

A A

A R

eu n

i n

i d

d d

n i

n C

cP ip vp ip vp ep ep ep ip vp ip S

o mm rm mm rm lm l m lm mm rm mm E

ro eu eu eu eu i u iu l u eu eu eu D

PT DP SP DP SP OP OP OP DP SP DP D

D D

D D

D D

P R

D D

D D

R R

R R

R C

C R

R R

R C

C C

C C

S S

C C

C C

S S

S S

S S

S S

S D

E E

L L

L L

L N

L L

L L

L I

L L

L L

L L

G L

L L

L J

A A

A A

A C

N A

A A

A YT B

B B

B B

S A

B B

B B'

E) 8 n.

4 4

4 4

4 4

4 4

4 4'

1i

/

/

/

/

/

/

/

/

/

/

5t 2

3 3

3 3

3 3

3 3

3 3

3 4

5 6

Y 8

9 0

1 2

3 o.

1 1 '

1 1

1 1

1 2

2 2

2 N

2 2

2 2

2 2

2 2

2 2

2 0

0 0

0 0

0 0

0 0

0 0

E V

V V

V V

V V

V V

V V

V L

C C

C C

C C

C C

C C

C A

L L

L L

L L

L L

L L

L V

A A

A A

A A

A A

A A

A i

l

,-l f

(l!l I

,Illll_

i sm.

. m..

---m..____

__=._...m

..=

,m.

l I

L t

TABLE 14 3526-004 i

AUX 1LIARY BUILDING EMTPGENCY LIQUID CLEANUP SYSTEM (EPICOR 11)

VALVE LIST DESIGN PRESSURE /

SIBE MANUFACTURER /

TEMPERATURE VALVE NC.

(in,1 7_IPE DESCRIPTION PO NO.

MODEL tosia / 'Fl COMMENTS ALC-V0224 3/4 BALL SCRD Sample Point. Va.

JAMESBURY Supplied by CAP GUN en Outlet of Pump TYPE 1000 ALC-P-3 FIG. NO.'

11 1100TT ALC-V0225 3/4 BALL ScRD Servlee Air to JAMESBURY Supplied by CAP-GUN Pump ALC-P-3 TYPE 1000 FIG. NO.

11-1100TT ALC-V0226 2

BALL SCRD Process outlet JAMESBURY Supplied by CAP-GUN From Pump ALC-P-3 TYPE 1000 FIG. NO.

11-1100TT s

ALC-V0227 2~

BALL SCRD Process Inlet J AMESBURY Supplied by CAP-GUN To Pump ALC-P-4 TYPE 1000 FIG. No.

11-1100TT ALC-V0229 3/4 BALL SCRD D* min. Water To JAMESBURY Supplied by CAP-GUN Pump ALC-P-4 TYPE 1000 FIG, NO.

11-1100TT ALC-V0229 3/4 BALL SCRD Service Air To JAMESBURY Supplied by CAP-GUN Pump ALC-P-4 TYPE 1000 FIG. No.

11 1100TT ALC-V0230

'3/4 BALL SCRD Demin. Water To Jr.MESBURY Supplied by CAP-GUN Pump ALC-P-4 TYPE 1000 FIG. No.

11 1100TT ALC-V0231 3/4 BALL SCRD Service Air To JAMESBURY Supplied by CAP-GUN Pump ALC-P-4 TYPE 1000 FIG. No.

I 11-1100TT j

ALC-V0232

'3/4 SOLND SCRD.

Oiled Air To ASCO Supplied by CAP-GUN Pump ALC-P-4 CAT. NO.-

8210D95 i

ALC-V0233 3/4 BALL SCRD Oiled Air To JAMESBURY Suppli.<d by CAP-GUN Pump ALC-P-4 TYPE 1000 FIG. NO.

i.

11 1100TT I i

,--mw_. _ _.

-..--a-,-,

45ein-w-..e.exe-.-*w*+=.--em,.we--=w-,--m.--=-,w+v-=me-uw..

--.r-..

w.%,

• ee---m.-m

..-,a~e...mw.++vw.,,,.,---..-e-

%..... ww e

.w w e

.. -, w w e,-ve-

a

.. =.

.=a c_-=

.--w=.

--~. -.,

TABLE le 3326 004 AUXILIARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPICOR II)

VALVE LIST DESIGN t

PRESSUPE/

j S18E MANUFACTURER /

TEMPERATURE VALVE No..

(in,1 7JPE DESCRIPTION PO NO.

MODEL tesis / *F1 COMMENTS ALC-V0234 3/4 BALL SCRD Oiled Air To NAPPEN PUPP Supplied by Mf r. of Pump ALC-P-4 Co., PART $

pump ALC-P-4 893-049-16 (Warren Rupp)

ALC-V0233 3/4 BALL SCRD Demln. WaterTo JAMESBURY Supplied by CAP-GUN Pump ALC-P-4 TYPE 1000 FIG. NO.

11-1100TT

+

ALC-V0236 3/4 BALL SCRD Seretee Air To JAMESBURY Supplied by CAP-GUN j

Pump ALC-P-4 TYPE 1000 FIG. NO.

11-1100TT ALC V0237 3/4 BEL SCRD Demin. water To JAMESBURY Supplied by CAP-GUN Pump ALC-P-4 TYPE 1000 FIG. NO.

11-1100TT ALC-V0238 3/4 BEL SCPD Sample Point Va.

JAMESBURY Supplied by CAP-GUN on Outlet of Pump TYPE 1000 ALC-P-4 FIG. NO.

11-1100TT ALC-V0239 3/4 BALL SCRD Service Air to JAMESBURY Supplied by CAP-GUN Pump E C-P-4 TYPE 1000 FIG. No.

11-1100TT ALC.VO240 3/4 BEL SCRD Process Outlet JAMESBURY Supplied by CAP-GUN From Pump ALC-P-4 TvrE 1000 FIG. No.

11 1100TT ALC-V0241 3/4 BALL SCRD' Oiled Air To JAMESBURY Supplied by CAP-GUN Pump ALC-P-2 TYPE 1000 FIG. No, 11-1100TT ALC-V0242 2

AIR OPERATED BALL Discharge From BILLS-McCANNA 130/120 2 Nay Normally Closed SCRD-405 Tonk CC-T-1 FIG.

Energised To Open S302-56-T-S6 ALC-V0243-DELETED' 249 ALC-V0250 2

GLOBE-SW-40 Discharge Line HENRY V0GT 150/120 From Compressor DWG. 4 ALC-P-7 E-44248-R6

-72 A

~

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

.. ~.,- ~.__ _ -.- _ _.

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

m m

s_

_m

-..m_

._ ~-

- ~

_m_

l.

TABLE 14 3526-004 AUXILIARY BUILDING EMERGENCY Ligv1D CLEANUP SYSTEM (EPICCR 11)

VALVE LIST i

DESIGN PRESSURE /

SISE KANUFACTURER/

TEMPERATUPE YALVE No.

iin,1 M

DESCRIPTION PO NO.

MODEL tesic / 'F)

COMMENTS ALC-V0251 2

GLOBE-Sw-40 Discharge Line HENRY VoGT 150/120 From compressor DWG, 4 4

i ALC-P-8 E-44248-R5 ALC-V0252 3/4 GLonE-Sw-40 Air Supply Line stock RANCoCK 150/120 From ALC-P-7 6 CAT. 4 ALC-P-8 Drain 5500W-1 ALC V0253 3/4 GLOBE-sw-405 Priming Vent Line 150/120 ALC-V0254 1/2 GLOBE-SCRD-405 Pressure Top on 150/126 Priming vent Line

. ALC-V0255 2

AIR OPERATED BALL Process Supply HILL 8-McCANNA 150/120 2 Way Normally Closed SCRD-408 Line to Prefilter FIG.

Energized to Open ALC-F-1 5302-56-T-S6 ALC-YO256 2

CBECK Sump to ALC-P-1 Suetion t

ALC V0257 2

GLOBE

. Sump to ALC-P-1 Suetion ALC+V0258 CATE EPicoR to spent Located in Unit 1 Fuel Pool

'B' ALC-V0259 GATE EPICOR to spent Located in Unit 1 Fuel Pool

'B' ALC V0260 3/4 GLOBE ALC-P-1 Air Supply Motor Operated Throttle ALC-V0261 3/4 GLOBE ALC-P-2 Air Supply Motor Operated Throttle ALC-V0262 3/4 GLOBE ALC-P-3 Air Supply Motor Operated Throttle l

ALC-v4263 3/4 CLoBE ALC-P 4 Air Supply Motor operated Throttle

[

t ALC-V0264 1/2 NEEDLE ALC-F-1 Bubbler i

Air Isolation ALC-V0265 1/2 NEEDLE'

- ALC-K-1 Bubbler Air Isolation t

ALC-V0266 1/2 NEEDLE ALC-K-2 Bubbler Air Isolation i

-YS-a b

f

__.,-.--..~.m_..,-,..-m_-....----.---.._.~.-,-

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

a

.m.

.m-I TABLE 14 3526-004 i.

AUXILIARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPICOR 11)

VALVE LIST DESIGN FPESSURE/

SIIE MANUFACTURER /

TEMPERATURE VALVE FO.

tin.)

- IJFJ DESCRIPTION PO 770.

MODEL icato / 'F1 COMMENTS f

f-ALC-V0267 3/8 NEEDLE Bubbler Air isolation ALC-V0269 1/2 PRESSURE REGULATCR ALC-F-1 Bubbler Self Centained Regulator (Int. Tap) h ALC-V0269 1/2 FRESSURE REGULATCR ALC-R-1 Bubbler Self Contained Regulator (int. Tap) i ALC-V0270 1/2 PRESSURE REGULATOR ALC-K-2 Bubbler Self Contained Regulat or (Inti Tep)

. ALC-V0271 1

CEECK Service Air to Bubblers /ALC-V-255 ALC-V0272 3/8 CLOBE Service Air to Bubblers /ALC-V-255 ALC-v0273 2

GLOBE Eump to ALC-P-1 Suction Isolation ALC-V0274 3/4 GLcBE Sump to ALC-P-1 Suetion Drain ALC-V0275 3/8 NEEDLE Air to ALC-V-242 1solatien ALC-V0276-2 GLOBE Sump to ALC-P-1 Suetion Final i

isolation ALC-V0277 2

.CLOBE ALC-P-4 Discharge ALC-V0278 1

GLOSE ALC-Fal Shield Drain ALC-v0279 1

GLOBE ALC K-1 Shield -

Drain ALC-V0290 1

GLOBE ALC-R-2 Shield.

Drain

.ALC.V0281 Deleted ALC-V0282 Deleted ALC-V0283

. Deleted ALC-V0284 3/4 GLOBE

' ALC-P-6 Discharge to ALC P-2 r m.

-~...~,.re-.~.-..,

...,.--...-~~e..

1. .-..m-<.-i..-w.--w.-w

-..-..-..+%.,-...-4

,...ec.,w.e,*

--w.,--

.-e.,-e-.. -,.

-w..e+.m-.e, ww..w.-

.,-4----.-,

,=,wm*,m--~.-,---

TABLE 14 3526-004 AUKILIARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPICCR II)

. VALVE LIST DESIGN PRESSURE /

SISE MANUPACTCRER/

TEMPERATURE VALVE NO.

M TTFE DESCRIPT104 PO NO.

MOCIL teste / 'F1 COM".INTS A!4.V0265 3/4 GLcBE ALC-P-6 Discharge to ALC-P-3 ALC-YO296 2

GLOBE CC-T-2 Process Inlet Isolation ALC-V0287 2

BALL MWRT Process isolation ALC V0290 1 1/4 GLOBE Minimum Flow TP-034598 shutoff ALC-YO291 1

SCLENCID Minimum Flow Autome*ic Cat 98400 Solenoid

)

ALC-YO292~

l 1/4 GLOBE CC T-1 Minimum TP-034599 Flow Shutoff ALC-v0293 1 1/4 glebe CC-T-2 Minimum TP-034596 Flew Shutoff ALC-v0294 3/4 GLOBE ALC DPS-1 BP Leg TP-034599 Roet vsive ALC-V4295 3/4 GLC3E ALC-P-5 Vent TP-034398 valve ALC-V0296 2

BALL ALC-F-1 Bypass MMA 3526 87-0016 Inlet Isol.

ALC-V0297 2

BALL ALC-F-1 Bypass MMA 3526-87-0016 Cutlet 1 sol.

ALC-V296 3/4 BALL ALC-P-9 Suetion

$27-1-42 WATTS ALC-V299 3/4 ALC-P-9 Recire.

C-0080 Yelen 3001 ALC-V300 3/4 CHECK ALC-P-9 Discharge 016163 Rockwell ALC-V301 3/4 BALL ALC-P-9 Discharge 007971 Velen 600/

ALC V302 3/8 TUBING ALC-PI-5/ALC-P-9 0$$133 Parker 639F Discharge ALC-V303 3/4 BALL CC-T-1/Eysp/

Velen 600/

PWST Cross-Tie ALC-Y304 3/4 BALL CC-T-1/Evsp/

Velan 6001 FFT PWST Cross-Tie

=75-

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

_._..m m.

. ~..

m

.m_

_m

s. _ _

381LE le 3526-004 AUXILIARY BUILDING EMERGENCY LIQUID CLEANUP SYSTEM (EPICOR 11)

VALVE LIST 1

DESIGN

(

7 PRESSURE /

$18E MANUFACTURER /

TEMPED.ATURE VALVE No.

(in.)

M DESCRIPTION PO NO.

MODEL desio / *F1 COMMENTS A!4-V305 3/4 BALL CC-T-1 to Evap.

053453 WATTS TYPE 1000/

Isolation 88S01 AI.C-V3 06 3/4 BALL PWST reed to 053453 WATTS TYPE 1000/

Evaporator 88501 ALC-V307 3/4 BALL Evaporator to WATTS TYPE 1000/

SWE PWST Isolation /

88501 PW-P-3 Suetion j

ALC-v308 3/4 SWE ALC-T-3 Outlet 018148 JACOBY-TARBOX 235/475 Fig, fr14 W344 BALL INTERNATIONAL 60152-C-20 ALC-v309 3/4 SWE Evaporator to 053533 WATTS 1000 WoG/

l BALL ALC-P-10 a

. ALC-V310 3/4 CHECK ALC-P-10 Discharge 01(163 ROCKWELL FIG. 36174 ALC V311 3/8 ALC-PI-6/AT.C P-10 055133 PAP.KER Discharge 638r ALC V312 3/4 SWE ALC-P-10 Discharge 43749 HANCOCK 1000/

316 S.S.

t 5500W1 ALC-V313 3/4 BALL ALC-P-9 Discharge MCF Ap66TF 1500/

Drain ALC-V314' 1/2 BALL ALC-P-9 Disel>arge JAMESBURY

[

vent ALC-V315 1/2 BALL ALC-P-10 Discharge 064281 JAMESBURY Vent ALC-V316 1/2 BALL ALC-P-9 Section JAMESBURY vent ALC-V317 1/2 NPT ALC-T-3 Drain 064303 JAMESBURY 800 WoG/

Type 1/2* 23-3600-MT-1 BALL ALC-V318 2

GATE ALC-P-11 Suetion.

052030 POWELL 200/

ALC-V319 3/8 TUBING ALC-PI-7/ALC-P-11 0337~

PARKER Discharge 638F ALC V320 2

SWING CHECK ALC-P-11 Discharge C0076 CRANE 150/

Tagged "WDL-V368*

ALC-V321 2

ALC-P-11 Discharge 021475 NEWCO 900/

+76-i m

m

__,_...~,+...-._...__w~.--..-

..~.~_,,rm_.,.U.m..w.._.,.m.._-,N.h..,.--_.m--m._,,.~_

___m,_,,m_.m

a E

TABLE 14 3526 034 AUXILIARY BUILDING EMERGENCY LIQUID CLEANUP g

SYSTEM (EPICOR 11)

VALVE LIST DESIGN PRESSURE /

S18E MANUFACTURER /

TEMPERATURE VALVE No.

lin,)

TJfrE DESCPIPTION PO NO.

MODEL lesio / *F1 COMMENTS ALC-V322 3/8 TUBING CC-T-1 Recire.

055133 PARKER Sample isolation 638F ALC-V323 2

ALC-P-5 to CC-T-1 VELAN Isolation ALC-V324 1-1/2 ALC-P-5 Mini Rectre.

225123 1solstion I

ALC-Y325 3/4 BALL ALC-7-3 Inlet 047900 MCF 5 1500/122 SRS66TFSWE ALC V326 ALC-T-3 Outlet same as valve ALC-V308 WG-V-05 2

BALL Storage Tank Inlet ECA 3230-87-0442 from MWHT FCR 987-079 WG-V-24 2

PLUG WG Flush Conn, 150/

WG-V-29 2

PLUG SDS Filters Bypass 150/

WG-V-34 1

PLUG WG-U-3 Conn. Isol.

150/

WG-V-47 2

PLUG Fuel Pool Ster.

150/

i to ALC Isol.

V i

WG-V-71 2

PLUG Feed to 8DS Filters 150/

WG-V-72 2

PLUG Misc. Wst. Sys.

150/

Isol.

WG V-87 1/2 GLOBE CN.FE-22 Root VLV 4000/

ECM-S-366 R.1 Capped

- Hi lool.

Downstream Lines i

WG V-89 1/2 GLOBE CN-?E 22 Root VLv 4000/

ECM-8-366 R.1 Capped f

to Isol.

Downstream Lines

[

i WG-V-99 2.

BALL WG Spool Piece ECA 3230-87-0442 l

1 sol.

FCR 987-011 I

I 5

t

. i l

i l

-77 l-i l

.!t l

F-Y t

n._,-.-.,

.. ~..

..+..,, _....

u-,.. - ~ ~,

.--.-,-.---....c,.

.,..-...-._.....,..-_..,.4,--..

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

7 TABLE 15 EPICOR II RADWASTE PROCESSING SYSTEM (IIIC POLISIIING MODE)

Overall Objectives:

I

a. Polish influent water sufficiently to satisfy Technical Specifications criteria.

b. Process water at 10 gpm.

c. Minimize personnel exposure.

d. Process water at the lowest possible cost.

Special Objectives:

Gallons Process Processed Vessel to Reach Projected Typical Changeout Changeout Shipping Container Vessel Size Primary Purpose Composition Criteria Criteria Cateaorv

1. 1 First Domin.

4'Dx4'H Cesium & Strontium Zeolite (top) 348 Ci Cs dependent Class C based 6'Dx6'H Removal Sand (bottom) on feed on integrated dose to HIC lid gasket

1. 2 Second Demin.

4'Dx4'H Na Removal Cation (top)

<1 Ci/cc dependent LSA 6'Dx6'H Cation Removal Anion (bottom) on feed Anion Removal

1. 3 Third Demin.

4'Dx4'H Polishing Mixed Resin

< 1 R/hr dependent LSA 6'Dx6'H Guard Bed on feed

1. 4 Strainer 2'Hx 1 %'Wx Catch Resin Fines Strainer

< 1 R/hr 200,000 LSA 1 %'L

1. 5 Post Filter 2'Hx1 % 'Wx Colloid Removal 1-10 Micron

< 1 R/hr 150,000 LSA 1 %'L Cartridge.

..