ML20247J225

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Rev 7 to Div Sys Description for Auxiliary Bldg Emergency Liquid Cleanup Sys (Epicor II)
ML20247J225
Person / Time
Site: Three Mile Island Constellation icon.png
Issue date: 07/31/1989
From: Richfeld S
GENERAL PUBLIC UTILITIES CORP.
To:
Shared Package
ML20247J209 List:
References
SD-3526-004, SD-3526-004-R07, SD-3526-4, SD-3526-4-R7, NUDOCS 8907310268
Download: ML20247J225 (81)


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Nuslear S D 3sas-m4 ngy 7 j ISSUE DATE July 1989 l @ its O won l O wits DIVISION SYSTEM DESCRIPTION FOR Auxiliary Building ' Emergency Liquid Clean-up System (EPICOR II)

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26-004 l

Title System Description for Page 2 of 81 {

Auxiliary Building Emergency Liquid Clean-up System (EPICOR II) l l

Rev.

SUMMARY

OF CHANGE Approval Da te O Initial issue per GPU Nuclear letter 4410- 82-L- 0017. N 2/82 1

i 1 Updated per GPU Nuclear letter 4410- 83-L- 0078. N 4/83 l 2 Updated per GPU Nuclear letter 4410-84-L-0023. $ 2/84 3 Updated per GPU Nuclear letter 4410-85-L-0074 Incor- h5 4/85 '

porated ECM 3475.8, Revision 8.

4 Updated per GPU Nuclear letter 4410-86-L-0069.  % 4/86 5 Annual update to reflect the current operating configura-tion of the EPICOR 11 system. Adds further detail as to

$ 5/87 the operation of the Transfer Pump ALC-P-5'in Section 2.1.2. Revised the description of demineralized ALC-F-1  !

in Section 2.1.3. Revised Section 2.1.19 concerning system isolation valves. Adds new Section 3.4.2 and 3.4. 3 6 Annual update to reflect the following: N 6/88

a. Clarification of Section 1.0 regarding approved receiving tanks for EPICOP. II processed water and routine /non-routine operations.
b. Installation of a stainless steei ALC-P-5 transfer pump has changed Section 2.1.2 and Table 2 regarding total dynamic head. .

a c. Replacement of ALC-RE-18 (ALC Ventilation Rad Monitor) required modification to Section 2.2.4 and Tables 10 and 12.

d. Table 15 (ALC Valve List) has been expanded to include two new valves added for MMA 3526-87-0016 (ALC r-1) Bypass.  !
e. Table 15 also now includes the descriptions of "WG" g valves commonly used when processing MWHT, RCBTs, and R Neutralizer Tanks through EPICOR II. When the E "TANKFARM" S.D. #3230-003 was cancelled, these "WG" y valves should have been incorporated into SD 3526-004.

8 s 7 Annual update to reflect the current operating configura- (pf 7/89 tion of the EPICOR II System and to reflect the out of

2 s service (005) condition of the Submerged Demineralized  !

i

% System (SDS). Table 12 was deleted for administrative g purposes; Table 13 was deleted as being redundant to Table 16; and Table 14 was deleted because SDS is 00S.

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3525-004 1

TABLE OF CONTENTS SECTION PAGE

1.0 INTRODUCTION

5 1.1 System functions 5 1.2 Summary Description of the System 6 1.3 System Design Requirements 7 2.0 DETAILED DESCRIPTION OF THE SYSTEM 11 2.1 Components 11 2.2 Instruments, Controls, Alarms, and Protective Devices 23 3.0 PRINCIPAL MODES OF OPERATION 26 3.1 Startup 26 3.2 Normal Operation 27 3.3 Shutdown 28 3.4 Special or Infrequent Operation 28 3.5 Emergency 30 4.0 HAZARDS AND PRECAUTIONS 31 l li l

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p TABLE OF CONTENTS (Cont'd)

TABLE PAGE l

1. EPICOR II Pumps 32
2. Transfer Pump 33
3. Filters 34
4. Demineralizers 35
5. Miscellaneous Waste Hold-up Tank 36
6. Clean Water Receiving Tank 37
7. Off-Spec. Water Receiving / Batch Tank 38
8. Sump Pump, Chemical Cleaning Building 39  ;
9. Monorail Hoist System 40
10. CCB Ventilation System Nameplate Data 41
11. Air Compressors 42
12. Deleted. 43
13. Deleted. 44
14. Deleted. 45
15. Valve List 46
16. Radwaste Processing System (EPICOR II) 81 Rev. 7/0185P

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1.0L INTRODUCTION L :1.1 System Functions-L The functions of the' Auxiliary Building Emergency Liquid Clean-up (EPICOR II) . System are:

'1.1;l To' decontaminate, by filtration and icn exchange, radioactive waste water contained in TMI. Unit 2. In the past. EPICOR II also served as a polishing ion exchanger system for the Submerged

' Demineralized System (SDS). SDS has been taken out of service-and will no longer process / filter contaminated liquids. .Therefore, 1 '

-EPICOR:II processes the-waste water dir.ectly.

p. 1.1.2 To transfer EPICOR.II processed water from the Clean Hater Receiving Tank'(CC-T-2) .to the following tanks:
a. Processed Water Storage Tanks (PHSTs or PH-T-1 and 2).
b. Off-Spec.. Hater Receiving 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. Evapor.ator Condensate Test Tanks (ECTTs or HDL-T-9A and 98) to be-used for various decontamination activities and make-up water / chemical additions via the Boric Acid Mix Tank-(BAMT).

NOTE: The transfer to HDL-T-9A/B passes through Unit 1 Turbine Building, but is physically. isolated from all Unit 1 systems,

d. On a non-routine basis to either the Condensate Storage Tank (C0-T-1A), Borated Water Storage Tank (BHST) or the "B" Spent fuel Storage Pool via the truck fill station.

1.1.3 To provide remote handling of spent resin containers from their position inside the Chemical Cleaning Building (CCB) to the l transport cask and truck.

1.1.4 To limit releases of radioactive material to the environment to "as low as is reasonably achievable." l 1.1.5 To provide for operation and maintenance of the liquid cleanup system in compliance with "as low as is reasonably achievable" l radiation doses to personnel.

1.1.6 To accomplish the above independently from TMI Unit-1 (for exception see NOTE above).

Rev. 7/0185P

3526-004 1.2~ Summary Description of the System Th$ Auxiliary Building Emergency Liquid Clean-up System, as the name im,;iles, was originally aesignea and constructed for the primary purpose of processing and cleaning up the accident-generated water that collected in the Auxiliary Building. It has, since then, evolved into a radwaste liquid processing system, differentiated from a regular radwaste liquid processing facility, in that the water processed by the former is accident-generated. The system is referred to as EPICOR II.

The system consists of a liquid radwaste processing system which is located in the CCB. It decontaminated, by filtration and ion exchange, radioactive waste water contained in the Auxiliary Building, Fuel Handling Building, Service Building, and Reactor Building of TMI Unit 2.

Contaminated water is pumped from a connection located on the Miscellaneous Waste Holdup Tank (MWHT) by a pump located in the CCB through the yard and into the process system; contaminated water can also be obtained from the Monitor Tanks (SDS-T-1A and IB), the Contaminated Drain Tarks (CDTs), the Reactor Coolant Bleed Tanks (RCBTs), or the Neutralizer Tanks (HDL-T-8A and 8B). Yard piping is shielded and enclosed within a guard pipe, the open end of which terminates inside the CCB.

The primary precess system consists of three demineralizers (ALC-F-1, ALC-K-1, and ALC-K-2), connected in series. Haste liquid is transferred from the source tank (MWHT, HDL-T-8A/B, RCBT, CDT, or SDS-T-1A/B) through the demineralizers, to the Clean Water Receiving Tank (CC-T-2).

Change-out Criteria for the various units are indicated in Table 16.

Processed water is delivered to CC-T-2 for sampling and analysis. The l processed water is pumped to one of the following: the Liquid Haste Disposal System of TMI Unit 2, the Spent Fuel Storage Pool, the PHSTs, the BHST, CO-T-1A, HDL-T-9 A/B or the truck fill station for transfer to the NLB Pump if within specification. Additionally, the processed water can be transferred to CC-T-1 for recycling through the process system or l use in the decontamination of the Reactor Building or 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; l this is not a routine operation since feed and bleed processing requires a long time to accomplish.

The CCB is a low leakage confinement building with an exhaust ventilation l system to maintain the building at a negative pressure. Moisture separators, high efficiency particulate absolute (HEPA) filters, and l 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 roof line of the CCB. All effluent air is monitored for radioactivity at this point. Provisions for grab samples are available.

Normal operation of the processing system is by remote means except for infrequent operations such as sampling, spent resin container removal and new resin container installation. All remote system operations are controlled from the TV Monitor and Control Building located outside the northwest corner of the CCB. l Rev. 7/0185P

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  1. Remote handling of. spent resin containers from their position inside the CCB to the transport cask and truck is.via a remotely-operated. l twenty-ten monorail hoist system.

A fire protection system is installed in the HVAC equipment room, the TV l' 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 Control Building.

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

. Storage System, the 80P Electrical System, the Service Air System, the Unit 1 Liquid Waste Disposal System, the Fire Protection System, and the Unit 2 Radwaste Disposal' Reactor Coolant Liquid System.

. NOTE: Although there 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 function independently. Valve ALC-V169 shall remain locked closed (unless transferring water from either CC-T-1 or CC-T-2 to.the "B" Spen; Fuel Pool) and a spectacle' flange is

. installed downstream of valve ALC-V169 at the transition between Unit 1 and Unit 2 liquid radwaste systems. Valves downstream of valve ALC-V169 are no longer accessible to Unit 2 operators due to l unit separation.

1.3' System Design Requirements i

1.3.1 Process System Design Requirements ,

1.3.1.1 The process line pipe size is nominally 2" schedule 40, based upon the EPICOR II System flow rate of 10-30 gpm. Other line l sizes are based on service requirements and function, such as )

service air, demineralized water, recirculation and sampling. j 1.3.1.2 Pumps ALC-P-1 through 4 have hose connections and are provided with drip trays to collect leakage. Drip trays have nozzles as close to the bottom of the tray as possible and are served by flexible tubing which leads to the nearest floor or equipment drain using the floor slope to induce flow. This tubing is placed well down into the floor drain.

1.3.1.3 Remote system operations are directed and controlled from outside of the CCB from the TV Monitor and Control Buildi.,g. I This area is provided with remote closed circuit television monitoring of the operating areas inside and outside the CCB. l 1.3.1.4 Process instrumentation consists of pH and conductivity monitors. Resin bed radiation levels, process line radiation levels, process flow rates, process totalizers, and l 1

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T ~E' . tank / demineralized levels are also monitored. Accelerometers for pumps ALC-P-1 through 4 are provided-for' equipment l protection and an alternate' method to determine. processing Lc flowrates.

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 drain demisted liquids back into the system tanks.

l.3.1.6 . Liquid ~ waste feed to the system will be drawn-from the source tank (MWHT, RCBT, SDS-T-1A/B, CDT, WDL-T-8A/B, CC-T-2, or

!> CC-T-1) to the first EPICOR II pump (ALC-P-1). The MWHT pump-1 is not used when. processing the MWHT water; this provides' better system pressure and flow control.

1.3.1.7 The EPICOR II System is contained within the CCB which was -l 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) l scope; however, the system has 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. i Instrument tubing systems are 316'SS tubing and are made up l using' compression fittings. The process system piping is rated at 150 lbs. and is designed, installed and inspected in.

accordance with ANSI.831.1 (Power Piping).

NOTE: Flanged and screwed connections are used as 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 l.

ALC-F-1, ALC-K-1 and ALC-K-2, while in a low radiation area in accordance with Regulatory Guide 1.21. Representative sample 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 shall be 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 shall be flushed for a minimum of three (3) minutes prior to drawing the sample.

NOTE: Demineralized ALC-F-1 is the first demineralized, followed in series by demineralizers ALC-K-1 and ALC-K-2, respectively.

1.3.1.10 The building sump is a covered sump.

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[ 1;3.1.11' System blowdown air-and demineralized water l'ines are provided with individual check valves ALC-V060 through V079 to minimize contamination of these systems.

l~.3.1.12 The demineralized water supply header is provided with demineralized water from TMI Unit 2 in the range of 80-90 psig to meet EPICOR II requirements.

L l'.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 ths system air header servicing the EPICOR II pumps. The Plant Service Air System is the normal and preferred air supply. Also two air compressors (ALC-P-7 and 8) are available for use and tie into the air supply header via valve ALC-V145.

l 1.3.1.14 If sampling indicates that the processed water is within limits for usage, the decontaminated liquid from CC-T-2 can be routed to one of the following: the TMI Unit 2 Liquid Waste l

. Disposal System, the TMI Unit 2 Spent Fuel Storage Pool, the PWSTs, CC-T-1, or a truck fill hose connection'that is provided as a means of transferring decontaminated 11gulds for use in the decontamination of the Reactor, Auxiliary and Fuel Handling Buildings.

.l.3.1.15 'All system overflow lines discharge to the CCB sump. All l floor drains also discharge to the sump. The water collected in the sump is staged in CC-T-1 by the sump pump for recycle l through the cleanup system or it is drawn and processed directly through the EPICOR II System via existing valves and piping.

I 1.3.1.16 Since the elevatloa 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, 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).

1.3.1.i7 Three resin traps are installed downstream of the demineralizers.

1.3.1.18 A one micron (nominally rated) cartridge type filter is installed downstream of the three resin traps.

1.3.1.19 The system has personnel shielding on various components to l reduce the radiation levels in the operating areas of the building.

1.3.1.20 A resin trap is installed on the outlet from the casks overflow line to prevent resin carryover into the sump.

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3526-004 I Ll. 3.2 Material Handling Design' Requirements 1.3.2.1 Normal operation of the EPICOR II System is by remote methods. l l.3.2.2 Demineralized water and service air connections are provided to flush and blowdown the entire system or portions of it to allow system maintenance.

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 by l making.use of the shield bell designed for this purpose. The shield bell is positbr.ed over the radioactive liner; the shield doors on the bottom of the bell are opened and the

. liner is. drawn up into the bell. The doors are closed and the -l bell is carried, by the crane,.to the truck which may have a concrete shield vessel for isolating the bell during

-transportation to the staging faci!ity. 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, and level instrumentation are repositioned and the unit is returned to service.

NOTE: The transfer bell is no longer routinely used and will only be used if operation of the 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 appropriate barriers limiting the approach 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 l negative pressure.

1.3.3.2 The MSA filtration unit is designed to meet the requirements I of NRC Regulatory Guide 1.140.

1.3.3.3 The moisture separator is provided to remove water vapor droplets from the air.

1.3.3.4 An electric heater is provided within the tiSA filtration unit to lower relative humidity (RH) to 30% with 100% RH inlet air. l Rev. 7/0185P i

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n k L1.3.3.5 The prefilter.has an average atmospheric air strain efficiency L' 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.

2.0 DETAILED DESCRIPTION OF THE SYSTEM 2.1 Components p' ,

2.1.1 EPICOR II Pumps ALC-P-1 through 4 (See Table 1)

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 pump; are utilized in the system to circulate the liquid l through the demineralizers. The hoses furnished for.the flexible i

connections to the pumps, filters, demineralizers, and traps have a design pressure of 100 psi.

' Air supplied to the pumps passes through an air oiler and an anti-freeze injector to a' valve manifold. Pump speed and capacity w),a be varied by the EPICOR II operator to achieve the optimum flow through the radwaste process system. Pump speed is-controlled by throttling the drive air at the Fava Control Panel. ,

Demineralized water and oil free air connections are provided on i y the suction and discharge side of each pump for flushing and l blowdown purposes. Pump noise and vibration monitors are present l for-pumps ALC-P-1 through 4 and have a read-out on panel ALC-PNL-2 in the TV Monitor and Control Building.

2.1.2 . Transfer Pump ALC-P-5 (See Table 2) l- .

Transfer pump ALC-P-5 is a single stage horizontal centrifugal l pump with a capacity of 200 gpm at 100' head. ThE pump motor is rated at 10 HF and is powered from MCC 2-33A in the TV Monitor arid Control Building. The pump is controlled by push buttons for START /STOP from MCC 2-33A, a hand selector switch for low level control of either CC-T-1 or CC-T-2 from the panel ALC-PNL-1 in the l TV Monitor and Control Building and level switches in panel ALC-PNL-1 for CC-T-1 and CC-T-2. The level switches receive their l signals from level transmitters ALC-LT-1 and 'ALC-LT-2 at CC-T-1 and CC-T-2, respectively. 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 d solenoid operated valve ALC-V136 controlled from the pump motor starting circuit. When the motor starts, the valve opens. The seal water flow rate is maintained at 1-2 gpm by throttling valve ALC-V134 when seal water injection is required. Seal water 4 injection is only required if the pump is handling water which  !

contains greater than 7000 ppm boron.

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3526-004 Iffthe pumpLhandles clean water, it is acceptable to allow the  !

mechanical real to be lubricated through the. pump's internal

, passages. As long as the water has passed through~the-one micron. l

. filter ALC-F-5, the water is clean enough (from a_ grit standpoint) to~1ubricate'the mechanical seal. .Thus, as long as filter ALC-F-5 c is in use, the demineralized seal water can be turned off with valve ALC-V134 to reduce the total volume of processed water or radwaste.

This' pump is used to transfer water from either CC-T-1 or CC-T-2 to one of.the following: the TMI Unit 2 Liquid Waste Disposal 'I System, the Spent Fuel Storage Pool, the PWSTs', or a hose connection at the truck fill station. It is also used to transfer-water from CC-T-2 to CC-T-1. l Furthermore, this pump is'also used for recirculating and sampling the contents of both CC-T-2 and CC-T-1. The sample connection

terminates at 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 and No. 2, the Spent Fuel" Pool, the PWSTs and the .l truck fill: station. Remote indication of flow (ALC-FI-2) and a flow totalizer (ALC-FQ-2) are located on panel'ALC-PNL-1.

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 CC-T-2; the direction of the flow is to the tank from which the water originates. .The operation of the minimum flow control valve is automatic, although manual control is provided as well. .

Automatic control is provided by differential pressure ~ switch ALC-DPS-1. The 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 L the flow has increased to approximately 90 gpm, at which time it l- will close. Manual control permits the opening and closing of the valve.at any time.

2.1.3 Demineralized ALC-F-1 (See Table 4) l The first stage demineralized (also referred to as a liner) is l' generally used to remove sodium and other non-radioactive chemicals and low concentrations of radioactive isotopes. The cesium and strontium radioisotope concentrations are low enough j that they do not. require removal prior to polishing. This

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demineralized is either a 4x4 or 6x6 carbon steel tank loaded with organic resins.

Should conditions require gross cesium and strontium removal, a HIC loaded with z d ite resins shall be placed in t M first j position to act as a aughing 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 design being the materials used 4

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during: fabrication of each type. HIC demineralizers are constructed of a very high. grade stainless steel, enabling the container to meet the burial limits of Class B or Class C waste. l 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 (pump suction), a cornbination vent / overflow, and an air type QD fitting for the level bubbler tube. As a means

.of backup level indicator, a threaded level conductivity probe also penetrates the tank top, An air connection is provided at the' top of the 6x6 liner 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" diameter-opening is installed on top of the tank.

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

The level probe or bubbler system maintains tank level between 4" and 6" from the top of the tank by opening and closing solenoid l valve ALC-V185 on the air supply to pump ALC-P-1, which is supplying the tank; starting the pump on low level and stopping the pump and closing valves ALC-V043 or ALC-V242 on high level.

On Hi Hi level 4" from the tank top, an audible alarin is sounded at the EPICOR II Monitoring Console, located in the TV Monitor and Control Building, valve ALC-V255 closes, and the pump motor operated valve closes. The EPICOR II opsrator may select either air bubbler or conductivity level control on the Fava Control Panel located in the TV Monitor and Control Building.

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

l A tee is provided in this vent line for a hose connection to a common header which discharges to the CCB sump. The line is provided as a demineralized overflow line and demineralized overpressure protection. A loop seal is provided to ensure that all cask gases are routed to 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 Centrol 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 shield-supporting steel. Radiation monitors (ALC-P,M-1 and 2) are located inside this shield 180 degrees apart at different 1

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

To avoid breakthrough of sodium to the second liner when demineralized ALC-F-1 is organically loaded, the batch size through demineralized ALC-F-1 is limited.

If a HIC is in service in the ALC-F-1 position, activity l breakthrough will be limited through batch size or by the activity as measured by radiation monitor ALC-RM-7, installed at the influent header of demineralized ALC-K-1. The second liner will then be organically loaded for sodium removal.

If the water source is very low in cesium and strontium, but still requires further polishing (i.e., recycle processing of either CC-T-1 or CC-T-2), a jumper hose will bypass the HIC demineralized in the ALC-F-1 position. In this configuration, the first liner in the series will be demineralized ALC-K-1 followed by

'. dem beralizer ALC-K-2 (i.e., two liners versus three). Processing reittively clean water will rinse cesium and/or strontium activity off of the HIC zeolites on to the downstream ALC-K-1 demineralized. This is the purpose of the " BYPASS" mode. Refer to Saction 2.1.19 for details regarding demineralized level controls. Refer to Sections 3.4.2 and 3.4.3 regarding operations and. systems that prepare a HIC / demineralized for shipping and burial.

Remote indication is provided on the cleanup panel ALC-PNL-1 for radiation monitors ALC-RM-1 and 2. During system operation, radiation levels as indicated on radiation monitors ALC-RM-1 and 2 should not be allowed.to exceed 1 R/hr.

2.1.4 Demineralizers ALC-K-1 and ALC-K-2 (See Table 4)  !

Two demineralizers are installed in series with demineralized l ALC-F-1 to further remove radioactivity from the waste liquid and polish the effluent.

Demineralized ALC-K-1 is either a 4x4 or 6x6 liner and is l primarily used to reduce the activity level of the process fluid through lon exchange and filtering. For this reason, the anticipated activity levels are high and the shielding around demineralized ALC-K-1 is identical to shielding around demineralized ALC-F-1 when demineralized ALC-F-1 is a 6x6 liner.

Demineralized ALC-K-2 is either a 4x4 or 6x6 liner and is primarily used to polish the effluent water from demineralized ALC-K-1 and to act as a guard in the event of a resin breakthrough from demineralized ALC-K-1. For this reason, the anticipated activity levels in demineralized ALC-K-2 are lower than in demineralized ALC-K-1.

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N- Each demineralized has the same external. connections as demineralized ALC-F-1. The demineralized resin composition and

)

q- quantity will be determined on.the basis of system samples and .

operating data. ]

l As with demineralized ALC-F-1, two radiation detectors are located l' l at diffe ent elevations 180 degrees apart inside the lead shield.

i Remote. indication is provided 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 demineralized ALC-K-1,  !

should not be allowed to exceed 1 R/hr, Radiation levels on ,

indicators ALC-RMI-5 and 6 for demineralized ALC-K-2, should not l be allowed to exceed 1R/hr.

2.1.5 ' Miscellaneous Waste Hold-up Tank WDL-T-2 (See Table 5) l The Miscellaneous Waste Hold-up Tank (MWHT) which has a capacity l of 19,518 gallons, can receive liquid from the following sources:

a. Auxiliary Building Sump Tank b '. Neutral 17st. Tanks
c. Contaminated Drain Tanks
d. Reactor Building Sump l

l

e. 'Deborating demineralized back wash outlet
f. Fuel Storage Pool Submersible Pump Discharge 9 Demineralized Water System
h. Condensate Polisher Sump l
1. Water Treatment Sump
j. Reactor Cnolant Bleed Tanks
k. Concentrated Waste Storage Tank i

The tank also has connections to the MWHT pump suction, recirculation capability, a caustic and sulphuric acid inlet, two nitrogen inlets, a vent, a gas sample connection and a relief valve. The tank is normally nitrogen blanketed, but may be vented to the Gaseous' Waste Disposal (WDG) System. To prevent acid l splashing on the inner tank walls, the inlet piping extends eight (8) feet into the tank. The diameter of the tank is 10'-9 1/4".

l The MWHT is located in the-Auxiliary Building at elevation 305'.

l l .A temporary tee connection is installed in place of the suction line strainer, WDL-U202B, on the MWHT pump (WDL-P-6B) suction line, Connected to this tee is a 2" line which supplies the l

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. liquid from the MWHT to the suction side of pump ALC-P-1. A 4" l guard pipe with a combination of lead and concrete shielding encloses the suction piping run from the Auxiliary Building i

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

2.1.6 Clean Water Receiving Tank CC-T-2 (See Table 6) l CC-T-2 is a stainless steel atmospheric pressure tank with a j capacity of 133,689 gallons located in the CCB. CC-T-2 receives '

i the processed liquid from the discharge of pump ALC-P-4 via, in order, three resin traps, a one-micron crud filter, conductivity cell, pH meter, and an inlet flowmeter / totalizer.

An overflow line with a loop seal is provided near the top of CC-T-2. A demineralized water supply is provided for the loop seal. A suction line from transfer pump ALC-P-5 penetrates the '

CC-T-2 skirt and connects to the bottom of CC-T-2. A connection on the top of CC-T-2 is also provided for the transfer pump recirculation line, a feature that enhances mixing of the contents. Level indict. tion and high level alarm are provided on panel ALC-PNL-1. A future xenon hold-up tank connection is provided on the vent line. A 2" demineralized water line is also provided on top of CC-T-2 for whenever large quantities of demineral'. zed water are required in CC-T-2. This would include preoperational testing or tank cleanup. A drain line is provided off transfer pump ALC-P-5 suction piping to drain the suction piping and the remaining water in CC-T-2 that the transfer pump I

cannot drain.

CC-T-2 has a 2" vent line exhausting to the CCB through a l l

two-stage demister filter. The first stage consists of two moistura separators and 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 controlled from power panel MP 2-33A.

Processed water is stored in CC-T-2 until a batch is completed. A l representative samole of the processed water ca.i be obtained from the discharge of the transfer pump at the sample sink after recirculating three volumes of CC-T-2 and purging the sample lines l for five line 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 l into the suction line of pump ALC-P-1 for reprocessing through the filter and demineralizers until the quality is acceptable for discharge to the plant or storage tanks. If sampling indicates that the centents of CC-T-2 are satisfactory for use in the plant (e.g., decon flush or makeup to other plant processes) the water is pumped normally into one of the following: the THI Unit 2 Liquid Haste Disposal System, the Spent Fuel Storage Pool, the ,

PWSTs, or the NLB pump from the truck fill station; however, the t water may be stored in CC-T-1, if desired. CC-T-1 will be flushed clean with demineralized water or clean processed water before it is used for clean water storage.

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3526-004 2.1.7 10ff-Spec. Water Receiving Eatch. Tank.CC-T-1 (See Table 7)

CC-T-1 is-a stainless steel tank with a capacity of 85,978 gallons l Ldesigned for. full vacuum to 75 psig. For the EPICOR II' System, CC-T-1 is operated at atmospheric pressure only. CC-T-1 can receive;the discharge from the CC-T-2 transfer pump whenever it is desired to either recycle the water for further processing, or store the purified water for future disposition. CC-T-1 may also be used as a source of processed water to supply the-NLB pump used for containment decontamination. This feature allows greater availability of CC-T-2.

CC-T-1.is piped to receive.the 'ischarge from the sump pump, if '!4 desired, but'normally the sump is drained by a 2" suction line to

. pump ALC-P-1 (see Section 2.1.8). A suction line at the bottom of l CC-T-1 can be lined up either to pump ALC-P-1 for reprocessing the

~

centents.of CC-T-1 through the system or to transfer pump ALC-P-5' for recirculation and sampling, or discharge. The recirculation line-connects to the top of CC-T-1.

CC-T-1 is vented to the building in the.same manner as CC-T-2. An l overflow line'.with'a loopseal is provided near the top of CC-T-1.

A demineralized water supply is provided for-the loop seal. A connection.at the top of CC-T-1 receives vents from the prefilter, the demineralizers and the crud filter. Level indication and high level alarm are provided on panel ALC-PNL-1.. A future xenon hold-up tank cc nection is provided on the vent line.

CC-T-1 has a 2" vent line exhausting to the CCB through a j two-stage demister filter. The first stage consists of two moisture separators and 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 controlled from power panel MP 2-33A.

2.1.8 Chemical Cleaning Building Sump  !

The CCB sump is a stainless steel lined pit with a capacity of 4000 gallons located in the northwast corner of the CCE. All leakage from the tank overflow, equipraent, and floor droins are collected in the sump. One sump pump (see Table 8) 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-AUT0) located on l MCC 2-33A. When in AUTO, the pump is controlled by conductivity type level switch ALC-LS-1 which starts and stops the pump automatically. A High Sump Level Alarm is provided on cleanup panel ALC-PNL-1.

]

The pump is started when the water level in the sump reaches a level that is 48 1/4 inches below the face of the pump mounting.

The pump stops when the level of water has been lowered to a level i

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3526-004 that is 90 3/8 inches below the pump face. The high level alarm is actuated when the water level reaches 36 1/4 inches below the

-face of the pump mounting. The. volume of water removed from pump 6

. 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 pump ALC-P-1. This permits the return of the sump water to the EPICOR II System directly from the sump without circulating-through 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 from an outlet downstream of valve ALC-V015 with a short length of hose.

2.1.9 20 Ton Monorail Holst System (See Table 9)

A 20 ton hoist is provided for removal and replacement of the demineralizers and other large pieces of auxiliary equipment in and out of the building. It is mounted on the monorail which extends'from the north side of the CCB above the resin traps l through the south end of the building, extending 18' outside of the building over the cask' loading area. l In order to minimize the radiation exposure to personnel during demineralized removal, the hoist is operated remotely using a remote pendant operating station in the TV Monitor and Control Building. Remote operation is aided through the ute of a closed circuit TV (CCTV) system with six cameras. The pendant has six l pushbuttons for trolley and hoist operation - one START, one STOP, two for north / south movement of the single speed trolley, and two for the hoist 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.

There is also a local monorail hoist pendant located on the CCB operating floor. This pendant is used for performing operations where there is little radiation exposure, such as bringing a new liner of resin into the building.

To aid positioning of the hoist remotely for demineralized

! replacement, the monorail has visible target markings above the ,

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

2.1.10 Resin Filters ALC-F-4A, B and C (See Table 3) l Three resin filters are provided downstream of pump ALC-P-4 to prevent resin fines from entering CC-T-2. If the filters contact l radiation level reaches 250 mR/hr on any part of the filter, the system must be shutdown and the filters replaced. Four sides of the filters are shielded by 8" thick solid concrete blocks. The l top is shielded with 1/2 inch of lead.

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< 2.1.11 Crud Filter ALC-F-5 (See Table 3)

~

A one. micron nominally rated filter.with isolation valves is

'provided between the resin filter and CC-T-2. The primary purpose- l of this filter is to eliminate most particulate present in the

-processed water. A vent line. connected to CC-T-1 and a drain line l to the equipment drain system is provided for draining the filter housing prior to inserting or removing a filter cartridge.

The filter is shielded by 3 1/8" 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 filter is replaced whenever the contact radiation level' reaches 250 mR/hr or when the. pressure drop reduces the process ficwrate below an acceptable value. A special lever is provided to aid in removal of the filter cartridge.

2.1.12 Ventil'a' tion Heating Unit and Moisture Separator I Heating unit ALC-E-H1 (see Table 10) is mounted on the inlet of I the. filtration unit at elevation 304' and consists of a moisture separator (ALC-E-F1) and a 60 KH 480 volt, 3 phase heater. The heater is powered from MCC 2-33A.

2.1.13 Ventilation Filter Unit The filter unit consists of a single housing containing, in order: a prefilter (ALC-E-F2) (not used), a HEPA filter l (ALC-E-F3), charcoal filter beds (ALC-E-F4) and a final HEPA filter (ALC-E-F5). A manually actuated fire protection water supply is'provided for the charcoal beds.

2.1.14 Ventilation Fan Assembly (See Tabie 10)

Fan assembly ALC-E-1 is a 30HP, 460 volt, 3 phase, 60 cycle, l 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 radiation detector) and out through the roof.

2.1.15 Ventilation Radiation Monitor (See Table 10) l This radiation monitor samples air in the fan discharge line l 1sokinetically at a rate of 4 cfn to provide local (at monitor) and remote indication on panel ALC-PNL-1 of discharge particulate 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 4.11E-2 pCi particulate or 3.81E-4 pC1/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.

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3526-004 l' 2 2.1.16 Ventila' tion Weatherproof Enclosure l: The~ weatherproof enclosure is located'at grade level.and houses t b

the components, discussed.in Sections 2.1.12 through 2.1:15. 3 2.1.17 Chemical Cleaning Building Radiation Monitors lFour area radiation monitors (ALC-RM-8 through'11) and an air-sampler radiation' monitor (ALC-RM-12) are provided in the CCB.

Radiation monitors ALC-RM-8 through 11 are provided with remote l indication on the radiation monitoring panel ALC-PNL-1 in the TV i'

Monitor and Control Building.. The air sampler radiation monitor ALC-RM-12' draws its. sample from the CCB near demineralized ALC-F-1. Remote indication for radiation monitor ALC-RM-12 is also provided on panel ALC-PNL-1. The area radiation monitors and air sampler radiation monitor 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.

2.1.18 Closed Circuit TV-System A'CCTV system is provided to aid in remote handling of the ~l 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 l mounted on the TV Monitor Console located in the TV Monitor and Control Building.

Camera No. l'is mounted on the monorail support structure outside the CCB to allow viewing of the prefilter or dem*neralizer while being loaded into the transfer cask. Camera No. 2 is mounted

'directly on the 20 ton hoist and provides a direct view of the monorail. Target markings which can be viewed with this camera are provided on the menorail to aid in the positioning of the holst. Camera No. 3 has a FAN-TILT control and is mounted.to provide a view of demireralizer 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 surveillance during system operatior., Cameras No. 4 and No.-5 provide a view of the top area of demineralizers ALC-F-1 and 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 through 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 provide remote monitoring of potential leak areas.

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2.1.19 Major. System Valves Inlet ~ Isolation Valve'ALC-V043 l One stair.less steel, 2", 120V motor-operated ball valve is installed on the inlet line from the source tank to the'EPICOR II l 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 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 demineralized. to prevent overfilling of the' vessel. -The choice of the controlling demineralized is dictated by the configuration of.the processing train through selector switch ALC-SS-1 (F-l'ON LINE or F-1 BYPASSED). If demineralized ALC-F-1:is in the processing train, its level controller will control valve L ALC-V043; if demineralized ALC-F-1 is bypassed, control of. valve l

ALC-V043 is transferred to demineralized ALC-K-1 level controller.

Service Air Regulator Valve ALC-V109 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 pressure to 80 psig.

Process Supply Line Valve ALC-V255 to Demineralized ALC-F-1 l

l l One 2" solenoid valve (ALC-V255) with a 150 lb. rating at 120*F is I installed on the line between pump ALC-P-1 and demineralized ALC-F-1 between manual valves ALC-V?91 and ALC-V207. Valve ALC-V255 is-norinally closed unless ener gized and is interlocked to close on high level in demineralized ALC-F-1. Additionally, it closes on loss of electrical power or wFen the EPICOR II System is not running.

Off-Spec. Water _ Supply Isolation Valves ALC-V08f> and ALC-V242 to ,

Pemp ALC-P-1 l

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 l 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. l Valve ALC-V242 is interlocked with valve ALC-V043 to assure that 3 1

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!' 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 avoiding

. uncontrolled' draining of either CC-T-1 or CC-T-2. The valve 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 level controller of demineralizers ALC-F-1 and ALC-K-1,-

in.the same arrangement as valve ALC-V043.

i Valve ALC-V086 is a stainless steel, 2", 120V motor-operated ball-Jvalve which is also installed on the outlet line of-CC-T-1. It is-l controlled by a manual handswitch mounted in MCC 2-33A, 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 20 Sample System A sample system is provided to_obtain a representative sample of CC-T-1 and CC-T-2 and the effluents of demineralizers ALC-F-1, 'l l ALC-K-1 and ALC-K-2.

The samples from the demineralizers and the sample obtained from the MHHT are used to determine the isotopic inventory held up on l the resin beds. The determination is made by analyzing the influent and effluent isotopic concentrations, the difference of which is held up on the bed. This information is required for shipment of the spent containers to the waste disposal site.

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

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

The saaple sink is orovided with demineralized water for the sink sprey header and bottle washing. The drain from the sink is routed to the CCB sump. The sink is also provided with l ventilation which consists of a hood and ductwork which is tied into the CCB ventilation system. l Recirculation of the sample lines from demineralizers ALC-F-1, AtC-K-1, and ALC-K-2 back to the suction of pump ALC-P-2, and the-collection of samples is controlled by solenoid valves. The ability to obtain grab samples is provided in the recirculation line for flow verification. Piping for the sample lines is 1/2"'

stainless steel tubing with compression type connectors.

NOTE: See Sections 2.1.6 and 2.1.7 for obtaining a sample from CC-T-1 and CC-T-2.

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2c1;21, Auxiliary Building Cleanup. System Air Compressors.(See Table'11)-

- Rotary air compr m ors ALC-P-7 and 8 are.provided as a. backup ~ air 3 supply for-the EE COR II System; the Plant Service Air System is-I the normal-air supply. Either of these air compressors have sufficient capacity for the operation of.the EPICOR II System.

,, These compressors are located in the ventilation unit's building.

~These compressors are-single stage rotary screw, electrically

. driven, packaged units (pre-wired and pre-plumbed) with capacities of 115 and 98.cfm at 100 psig (the compressors are not the same.-

model).

The compressors are controlled by' local hand switches which allow-the' choice of-either START /STOP (for intermittent. air demand) or-CONTINUOUS (for continuous air demand) control modes for flexibility. The units are piped so that they can be used individually when a_small-volume of air is required or in parallel to, handle larger air demands. In all of the operating modes, the

. air pressure in each unit's reservoir is automatically maintained within preset limits.

J 2.1.22'ALC-F-1' Liner Breakthrough Monttor f Radiation monitor ALC-RMI-7 is installed on the' discharge of demineralized ALC-F-1 to monitor for activity breakthrough on the-first demineralized. 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 Protective Devices, J 2.1 Cleanup System The EPICOR II. System is.normally operated and monitored from- 1 control-panel ALC-PNL-1 located in the TV Monitor and Control l J Euilding which is a separate prefabricated building. The TV Monitor and Control Building is adjacent to the necihwa t corner of the CCB.

l 1 Electrical. power is supplied to the EPICOR II System from 750 KVA l 3 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. 480V power from USS 2-33 is supplied to MCC 2-33A located inside the TV Monitor and Control Bu?1 ding. The ,

HVAC system fan and heaters, the transfer pump, building sump j pump, and the 20-ton ho!st are. powered from MCC 2-33A. A j

'480-120/208 Vac 25 KVA transformer, supplied from MCC 2-33A, )

supplies all other system electrical loads from power panel i MP 2-33A, except heat traces and pump ALC-P-8 which are supplied ]

from the control rod breaker MCC 2-43.  ;

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The-EPICOR II. pumps are controlled thtough an automatic control unit which provides AUT0/ MANUAL on-off switches and indicating l lights for the pumps, demineralized hign level alarms,'and an 6

ON/0FF switch for the unit. ' Control power is provided for the.

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

All. process instrumentation monitored in the control center is mounted on cleanup panel ALC-PNL-1. Audible alarms and indicating lights are provided on this panel for CCB Sump High Level,'CCB Ventilation-System Trouble, CCB Charcoal Filter High Temperature, CCB High Exhaust Radiation Level, CCB Radiation Monitor Failed,

. Building Radiation Level, and demineralizers ALC-F-1, ALC-K-1 and l

2 Loop Seal Flow. Remote indication is provided for the area radiation monitors and the air sampler on the radiation monitoring panel located adjacent to the cleanup panel.

2.2.2 Ventilation System 2.2.2.'1 Heating Unit and Moisture Separator The moisture separator is instrumented with a differential pressure indicator and switch, ALC-DPI-11 and ALC-DPS-11, respectively. The heating unit.(ALC-E-H1) is provided with a l temperature indicating controller and a high temperature switch.

The temperature indicating controller functions to maintain the heaters energized providing a heater outlet air temperature of no more than 146*F. If the air temperature l rises to 160*F, the high temperature' switch will automatically deenergize the heaters. If the heaters are to be reenergized, the reset but ton must be depressed when air temperature at the thermocouple drops below the 160*F temperature switch setpoint.

Indication of opera N n of the temperature indicating controller and high temperature switches are provided on the switches, both of which are located in the heater control panel near the heaters on the filtration unit.

elanual energizing /deenergizing of the heater control panel occurs at MCC 2-33A. The heater panel is also de-energized. .

automatically shmid the system ventilation faa trip or in any other way fail to maintain minimen flow at the fan discharge flow switch.

A red light on the heater controller panel indicates power available to the heater control panel.

Rev. 7/0185P

3526-004 4 '4 2.2.2.2 , Filter Unit Differential pressure indication is provided for the filter

. unit's prefilter (ALC-E-F2). While a differential pressure indication (ALC-DPI-il) is provided locally, a differential-pressure switch (ALC-DPS-11) will actuate a remote " Trouble" alarm warning _the operator of-a restricted flow condition

~

existing in the prefilter. (Note: The prefilter is repl. aced l.

when it exhibits a pressure drop of 1" 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 warns 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-TS-15-1 set at.250*F) will l actuate a local amber light, a remote high temperature alarm and a horn warning of increasing temperature in the charcoal-bed. ~At 300'F, remote common " Trouble" and local red light-alarms will be actuated from switch ALC-TS-15-2 indicating a Hi Hi temperature condition exists in the bed.

Indication of operability of the fire detection system is 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 controller (ALC-DPI-14). This is not connected.

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 ]

(ALC-DPI-16), the reraote " Trouble" alarm is actuated on a high l HEPA filter differential pressure of 3" w.g. by the locally -

" mounted differential pressure switch (ALC-DPS-16). l l 2.2.2.3 Fan Assembly The fan assembly, as previously noted is interlocked with the I 60 KH heater. A control interlock is provided through the fan and heater circuitry such that the heater may not be energized unless the fan is running. A flow indicating switch 1 (ALC-FIS-17) on the discharge of the fan provides a safety l interlock: if the filtration unit is operating and the discharge flow of the fan falls below 4,000 cfm, the heater 4 and fan monitor will trip. Switch ALC-FIS-17 is also tied l ,

into the common, remote panel mounted " Trouble" alarm. The fan is started and stopped from MCC 2-33A.

j Rev. 7/0185P l' i

_.._______...____1- - - - _ _

3526-004 2.2.2.4 Radiation Monitor (Controls)

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

Local indication of the ventilation exhaust particulate and/or gaseous activity level is provided on the monitor. At a radiation level of 4.llE-2 pCi particulate or 3.81E-4 pCi/cc, noble gas the High Radiation alarm will sound on the panel in the control shed.

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-D1 and D2 are checked open and the radiation monitor is energized and operational.

When the fan is started (at MCC 2-33A), sufficient air flow will  !

exist (approximately 4000 cfm minimum) through the unit prior to energizing the heaters. After startup, ventilation unit temperature, flow, and activity indications are verified normal before the unit is left unattended.

3.1.2 Cleanup System Initial startup of the EPICOR II System is with the demineralizers empty of liquid, The CCB Ventilation S3 stem shall be in operation prior to operating the EPIC 0rt II System.

Normal startup of the EPICOR II System is accomplished by supplying the system wtth the process feedwater from CC-T-1, CC T-2, or the varloes source tanks. Except for the MWHT, the l process feedwater is delivered to the process stream by source tank's motive power systen. If MWHT is the feedwater source, the l supply header is primed initially. Dependirig on the source of the 4 process feed, the feed supply valve (e.g., ALC-V043 or ALC A.'242) is then opened and process pump ALC-P-1 started. Startup of pump l ALC-P-1 is accomplished by opening the air supply valve ALC-V0ll, stop valve ALC-Vl85 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 demineralized ALC-F-1.

When demineralized ALC-F-1 is full, pump ALC-P-1 will stop automatically on high level. Similarly, process pump ALC-P-2 is <

operated until demineralized ALC-K-1 is full, then pump ALC-P-3 is l j operated until demineralized ALC-K-2 is full. As soon as the 1 Rev. 7/0185P j l

)

3526-004 demineralizers are full, processing is then commenced by starting pump ALC-P-4 and opening discharge valve ALC-V277. Using the process pumps respective control valves (ALC-V260 through 4 ALC-V263), the pump speed is adjusted to maintain a balanced flow l of about 10 gpm through the demineralizers.

NOTE: The initial batch quantity will be determined by the efficiency of the demineralized resin charge and may require a change in resin composition and/or flow rate to effectively process the radioactive waste water.

3.2 Normal Operation 3.2.1 Ventilation System During normal operation, the ventilation unit requires little operator action. The unit will be periodically checked to ensure that indication is operable and that temperatures, flows and radiation levels are within the normal ranges.

Increasing differential pressures across the moisture separator a.nd HEPA' filters are an indication that the components are retaining dirt, etc. These components will be replaced as l required to ensure that flow through the ventilation unit is maximized.

The radiation monitor and recorder will be checked periodically l and reviewed for evidence of trends indicating that increasing levels of activity are being discharged. A trend showing increasing discharge activity levels is indicative of carryover from the filter unit and will be treated accordingly.

3.2.2 Cleanup System Once the flow rate is established for the process, the system cperates automatically by starting and stopping the pumps (ALC-P-1 through 4) in order to maintain the proper level in the process v^ tanks. Instrumentation is provided on the control panel to monitor system parameters and to l'alance the system to minimize pump cycling.

When a desired volume has been reached in CC-T-2, transfer pumo ALC-P-5 is started to recirculate at least three tank volumes of water through CC-T-1 after which a tample is Grav.n for analysis by l the TMI water chemistry letoratory. Water acceptable for use in the plant will be pumped to the TMI Unit 2 Liould Wiste Disposal System, CC-T-1, CO-T-1A or to the PWSTs. Out of specification l water will be pumped to CC-T-1 for reprocessing (See Sections l 2.1.6 and 2.1.7) or it will be processed directly from CC-T-2 under a feed and bleed scheme. >

Rev. 7/0185P l

3526-004.

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 l of the ventilation system will preclude filtration and monitoring of the. air and will not.be performed unless dictated by other- l casualty / operational considerations. To shutdown the ventilation'.

unit, the 60 KH heaters, fan (ALC-E-1) and radiation monitor are.

de-energized.from their respective breakers in MCC 2-33A.

3.3.2 ' Cleanup System

'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 l shutdown the system upon completion ~of processing a batch.-the pumps 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 l of the third demineralized to CC-T-2.

The system is shut down and the affected unit replaced when radiation monitors on any of the demineralizers indicate the unit has collected a quantity of' material which is limited by shipping regulations, or system sampling indicates that the resins are exhausted chemically. To replace one 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 demineralized to the outside of the CCB'to the transfer cask. The replacement unit is then l installed,'the hoses, the level probe cable and the bubbler line reconnected and the system started as described in Section 3.1. l Each liner.has its own level probe which will be discarded with the liner.

3.4 Special or Infrequent Operation 3.4.1 -Filter Charege-out When a filter bank rc-quires changing, the EPICOR 11 System will be shutdown. The ventilation system will be shutdown during the filter change-out.

3.4.2 HIC / Demineralized Dewatering and Drying i The Zeolite Resin Drying System dries process media (i.e., zeolite resin, activated carbon and/or sand) in a 50 cu. ft.

HIC / demineralized for transportation and disposal at a low level waste disposal facility.

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3526-004

[ .This is accomplished in a three (3) step process.

of the free water is removed using procedures associated with HIC First, the bulk installation and removal.in the EPICOR II System and the Defueling

. Water Cleanup System (DHCS).. .Second, the drying unit's sandpiper is started and its blower is energized to recirculate air down through the media. The air is heated as it passes through the blower and as thisiwarm dry air passes through the media it entrains and vaporizes' moisture. This warm air then passes through the entrainment separator, enroute to the blower inlet, where refrigeration coils condense the water vapor in the air and any entrained water is removed. 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 order 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. storage and shipment.

Air is circulated up through zeolite resin for 12. hours or in the

. case of 6ctivated 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 (.ontainer 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 .l from the separator tank but, for the most part, maintains the l process under a vacuum thereby minimizing the potential spread of contamination due to hose / connection leaks. The excess air I removed by the dewatering pump is directed through a filtered drain path / container approved by Radiological-Controls personnel. l The drying system is a skid mounted unit which provides the mobility necessary to dry HIC /demineralizers at their respective locations (EPICOR II/DHCS), versus relocating the liners to a l central' area. This will reduce the amount of person-rem exposure generally received when handling radwaste processing liners. The services required for drying operations are 480 VAC (standard 4 pole weloing receptacle), 100 psi service air and demineralized water or processed water needed to fill and flush the system.

o

'3.4.3 Remote Closure Device l

!. The remote closure device is designed to provide a safe and l l efficient means of sealing an EPICOR II or DHCS HIC /demineraitzer l L to meet the requirements for disposal at a low level waste disposal facility.

Performing this operation (installing the ENVIROALLOY lid) to a 1- HIC / demineralized 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 I head with the HIC / demineralized is performed using the CCTV cameras and monitor. Maintaining proper alignment is important so Rev. 7/0185P

'3526-004

  • that(theeightwedgesaredrivenevenlyintotheirrespective holes on top of the HIC / demineralized. 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.

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, and the CCB sealed.

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 supply lines fail closed on loss of power. Valves ALC-V043 and V086 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 through the system is from the MWHT, operator action is required to close valve HDL-V2628. Power will be lost to the CCB Ventilation System 60KW heaters, exhaust fan and radiation monitor.

On loss of power to the MCC 2-43 supply, backup air supply and- l heat traces.will not be available.

When electrical' power is lost, all automatically controlled equipment will. be placed in the manual 0FF position. When emergency power is available, the system will be restarted.

3.5.3 Loss of System Air-Loss of system air will cause the EPICOR II pumps to secure until either the sysu m compressors c.an be put into service or the Service Air System can be returned to service.

!!O_TE_: EPICOR II uses in-plant service air as normal supply air.

3.5.4 Fire 3.5.4.1 Venti 3ation System Tne charcal absorber beds in the ventilation: unit ignite upn high temperature. Upon verification of ignition of the charcoal bed, the manually actuated fire protection spreys will be cut in.

l.

3.5.4.2 Cleanup System If a fire occurs in the TV Monitor and Control Building the sprinkler system will automatically initiate.. The CCB is provided with a hose station on the mezzanine for manual l firefighting.

Rev. 7/0185P u__=__________ - . _ _ _ _ _ _ xi

3526-004 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 l environment without proper authorization. l The CCB Ventilation System will process potentially contaminated air. As such, any operations or maintenance associated with the system will fully incorporate appropriate Health Physics guidelines / requirements. Any solid or liquid ventilation system waste will be sampled and cleared by l HP before release to the environment.

Positive verification of a charcoal bed fire will exist before manual initiation of fire protection spray system since water will damage the charcoal bed.

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

Flushing will be exercised when maintenance is performed.

l l

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Rev. 7/0185P u21____ _.___ _ l

3526-004 TABLE 1 l EPICOR II PUMPS Pump Details l

Identification ALC-P-1, 2, 3, 4 Number Installed 4 L

Manufacturer Warren Rupp Co.

Model No. SA 2-A ,

1 Type Double opposed diaphragm ,

.I Maximum rated capacity at 90 psi air supply 120 gpm at 45 ft of head i Operating point capacity at 90 psi air supply 20 gpm at 170 ft of head Max. air pressure 125 psi Lubricant Oil I l

I l

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3526-004 TABLE 2 TRANSFER PUMP Pump Details Identification ALC-P-5 Number Inst 211ed 1 Manufacturer- Ingersoll Rand Model No. 3 x 2.x 10 Type HOC, Group 2, ANSI A60 Type Horizontal Centrifugal Standard Material Designation Col. DI Rated Speed 1750 rpm Rated Capacity 200 gpm Rated Total Dynamic Head 100' Shutoff Head 121' Design Pressure, Casing 200 psig Design Temperature 110*C Lubricant SAE 20 or 30 Oil Motor Details Manufacturer Gould Century Elect. Div. ,

Type F-C Enclosure TEFC Rated Horsepower 10 HP Speed 1700 rpm Lubricant / Coolant Grease / air Power Requirements 480V AC/12.5A, 3 Phase, 60h2 Power Source MCC 2-33A Rev. 7/0185P

3526-004 ,

. . 1 TABLE 3 FILTERS  :

Resin Filters (Traps)

Tank Details Identification' ALC-F-4A, B, C i i

Number Installed 3 Manufacturer Capolupo & Gundal, Inc.

]

Installation Horizontal i i

Outside diameter and height 10" x 28" l Shell material . PVC Design pressure 100 psi 1

Crud Filters Identification ALC-F-5 Number Installed 1 i

Manufacturer of Housing Pall Trinity Micro Corp.

1 Installation Vertical Outside diameter and height 7" x 34" ]

1 Shell. thickness 0.165" j i

Shell material SA-312 TP304 Design pressure 150 psi

)

Particle size rating 1 micron., nominal i

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3526-004

.. TABLE 4 DEMINERALIZERS Tank Details Identification ALC-F-1, ALC-K-1, ALC-K-2 Number Installed 3 Manufacturer EPICOR Installation Vertical Outside diameter and height 4'x4' or 6'x6' Shell thickness 1/4" Shell material Carbon Steel Design pressure 2 psi OR Identification ALC-F-1 Number Installed 1 Manufacturer Nuclear Packaging Inc.

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

. Design pressure 10 psi l

j Rev. 7/0185P I

L 3526-004 l 1

TABLE 5 I MISCELLANE0US WASTE HOLD-UP TANK i

Tank Details l

. Identification WDL-T-2 ,

Manufacturer Richmond Engineering Co. Inc.

Capacity 19,518 gal. l Installation Horizontal ]

1 Outside diameter and length 10' - 9 1/4"; 32' - 4 5/8" Shell material SA-240, 304 S/S f

Shell thickness 3/8" Design temperature 150*F Design pressure 20 psig l

Corrosion allowance 0" j J

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

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3526-004 4 j

TABLE-6 i

CLEAN WATER RECEIVING TANK

  • Tank Details  !

l Identification CC-T-2 I

Number Installed 1 Manufacturer Chicago Bridge & Iron Co. I Capacity 133,689 gal.

Installation Vertical i

Outside diameter and height 25'; 35' i Shell material 304 Stainless Steel Shell thickness 3/16" to 3/8" Design pressure Atmospheric Corrosion allowance 0" Code stamp required No Rinse Hold Tank for Once Through Steam Generator Chemical Cleaning System i

Rev. 7/0185P

3526-004 TABLE 7 0FF-SPEC. WATER RECEIVING / BATCH TANK

  • Tank Details I Identification CC-T-1 Number Installed 1 Manufacturer Chicago Bridge & Iron Co.

Capacity 85,978 gal.

Installation Vertical Outside diameter and height 21'-10"; 39'-0" Shell material 304 Stainless Steel Shell thickness 13/32" to 11/16" Design temperature 250*F Design pressure Full vacuum to 75 psig i

Corrosion allowance 0" Code stamp required Yes I Chemical Cleaning Solution Tank for Once Through Steam Generator Chemical l Cleaning System j l

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3526-004

.T_ABLE 8 SUMP PUMP CHEMICAL CLEANING BUILDING Pump Detail Identification CC-P-2A Number Installed 1 Manufacturer Gould Model No. 3171 Type Vertical Rated speed 3600 rpm Rated capacity 100 gpm Rated total head 250' Min. Submergence required l' Design pJessure, casing 150 psig Design temperature 450*F Lu5ricant Water Motor Details Manufacturer General Electric Type Vertical Induction Enclosure TEFC Rated Horsepower 20 HP Speed 3600 rpm Lubricant / Coolant Grease /Al' Power Requirements 480V AC, 3 Phase, 60 HZ Power Source MCC 2-33A Rev. 7/0185P j

_ - _ - _ _ _ _ _ _ - _ - _ _ _ _ _ _ - .l

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< -l

., 3526-004 TABLE 9 MONORAIL HOIST SYSTEM Number Installed 1 Manufacturer Harnischfeger, Inc., P&H Model '#36CS23E Capacity 20 ton Total Lift 25'-6" Speed Holst 20 fpm maximum (90% load) 10 fpm medium 5 fpm low 1 fpm creep Trolley 50 fpm Control Holst Quad - Speed Trolley Single Speed Power Supply 460 V AC, 3 Phase, 60 Hz MCC 2-33A Control Voltage 110 V AC Control Station Local and Remote six pushbutton pendant control; deadman type element control Reeving Four part single reeved i

Rev. 7/0185P N_______-____-_

I 3526-004 l TABLE 10 CHEMICAL CLEANING BUILDING VENTILATION SYSTEM NAMEPLATE DATA MSA Filter Unit Identification No. ALC-E-H1 60KW Chromolax Heater Unit 480 solts AC, 3 Phase, 60 Hz Cat. Number SCCP-080-3480 Type J 0-800 *F Temperature Controller Type J 0-800 'F High Limit with Manual Reset Internal Industrial Fan Identification No.'ALC-E-1 8000 cfm Fan Unit 30 HP 460 volts AC,.3 Phase, 60 Hz 10 Number P28G353G-G7-XD Eberline Ping - 2A Off Line Effluent Monitor 3 Channel Readout - gaseous, particulate, iodine 110 volts AC, 1 Phase, 60 Hz Self contained sample / return pump (4 cfm) i I

Rev. 7/0185P

_ _ _ _ . _ _ _ _ _ _ _ _ . . _ . . _ . _ _ _ 1

3526-004 TABLE 11 AIR COMPRESSORS Identification ALC-P-7 ALC-P-8 Number Installed 1 1 Vendor Le Roi (Dresser Industries Inc.)

Type Single Stage Rotary Screw Model No. 305S 25SS Capacity (cfm at psig) 115 at 100 98 at 100 110 at 125 (Max.) 95 at 125 (Max.)

Rated Motor 30 HP at 1755 rpm 25 HP at 1760 rpm Power Source 460V, 3 Phase, 60 Hz 460V, 3 Phase, 60 Hz MCC 2-33A Power Panel PDP-W2 Rev. 7/0185P  !.

- _ _ _ _ _ _ _ _ _ - _ - _ ._ ._O

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3526-004

~j TABLE 13 l l

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_ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ __ _ - - - _ _ _ __ _ _ _ __ _ _ _ _ _ _ - _ . - - . _ _ _ _ _ _ _ - - - . _ _ _ _ _ _ _ _ _ - - - . _ _ _ _ _ _ _ _ _ _ - - - - _ - - - - _ _ __ __ ________-------------u

l 3526-004 TABLE'14 DELETED Rev. 7/0185P

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