ML20235J638

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Rev 6 to Submerged Demineralizer Sys, Sys Description
ML20235J638
Person / Time
Site: Three Mile Island Constellation icon.png
Issue date: 08/31/1987
From: Buchanan D, Eichfeld S
GENERAL PUBLIC UTILITIES CORP.
To:
Shared Package
ML20235J576 List:
References
3527-005, 3527-005-R06, 3527-5, 3527-5-R6, NUDOCS 8710020038
Download: ML20235J638 (394)


Text

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, D une- ,, DIVISION SYSTEM DESCRIPTION l FOR Submerged Demineralized System I ( l COG ENG d O cPeAAA0 7e gwqo RTR 10 be 35 8-3/-87 c=eemee9 P E X , om sug., ie 8 5 3 W DOCUMENT PAGE 1 OF 8710020038 870928 DR ADOCK O gO 3

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No. l [C NI 3527-005  ; Tith System Description.for the ' Pa ge . of  ! Submerged Demineralized System' 2- _l 1 Rev. *

SUMMARY

OF CHANGE. Approval' Date , i

                                                                                                                             ~i 0     Initial issue per GPU' Nuclear letter 4400-82-L-0017.                     2/82-l 1     Updated per GPU Nuclear letter 4410-83-L-0018.                           '4/83; 2     Updated per GPU Nuclear letter 4410-83-L- 0154.                           6/83 i 3     Updated per GPU Nuclear letter 4410.'84-L-0030.                           7/84 Incorporates changes made by ECMs S-1163 (Revision 0                               (

through 3),1100 Revision 0,1140 Revision 0,1237 1 Revision 0,1058 Revision 2,1151 Revision 0,1161 Revision 0,1157 Revision 0,1159 Revision 0, and 1141 Revision 0. J 4 Annual Update. 8/85 l I incorporates changes by S-ECM 1110 Revisions 0 ar.d I; d ECAs 072, 042, 047, 041, and 1.02. 5 Annual Update. 8/86 Incorporates changes made by S-ECM 1058 Revision 2; ECAs 041, 072, 087, and 312. 6 Annual Update. 9/87 Incorporates updates to the valve and component lists; updates historical data, deletes the Early Defueling DWC Reactor Vessel filtration. System which is no longer applicable, f

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THREE MILE ISLAND - UNIT #2  ;

i i SYSTEM DESCRIPTION  ! 1 OF THE-jjlBHERGEDDEMINERALIZATIONSYSTEM (SDS) i I 1 1 I l \ l l l

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SD 3527-005 TABLE OF CONTENTS FOR l SUBMERGED DEMINERALIZATION SYSTEM Section 1.0 Introduction , 1.1 System Function 1.2 References 1.3 Summary Description of System j 1.4 System Performance Characteristics i 1.5 System Arrangement and Interfaces 1.6 System Design Requirements  ; 2.0 Detailed Descri'< tion of System 2.1 System Components l 2.1.1 System Pumps 2.1.2 System Tanks -- - - 2.1.3 Filtration / Demineralization Units 2.1.4 Manifold Containments < 2.1.5 Off Gas Ventilation i 2.1.6 Major System Valves 2.1.7 Dewatering Station 2.1.8 Remote Operating and Manipulating Tools 2.1.9 Sampling Devices 2.2 Instruments, Controls, Alarms and Protective Devices 2.2.1 Instrumentation and Controls 2.2.2 Alarms i

                                                              ,                                                 7 g lSD 3527-005' LSection'                                        ,

3.0- Submerced' Demineralized Systemi

                                               -Modes of Operation
                                . 3.1           Off Gas System.

3.1.1 System Startup-- 3 .1,. 2 SistemOperation f

                                .3.1.3          System Shutdown 3.2           System Operation-
                                '3.2.1          tiltration Operation Startup 3.2.2         Normal _ Operation 3.3           Processing'the Filtered Water 3.3.1         Processing System Startup 3.3.2         Processing System Operation 3.3.3         Processing System Shutdown.

3.4 Special. Evolutions-3.4.1 Cation Vessel Change Out 3.4.2 Leakage Containment 3.4.3 Ventilation Filter Replacement 3.5 Transfer of Hater from SDS to.EPICOR II 3.6 Staffing Levels 3.6.1 System Operation 3.6.2 System Outages 4.0 Abnormal Operating Conditions and Emergency Events l 4.1 Types of Events Considered 4.2 Abnormal Operating Conditions-4.2.1 Loss of SDS Off-Gas System 4.2.2L Leakage from SDS into the Spent Fuel Pool' 4.2.3- . Loss of Instrument Air J 4.2.4 Loss of Electric Power l l 33

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                                                                                                 'i SD 3527-005-
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Section l 4.3 Emergency Events 4.3.1 Fire i 4.3.2 Vessel Drop in the Spent Fuel Pool j 4.3.3 Cask Drop 4.3.4 Man in the "B" Spent Fuel Pool j 5.0 Maintenance i 5.1 Maintenance Approval 5.1.1 Instrument Maintenance and Calibration Approval 5.1.2 Pump Maintenance- 1 l 5.1.3 Valve Maintenance i i 5.1.4 Hansen Coupling Maintenance

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5.2 Corrective Maintenance l 5.2.1 Retesting Requirements 5.3 Preventive Maintenance and Inservice Inspection j 5.3.1 Preventive Maintenance  ; 5.3.2 Inservice Inspection 6.0 Acceptance Testina 6.1 Construction Testing 6.2 Cold Functional Testing 6.3 Hot functional Testing 6.4 Ancillary Testing Figure 1 Arrangement of SDS Figure 2 Processing Logic Plan Figure 3 Allowable AP Across Single Sand filter Table 1 Liner Radionuclides Loading Criteria Table 2 SDS Components Vents and Drains 111 L__-_-____________-____-- _ _ - _ -

SD 3527-005-

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APPENDICES Title Number SDS Pumps / Blowers 1 SDS Filter Vessels 2 SDS Demineralized Vessels 3 Deleted 4 SDS Monitor Tanks 5 i SDS Off Gas Separator Tank. 6 ) l Instrumentation and Conte Index 7 Typical Analysis of Hater Processed 8 SDS Drawing List 9 SDS Valve List 10 SDS Procedure List 11 q Reactor Building Basement Jet Pump System Description 12 Process Program Limiting Parameters 13 Honitor Tank System Description 14 SDS Off Gas filters 15 ] Liner Recombiner and Vacuum Outgassing System 16 Deleted 17 fuel Transfer Canal Draining System 18 fuel Transfer Canal Shallow End Drainage System 19 Deleted 20 l l l iv e

SD'3527-005

                .l.0'     Introduction.

1.1 System Function's The Submerged Demineralized: System (SDS) _is a . temporary liquid'radwaste. processing. system designed to. reconcentrate _the fission productsc

contained in the waters in the Reactor Building & Sump, the. Reactor' l . Coolant System and other. liquid waste systems'(WDL, etc.), reducing the fission product levels to a level acceptable.for final treatrant.

through the Epicor II System. -To accomplish this~ decontamination' process, the SDS has been designed to perform the following basic functions: I a) To decontaminate, by demineralization, the contaminated waters contained in the Reactor Containment Building and the Reactor. Coolant System at TMI-2 to a level acceptable for. processing through Epicor II. b) To transfer the decontaminated waste water'from the Submerged Demineralization System to the Epicor II System or recycle back to the RCS Manifold for further processing.to further reduce-radionuclides concentrations in the water, c) To provide a location in the spent fuel pool for temporary storage of the spent high activity ion exchange vessels to take advantage of the shielding provided by the pool water. 0396B/LC w___-_--_=__________--____

r SD 3527-005 d) To provide for the underwater loading of the spent vessels into their transport casks and the preparation for shipment of these casks. e) To p ovide the capability to control, monitor and treat gaseous effluents prior to release to the atmosphere to meet the imposed requirements of Appendix B of the THI-2 Interim Recovery Technical Specifications. f) To provide for the installation, testing, operation, and maintenance of the Submerged Demineralization System in compliance with "as low as reesonably achia/able" radiation doses to personnel. g) To process the radioactively contaminated waters independent from the operation of TMI Unit 1. Decon; amination and decommissioning of the SDS will be treated in a separate document. 1.2 References 1.2.1 Epicor II System Description 1.2.1.1 B&R Dwg. M-006 1.2.1.2 B&R Dwg. M-013 0395B/LC

l SD 3527-005

                -1.2.1.3     B&R Dwg. M-015 1.2.1.4     B&R Dwg. M-208 l

1 1.2.2 Radwaste Disposal System Description 1.2.3.1 Reactor Coolant Liquid System Description 1.2.3.2 Miscellaneous Liquids System Description 1.2.3 SDS Technical Evaluation Report I 1.2.4 SDS Design Criteria 1.2.5 SDS Process Control Programs 1.2.6 Reference Drawings Burns & Roe Drawing 2076 Chem-Nuclear Dwg. 527-D-A-5001 Burns & Roe Drawing 2027 . Chem-Nuclear Dwg. 527-D-A-5002 Burns & Roe Drawing 2045 Chem-Nuclear Dwg. 527-D-A-5004 Burns & Roe Drawing E-032 Chem-Nuclear Dwg. 527-D-A-5006 i Burns & Roe Dwg. 2007 Sht 2 of 2 Chem-Nuclear Dwg. 527-D-A-5009 l l Burns & Roe Dwg. 2012 Sht 2 of 2 Chem-Nuclear Dwg. 527-D-A-5011 , 1 Burns & Roe Dwg. 2014 Sht 2 of 3 Chem-Nuclear Dwg. 527-D-A-5013 1 Burns & Roe Dwg. 2026 Chem-Nuclear Dwg. 527-D-L-5026 Burns & Roe Dwg. M043 Chem-Nuclear Dwg. 527-0-L-5027 l Burns & Roe Dwg. M323 Chem-Nuclear Dwg. 527-D-L-5031 0396B/LC 1 ___ __-__- _ A

SD.3527-005~ Bechtel Dwg. 2-M74-SDS01 Chem-Nuclear Dwg. 527-D-L-5032 Bechtel Dwg. 2-M74-PH01 Chem-Nuclear Dwg. 527-D-L-5033 Bechtel Dwg. 2-M74Y-DHCO3 GPUSC Drawing 2R-950-21-001 Chem-Nuclear Dwg. 527-D-L-5034 GPUSC Drawing 2E-950-02-001 GPU Nuclear, Recovery Support Engr. Dwg. RSE-027-l t 1.2.7 DHCS TER and System Descriptions I 1.3 Summary Description of the System The Submerged Demineralized System (SDS) is a temporary liquid radwaste processing system located in the TMI-2. "B" Spent fuel Pool and the area immediately adjacent to the spent fuel pool. The system is designed to reconcentrate the fission products contained in the Reactor Containment Building & Sump, the Reactor Coolant System and other liquid systems such as HDL, etc. by the process of ion exchange. l l The Submerged Demineralized System utilizes a number of other systems l to perform its various functions. These include:

1) The Reactor Building Basement Jet Pump System (SHS-P-1) as described in Appendix 12;
2) The Reactor Coolant Bleed Tanks and installed plant piping as depicted and described in Reference 1.2.2.

l l 0396B/LC

SD 527-005

3) The Epicor-II System as-described inlEpicor II-System Description-
                               .as a polishing and sodium removal subsystem;.and.
                      '4).    :The Processed Water Storage Tank ~ System
5) . The Spent Fuel Cooling. System piping.

6). The miscellaneous Haste Hold-up Tank and associated piping.-

                      '7)'      Fuel Handling, Building'HVAC, Electrical,.and Instrument Air 1

Systems

8) The Fuel Transfer Canal Draining System as described.in Appendix No. 18 l
9) The Fuel Transfer Canal Shallow End Drainage System as described in Appendix No. 19
10) The DHC fuel Transfer Canal / Spent Fuel Pool Cleanup System as described in Reference 1.2.7.

The Reactor Building Basement Jet Pump System-(SHS P-1) will be utilized as the primary'means of de'11vering water from the Reactor. Building Sump via penetration 626 through the SDS prefilter and final-filter to the SDS jon-exchange trains.

                                                                                       '0396B/LC L_____._____ _ - _ _

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                                                                           'SD 3527-005 ij The pump is operated from the: control. panel-(CN-PNL-1)Jwhich is' located'                 l on the SDS cask support platform spanning'the'"B" spent fuel; pool,
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This panel is' located in close proximity.to the,SDS Filter Mant'fo' which contains theLvalves for operation of-the filter system'and thel pressure and. differential ~ pressure instrumentation which provide an-

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indication of flow from.the Reactor Building Basement Jet pump and the L mechanical condition of the filters. SDS process. flow is filtered prior to processing.through the ion exchange trains. The' purpose of the #ilters is.for removal of gross size particles-from the process stream to' prevent plugging of the ion: exchange beds. The process water can be directed to either zeolite train "1" or!. zeolite train "2" or both trains simultaneously. Our present plans are to process through one. train'at a time during sump water and.RCS. processing operations. Process sampling capability is provided.to enable determination and evaluation.of bed performance. based on influent and effluent sampling- . From the train 1 or train 2 exchangers the process fluid is directed into a common line which directs the flow to either " cation" sand-filter "A" or " cation" sand filter "B". This feature allows the final vessel to be removed from operation by switching to-the standby vessel  ! l without shutting the system down for' change out', if desired.. 'i 1 l 0396B/LC 1 l j

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SD'3527-005 The ion exchanger and1 filter vessels are contained in~ secondary 1 containment boxes located'approximately 15 feet ~below the surface of- l the pool water. The-containment boxes have' slotted openings'in the. q l- containment box lids. This feature fulfills:a two-fold purpose;.1) it I

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allows the lids to close around the remote handling tools and 2)~it allows pool' water to flow.into the top of the' containment box,.over-and () around the 11guld disconnect coupling and out through the bottom of the l containment box, into a common h'eader for transport-to'the pool-cleanup j i ion exchangers. The effluent of:the leakage ~ containment ion;exchangers 1 1 is returned directly.to the pool. j lH

                                                                                             ,1 from the effluent of the system, the water passes through a .0.45=                       i micron (3 micron absolute) filter which has.been placed in the process stream to trap small resin fines which could be carried through the-j resin retention screens contained in each ion exchange vessel. The a

filter contains a differential pressure indicator-(CN-DPI-PF01) to provide indication of particulate build up. During some phases of the j l cleanup, the post filter may be.bypasted, and replaced by a sand filter I in the cation position. j i from the effluent of the resin trap post filter or " cation" sand filter, the SDS processed water is sent through a common' header wht'ch  ! allows it'to be directed to the Fuel Transfer Canal, Spent Fuel Pool 1 "A" or any of the following tanks: i L 0396B/LC l l

i',

                                                                                  .S'D 3S27-005:
                 -1)l , The Reactcir l Coolant Blee'd Tanks z2). TheMiscellaneousWasteH$1d-UpTank-s)~     The"SDS' Monitor Tanksi

, .c . m l!- 3 From.these tanks.the SDS processed water.will either be recycled.b'ack'- L , through:SDS',~ undergo further procesting via the EPICOR IILSystem l'ocatedin'theChemical'CleaningBuildl'ng,or'berecyciedba.ckuto;the

                 'RCSc                                                        ,

The EPICOR-II, system is described separately in EPICOR-II SYSTEM DESCRIPTION."'The function of EPICOR-II in the.SDS Pro (essing scenario Listoremove'sodiumwhichise,prmrequisiteLtotheremovalofTantimonyy (Sb-125);- This< sodium'removalwill'bepeEformed[fn.thefirstorsecond: s f,PICOR-II liner. The'last EPICOR-II.1,iner will be used to polish thel remaining-_ residual radionuclides from the water. .After proccssing the

                 >30S( the EPICOR II-effluent is sampied ptlor to being~ pumped to the Processed Water Storage-Tanks (two 500,000_gallonitanks) and retained               ,

l' for future disposition. I: Th6 Submerge'd Demineralized System contains,1 as an-integral part of the System, an H3A off. gas. unit. This unit. consists of a 1000 cfm blower

                 -taking suction ths'ough a roughing filter, two HEPA~ filters and a charcoal absorber filter. The'off gas system also contains an off gas separator tank with a demister for.the removal-of entrained moisture in the off gas. stream prior to treatment by the off gas' unit'.

1 I l 0396B/LC' c _ -__ _ _ -

y <

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                                                                                                    ;50'3527-005      l e           '

The off gas separator tank is a 590 gallon tank. located in the Unit 2

                                 - "C"   spent fuel pool surgeLehamber. The off gas. separator tank is- piped       j j

to a stand pipe, also located-in'the surge chamber,:which contains the off gas bottomi. sump pump.(S27-G-02). Moistuie from vaEiou's operational functions performed during system operations, i.e., vessel: q filling. operations, dewatering operations, sampling operations, leakage.

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collection from the' manifold boxes,:and water removed by the 1ntegral-demister is collected.in'the' tank with tank-level indication displayed. on CN-LI-VA03. Automatic level control instrumentation = indicates the tank level and by operator action transfers the collected water to th'e RCS Manifold. The off gas system discharges into the fuel handling. , building HVAC System.

                                                                                                                    'I Included in the system installation are two (2) 12,000 gallon' monitor tanks which are installed in the FHB model room on the 305' elevation.

These tanks will be used for either storing processed water to be used

                                  .in flushing of the system prior to vessel change out or for storing SDS Processed Hator. The monitor tanks system includes pumps (SDS-P1A &

SDS-PIB) and level instrumentation (SDS-LE1 & LE3..SDS-LT1 & LT3) The system may be operated locally or remotely from th'e SDS operating area located on the 347'-6" elevation of the fuel handling building. The design of the Monitor Tank System is such that it'could be used for 4 temporary hold-up of the SDS effluent should processing dictate.that this would be advisable. The monitor tanks are accessed from the effluent of the resin filter by installed valving. The Monitor Tank' System is further explained in the Monitor Tank System Description, )

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Appendix 14 of this document. l 0396B/LC Ri

SD 3527-005 1.4 System Performance Characteristics The basic water processing strategy utilizing 505 for the decontamination of the Reactor Building Sump Water (625,000 gallons) the Reactor Coolant System (90,000 gallons), the fuel Transfer Canal and water accumulated in RCBT's or MWHT incorporates the SDS in combination with EPIC 02 II. The clean-up or reconcentration of fission products is accomplished by demineralization and is enhanced by filtration of gross size particulate matter in the SDS filtration sub system. Filtration is considered necessary for protection of the ion l exchange beds. Water is delivered to the prefi~lter and final filter at a flow rate of 5 to 30 gpm, 70* to 90'F, and then into the SDS ion exchange trains. l The expected radionuclides concentrations contained in the Reactor Building sump water and the Reactor Coolant System are represented in Appendix 8. The actual demineralization process would begin in the first zeolite  ; exchanger vessel in the 505 system. This section of the system is divided into two (2) parallel trains containing three (3) vessels in 4 series. Either train may be operated individually or both trains simultaneously. The residence time necessary for proper ion exchange in the zeolite media dictates a < nominal flow rate of 5 gpm per train in this section. For protection of downstream EPICOR II organic ion exchange media, the process fluid temperature is limited to 125'F. 0396B/LC ' i 1

                                                                                              -SD-3527-005 To accomplish these. goals,:we intend-to use a. homogeneous mixture of
                             'Ionsiv.IE-96:and.Linde'A zeolite in all three SDS. liners; -Ionsiv IE-96 is the designation for.IE-95 zaolite:in the sodium form.' In this form.

it, has'a high-capacity and selectivity forfCs, and will provide fo~r some removal-of.Sr. Linde A has a high capacity,and selectivity for

                             .Sr. Combining'these two zeolites in the-three SDS' vessels will load mostbfthecesiumand-strontiuminthe.firstin-linevessel. The exact. percentage mixture of these two types of zeolite will-vary-as-influent concentrations change. 'It is anticipated that the first vessel can be loaded to about 60.000 curies Cs, and;about 6,000 curies Sr. The remaining two vessels.will contain any breakthrough and further polish the' water.

A'n administrative lim'<t of 60,000 curies of cesium, based on the DOE

                              . task force recommendation has'been placed on the zeolite liners, strontium will be limited to 6,000 curies per liner, or Sr effluent of less than 1 UC1/ml.

Downstream of the zeolite exchanger vessels are the " cation" sand' 1 filters. This section of the system is divided into (2) parallel l trains containing one (1) vessel each. The design mode of operation is 1 to use one " cation" sand filter at a time with the other being an  ! installed spare. l I 0396B/LC

s [ _ SD 352'i-005t q Extensive sampling will'be performed at each point;in the system'where' J a decontamin'ation factor can be expected. . Basically,.this amounts to: i i influent and effluent samples'at each_to' nexchanger' vessel. .The projected radionuclides concentrations' at each sample point are specified in the SOS TER, The EPICOR II system will'be: utilized'as a poltshing' unit and'for the removal of sodium which is key to the. removal of trace quantitles of

                                                                                                                       .I ruthenium, recalcitrant species of cesium'and strontium'and! primarily-                          .'

antimony. EPICOR II 6 x 6 liners for'the removal of sodium are

4 expected to be changed out at 25,000 gallons' . This assuines 'a . resin utilization factor of 80% and less than 10% sodium breakthrough. The ,

l RCBT's or the monitoring tanks will be utilized as hold.'up; tanks and' 1 monitoring station to attempt to limit EPICOR II liner radionuclides-- - concentrations to permit EPICOR II liners to be buried in shallow land i burial facilities'without solidification. The processing logic plan  ! which depicts the decision making logic is shown in Figure 2. Table i shows the various vessels, their sizes, function, projected: exchanger- ) media, and number of liners expected to be generated.  ; 1.5 System Arrangement and Interfaces  ; The Submerged Demineralized System is housed in the TMI Unit II fuel , Handling Building. The majority of the system components are located within the "B" spent fuel poo1~which will be flooded with water to afford radiation shielding for-submerged components. Most components-

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0396B/LC

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        ,  that are not-submerged are shielded with lead, steel'and/or~ concrete as!

necessary.. The SDS Monitor Tanks'are-located in'the model room (El. 305'). i 1 1.'5,1 "B" Spent Fuel Pool SDS Components 1 1 The Unit II "B'E Spent Fuel Pool is directly north of and connected to 1 1 the "A" spent fuel. pool. The "B"; Spent Fuel Pool,.is approximately 24 ] feet wide 32' feet 6 inches long, and'41 feet 6:inchesLdeep. The -l Channel th'at' connects the "A" and "B" pools'has'been sealed. l Immediately north'oflthe"B" pool proper are two small pools. The one-on theiwest side is connected to the "B" pool.by a .largeltransfer canal i and is called the cask pi n The cask pit is 10 feet wide, 10 feet long, and 43'.6" deep. On the east side of the~ cask pit:is the surge

                                                                                       .i chamber which is 10 feet wide, 10 feet long, and 17. feet deep. The            1 surge chamber is connected to the cask pit by underwater piping.

i The SDS cask support platform is located at the' extreme south end of

                                                                                       'j the "B" spent fuel pool. The cask support platform spans the pool'in the east-west direction, sits on the pool curbing and is not' submerged during operation. The cask support platform supports the RCS clean-up manifold, the filte inanifold, the SDS effluent post-filter (not' currently used - replaced by " cation" sand filter) and the CN-PNL-1         1 control panel. The RCS clean-up manifold is located on the southeast j

corner of the cask support platform. AllLliquid process piping interconnecting with the SDS feed system enters or exits' the "B pool under the cask support platform at the east end of the RCS clean-up 0396B/LC 1

SD'35272005-

              ,  m'anifold. Under the RCS' clean-up manifoldLthe.'pipingLtraverses the air!

spacebetweenthecasksupportpictform,andthewater'inaleadLfilled annuluscall'editheRCShipechase,.

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The' piping exits the p1pe' chase underwater'and travels to the'various underwate'ricomponents. At each place;where the' piping must,come~to'the surface'it does so via.a shteided-pipe-chase since the shielding effect'~of'the' water and air:is not adequate. , i The filter manifold:is-' located on the' north side'of.the' cask support l . platform midway between the' east'and west pool. sides. The filter-l ~ manifold provides the' valving.and. Instrumentation-for-the.prefilter and final filter: located just' north of the fil.ter manifold,' underwater. in ' the filter support rack. Immediately west of the filter manifold is the post-filter' unit'which filters SDS effluent pr-iorito transfer to processing.by EPICOR II-; and/or storage, if not jumpe. red out of..ser'vice. Directly south of the post-filter is.the CN-PNL-1-control panel; Directly west of the post-filter,.off of the cask support platform, located on the west pool curb is the high rad filter glove box. This glove box is used for-sampling the: filtration process and is' connected to the prefilter and final filter through the' filter manifold. Thef glove box has glove ports on the west side. 1 0396B/LC; J

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SD 3527-005 All operating stations on the cask support platform are accessed by the stairs on the southwest corner of the cask support platform just south of the high rad filter glove box and west of the CN-PNL-1 control panel. The remainder of the area in the "B" spent fuel pool proper, north of the cask support platform contains the majority of the submerged components of the processing trains and the underwater storage racks for depleted ion exchangers and filter canisters. Four basic structures, resting on the pool floor, make up the processing and storage Units. They are the filter support rack, the main process stream ion exchanger support rack, the pool clean-up ion exchanger i rack, and the storage racks. As mentioned previously, the filter support rack is located immediately north of the cask support platferm midway between the east and west 1 pool sides. Running along the east side of the "B" spent fuel pool between the north edge of the cask support platform and the north edge of the pool is the ion exchanger Support rack which contains the two parallel trains of three each zeolite vessels and the two parallel

    " cation" sand filters.
    . lust south of the north edge of the pool, midway between the pool l

uides, is located the pool cleanup exchanger rack which contains two , a ion exchanger vessels for maintaining clean pool water. j i l l 0396B/LC , l

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y 5013527-005~ j Each'of these three.:racksfrests on the bottom of~the pool. Each rack _ has an operating platform which is.a few feetLabove the: water level-to' provide operator access. Remote handling tools for_ coupling'and J

                     'decoupling vessels are provided_for changeout. operations. Each rack-

_has its own. underwater lighting _ Underwater storage.for. sixty (60)~  ;._ 1 spent vessels is as follows: -1) the' main storage rack runs,along the~ west side of the pool tetween the cask support platform and the north'

                                                                                                                   ]1 edge of the pool. This storage. rack has three rows each'having eight                  1 j

L storage locations for a total of twenty-four-slots, 2) four storage locations are provided on'the pool floor in the' space'between:the- - filter support rack and the pool cleanup exchanger rack'(leakage; .)

                                                                                                                 ;j containment ion exchanger rack) and eight locations are located on the                      i pool _ floor in the space west of the ion exchanger support rack and east'                ,    1 of the filter and. leakage containment' racks (total of 12), 3) four' moveable spent exchanger racks of six locations each can be placed on                          i top of the main storage. rack giving twenty-four space for storage.      The:

total of items'1, 2 and 3 is sixty storage spaces. Eight additional storage spaces can.be provided by utilizing processing locations,. Personnel access to the filter support rack and leakage containment _ rack operating platforms is by moveable' personnel bridges which span.

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the gap from the west pool curb to the west side of the working platforms. Access to the ion exchanger support rack operating platform

                                                                                                                   .i l

is from the east pool curb, j i d 1 03963/LC.  !

SD 3527-005 Immediately north of the ion exchanger support rack, the. ion exchanger manifold-is located on the pool wall that separates the"B" spent fuel pool from the surge chamber. The exchanger manifold is divided into two sections. The east portion is more heavily shielded ard contains- , 1 valving and instrumentation for feed water to the first zeolite in i either zeolite train. The west two-thirds of the manifold contains all , remaining valving and instrumentation for the ton exchanger process flow control. 4 Directly west on the same elevation is the leakage containment pump which circulates pool water through the leakage containment lon i I exchangers. The pump discharges underwater in the channel between the cask pit and the "B" spent F.M. pool. j The shipping cask support platform sits on the floor along the south end of the task pit. It supports the shipping cask to be used for transporting spent SDS lon exchanger and filter vessels. The 1 dewatering station rests on the east side of the shipping cask support platform and is anchored to the concr6te between the cask pit and the l l surge chamber. Personnel ~ access to the dewatering station operating platform is from the east side. The yoke hanger assembly sits on the ) curb along the north side of the cask pit. The ion exchanger handling i

                                                                                                  )

tools and the retrieval tool hang into the cask pit from hangers j installed on the south side of the yoke hanger assembly. 1 03968/LC l

 -w_-----__x-a.aw---

e y, i SD 3527-005 1 Theloff-gas separator skid is located in the surge chamber. ThisLunit-consists'of the off-gas separator /tankeand the'off-gas bottoms' pump . standpipe. The off-gas separator tank has an. Integral moisture < separator which separates ~the entrained moisture from gaseous' releases vented through.the tank. The tank communicates.with the off-gas'. bottoms pump standpipe in whith;the off-gas bottoms sump' pump. resides. When the.off-gas separator tank is filled, the off-gas bottoms' pump transfers.the contents-of the separator tank to the'RCS manifold'for

                                      ~
                                                                                       .j processing or transfer to storage tanks. SDS processing-component-                      -
                                                                                          ]

vents and drains are listed in Table 2. i

 -The surge chamber is covered with concrete shield blocks, a layer of                    j y

lead' bricks and. steel' deck plate. Off-gas piping and drains penetrate I

 .the shield plugs'to connect-to-the off-gas. separator skid. On the top                    l of-the surge Chamber cover are located 1) the.high rad feed sample glove box, 2) the intermediate level sample glove box, 3)-the beta.

monitor manifold,'4) the annunciator. panel, 5) the radiation monitor panel, and 6) the off-gas separator level itistrument par,el. l The high rad feed sample glove box is tsed to sample the-feed water to the first zeolite vessel in either of the processing trains. A j provision to sample effluent from the first zeolite vessel in the high i rad feed sample glove box is also provided if activity levels of the i feedwater passing through this vessel exceed 1pC1/ml. The- l intermediate level sample glove: box is utilized to' sample'all ion .; exchange vessel effluents. starting with the first-zeol.ite in each i

                                                                                         -i train. Both of these glove-boxes are located on the north side of-the i
                                                                                            )'

0396B/LC ,

                                                                                 .           l 4;                                                                        SD 3527-005

surge chamber cover facing each other. Both glove boxes'are accessed from the middle of the surge chamber cover area. The high rad feed .j glove box is located on the wes't side:and faces. west. The: beta monitor.. manifoldLis. located between the intermedia.te level: glove. box and the ton exchanger manifold .This' manifold monitors the' process stream'at I selected points.for gross breakthrough and can indicate major activity ., trends.1n the process. stream. 1 L. l l -On.,the-south. side of the surge chamber cover are' located the i annunciator panel,.the rad monitor panel and the off-gas separator. tank level indicator. Th.e majority of the. system alarms and diagnostics ar_e located here. .They are discussed in detail-in,Section 2.2 of this document. 1 . Located on the east pool curb adjacent to the ion exchanger manifold is the SDS off-gas blower and air filtration unit. The unit maintains a negative pressure on all vented SDS components and.provides suction on the off-gas separator system. The blower exhaust is routed via ducting south along.t_he east Feel Handling Bullaing wall to where it ties into the existing fuel Handling. Building ventilation system. Off-gas system influent gamma radiation is monitored by CN-RE-VA-06 mounted on off-gas l piping upstream of the filters. l l Installed immediately downstream of the blower, the off-gas sampling unit (PING-1A)' continuously monitors the.off-gas effluent for airborne. radioactivity. 0396B/LC _ __ __J

l

                                                                       ' SD 3527-005-
A chemistry laboratory is. located on the floor. space immediately north!

of the."B" spent fuel' pool on'the west side of the fuel Handling-

      , Building.

Operator,and supervision work, area is provide'd on the~ south en'd of the new fuel storage pit cover which.is: located.on the' east side'of!the Fuel Handling Building, north'of the "B" spent fuel pool.. L l Under the' floor space' occupied by the chemistry' laboratory,.at'the next lower floor level (305' elevation, 42' below the fuel pool. operating level).is located the SDS monitor tank' system. This system consists of-two 12,000 gallon tanks, each 8 feet in diameter and 32 feet ~high with i associated pumps (2) and all related piping to effect recirculation, l. sampling and transfer of the contents to' storage tanks, to 505 for use as flush water, or.as staging tanks for EPICOR II. processing. Flushing connections are provided on all of the manifolds and glove boxes. Flush water can be processed water'or demineralized water. Flushing is accomplished by attaching rubber. hose from the flushing water supply station to the' flush connection on.the component to.be flushed; a portable turbine flowmeter is also'placed in-line with the I

                                                                                               'l flushing operation. Flush water stations and air purge stations are                 j
l located within close proximity of all components which may require- .

l- water flush or air purge. All flush and purge connections are made via. Hansen quick disconnent couplings. , i l  : l 0396B/LC

n a

                                                                                            ' SD 3527-005 li5.2 LSDS Interfaces to Other Systems'
                            ~

d 1.5.2.1 Electrical

                                  'All SDS electric power is tied into the Unit lII BOP. electrical;      '
                                   . systems'at distribution panel PDP-6A, which is located atLth'e-347'6" elevation of the Fuel. Handling Building, and motor control) center 2-42B located at the 328 Elevation of the Aux 111ary
                                   . Building.
                   '1.5.2.2 HVAC:

The-SDS MSA off-gas unit exhaust ducting penetrates the 347'-6"~ elevation'at an_ existing penetration. The ducting ties into existing. Fuel Handling Building ventilation ducting immediately. below that penetration'at elevation 341'-2". 1.5.2.3 Demineralized Water The SOS demineralized water header is' tied into the plant' system

                                   'at valve DH-V-272 located under the: east curb of "B" spent fuel:

pool curb. An additional check valve, CN-V-DH-357, and isolation valve, CN-V-DH-355, were added ju!t downstream of DW-V-272.to

                                  ~ protect the plant demineralized water system.

l 21 - 0396S/LC _ _ _ _ _ _ _ _ _ _ _ = _ 1

t ' s,

                                                                                           'SD:3527-005~

1.5.2.4. Service Air m The service air; tie-in to the SDS service air header is at the plant service air valve, SA V-154, located adjacent to'the. demineralized water-system valve addressed in Section 1.5.3.3. L; 1.5.2.5 Instrument Air-The SDS. instrument. air. tie-in i_s at the plant instrument' air valve, IA-V-175,. located on the west side of the fue.l. pool curb.. 1.5.2.6 EPICOR 11 SDS effluent water can be transferred.to EPICOR II'from either the Reactor Coolant Blecd Tanks (RCBT), the Miscellaneous Waste'

                                                          ~

Holdup Tank (MWHT) or the' Monitor Tanks. The SDS effluent may be directed to any of these tanks-by selecting the appropriate.  ! valving on the SDS transfer line at the 347'6" operating elevation of the fuel Handling Building. 'The SDS interface to. the MWHT is through valve SF-V-234 located under the east curb of 4 i the "B" spent fuel pool. The SDS interface..to the RCBT's is. through a spent fuel cMing line connection to the.RCBT's inlet

                                                                             ~

header upstream of HOL-V-191. _ Double isolation valves in the SDS transfer line at the 347'6" elevation precede the p'lant isolation ] l

             -valves. The SDS interfaces with the Monitor. Tanks.through                .

installed SDS piping downstream of Isolation Valve CN-V-PF-68. .,

                                                                                       '0396B/LC' a

l~ , ( .. _ ._ __ _ _ _ _ _ . _ . _ _ _ _ _ b

g SD 3527-005 1.5.2.7 Processed Water Stor_ age Tanks (PWST) 1 EPICOR II effluent is transferred to the PWST using the EPICOR II transfer pump. The PWST's are tied to EPICOR II at valve ALC-V-006. SDS effluent can also be transferred to the PWST"s  ; from the monitor tanks or from the RCBT's. The PWST system is tied to the monitor tanks at valve PW-V-39 which is located in the Unit I/ Unit II corridor. 3 l l 1.5.2.8 Reactor Building Basement Jet Pump (SWS-P-1) l l The pump currently in use for removal of water from the Reactor Building sump ties in to the RCS manifold at valve CN-V-RC-364. The Reactor Building Basement Jet Pump system is described in Appendix 12 of this document. 1.6 System Design Reautrements 1.6.1 General Design Requirements i 1.6.1.1 The design basis considers the guidance in the following documents: l 1.6.1.1.1 U.S.N.R.C. Reg. Guide 1.143, July 1978 1.6.1.1.2 U.S.N.R.C. Reg. Guide 1.140, March 1978 , 1.6.1.1.3 U.S.N.R.C. Reg. Guide 8.8 1.6.1.1.4 U.S.N.R.C. Code Guide 8.10 i 0396B/LC

L,6 ,

                                                                                                ,   l 4

SD.3527-005 1.6.1.1.5 U.S. Code of Federal Regulations 10CFR20 App. B 1.6.1.1.6 U.S. Code of Federal Regulations 10CFR50 j as imposed by Reg. Guide 1.143 l 1 1.6.1.1.7 U.S.N'.R.C. Reg. Guide 1.21 June 1974 d 1.6.1.1.8 ANSI /ASME N45.2.15 f 1.6.1.1.9 US NRC Regulatory Guide 3.4 l 1.6.1.2 The process shall function in such a manner as to limit releases l to the environment and limit plant personnel exposures levels to levels which are "as low as is reasonably achievable" in aCCordance with 10CFR Part 50,10CFR Part 20, Regulatory Guide 8.8 and TMI II Recovery Technical Specifications. 1.6.1.3 Capacity 1.6.1.3.1 The processing rate through the filters shall be 5 to 30 gpm. The sand filters are designed to operate as shown on Figure 3. Other filters are designed for operation with up to 20 psid above clean f'elter differential pressure. 1.6.1.3.2 Process flow rate is 7.5 gpm per trair.. 15 gpm total through'the zeollte beds, and 15 gpm total through the cation vessels. f Process flow rate is a function of residence time, and can be varied depending on the choice of resins. b 1.6.1.3.3 Storage capacity of spent vessels is 60 vessels (not including the processing stations). j 0396B/LC

                                                                                                  )

{ __ l

j SD 3527-005 N

1. 6. l '. 4 Th'e: system is designed to facilitate decontamination and decommissioning to the' maximum extent possible.  ;
                                                                                                         }

4 l l 1 6.1.5 SDS pressure. components are considered:"Important_to Safety". < 1

.o l
   - l ~. 6 '. 2 ' Process' Piping Design Requirements.

j

                                                                                                       .i 1
1.6.2.1- Piping is designed to ANSI B31,1.in accordance with.the'  :

1 i j requirements of. Regulatory Guide 1.143. Welded construction has been utilized to the maximum extent possible with butt welding :j utilized in' anticipated high radiation. level. areas to minimize'

                       " crud" traps.                                                                  .
                                                                                                 '      ;j 1.6.2.2            The piping system has been designed for 150 psi.100'F service.and-                l
                                                                                                        .i utilizes schedule 40, type 304 stainless steel pipe and fittings.               d 1.6.2.3            All instrument tubing systems communicating with process media utilize type 304 welded stainless' steel tubing.and fitting.

Process instrumentation generally is not fitted with isolation s block valves as the instrumentation is designed to be maintenance.- 1 free over the service life of the system.  !

i. 1.6.2.4 Pressure sensing instruments communicating with high activity-process fluids utilize liquid filled diaphragm isolation devices with filled capillary tubes communicating with the actual.

pressure indicating device. This minimizes the possibility of i contaminated fluids' entering the pressure indicator. The device-may be removed remotely for' calibration or replacement. l 0396B/LC l

                                                                                                                          ?

SD 3527-005' l.6.2.5 Valving.in the process. stream is contained in enclosed. shielded. manifold boxes which are v'entilated by.the Off Gas handing unit and have sumps which empty into the Off Gas Separator Tank. Shielded' access ports in the box are'provided for inspection and

                                                                                                                        ']

maintenance of the valves. Valves are operated remotely. l utilizing reach rods (valve handle extensions) which protrude through the shielding plugs. Process valving is of the top. entry j type to facilitate maintenance and repair. l.6.2.6 The process line pipe size is normally 1" based on the SDS Design i flow rate of 5 to 10 gpm. Other line sizes are based on. service requirements and function.  ! 1 1.6.2.7 Piping runs tihich are not submerged or are not contained in l manifold box are shielded as necessary to yield maximum exposure i i rates of 1 mr/hr general areas. In service radiation surveys ar.e conducted to insure that these limits are met. 1.6.3 Ton Exchange Vessel and Fi_ Iter Vessel Requirements l 1 1,6.3.1 Vessels are designed, fabricated and tested to the ASME Boiler and Pressure Vessel Code, Section VIII, Division 1, 1977 addendum < through Hinter '78. 0396B/LC 1

SD 3527-005 1.6.3.1.1- The high integrity type 316L vessels will also be code stamped; 1.6.3.2 Early CUNO-type filter-vessels and lower activity APCO ion-l exchange' vessels.are designed to 150 psi, 100*f using type 304 stainless steel. Subsequent filter vessels are the same design I as zeolite ion exchange vessels. 9 1.6.3.3 Zeolite ion exchange vessels are designed to 350 psig, 400*F using type 316L stainless steel. l 1.6.3.4 Zeolite vessels are designed to allow ease of removal of ion j exchange media for future disposal. 1.6.3.5 All vessels utilize Hanson. quick disconnect fitting to allow remote connection and disconnection. i i l 1.6.4 Monitor Tank Requirements 1 1.6.4.1 Monitor tanks are designed, built, and erected to API 650, Appendix J except material is type 304L stainless steel. I l 1 1 0396B/LC 4 _-_-----___----_--_J

SD 3527-005 2.0 Detailed Description of the System 2.1 Components 2,1.1 Submerged Demineralization System Pumps 2,1.1.1 Reactor Building Basement Jet Pump (SHS-P-1) See Appendix 12 i 2.1.1.2 Monitor Tank Transfer Pumps (PIA & PIB) These pumps are two identical, electrical, mechanical seal centrifuga' Goulds pumps arranged in parallel. The system is designed to operate using one pump,-the second pump is an installed spare. The pumps provide the capability to transfer processed water to either the RCS manifold, the influent to Epicor 11 system, the Process Water Storage Tanks or the SDS flush header. In addition the pump discharge can be directed back to the monitor tanks which allows these contents to be recirculated prior to chemical analysis and sampling. The pump is rated at 50 GPM with a total dynamic head of 111 feet.

                                                                                                       )

l i 0396B/LC 4

m .. - .

                                                                               -~-

50 3527-005-3

                    . Pump operation.is controlled by start /stop pushbuttons located
                              ~

local 1y at the pump starter on'the'305' elevation and remotely in control _ panel (SDS-LCPI)'on the 34N elevation. A selector

                    -switch is also installed which aligns the monitor. tank transfer pump .to a particular ronitor. tank to allow the system to automatically trip the transfer pump in the event a monitor tank low low level condition is experienced.

l:

        '2.1.1.3     Off Gas Separator-Bottoms Pumo'(CN-P-VA04) l This pump, during normal operation, will.be used.to' maintain the level'inthe off-gas separator tank within a preset band (80" to:                               !

I 18"). . Pump operation will be contre 11edl.by an electrical. switch. The separator' tank lis. pumped down'by operator action. The pump operates until the tank level reaches eighteen. inches, - and the level switch de-energizes the pumps motor-controller. The'off gas bottoms pump takes a suction on the off gas moisture separator tank well, and' transfers the water to the RCS manifold' for processing through'the Submerged Demineralized System or for i transfer to other storage tanks. 1 The off gas bottoms pump is'a submersible centrif'ugal Goulds pump powered by a 5 HP motor. It is capable of producing 30 gpm at a- q i 55 ft. head. The pump,' tank, and well are located in the'"B" i spent fuel pool surge tank. 0396B/LC l

                                                                    'SD 3527-005 The control panel for the pump is mounted on a skid located above
  • the surge tank. An on/off/ auto key switch is provided on the panel to allow manual operation of the pump. During normal operation, the switch will be placed in the manual position. The pump is powered from the SDS power panel (PDP-6A).

2.1.1.4 Off Gas Blower (CN-E-VA05) Submerged Demineralized System Components (except for the monitor tanks which vent directly to the Fuel Handling Building Ventilation System) are maintained under a slight vacuum by the off gas blower. The blower is designed to exhaust 1000 cfm at a nominal differential pressure of 12" of water vacuum. This amount of differential pressure allows for worst case pressure losses through the filters due to a dirty prefilter and' dirty charcoal and HEPA filters of 0.5 and 2.0" of water vacuum, respectively, while maintaining adequate vacuum in the off gas header. The off gas blower is a fifteen inch, radial flow, centrifugal type with single inlet unit. Suction and discharge pressure gages are provided to monitor blower performance. The-motor is a 5 HP., 460 volts, 3 phase, 60 H2 Unit powered from the SDS Hotor Control Center. The blower is mounted on the off gas unit skid which is located near the east wall of the "B" spent fuel pool. The blower is controlled with start /stop pushbuttons located next to the off gas blower. The blower discharges to the Fuel Handling Building HVAC system. 0396B/LC

SD'3527-005-1 .

                                                       ~

2.1.1.5 ,

                            .Leakace Containment. System Pump'(CN-P-LC06)                                           ;.

i

                            .The leakage containment; pump is' designed to maintain an inward flow of fuel pool water into the. leakage containment boxes which
surround'the 50S' filters'and demineralizers. IThe' pump discharges the pool water, and..any leakage fromLthe vessel fittings, to a.

pair'of' parallel of ion exchangers.and then.to the fuel" pool. The leakage containment pump is'a centrifuga'1l pump ~which is mounted'on the catwalk between.the "B" fuel-poolfand the cask handling' pool. The pump'is driven by.a.three HP motor which.is..

                            . powered from the SDS motor control center.             It'is controlled with:

stop/ start pushbuttons. mounted on a pump control panel located t next to the pump. The' pump. takes suction on a common header-containing throttle valves which, through the'use of' manometers located on the ion exchange. rack operators platform where'the I remote reach rods are also located, allow the flow through each ~ containment. box to be throttled,'t'oL10'gpm per box in use. The design total flow through the pump is-100 gpm.and is delivered as 50 gpm per leakage containment ion. exchanger. 'The pump developes 120 gpm at 55 ft.' total dynamic head. { i i 1 < l j

                                                                  .31 -                            0396B/LC                l 1

i Sir 3527-005-2 1.1.6 RCS Manifold.-H1T Rad Filter Manifold and High Rad' Sample Glove

Box-Sump Pumps (CN-P-FLO7. CN-P.SA08 and CN-P-RC09)
                           .These pumps are mounted locally.in the.Hi Rad. filter.. Manifold, Hi L             ,

RadFilterSample.~GloveBox:andthelRCSManifold They. provide: the capability to transfer 11guld waste from the sumps of these components to the offgas separator. tank. The. remaining SDS. component sumps, unlike those above,;do'not need a similar. arrangement since.they gravity drain to;the off. gas separator tank. 1 The. sump pumps CN-P-SA08 and CN-P-RC09 are identical rotating pumps with a capacity of.0.5 gpm at:81 feet of dynamic head. The sump pump CN-P.-FLO7.is a magnetic drive 2 gear pump with a capacity of 0.5 gpm at 95'.psig.

 .                          The pumps will be operated automatically'to maintain level in these sumps within a preset band.       This is. accomplished by level switches'in each sump which energizes /the' pump when the water level reaches 2. inches and de-energizes the.' pump when the' water is removed. They are powered from panel MP-CN-1 which also has a breaker to allow them to be de-energized. manually.                  These pumps must not be operated during offgas. separator tank. pump down.

l 1

                                                                                                                                     )

1 0396B/LC-i 4 o

j_i i . .g

                                                                                                              'SD 3527-005:

b '2.1.1;7 FTC. Drain / Processing Pump'(FCC-P-1)'- l See Appendix.18. 2.1.1 8. FTC Shallow End Drainage Pump (DHC-P-1.) i Note: Uses old IIF Processing. Pump. See Appendix 19.

                            - 2.1.1.9-              DWC Fuel Transfer Canal / Spent-Fuel Pool Cleanup System Pumps-(DHC-P-3A & B and DWC-P-4A & B)
                                                 'Early Defueling'.

See Reference 1.2.7. 2.1. 2 Submerced Demineralization System Tanks 2.1.2.1 Off Gas Separator' Tank (CN-T-VA02) The. moisture separator tank provides the capability of. removing large amounts'of liquid from' ventilation and drainage lines associated with the Submerged Demineralization.. System. Drain l lines throughout the SDS (except.for the monitor tanks, and~ components discussed in 2.1'.1.6 above which have a separate drain arrangement) combine into a common drain header that empties directly into the moisture separator tank.' Ventilation lines from various SDS components (see Table 2) combine'to join a common header. The tank is a vertically mounted stainless steel tank located (along with the off gas. bottoms pump standpipe) i n'- the spent fuel pool surge. tank. It is 36 inches in diameter, ten g 0396B/LC

     +

i l-

                                                     /.

SD 3527-005-foot:in. length and has'a capacity of_590 gallons. ll j

                                                                                                                       .}

Theseparator-tankis"ventedtothe'offgasheader.-Afdemister

                                                                                                                       't assembly is located in the: top of the. tank to. remove.motsture

' from the' tank's ventilated gases. The demister assembly has been testedinaccordance'wlth'USAECreportMSAR-61-45.-'Itwilllbe. i capable of. removing 99 percent:of all free droplets of water, down to one micron in diameter, without.'any visible carryover.'

                                        ~

i A' three inch drainline runs from the bottom of the tank'to.the j off gas' bottoms pump standpipe (CN-U-VA01). The standpipe is 161 inches in diameter!and 16 feet long. .It' houses the off gas l bottoms pump (CN-P-VA04). ' The separator tank has a Barton type level instrument' associated with it. The meter reads from zero. percent to .100 percent full' scale. L 2.1.2.2 Submerced Demineralization System Monitor Tanks (SDS-T-l'A'&-- q SOS-T-1B) 1 The Monitor Tanks are two 12,000 gallon tanks designed for collection and' temporary storage of: liquids'that have been i processed through the Submerged Demineralized System. They have also been installed with the intent to utilize them as.a storage. location for SDS Flush Water. The Monitor Tanks along with other; components which comprise this system are described further in Appendix 14. The Monitor' Tanks-can beJ operated in the' batch, .)

                                                                                                  ~

continuous feed, or bypass mode. . In the batch mode the liquids I 0396B/LC 1 1

SD 3527-005 a're stored in<the tanks until an accurate sample'of the' tank's. q contents,are analyzed,?and'the disposition (based on:sampic -) results)'of the' processed liquid is^ determined. . Based on the;

                                                                                                                                                             .l sample results, the contents-may beLdischarged to: 1) the                                                                                 l
                                                                                                                                                            -1 processed water storage tanks, 2) the SDS flush water supply header 3) the'RCS manifold or 4) .to.the EPICOR II System. :In the                                                                       !

continuous feed mode the~ tanks:are used as surge' tanks ~between the SDS and EPICOR II Systems. To maintain tank level approximately, constant, flow' rat'e in and out of the tank is'kept. j a. identical. In the bypass mode.the SDS~ Processed Water bypasses-  ;) the Monitor Tanks by being transferred to either?the Reactor l Coolant Bleed Tanks.or the Miscellaneous Waste Holdup Tank. Int this mode ~the Monitor Tanks are used only as'a' source of SDS q 1 Flush Water. i llj The tanks are vertically' mounted, stainless steel tanks, located 1 in the northwest corner.of the' Fuel Handling Building Model Room. The monitor tanks are atmospheric tanks built to API-650,-- Appendix J, and meet the desigh criteria set forth in Regulatory Guide 1.143. The tanks are vented directly through a vent!line to the fuel Handling Building Ventilation System. The influent line to each-

                                                                                                                                                               ]

tank is equipped with an automatic' isolation valve,'which stops i i influent liquid flow when the level detector, associated with the. 1 tank, senses a high level (364").

                                                ~

0396B/LC

xr. , .,. SD.3527-005 , ciy Associatedwitheachtankisfa'Fokb6rol type 11eveldetect6r..Its.

                                                                   ~
                     . meter, indication ranges.from 0[to.400 inches ' full scale. 'These-a                           -

level'. detectors also-p'rovide high/ low level signals to' shut' the(

                                                                                                           )a tankinfluentautomaticalsolation'valveonhighLievel;andtostop' i

theLmonitor' tank transfer pump-on low level (6"). . In additio'n,. 7 these ' signa.ls also. feed the SDS alarm panel t to' alert the ' operator ' i, in the event that any of thEse. conditions exist..' Priorto ' 1 transferring of processed'. liquids' stored:indthe-monitor tanks, the tank contents: are recirculated..using oneiof. the two monitor - tank transfer pumps through: eductors.to insure proper mixing, q The' valves and piping ~are set up to allow either tank.to be= l recirculated'using'either. pump.or 1.t is possible to set up-simultaneous, independent recirculation,of both tanks. 1 2.1.3' Filtration / Demineralization Units i 2.1.3.1 Submerced Demineralized System Prefilter and' final Filter The prefilter and final filter 'are the'first process vessels of-the Submerged. Demineralized Systetn. .They are used to remove debris and suspended solids from the untreated Radioactive Waste

                                                                                                          ]

Water. The SOS utilizes two types of prefilter and final filter l q vessels. This allows for either a.Cuno Cartridge or sand' filtration media to be employed. A description of.each type is j discussed below. i

                                                                                                            ]

36 - ' 0396B/LC

r v. SD 3527 00$-~ t 2 .1. 3.1.1 : Cuno Cartridge Prefilter ' The'cuno cartridge'prefilter unit'is,a. stainless-steel, type,304,

                        . vessel,lwith approximately 10 cubic. feet of volume. The vessel, including.the male' half of ths' quick disconnect.=1s.4 feet; 5/1/2 inches in. height.and 2 feet outside1 diameter. .The. top of the.

vessel'has four. male Hansen disconnect fittings; an inlet nozzie', an outlet nozzle, a' vent nozzle,'and a dewatering nozzle. l 1

                                                                            ^

Within the vessel is'an enclosed area,. constructed.of-16 gage'  ; perforated plate. This cylindrical' column constitutes the initial f.iltering. unit of the prefilter vessel. The inlet nozzle. consists of an open ended pipe. equipped with (2) two internal ball' check valves. The nozzle is located outside of the enclosed .h i area, between'the perforated plate and.-the prefilter vessel wall'. The inlet nozzle extends down.into the vessel. approximately one-half the height of the vessel. The. inlet'

                        .Hansen quick disconnect is a non-check valve design to prevent..

plugging from debris in the waste water.- The: inlet nozzle is equipped with two ball check valves which prevent a reverse. flow of water out of the vessel when the; vessel:is disconnected from the process stream. Contained within the enclosed cavity fo'rn.ad by the' perforated - plate is a network of fifteen,125 reicron cuno filter cartridges. The opening at the upper end of each filter seals U around a nozzle which empties into an outlet header. The opening;

                                                                                                              .I t

g 0396B/LC' l

                                                                                              .              :i
SD 3527-005 . '

i I

             .at the lower end of;the filter is plugged.

The cartridges are J supportedbysprings.(onithebottom)which~ald'insealinglthe upper opening'around:the outlet nozzles. The prefilter assembly'is'also equipped withia. dewatering ~ leg and - a vent no'zzle. The dewatering leg consists.of a:1/2 inch.

                                                                                                              -i stainless steel pipe, extending'from the bottom centercofL-the                               j
                                                                                                            ~1 filter,'around the outside~of the perforated' plate,.and out the                                   1 top of.the vessel;    It.' terminates with'the male' half of a-Hansen.                       3 1

q l quick. disconnect. The vent. consists of a short nipple (with the' .R i male half of a'Hansen quick-disconnect attached to the end)

                                                           ~
1 welded'around an opening in.the top of the vessel.  ;

2.1.3.1.2 Cuno Cartridge Final Filter The Cuno Cartridge fina'l= Filter Vessel shell-1sildentical~tolthe cuno cartridge prefilter vessel shell. It is a Stainless steel, type 304 vessel with approximately ten cubic feet of' volume. The  ! vessel, including the male half of the quick' disconnects, is 4'

                                               ~

l feet 5 1/2 inches in height and two~ feet outside diameter.- The j top of the tank has four male ~ quick disconnect fittings, an. inlet. nozzle, an outlet nozzle, a vent nozzle, and~a dewatering nozzle Arranged within the filter.are three concentric-circles of 10 micron "Cuno" filters totaling ~ thirty cartridges. The cartridges are mounted in'the final filter in the same manner.as they are < mounted in the prefilter. A spring on the bottom seals the i

                "cuno" filter against the effluent header nozzles.

0396B/LC l

SD 3527-005 The final filtet inlet nozzle is a short nipple with the male half of a Hansen quick disconnect welded to it. The other end of the nipple is welded around an opening in the top of the vessel. The filter vent nozzle is. constructed the same as the inlet

         . nozzle.

The outlet nozzle is a short run of pipe extending from the-filter effluent header, through the top of the vessel and ending with a male quick disconnect. The dewatering leg is a 1/2 inch pipe which runs from the bottom center of the vessel, up through the vessel, 8 inches from the vessel centerline. The line penetrates the top of the vessel, and ends with a male quick disconnect.  ! The flow path through the filter is as follows: the water enters the vessel through the inlet nozzle and flows down and around the Cuno filters. The water then passes through the cartridge and leaves the vessel through the outlet nozzle. 2.1.3.l.3 Sand Pref 11ter, Final Filter, and Cation Sand Filter i The sand filters consist of two layers of sand contained in a  ; l stainless steel, type 304 vessel, identical in size to the cuno l cartridge prefilter and final filter vessels (4 feet, 5 1/2 inches in height and 2 feet in diameter). I 0396B/LC _-_-______a

, Sb3527-005. l-The vessel is equipped with four nozzles on the top. Three nozzles terminate with the' male half of.a.1 1/2Linch Hansen' quick disconnect. The fourth.is a three inch. fitting with a' screwed; pipe" cap closure. ;The filtration media consist of~200 pounds of' O.85 millimeter sand and 700: pounds of.0.45 millimeters sand in two separate layers. Approximately 6 pounds of 2 millimeter borosilicate glass with a nominal boron concentration of 22-t percent is added uniformly;to the sand filled protion'of the.

    . filter, for reactivity control. These filters remove suspended solids in a range of 20 to.30 microns in size.

The inlet nozzle is a short run of pioe, which extends from the t quick disconnect, down into the vessel..and emp, ties:into a spray' ring. The ring is a 1;1/2 inch pipe rolled into a 12 inch' diameter ring, located. horizontally near the top of,theLvessel. There are six 5/16 inch di6 meter holes drilled through the;bottorn I of the ring. The holes are covered by a one inch long 3/4 inch diameter, .007 inch screen' cup (Johnson screen), which 1's welded. l l around the hole. l l The vent nozzle is a short nipple welded around a hole.in the top of the vessel. A three inch.in diameter, .007 inch screen cup is welded around the hole on the inside of'the vessel'as a sand i retaining device. l' 0396B/LC 1

                                                                .____.._____E_i___1.___              i
        ,              ..i' I                                                                      SD 3527-005~

L b .. . l The outlet;line from the:. vessel-serves' two purposes. It is the- - l: i; normalcoutlet line and it. serves as a dewatering-leg. The' L outlet Lline .ls' a 'l' 1/2 ' inch straight ' pipe' wht:ch extends from just - 1 g .off the' vessel bottom,=up through the center of the vessel and

l. . .

L penetrates the top of the' vessel. , The bottom end of the pipe is; 1-enclosed within a screened area,iwhich.act as:a; sand retaining-screen. < l LThe fourth nozzle on the vesselvis used as an access opening. 'It is a three inch nor21e welded around an opening'in..the. top of the-l vessel. The nipple is capped with a three inch screwed pipe cap',' The influent water enters the vessel through the inlet nozzle. Water sprays out into the-sand media from the spray ring holes.

          'The water is forced down through the media, and up through'the outlet line where it leaves the vessel.

Both the prefilter; final filter, and cation. sand filter, when

installed in the system..will. set inside a
secondary containment l-L ' located underwater at'the south end of the'"B" fuel pool'. The 1,

l pu'rpose of the: secondary containment is to collect any leakage which might be'present from the fittings associated with the. I !. 1 vessel.-and to provide support for the filter-vessel. Pressure instruments-have b'een install.ed in the s'ystem to monitor. filter performance. There are pressure gages located on the influent and' effluent lines to allow the operator to monitor the i 0396B/LC

's . i

                                                                                                                                          'SD 3527-005 pressure the filter.is subjected to,1and the pressure. drop'across each filter.- Allowable sand-filter l differential pressure is shown on Figure 3.                                                        ,

i l Because plugging of the' inlet Johnson screens occurred in;the

                                                                                               ~                                                             1 sand filters, all' sand filters of'the'304cstainless steel. type after the initial' pair have the spra'y headers modified. The spray ring on these headers has three 0.5 inch holes. drilled on            y the top side;to allow flow if the Johnson. screens plug.-

1

                                                                                                                                                             'l q
)

Also a special series'of 316L. vessels fabricated by Buffalo Tank i Company and APCO were procured'which have specially designed spray headers to' allow'high flow rates. LThese vessels'are l L i l- identical to other 316L zeolite:lon exchanger vessels in every-1 L respect except for spray header design. The spray > headers in'  ;; these vessels do not contain Johnson screens. These've!,sels.are j [ for use as sand filters and leakage containment' Lion exchangers- d where unrestricted flows of greater'than 10 GPM are required. o l- H

                                                                                                                                                             .]

2.1,3.2 Submerged Demineralization System Post Filter l The post filter is the third filtration unit in the 505. The L filter is used to remove any resin fines which escape through the resin _ retention screens contained.in each' ion exchanger vessel. It is located at the south end of the Fuel Pool deck just east of the high Rad Filter Glove' Box. In the system,lthe post filter is. positioned on the effluent side.of the cation vessels. 1 1 0396B/LC' 1

                                                                   'SD'3527-005L d

The post filter Tunit consists of a filter housing'which.contains a replaceable cartridge fil'ter. The housing lis constructed of j 3/16.thch 304' stainless. steel 3and is 7 inchesfin dia' meter.by , 7/16 inches in height'and' mounted on a.16'. inch high support. The. 1 top of the. housing >.is equipped with a. lid'to allow forj installation and: replacement of the filter.. Consistent with.the

                                        ~
     . remainder 'of. the -50S Lsystem the. housing is' designed for.150: psig and.100'f.' The filter is mounted inside the housing and is 21.-

5/16Linches-tr height.by.6 3/4 inches.Lin' diameter. -It is' constructed of epoxy. impregnated cellulose' fiber. media with stainlessLsteel supports. It is built;with a particle removal: capability of 0.45 micron nominal.at'a1987, efficiency and 3.00-micron absolute. The filter lis designed for a. clean filter pressure' drop of.12 psig at 20 GPM and a maximum flowL rate' of 150 GPM. The filter is lor:ated within a lead shield; Differential pressu're, flow and radiation' detection instrumentation have been installed in the system-to monitor filter performance.1 The differential pressure gagelis'used'to. indicate the pressure drop across the filter, the turbine flow meter is used to monitor effluent flow rate and; total volume' :j

                                                                                  .]

processed. The radiation-detector is positioned next to the i i filter to monitor the radioactive loading on'the filter. At a. i differential pressure of 25 psig and/or..a filter radiation: level- l

     .of 2R/hr, the filter is considered depleted and will'be-changed-out, a

0396B/LC. 1 I

y" , x ' ! , t'

                '                                                                  'SD 3527-005, The SDS post filter may be. bypassed 'during' processing operations; and.its function assumed by a sand filtert similar.to those-                    <
                      'previously discussed. installed'in:one=of:t'he: cation ~. positions.

L 3 L 2.'l .3.3 ' Leakage Containment' Ion Exch'ance'VesselsL Leakage containment'lon e(change beds are contained in a-standard . vessel, identical in size.to'the sand: filtration' unit' vessels -(4' . fe'et,.5-l/2' inches-in~hel'ght and 2 feet in diameter). These vessels are equipped (as are the .filtratic,n vessels) with-four nozzles'on the-~ top. Three nozzlesEterminateLwith the m les half of a 1 1/2 inch Hansen. quick' disconnect. <The fourth is at three inch fitting with a screwed pipe capeiclosure; 1 L The inlet nozzle is a short run of pipe, which extends from the; j l l quick disconnect, down.into'the vessel,, and empties-into a spray. .l ring. The. ring.is'a 1 1/2 inch pipe rolled:intoLa 12 inch diameter ring, located horizontally near-the top of the' vessel.. i l There are six 5/16 inch diameter holes drilled through the bottom' 1 i of the ring. The holes are covered by a'one inch 1Uig;3/4 inch q diameter, .007 inch screen cup (Johnson-screen), which is welded around the hole. i l u 03968/LC. s

SD 3527-005 The. vent nozzle is a short nipple welded around a hole in the top of the vessel. A three inch in diameter, .007 inch screen cup is welded around the hole on the inside of the vessel as a sand retalning device. l The outlet line from the vessel serves two purposes. It is the normal outlet.line, and it serves as a dewatering leg. The outlet line is a 1 1/2 inch straight pipe which extends from.just off the^ vessel bottom, up through the center of the vessel and penetrates the top of the vessel. Tne bottom end of the pipe is enclosed within a screened area, which act as a sand retaining screen. l The fourth nozzle on the vessel is used as an access opening. It is a three inch nozzle welded around an opening in the top of the vessel. The nipple is capped with a three inch screwed pipe cap. The influent water enters the vessel through the inlet nozzle. Water sprays out into the ion exchange media from the spray ring holes. The water is forced down throSgh the media, and up through the outlet line where it leaves the vessel. l The leakage containment ion exchangers will also be enclosed by a secondary containment, however, the containments will not have  ! covers on them like the zeolite vessel containments. They will . l be located at the center of the north end of the "B" fuel pool, i 0396B/LC l

                                                                    'SD 3527-005 The icn exchange vessels are provided eith pressure gages.on the

) influent and effluent lines. The gauges are used by the' operator to monitor pressure drops across the ion exchange medias. Curie loading will'be calculated from sampling results of the influent and effluent samples from each vessel.in the process train. Because flow restriction caused by plugged Johnson Screens occurred in leakage containment vessels, the 304 stainless steel l l vessels'have modified spray' headers. The spray ring on these  ! headers has three 0.5 inch holes drilled on the top side to allow flow if the Johnson Screens plug. The modified Buffalo Vessels 1 addressed in Section 2.1.3.1.3, also may be esed as leakage containment vesselt.

                                                                                 .j I

2.1.3.4 Zeolite _ Ion Exchange Vessels 1 The zeolite ion exchange beds ~are 4 feet, 5 1/2 inches in height and 2 feet in diameter. These vessels are high integrity 316L stainless steel, designed to withstand 350 psig at 400'F and have  ; 3/8" thick walls. l 1 i Each of these vessels are equipped with five (5) nozzles on the upper head. Three of these are 1 1/2 inch nominal pipe size ) l fitted with the male half of a 1 1/2 inch Hansen quick disconnect  : fitting. The other two are 3 inches (nominal pipe size) and closed with standard, gasketed bolt-on flanges. 0396B/LC

                                     *g'                                           I             ,,

50 3517-005~ The inle? nozzle is a-short nipple extending from.the..Hansen .. l coupling into the vessel then leading to'a. spider-type _ inlet spray. header. ~There.are four s' pray outlets:each terminating'in a-L3" 00 Johnson screen, 1.1/2. inches in' length with a gap size of l 1 0.006. inches. At the inlet.to each screen a 0.32 inchd'rille'd-

                                                                                                           ]

passage assures the proper distributing:at each' outlet. j LThe vent nozzle ~1s'a short 1-1/2. inch (NPS)' nipple extending'. through the! top of.the' vessel. A three; inch diameter. 007 inch. I screen cup lis welded around.-the pipeLon the;inside'of.the vessel as a resin retaining measure and the outside end.is;provided.with' a 1 1/2: inch male Hansen fitting. l l The outlet line consists of three 1.1/2 inch (WPS) segments, two A of these are st#aight stainless. steel pipe segments'and the third l' is a 24, inch long flexible convoluted stainlessLsteel hose connecting the pipe segments. The flexible portion allows for  ; differential heating of the. vessel components. The bottom pipe # { segment extends from 1/8 inch from'the'. bottom of the liner, through an inverted 6 inch ODLJohnson' screen (0.007, gap)'_to mate with the hose, The screan is welded to the outlet pipe segment ~ ' and the vessel head to form a. sealed area and'thus act as a resin

                                                                                                      ~

I retainer.to prevent' zeolite escape from.the bed. l The two 3 inch nozzles on'the. vessel head are used for general vessel access and loading and. unloading the-ion exchanger media. > Each is constructed ofLa'short 3' inch-schedule 160 pipe welded to 1

                                                         -47.-                           0396B/LC'              I E  _______z_:-___ _ _ . _ _ _      ._
                                                                  ,     50 3523-005-the vessel l head andlprovided with a; standard ANST. flanged
            ~closu're. Each blind flange is: drilled'and tapped'for a'l/4; inch
            .NPTsvent' connection.. Stainless: steel,1/4"'flexibictubingLis; attached to the one. blind flange for venting vessels.of ~     ,

radicly_ sis gases during storage. A 3/4" 00.' Johnson .007' inch' screen cup. one inch in length is welded to the inner side lof-

           .each blind flange to' prevent resin fines from entering the' vent,
            'line, tihese vessels ~will be located (whenLinstalled in the system) in secondary containments that are the'same as those used'with the

pref 11ter and final filter. The leakage containment pump' takes a' suction off the bottom of all'the. containments and' draws any leakage from the vessel fittings =along with pool water down 8 through the containment to the pump and discharges'_through the' leakage containment ion exchangers back into the' pool, These vest.els are located along the east' wall of the 'B" fuel' pool.

                                                                                        .]

2.1.4 Manifolo Containments 2.1.4.1 Hi Rad Filter Manifold Containment. s i A majority of the valves, instruments, and piping runs, associated with the prefilter and final filter form the filter manifold which is housed in a shicided, ventilated' containment. -l l This manifold is located on the' cask support platform at the  :

                                                                                           ]

south end of the "B" fuel ' pool..

                                                                                         .i t
                                        -                            0396B/LC        i

SD 3527-005 The containment is 3 feet, 6 inches aide, 6 feet 10 inches long - and 1 foot 10 inches deep. It is constructed from 3/16 inch thick stainless steel plates and frames. Shielding is provided on the outside of the containment, on the top and sides. The bottom of the containment is sloped to one end for drainage. Any collected fluids will energize CW-Li-FLO6, activate the local alarm and initiate sump pump 527-G-07, which pumps.the water to the off gas sepsrator. tank. The containment box is ventilated and maintained at a negative pressure by.the 505 Off Gas System. The intake and exhaust connections are 2 inch lines' located at 1 opposite sides of the containment box. Access ports are provided in manifold containments for maintenance of the valves and instruments and are shielded with lead blocks. Valve operation will be performed using reach rods which protrude through the top shield. All reach rods for manifold containments utilize lead. collars under the lead block which cover the six inch diameter access holes. This feature prevents streaming at the valve stems. 1 2.1.4.2 Ion Exchange Manifold Containment The ion exchange manifold containment houses valves, piping, and instruments associated with the ion exchange process train. The manifold is located on the walkway between the "B" fuel pool, and the "B" spent fuel pool surge tank. 0396B/LC

                                                        ;;[ :       i                  ,
                                                                                                                   ~
                                                 'y ,                                             ..         .

SD 3527-005, Thecontaj$ientis.13 fee?3incheslong.?3. feet 6. inches. wide-' . and 2 feet 4 inches deep. It'is constructed'of 3/16' inch '

                            = stainless steellplating and reinforced.with stainless stsel supportsyf
                                    %j Thed?ntainment'is; divided linto.two. sections,;a.highlevel' r,ecticm and a flow level section, Pipin(YUnsan'd associated                               .

equipment,; subjected- to waste which has not been processed through'a zeolite train 'are located in'the high level' area. The~ south end of the containment box has an external shielded chimney which overnangs the "B" fuel pool wall and descends.to the watcr' surface,and i's partially submerged underwater. With it the exception of sampling and flushing lines.. piping enters the containment underwater linto this' dropoff) for. shielding  ; considerations. o 1. A one inch thick carbon steel plate covers the low'. level area and l a five inch thick carbon steel plate covers the high'1evel area, The sides and' top of the' containment are shielded with lead according to the radiation' levels estimated to exist. l

l. j i

The' containment is ventilated and maintained at a negative pressure by the SDS Off Gas System, ' Liquid' leakage'and gravity 1 drains to the moisture separator tank. The air intake nozzle is I located in the low devel end; and the.exhailst is'in the'high level end of the manifold.  ;' . 4 a n s I

                                                         .                                     0396B/LC 1

f _, l

                                                                      'S c y                                      ,

SD 3527-005 2.1.4.3 Reactor Coolant System' Cleanup Manifold The RCS cleanup. manifold was developed in order to establish tie-in points in the SDS System which can enable it to process the Reactor Coolant System via the reactor coolant bleed tanks. The RCS cleanup manifold is l'ocated on the south-east corner of the SDS cask support platform. The RCS cleanup manifold is four feet wide, four feet long and two feet high. The manifold is ventilated and maintained at a negative pressure by the SOS Off Gas System, and sump liquid accumulations are pumped to the offgas separator tank by an l automatic level controlled sump pump. The manifold is shielded 1 i

                     'and the valves are operated from outside of the containment using reach rods. Valve and instrument access holes and reach rod shielding is accomplished using the techniques described for the        i other manifolds.                                                        i 1

2.1.5 Off Gas and Liould Separatio,n System 1 2.1.5.1 Off Gas Heater The 9 KH off gas heater is provided to decrease the relative l humidity of the gases to insure proper operation of the prefilter, HEPA filters and charcoal adsorption bed. l l 0396B/LC

w

 .. v                                   a.

SD 3527-005-u c,g . # <

                                                    ..  .X    .

cDuring'normaloperation,theoffgas' heater. cycles:onand.off., p: a-automatica11y'to control.the air temperature downstream of the heater at'122*F b'y means of.a temperature element:, sensor. IThis. temperature element. sensor also: supplies the~ signal,which v. g activates a high; temperature' alarm which alerts the operator'in' '

            -the event hea'ter sffluent' air temperature reaches'200*E.' To:

r w } f" g

j. ,

further protect the hsater the': Unit is=also equipped with both an-Auto and Manual Reset heater: effluent high. temperature cutout; which interrupts' power' automatically to the heater'at 285_.2 15

  • F.
            -and;320'g 15'F, respectively.
            ?    t Temperature element sensors are also installed on the.off gas-unit at the heater influent'and' charcoal adsorber effluent.

These indications allow the operator.to monitor the heater i performance relative to maintaining relative humidity'less than , 70% leaving the adsorber stage. 'A temperature rise in excess'of 11*F ensures that this condition:is present even =1f air entering the unit is at.100% relative humidity. .A flow indicator, also mounted on the heater influent .line, allows thel operator to verify that air flow between 650 to 1000 CFM it present:for heater operation. An interlock is installed in the heater controller which. prevents-heater operation if the1 off gas blower-circuitry.is deenergized. 4 a-al . 0396B/LC' l 1 I -.

       > ,                                        o                 ,                              ..,

y SD 3527-005

           .2.1.5.2   Off Gas' System Filters.

1 i Exhaust gases, from components ventilated by the. Vent and Drain System, will pass'through1four-filters (in the off gas; System  ; I befo're being exhausted to the plant ~ vent stack. 'The four filters '

consist of a roughing filter, two HEPA filters, and-a charcoa11 .

adsorber. .

                                                                                                     .i All.four filters are equipped with differential pressure
                    ' detectors. These instruments allow the' operator to monitor filter loading, 'and determine when a filter needs' replaci,ng'due 1            !

to crud buildup. Test connections are also provided on:the influent and effluent. side of each filter. The HEPA~and charcoal filters will be DOP and. Freon tested, respectively, after the off gas filtering unitsare. installed'in the SDS, -These. filter types will be retested when replaced. Testing is' performed in i accordance with Regulatory Guide l'.140. The roughing filter is a waterproof, fiberglass type filter,- compatible with the air stream. The' filter'is designed to 1 withstand a pressure drop of,8 inches H.G., either new, wet or loaded with dust, for at least 15 minutes without damage. At a differential pressure of.0.5' inches W.G. or a radiation level.of 100 mR/hr at contact with the filter housing,;the filter will be i replaced. i l

                                                                                                       )
                                                                                                  >l 0396B/LC' l

_______ A

                                   'I' 3                                            . SD 3527.- 005       I
                ~

There are two.HEPA filters installed in the off' gas unit designed ' to be 99.97 percent efficient for, particles;down to'O.3 microns-

       .in size. The filters are'24' inches by 24 inches. square and 11
                    ~

1/2' inches deep. The'fil.ter medium is principally inorganic fiber.'~ Organic fibers.will~not exceed 5' percent. .At.a h j differentia 1' pressure of 2 inch W.G.'orfa radiation level of 1001 j o mR/hr at. contact with.the filter' housing,-'.the filter'will.be j replaced. The system also utilizes a charcoal adsorber bed for

       .the removal of. radioactive iodine. This'adsorber filter has the-              Lj same replacement requirements as those of the:HEPA filters.                      I 2.1.5.3  Stored Vessel Venting Manifold A venting manifold is provided for' exhausting gases generated in the stored ion exchange vessels after these vessels have been dewatered. This manifold consists of a 1" diameter stainless steel pipe approximately 26' long containing 60-3/8" nipples, with caps, on 4" centers.      It is' located above.the spent vessel' storage racks on the west side'of fuel pool "B", level with the floor elevation, running north and. south. On the south end of the manifold it ties into a 2" diameter stainless-steel pipe (L527-80-2) which connects to the off-gas filtration unit. The north end of the manifold contains.a Dollinger Air Filter which provides an air sweep for the prevention of gas build-up.in the venting manifold. The vessels are connected to.the manifold by a 1/4" diameter flexible stainless steel hose 25'-6" long.

0396B/LC  ;)

3 'l x w SD,3527-005-Provisions are also made for connecting.a non-dewatered vessel into the manifold. This:is accomplished by inserting a 0-400 psi.- pressure gauge and ball valve on the vent manifold nipple an'd then connecting the vessel vent'line to the gauge. 2 .1.' 6 Major System Valves l 2.1.6.1 Submerced Ion Exchance Manifold Influent Automatic Isolation , L L yaive(CN-V-IX24)- The automatic isolation valve is a 1 1/2' inch solenoid operated- I ball valve. It is located ~in the high activity area of the j submerged ion exchange' manifold' containment, at the north end of I fuel pool. the "B" The valve incorporates an automatic shutdown function to preclude i the consequences of adverse conditions frcm occuring which might damage equipment and/or cause injury to. personnel. Feed j Isolation Valve (CN-V-IX-24) is controlled from the Feed Shutdown System Relay Panel (RP-1). The " Auto-Trip" selector switch in the " Auto" position energizes the Feed Isolation Valve Solenoid 1 Valve (CN-UY-IX24) admitting air to CN-V-IX24 to open, providing a trip signal is not present. Trip signals from Off-Gas Header  ; l Influent Pressure High High Switch (CN-PISH-VA28), IX Manifold- l l .. Effluent in'Line Radiation High (CN-RSH-IX04), or Leakage Containment System Influent Radiation High (CN-RSH-LC05) deenergize CN-UY-IX24, and IX Manifold General Area Radiation 0396B/LC

                                                                            \

_______.______.________._________w

                     ., .                                                                                                                     A          }
                                                                                                                                ;s.:        .             1 4                                                                                      SD 3527-005                 ]

1 High'(CN-RAH-IXO3)-deenergizes CH-UY-IX24 on~an adjustabl~.5'tos e ,

                                                                                                                                                         .1 50'.second time delay.       Instantaneous closureJis affected by.                  <
                                                                  . placing'the " Auto-Trip" selectoriswitch in the." Trip". position,.

or upon loss of power.to,elther RP-1 or the solenoid valve orL Lupon loss of air.to the solenoid valve. 2.1.6.2 Monitoring' Tank Fill Isolation Valves ' a The Monitor Tank' fill' isolation valves, SDS-V-002A and i 1 SDS-V-002B, are designed to automatically isolate the monitoring. 1

                                                                                                                                                         .g
                                                                  ' tanks if the tanks are fil. led above a pre-set level.                                   ?

q 2.1.7 Dewatering Station I The dewatering. station ~1s located in the cask pit at the; north s end of the Unit 2 Spent Fuel Pool. It consists of two containment boxes positioned underwater, one'for filter vessels < i -- and one for ion exchange vessels, along with' associated piping, valves and instrumention. Shielding is provided by th'e Spent Fuel Pool water and by. utilizing lead shielding on pipe runs above water going'to the.off. gas separator tank. The dewatering containment boxes are not connected to the leakage containmen't-system. The purpose of the dewatering station is to dewater filter and ion-exchange vessels by the use of air or. nitrogen'in preparation for shipment.

                                                                                                                                '0396B/LC l
    . _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ . _ _ _ _ _ _ _ _ _                                                            _               _                     l

i SD 3527-005 l The dewatering process involves passing a constant air or 1 j nitrogen flow through the spent vessel for a fixed amount of ' time. When nitrogen is used as a dewatering gas, the nitrogen is ] 3 supplied by a 200 ft , 2200 psig bottle. To preclude ,l 1 overpressurization of the system the nitrogen supply is connected i to the dewatering station through special piping equipped with a l relief valve. j 1 l The spent filter and ion-exchange vessels can be dewatered prior l 1 to storage in Spent Fuel Pool "B" or shipment to interim storage { l elsewhere on Three Mile Island. When it is decided to move.the l 1 vessels from the Spent Fuel Pool "B", they will be dewatered and i then loaded underwater into an appropriate shipping task prior to removal. Also see Appendix 16, Liner Recombiner and Vacuum Outgassing System. l 2.1.8 Remote Operating and Manipulating Tools i l J 2.1.8.1 Hansen Connect / Disconnect Tools l l The Hansen Connect / Disconnect tools are fabricated from stainless a ' steel and are mounted on the Ion Exchanger, Filter, Leakage Containment and Dewatering Station racks. 0396B/LC u____- - _ - _ _ _ - _ -

SD.3527-00$

           .0peration is achieved by a mechanism that disengages a 1 1/2" stainless steel female Hansen coupling, and couples it to a 1 1/2" male Hansen attached to the Ion Exchanger or Filter vessel.

Each vessel has three (3) nozzles associated with SDS operation: inlet, outlet and vent, and each nozzle has a separate tool to connect the appropriate hose to the corresponding vessel nozzle. The coupling operation is performed from approximately. twenty (20) feet away.from the vessel from the operators work platform located at each station. The platforms are located approximately (2) two feet above the pool water level. A quarter ton electric hoist is provided on a monorail overhead for ease of lifting, and-lowering the tools into position, I These tools provide the means of remotely coupling and uncoupling filter and exchanger vessel connections while keeping radiation exposure to the operator to a minimum. The Dewatering Station utilizes two (2) tools per vessel, an inlet air connection and an outlet connection that directs I effluent to the off gas separator tank. 2.1.8.2 Exchanger and Filter Vessel Lifting and Positioning Tools 2.1.8.2.1 Unspent Vessel Tool: The unspent vessel lifting tool is constructed from stainless steel. It consists of two (2) J-hooks , which pivot and are attached to a lifting shaft. The hooks are 0396B/LC

1 SD 3527-005

         ! aligned with the vessel b'y a. guide arm that fits into a'. notch'in the. vessel upper skirt. 'The: tool also has a. set of guide arms to position the vessel properly in the. containment box. These arms
         . have guides of two different sizes that mate with slots of corresponding sizes in the containment. boxes and storage racks,
         . to insure correct orientation of the vessel' nozzles when placed
         ' in a containment box; additionally the.' Tool and. Fuel Pool deck-are marked with arrows which are positioned in the same directi.on.

l-The' bottom of the containment boxes also: Utilize a guide assembly which mates with the bottom of the vessel'to keep,the vessel from rotating or tipping after the handling tool ~is released. f 1 The Fuel Handling Building Overhead Crane is used to manipulate the li.fting tool., i The J-hooks are engaged manually into lifting lugs welded-to the vessel upper skirt at the pool curb prior to lowering the vessel  ; into the pool. Disengagement occurs once the vessel is positioned and its weight is released from the tool. .The weight of the hook itself allows the hook to drop clear of the lifting lug and the tool can-be removed. I l 1 A spring actuated locking mechanism located on the J-hooks keeps ' the vessel from inadvertently disengaging the hooks if the vessel is accidently bumped. The locking device is unlatched manually. from above the water surface by means of a' pull cable.  ! l 0396B/LC

i SDL3527 005

 ,                                                                                               i Th'is tool is'used'only:for loading unspent Exchanger;and Filter-      i vessels into containment. boxes. The manual latching requirement:           ,

precludes the use of the tool.for'the movement.of spent' vessels. When not in'use it is stored in the cask pit on.the yoke hanger j i assembly. -{ l

                                                                                               'l 2.1.8.2.2        . Spent' Vessel Tool: The spent vessel. tool'is basically identical to the unspent tool with:the following differences:                          l 1

i a) 'This tool'is used to move spent vessels from containment box-to containment box, or,to a' storage rack, or to the Dewatering Station for dewatering.:or to the Shipping Cask for removal from the pool. I l b) The lifting shaft is longer to prevent inadvertent. lifting , of a spent vessel too near the surface of the pool. The shaft is long enough such that when'the' crane hook is at its l top travel, the vessel will remain submerged and property' shielded. c) The J-hooks are engaged and disengaged using air operated cylinders. The locking mechanism is spring loaded and must l be unlatched manually. . l V , This tool is also stored in the cask pit on the yoke hanger  ! assembly when not in use. l

                                                - 60 .                            0396B/LC.
                                                                                       , l SD 3527-005'    d 2.1.8.2.3, . Alternate Spent Vessel 1 N 1_

a Operatincj experience. with SDS necessitated _c'esign and fabrication-of an alternate spent vessel lifting tool'for.two' reasons;- .1)-  ; leakage. containment vesselsLare-not'. highly loaded and are' removed D1 from the pool for resin changeout .and 2):in the deep st'orage location, delatching problems tended to off: center some vessels-since the storage locations', unlike the processing locations, do not have guide assemblies in the bottom. , The origira1-spent vessel' tool coul'd not be used'to remove-leakage containment vessels since it was desinged to' prevent-

            -lifting of highly loaded vessels'from'the poolfand out of the           -

water shielding. The original' tool also centered inside the container cubicle and not on the vessel thus making retrieval o' f' an off center vessel impossible. The alternate retrieval tool is identical to the original tool except in length and the method of_ce'ntering'on the vessel. The. I length _is shorter to allow retrieval of_ leakage'~ containment ion exchangers and the tool has been' redesigned'to' center on the center nozzle of the vessels; allowing retrieval of off center vessels. Because the vessel movement tools have become bent'during'use all I vessel handling tools have replaceable. spool pieces at the bottom

             ~

i end, which when they are bent may_be replaced. The bottom end of l 0396B/LC l

e. ;j q

SD 3527-005- j

                                                                                                                 'I the tool can also be replaced if damaged. The alternate' spent'.             l
                                                                                                ~

vessel tool bottom assembly can be removed from the shortiversion '

                                                                                    ~

and placed on the.long. version:for handling of highly . loaded vessels safely. 1 J 2.1.8.3 Recovery Tool

                                                                                                                    .I The recovery tool is fabricated from stainless. flanged pipe.

sections which serve to allow.the length of the. tool to be j l alterednecessarybyaddingjor.deletingfpipe. sections. '

                                                                                                                    ,1 1

r ! l l The tool is manipulated-by the' Fuel Handling' Building Overhead. 1 1 Crane or can be attached-to'one'of the'1/4 ton hoists located-on-  ; each rack for Hansen tool manipulation. l l There are three (3) attachments associated with the recovery < tool, two (2) types of.J-hooks and a flexible hose handling i attachment. sThis ter) is a general recovery tool to be used for misce'llaneous recovery and manipulation which may arise during the course of operation. 2.1.8.4 Noveable Spent Vessel Rack Liftina Device i The moveable spent rack lifting device is constructed from carbon i' steel with stainless steel locking pins. The' pins are engaged and disengaged by air actuated cylinders.  ! 0396B/LC L

y.

                                                                           .SD 3527-005
                                                                                           .i
                .The device is manipulated using:the fuel Handling Building                  !

ove'rhead crane and is used to lift and position the four (4) moveable spent storage racks. l 1 l 2.1.825 Vessel Nozzle Plugging Tool i l l

                                                                                         ;{

The nozzle plugging toolt is constructed of' stainless steel. . I t' .l

                                                                                              \

consists of a mechanism for remotely placing a plug in the l 1/2" male Hansen on'theLvessels. .'Once the plug is:in place, the tool release's and disengages from the plug.  ;; i U This tool is manipulated using the' Fuel Handling Building  ; Overhead Crane and.is operated manually.  ! 2.1.8.6 Pressure Instrument Diaphragm Removal Tool l l The diaphragm removal tool is fabricated from carbon steel bar. stock and is manipulated manually. It is'used to remotely loosen the diaphragm of the Ashcroft pressure indicators located in manifold boxes and glove boxes for maintenance, removal or replacement. 2.1.8.7 Vent Hose Handling' Tools The vent hose handling tools consist of four' specific _ tools each of-which are twenty-four feet in length, constructed of stainless steel pipe and having different end fitting. Their function is 63 - 0396B/LC ,

b. <

lSDf3527-005l ,' '

            - to.allou. stored spent lon exchanger; vessels vent. hoses to be-              , .!
                                                                      ,                         s raised and' lowered out of, Fuel: Pool "B",1th'us' allowing these vesselsiobevented. This venting..' operation (1s'necessary-to I

eliminate any pressure buildup.inside these vessels due"to-  !

                                                                  ,                             i radiological decomposition ~of> water. held:by-the spent zeolite;      A-
           ' description'of each" tool _ type.'and.their function"is presented-                 ;

l bslowi i (a). Single J-hook Tool I

                                                           ,                                  j This tool'it;used to;1ift the spent! ion exc' hanger ' vessel.

vent hose.from its. position on topf of the vessd 'to above the Fuel Pool "B" water level.

                                       -                From~this location the vent l:'                  hose is manually connected to the SDS' vent header and the I
                  ' valve'on the ven.t hose cycled. The tool ccnsists of'a stainless steel pipe with a J-hook end fitting.

(b) Double J-hook Tool This tool is used_to_ assist in guiding the~ vent hose in j i place on top of the spent ion exchanger. vessel:as ft is lowered into Fuel Pool "B". The tool consists of.a , stainless steel. pipe with two_J-hooks each in.oppos.ite direction as an end fitting. This design allows the vent hose to be held securely during this lower. operation. l l  ! 0396B/LCl

                                                                                                                  ^ ~ 'l:

j 'r iSD 3527-005

                                        -(c)- Inverted Y Tool 1

This tool:is'used.to position and hold the vent hose in' j place'on top of the spent 11on' exchanger vessel as'the-. vent- . hose is. lowered into Fuel Pool "B". The tool consists'of a - _ stainless' steel pipe with an inverted Y.end fitting. l (d) Retainer Clip Tool This toollis used to hold the vent hose'as'it isilowered into Fuel Pool "B" and to clip the vent hose retainer clip-on the top of the spent lon.. exchanger vessel. .The ' tooli consists of a stainless steel pipe with a threade': dmale-end' i fitting'which mates to the^ retainer. clip on the vent hose. .l l l l All of these tools are. manipulated by the operator. manually. In ) the case of the Retainer Clip Tool it is> supported by the' Fuel-Handling Building overhead craneLduring the lower operation of i the vent hose. l 2.1.9 Samplino Devices 1 f'mpling of the SDS process' stream is accomplished by' utilizing l three sample boxes. These devices provide central locations " where intermediate 0'd high level radioactive samples can be i taken for evaluating the system performance. They are:- i 0396B/LC 1

SD 3527-005

         '1. Hi Rad Filter Sample Glove Box
2. Hi Rad Feed Sample Box
3. Intermediate Level Sample Glove Box In addition, samples can~also be taken at other SDS locations which handle low levels of radioactive water and, thus, do not l require special boxes. These locations are:

I

1. Leakage Containment Pump Area.
2. Monitor Tank Pump Area.

2.1.9.1 Process Stream Sampling The process stream water is sampled at various stages of treatment using centralized sample boxes. These sample box containments are designed to be completely sealed. A negative J pressure greater than 0.25 inches of water is maintained inside " l the sample boxes by the SDS Off-Gas System. Each sample box is l also equipped with a differential pressure gauge and a low l differential pressure alarm. All sample boxes are double wall construction with lead shot between the walls to provide shielding during sampling activities. Additional lead sheet has l been added to the exterior of each box to further reduce occupational exposures where required. The sampling boxes and the locations which they monitor in the process stream are discussed separately below. 0396B/LC

SD 3527-005 2.1.9.1.1 Hi Rad Filter Sample Glove Bo.x l This sample box is located on the west wall at the southwest corner of the "B" fuel Pool. There are two sample points inside the glove box; the influent of the prefilter and the effluent of 1 the final filter. These two sample points incorporate a l continuous loop sampling design. Throttling of the process stream is required using CN-V-FL-3 for the prefilter influent sample and CN-V-FL-6 for the final filter effluent sample. Since flow does not continuously go through the sample line, it is necessary to recirculate through the lines prior to taking a sample. To prevent the sample box sump from overflowing, a sump pump is installed which transfers the waste water to the off gas separator tank. 2.1.9.1.2 Hi Rad Feed Sample Box This sample box is located on the surge tank cover at the north end of the "B" Fuel Pool. The box contains only one sample point which is used to obtain influent samples to the first zeolite in 1 each processing train. Provisions are also provided to allow samples to be taken from the first zeolite vessel effluent in i each processing train if activity levels of the feedwater passing through these vessels exceed 1 pci/cc. This information coupled with other data is necessary for calculating the ion I exchanger vessel loading and efficiency. Since flow does not l continuously go through the sample line, it is necessary to 0396B/LC 9 l l

       .o         4 J
   ,                                                                       .SD.3527-005-recirculate through the linesLprior to taking a' sample.       The su'p.

m

               'in this box is designed to' gravity' drain to the off-gas separator tank.

2.1.9.1.3 Intermediate Level 5 ample' Glove Box Thisl sample box is~ located on the surge tankEcover, next to the beta monitor manifold, at the ncrth end of the "B" Fuel Pool. The box.contains.eight-(8) . sample _ points which provide the capability'to monitor individual' ion exchanger bed performance. The samples are:taken.fromhe t following system points:  ; 1, Train #1', Zeolite "A" Effluent.

2. Train #1,' Zeolite "B" Effluent.

L

3. Train #1, Zeolite "C" Effluent. l
4. Train #2, Zeolite "A" Effluent.
5. Train #2, Zeolite "B" Effluent.

6, Train #2, Zeolite "C" Effluent.

7. Trains #1 and *2, Cation-Influent. ,

[ - .

8. Trains #1 and #2, Cation Effluent.

1, Flow for this sample box comes from a diverter-valve in the beta-monitor manifold. After placing this valv'e in the' sample' l position, it is necessary to first recirculate-process fluid J through the sample line prior to taking.a sample. _ Samples;are collected in a common, replaceable sample bomb. The sump-in this box' is designed to ' gravity drain to the off-gas separator tank. ) I i l 0396B/LC'

                                                                                         .]

i

                             ,                                                                                ,1
                                                                                -SD'3527-005:

2 , l' . 9. 2 - 'Other Sampling-The remaining SDS sample locations, due to the low level of radioactive water which.they handled,'do.not employ special lead. shielded sample boxes;.although the monitor' tanks employ a-special plexiglass enclosure to reduce the potential for airborne actlyity and provide. shielding from beta radiation. These-components are:the monitor; tanks which contain.SDS effluent  ; water, and the leakag'e containment system which keeps'the fuel Pool water from.becoming. contaminated. These areas _are discussed-separately.below. 2.1.9.2.1 Leakage Containment Syst'em The le?kage' containment sample points are' located on the ion

                                                                            ~

exchange platform in the nor th end of the "B" fuel Pool. Since the water being processed is pool water and potential leakage from various SDS components, it does not require an enclosed Il manifold or special sample box. There are two sample points in-J the leakage containment system, the leakage containment ion f exchangers influent'and effluent. The Influent sample point will  : provide an indication of component leakage and the effluent sample will provide an indication of containment ion exchanger

                                                                                                               . .I
                                                                                                                   ]

removal efficiency. i 0396B/LC , i ______.a - _ _ _ _ _ - - -

                                                                              .SD 3527-003 2.l'.9.2.2     Monitor-Tank System J

The-monitor tanks.and pumps arel located in the Fuel Handling l i Building Model Room at thel305'. elevation. The monitor tanks are sampled locally at the discharge of the respective pump. The-l monitor tank contents are recirculated via the pumps throughL 1 installed eductors-in'each. tank 1and then. sampled. The sample'is a a " grab sample" taken from a spigot. These' tanks will contain'- 1 i only SDS processed water used for. flushing SDSfcomponents or.as 'l I staging tanks for EPICOR II processing. .j J l , 1 2.1.9.2.3 Spent Vessel Gas Sampling-1

                                                                                            .)
                                                                                            'l
                                                                                            .)

Gas sampling of the spent ion exchange vessels is provided by.thef l Liner Recombiner and Vacuum Outgassing System (Appendix 16). 1

                                                                                            .j 2.2      Instruments, Controls, Alarms and Protective Devices:-                         l y
                                                                                             )

2.2.1 Instrumentation and Controls j l i Instrumentation and' controls are located on the 347'6" elevation J j of the Unit II Fuel Handling Building except.for local start I capability for the Monitoring Tank Transfer: Pumps PIA and PlB, local Monitor Tank Level Indication SDS-L1-1A and SDS-L1-3A and i i SDS Monitor Tank Transfer Pumps Discharge-Flowmeter readout.  !

                                                                                            'i l                                                                                            l 1
                                                   .70 -                          0396B/LC'

SD 3527-005 Radiation monitoring is performed at the Radiation Monitoring  ! Panel (RMP-1) and.the packaged Off Gas Radiation Monitor 1 (Eberline PING-1A). The RMP-1 contains linear ratemeters and a multi-point recorder for the seven Beta detectors (CN-RE-IXO4,  ;

                                                                 -LC05,-PM07,-PM08,-PM09,-PM10, and-PMll) and the gamma detector CN-RE-IXO3. Only channels CN-RE-IXO9 and CN-LC05 are recorded by the Multi-Point Recorder. It should be noted that the Beta          I i

Manifold is in place but has not been used to date or is its use planned in the future. I' The Beta detectors are G-M tubes monitoring the process water through teflon tubing winaows located in the Beta monitor l manifold. A nylon window is used on the suction of the containment water pump and nylon tubing on the exchanger manifold effluent. The high voltage and 12 VDC required to power these units is distributed through fan-out connectors in the radiation I monitoring panel. The pulse discriminator output provides a posit!ve six volt square pulse for every negative input pulse from the G-M tube that exceeds the discriminator threshold level. The output of the pulse discriminator 1s connected to the input of the linear ratemeter/ alarm where it is displayed as a count-rate. The gamma detectors consist of a G-M tube, selfcontained high voltage power supply,. pulse amplifier, low voltage regulator, and line driver with output to an electronic readout / alarm channel. CN-RE+IXO3 is the area monitor detector mounted on top of the radiation monitoring panel (RMP-1). 0396B/LC

                                                              'SD 3527-005; "Both channels are recorded on the multi-poin't; recorder (CN-RR-RR16).                                                                         V Measurement of the'off-gas effluent beta particulate, lodine'129' and noble gases is' accomplished'through.the packaged PING-1A.

sample system. : Ambient background radiation.is also measured and subtracted from the activity in.the: air' measurement providing. higher sensitivity'to:the radiation. level in the process' stream, i~ Sample intake goes through a filter paper on whi_ch.any particulate is deposited, then through a charcoal cartridgefwhii:h - l'f traps the iodines, then. into the gas: chamber .and .is exhausted back'into the off-gas ducting. Localcindication and recording; are provided on the PING-1A. Start /Stop control for the Reactor Building Pump (SWS-P-1) is. located on SDS Control Panel CN-PNL-1 with stop capability lon the local panel on the east wall of the fuel Handling Building. Control for pump WG-P-1 is also located on CN-PNL-I with

   " Remote-Local" selector switch.

The Off-Gas Bottoms Pump'(CN-P-VA04). Leakage Containment' Pump (CN-P-LC06), and the MSA Off-Gas Blower (CN-P-VA05) are all controlled from their respective local starters. The Off-Gas Bottoms Pump has'an " Auto /Off/On" key-operated  ! l selector switch. This pump is used in the manual position:and tank contents are pumped out by operator actio7. l j

                                                                                                 .C
                              -                                            0396B/LC j
                                                                                                .j a

50'3527-005 The MSA Off-Gas. Blower and, Leakage Containment pumps'have1 simple

        " Start /Stop" p'ush buttons.                                 '

l

      .After filtration by the pre.and final filters, the ' influent water;
                                                                                   .f i
      . passes;the Feed Isolation Valve.(CN-V-IX24) which is controlled from>tte Feed. Shutdown. System Relay Panel (RP-1). 'The
        " Auto-Trip" selector switch'in the"" Auto" position' energizes:the feed Isolation Valve Solenoid Valve (CN-UY-IX24) a'dmitting. air.Lto      .1 CN-V-IX24 to'open providing a trip signal.is not present.' Trih;           .j u

signals from Off-Gas: Header Influent Pressure High High Switch

                                .                                                 'l
                                                                                   'l (CN-PISH-VA28) or IX Manifold General Area Radiation.High:                  1 1

(CN-RAH-IXO3) deenergize CN-UY-IX24 on a 5:to 50 second time O delay. Trip signals.from IX_ Manifold' Effluent'in Line Radiation high (CN-RSH-IX04) or Leakage Containment System Influent l Radiation High-(CN-RSH-LC05) deenergize CN-UY-IX24 on a 5 to 50' second time delay. Instantaneous closure is affected-by' placing g i the " Auto-Trip" selector switch in the " Trip" position.  ;) l l

                                                                                     )

Downstream of CN-V-IX24 are two (2) vortex shedding" type flowmeters with totalizers to measure the flow into either Ion Exchange Train. The vortex flow meters have a local readout.

                                                        .                            1 Local Pressure instrumentation is located throughout the process-
                                                                                     )

in areas such as the inlet and. outlet'of each exchanger of filter. Many of these pressure indicators are unnecessary for- . system operation but provide indication of individual exchanger performance. -The pressure gauges are. weatherproof and 11guld i filled such that the process pressure is sensed through a remote diaphram. ( 0396B/LC.

I SD 3527-005; , d l

 ' Feed temperature is measured.in the'RCS' cleanup manifoldL (CN-TI-RC07). Measurement 1s made'with'a thermocouple.with a hot' junction welded to the feed line. The, thermocouple is connected-
 'directly to the input of.a' digital' readout temperature
 . indicator. The indicator'and housing are on a support stand' mounted on top of the manifold.
                                                                                 .a
 'The.SDS System.is' flushed;using deionized or' low activity processed water whose flow is measured through a hand held flow totalizer. The flow isicontrollert with the off-on action of
 ' solenoid valve CN-V-DW-339.

The system is started by-. setting the: total gallons desired with the dial on the batch register and. pressing th'e start button. This'will energize CN-V-DH39 allowing water to flow through'the meter. The register will count down the gallons of water to zero, where it will de-energize CN-V-DW-339,. shutting off. water flow. The Leakage Containment System surrounding all of the Ion Exchangers,' Pre and Final Filters have. flow'. orifices with manometer readout to indicate positive. flow into each containment from the. pool water. The Leakage Containment Pump has a local  ! pressure gauge on its discharge and. Inlet.

                                                                                 'l
                                                                                    )

J l 0396B/LC

i

                                                              .SD 3527-005-An'07f-Gas System maintains a negative pressure'on.the'five.505 manifoldsandthreesamplinggloveboxes..Eachmanffold'orgicve box as well as the 0ff-Gas Header Influent has a Pressure Differential Indicator / Switch. Pressure differential is sensed through a 1/4-inch' pipe' nipple and 3/8-inc'h 0.0.' tubing connected         j i

to the' low pressure side of a' pressure differential ... indicator / switch (high. pressure side . vented to atmospherd. The-sensed pressure differential is indicated on a-0 to 1 Inch of 1 q water scale-(0 to 15 inches.of water on the:Off-Gas Header ' j u ' Influent). 'A low pressure._(high' vacuum) snitch actuates a. local i audible-horn at .25 inches of water for.the filter,, feed and RCS. manifolds and the Hi Rad'F11ter Sample Glove Box. A remote alarm' ' and flashing alarm window on Annunicator Panel No, l'is actuated by low pressure switches at .25 inches of water.for the, Ion  !

                                                                              .i Exchangers and Beta Monitor Manifolds and the Hi Rad Feed and                ;

5 Intermediate Sample Glove Boxes. The Off-Gas Header Influent ' Presure High Switch actuates a remote alarm and flashing alarm' window on Annunicator Panel No. 1. ) i The Off-Gas Filtration unit has a 9 KH heater on the inlet sized to dehumidify air from 100% to less than 70% relative humidity at I rated flow. The heater has an on-off controller with temperature indication from a thermocouple mounted near the heater. ' Protective thermodiscs de-energize'the heater at 285*F and 320*F-

                                                                                  "I as does a fan interlock, should the off-gas blower be secured or a loss of power occur. The off-gas blower is started and stopped through a. local controller. Filter differential pressures, inlet               i and outlet temperatures' flow indication, and inlet and outlet pressure indication are provided locally.                                       ;

0396B/LC l

( 1 ' SD ' 3527'- 005 i The' controls'and instrumentation of-the SDS Monitor Tanks consist ,

                        .1
                                         ~        ~

e of controls for;the transfer pumps and inlet: valves a,nd1

      . indication .for Ltank level, pump discharge l flow and ~ pressure.        The--

SDS Monitoring Tank Transfer Pumps PIA _and PIB can befstartediand. stoppedlocallyonthe305'elevationoftNe.FuelHandling

      ~ Building or remotely at the'SDS 4eed'and MonitorLTank' Panel' (SDS-LCP1)'on the 347'6" elevation. Run/Stop' indication'is provided both locally'and remotely. .A selector switch permits:                               d
      . the operator t'o choose the correct nonitor tank / transfer pump'
      ' alignment which in' turn aligns the-appropriate'tanki.s. low-level switch to trip the. pump.

Pump discharge pressure;is displayed locally and on SDS-LCPI.via-a pressure , transmitter. ' A local.reado'ut. flowmeter / totalizer is: located on.the common pump discharge. -Level indication for.T-1A and T-1B are~ readouts locally on SDS-LCP2 and remotely on l SDS-LCP1. I

                                                                                                   .i SDS Monitor Tank Inlet Valves SDS-V002A and B are controlled from                             J SDS-LCPl. The valves close automatically on a high level in                               q their respective-~ tanks. The valves can only'be.opene'd if the:

high level alarm has cleared. I 1 Local oresure and/or flow indication is provided in each of the l l~ three (3) sampling glove boxes. i l l .o l l 0396B/LC l

SD 3527-005 2.2.2 Alarms Annunicator panel No. 1 All field contacts are closed during normal operation and will open for alarm condition. The alarms work as follows: A sensing voltage of 120 VAC is applied through the individual annunicator points via a field contact. Opening of the field contact (signaling an alarm condition) will remove the 120 VAC causing that point-light to flash and sound the horn. Depressing the " Acknowledge" push button will silence the horn and change-the light to a steady-on condition. Closing the field contact (process return to normal)'will turn off the light. The I annunciator point is then reset for.another sequence. Depressing

                          " Lamp Test" push button will illuminate all point lights.

Annunciator Panel No. 1 includes the following alarm points: ALARM ACTUATED BY

1. Feed Valve Closed
2. Exchanger Manifold Low Diff. Pressure CN-DPSL-VA04 -
3. Hi Rad Samples Low Diff. Pressure CN-DPSL-VAll 4.* Beta Monitor Sample Return Low Flow CN-FSL-M18 i
5. Off Gas System High Pressure CN-PISH-VA28  !

6.* Beta Monitor Manifold Low Diff. Pressure CN-DPSL-VA10  !

7. Inter-Rad Samples Low Diff. Pressure CN-DPSL-VA09
8. Off Gas Filter Unit High Temperature CN-TSH-VA04
9. Off Gas Separator High Level CN-LSH-VA03-
                         .10. SDS Monitor Tank T-1A Level H1/Lo               SDS-LSHL                            11. SDS Monitor Tank T-1B Level Hi/Lo                 SDS-LSHL-3          1
12. Leakage Containment Pump Low Pressure' CN-PSL-LC17 .

Not in use 0396B/LC l - - - _ - - - _ - -- -- - - - - 1

                                                                                           ....i       '

jp lS0 3527-005 ) E jp05' Control Panel (CN-PNL-1)

               ~
                       ;i                                                                                ;l 1

The.SDS Contro1LPanel alarms function in a'n identical say to.- -l Annunicator Panel'No. I' .SDS~ Control Panel.CN-PNL-1 includes-the g Jfollowing alarm points:: i

                                                                                                            .I ALARM'                                                             : A('TUATED BY -

1

A6 New FueI. Pit Level'H1' - FCC-LSHL-5 B)f,IIF' Level'Hi " -.

RC-LIS-103L -] B2 IIF Level Lo:<. . RC-LIS-103- 1 86 New Fuel Pit Level'Lo  ;; FCC-LSHL-5 ) Radiation Monitoring Panel 1

.3 ,

The Radiation Monitoring. Panel' Common Alarm (CN'-RAH-IX04) isL 4 located on top of fhe' Panel. :It consists of a bell alarm, alarm

                 . light and a silence and test pushbutton. The alarm is' actuated 1                     .;

when the field > contacts open (deenergized state) from.the

                -following alarm points:                                                                     ,

i ALARM , ACTUATED BY- ) i

1. IX Manifol'd General Area Rad. Hi 4CN-RSH-IXO3'
2. Off Gas Header Influent-Rad. Hi ., CN-RSH-VA06
3. "A" Zeolite Beds. Effluent Rad- Hi
                                                               .                        CN-RSH-PM07

. 4. "B" Zeolite Beds Effluent Rad. Hi: L CN-RSH-PM08-l 5. "C" Zeolite Beds Effluent Rad. Hi 'CN-RSH-PM09 l

6. Cation Beds Influent Rad. Hi- CN-RSH-PM10
7. Cation Beds Effluent Rad. Hi . CN-RSH-PMil i
8. Leakage Containment System Influent Rad. H1 CN-RSH-LC05' I
9. IX Manifold Effluent in Line. Rad. Hi- CN-RSH-LXO4 1

, .i . l

                                                                  ?

l 0396B/LC o , 4 ;! 3

                                                                                                                 ]
                                'c                                                                                 !

SD 3527-005'.. , Off~ Gas-Sampler q The Off Gas Sampler contains Alert and High Level Alarm and. 1 a Normal light. 'The Alert and..High' Alarms have identical circuits with adjustable trip points.and inputs from the Particulate. Iodine and Gaseous readouts. . Exceeding the. trip point energizes the lamp on the'frontipanel and changes the. state of:the: alarm relay. Relay;1ogic is reversible'and alarms may be' locking or. non-locking, selectable by internal switches. .The reset of:a-l

                                   ' locked alarm.is accomplish'ed by pushing the lit alarm light.      In l'                                   addition to the above, the High Alarms activate a fin hingslight and sound a bell.

The Off Gas Sampler contains the following alarm points: I ALARM ACTUATED BY

1. Off Gas Particulate Sample Rad. Hi 'CN-RS'H-val 2
2. Off-Gas Charcoal Sampler Rad.' Hi CN-RSH-VA13 L 3. Off Gas Ion Chamber Sampler Rad.'Hi -CN-RSH-VA14 A failed alarm consisting of a NORMAL light being deenergized is /

I l actuated when the count rate drops'below'one count per minute. l The alarms are disabled during the use of the check source. l 1 Local Annunicators Local annunicators with audible horns include the following alarm l i points:  ; i i l 0396BILC - _ _ _ ._ _ _ - _ - _ . c

       - _ _ _ _ _ _ - _ = _ _ _      ___ - _ ___ ______ _ . _ = . _       _ _ _
                                                                                 - _ - _ _ _ _ _ _ _ _ _ _ _                    _ _ _ _ _ _ _ - _ _ . _ - _ . = _ _ _

e

                                                                                                                               -SD 3S27-005-ALARM:                                                                                     ACTUATED BY l '. Filter Manifold' Containment'DP Lo                                                 CN-DPSL'-VA01 2; Hi Rad. Filter Sample Box DP Lo.                                                     CN-DPSL-VA02                              ;
                                  - 3.            RCS Manifold Containment DP Lo                             . ..          -CN-DPSL-VA12
                                  ,4.              Filter Manifold: Containment: Sump' Level Hi:                           :CN-LS-FLO6t
                                  'S. .Hi-Rad Filter Sample Glove Box Sump' Level'H1 CN-LSH-SA07; 6~.:;RCS Manifold Containment Sump. Level Hi.                                                                                        #
                                                                                                                          'CN-LSH-RC09-All field contacts are closed during' normal) operation and will-open for alarm condition. A sensing. voltage.of 120 VACris                                                                            '

applied through. field contact. 1 Openingofthefield.l contact l(signalingan'alarmcondition)will interrupt thel120 VAC causing.the annu_nicator bullseye l light to= I l flash and sounding an audible horn. . Depressing the

                                  " Silence / Test" push button will silence the born and change the; nlight to a steady-on condition.                            Closing:the field' contact (process return to normal) will turn off'the light.                                          The annunicator point is then reset for another.sequen:e-                                      .             Depressing I

the " Silence / Test" push button will illuminate the bullseye' light. There are two. independent' valves, one for each tank, located'on " l the influent lines to the monitor tanks. They are 1Tl/2 inch. l motor: operated ball valves. The actuators associated with these-valves are interlocked with the monitor tank level transmitters. 1 Position switches are provided on each valve. actuator with

                                                                                                                    ~

indication on the SDS control panel. These valves may be opened simultaneously to avoid hydraulically shocking the SDS ion exchangers and generating fines during monitor tank switch-over. 0396B/LC' A

SD 3527-005 I Associated with the valve is an open/close hand switch, each j inlet valve can be opened manually using its. associated hand , 1 switch. Closure of the' valves can be accomplished manually; at i 1 any time, using the hand switch, The valves will close j l automatically if the tank level is high.- ] 1 Control Room Panel (SPC-PNL-3) 3

                                                                                                                                                                                         -1 The following IIF alarms are located on SPC-PNL-3 in the main control room:

ALARM ACTUATED BY l

21. IIF Level Hi RC-LIS-103
22. IIF Level Lo RC-LIS-103
23. Bubbler Air Supply Pressure Lo RC-PSL-105 FCC Level Hi/Lo FCC-LIS-103
                                                                                                                                                                                             )

l l I l l 0396B/LC

l 50 3527-005 3.0 Submerged Demineralized System Modes of Operation. 3.1 Off Gas System 3.1.1 System Start-Up j 1 Prior to_ operating'any. portion of the Submerged Demineralization j System, the Vent and Drain System comprising the Off Gas System and the liquid separation module must be operating. A prerequisite for the operation of these systems is operation of the Fuel Handling Building HVAC system. l l 3.1.2 System Operation l During normal operation, the off gas filtration unit is designed to require little operator action. The unit should be periodically l checked to ensure that temperatures, flows and radiation levels are  ; I within the normal ranges. l Increasing differential pressure across the roughing filter, charcoal filter, or the HEPA filters is an indication that the filters are l retaining dirt and other airborne particulate. These components should i be replaced as required to insure that flow through the ventilation unit is adequate. 1 l I i

                                                                                       )

l 0430B/LC l 1 I

                                  ,f '                                                 ;SD1527-005 The off gas moisture separator. tank; level should be monitored.

4 periodically to insure that.the' level control system is functioning. I prop'erly. -During_ initial. component' venting /(i.e. venting of the

                      .prefilter and final' filter), or..other operations.during which large               j
                       ' amounts of liquids are dumped int'o'the Vent-and Drain System, moisture            f separator tank level should be monitored more. frequently.

3.1.3 System Shutdown

                                                                                                           .j i                                                                                                            i The' purpose of the Ventilation System is-to ensure that all ventilated            '!

gases, from the Submerged Demineralized System components, are filtered and monitored for radiation. Shutdown of the Off. Gas System will preclude filtration and monitoring of the air, and should not be performed unless dictated by other casualty / operational. I considerations. To secure the Off Gas System, secure.the off gas blower and then place the system in a normal shutdown line-up. 3.2 - System Operation i 3.2.1 Filter Operation Start-Up Prior to system operation, system operators will be required to have in

                                                                                                             ]

operation the SDS Off Gas Syster and the Leakage Containment System. j j

                                                                                                             )
                                                                                        .'0430B/LC I
                                                                                        ,    ,4 i                                                                        lS0:3527-005"          -l    .

Thesesupport1systemsmustbe.in' operational:thelonsetofand ithroughout the duration of, the. processing operation. After system:

                                                                                                           ]

operators have completed the line up'to fil.ter theLinfluent water, they

                                                                  ,3.

o- will start the Reactor. Build ng Jet pump (SHS-P-1). tor other applicable _ j c, i pumps. Initially, all system parameters wil.l'be continuously. monitored?

                                                                   ~

1 i until proper operation of the' system has.been verified. 3.2.2 Normal Operation, The filtration operation'will be a batch process (the water will be filtered and the water processed. 1 System parameters will be periodically monitored while filtering the' ' l ' influent water. SDS filters will be replaced if instruments indicate J they are expended. Changing out a filter requires-the filtration operation to be secured. 1 i Periodic sampling will be performed to' provide an indication of t'he.  ! approximate chemical and radionuclides loading of the filters. 3.3 Processino the Filtered Water i 3.3.1 Processing System Start Up Throughout the duration of the processing, the SDS Off Gas System and Leakage Containment System will be in operation. , 0430B/LC' l

SD 3527-005 The ion exchar,ge vessels will be filled and vented prior to installation into the system. Line venting will be accomplished on i l initial system start-up, and will not be repeated on subsequent i restarts. With all vessels installed in the system, the operators will J l' align the system for operation. The feed pump will be started after the submerged ion exchange manifold and the transfer lines to Epicor II via the RCBT or MWHT are aligned for operation. Throttle valves will be adjusted to provide the proper flow rates through the system. Initial system operation will utilize one (1) train of ion exchangers at flow rate of 5 gpm. In some processing schemes this arrangement will differ. The system will be surveyed for indication of leakage or radiation streaming on system start ups, and during initial operation. System sampling will be conducted in accordance with approved

                                                                              ]

i procedures. During initial operation data will be recorded from all { l system instrumentation to establish baseline data points, for future ' reference and system trouble shooting. When sufficient operating experience has been gained, the data points necessary to support the Process Control Program will be recorded each shift. l l l 04308/LC l

                                                                         ,                 ,5SD3527-005~
                                                                                                               \

i3.3.2 Processina System Operation'  ! i i Once.the flow rate,.is established, the system functions with little ] operator' action; Instrumentation is provided on the system monitoring panels and at various locations throughout the. system as described in previous chapters to monitor system parameters. Operators will. insure'  ; that proper.. system flow rttes are maintained. ,j Periodic sampling.(at various' sample points) will be performed to' :j l

                              . verify bed performance and decontamination factors.-                       ';
                                                                                                            .j l

3.3.3 Processina S_ystem Shutdown i When it has been determined.that.a process demineralized.is expended or - 1 the batch completed, the. operator will secure.the' feed pump and flush -j the system with demineralized water,'or processed water. The expended exchanger in the train, if any,.is'then removed, and stored in storage racks in the~"B" Fuel Pool. Expandable plugs a're installed in each Hansen connector and the vessel is connected to the j 1 storage vent header. H l 3.4 Special Evolutions l l 3.4.1 Catton Vessel Chance Out j Replacement ~of a vessel located in the fourth (4) exchange position can-be performed without securing the process evolution. When it is determined a cation vessel needs to be replaced in the fourth bed -l I 1 0430B/LC

                                                                                                    - l:
                                                                                      .SD 3527-005:

Lposition', the. standby vessel is valved into the system. ' The: spent-vessel is then isolated. The vessel is then flushed and' removed from the system; it is 'tored~and s a new vessel is installed ~in its place. 3.4 2- Leakace Containment Ion Exchanger Vessel Replacement There are two leakage' containment ton exchangers arranged in_ parallel 1n.the system. Both ion exchangersDaresin' service' simultaneously. When it is. determined that the:lon exchangers'must be. replaced! The' SDS is shutdown and both' leakage containment vessles are replaced. After both.ve'ssels'are replaced the. system will be returned to normal

                                ~

operation utilizing both vessels. 3.4.3 Ventilation Filter Replacement When the roughing, HEPA or. charcoal filter;in the.off: gas unit requires replacement, the Submerged Demineralization System will first be l' shutdown. After a suitable period, the ventilation system will-then be l shutdown and the filter replaced. When.the bypass filter requires  : replacement, the filter will be valved out and changed without shutting

                                                                                                            ]

down the Submerged Demineralization or ventilation systems. i I i On loss of the'SDS Off Gas System, the SDS will be shutdown and system components sealed until the off gas system is restored to service.  ; Unit II Control Room notified. Appropriate radiation control procedures will be instituted.

                                                                                                         '\

l 0430B/LC: l. u___--___--_-_-_--____-__- _____

1

                                                                                ;-SD 3527-005          c.

i n L 3. 5.. : Transfer of Water from SDS to:EPICOR II< 1 l There are t'wo major path' ways available for: the SDS ' effluent to be-transferred, 'j i 1 The first' pathway utilizes the Reactor Coolant: Bleed' Holdup: Tanks 1 (NDL-T-1A,.1B, IC) as'the hold-up; tanks for. transferring'SDS effluent. This scheme.uses existing piping.on the 347 elevation of the Fuel l JHandling Building.to transfer water through,the Spent Fuel Cooling: ' l System to'the Radwaste Disposal System- *In the Radwaste' Disposal System..the effluent can be directed to the Reactor Coolant. Bleed s Holdup Tanks for eventual EPICOR II processing or for transfer'to other locations within-the plant, i The second pathway utilizes the SDS;line to the Monitor Tank' System. This system is capable of collecting and monitoring l decontaminated 11guld effluent from the SDS:and transferring it to the EPICOR II-

                                                                  ~
                                                                                  ~

System, the Processed Water Storage Tanks or back to SDS.for recycle of the water through.the system. The: Monitor Tank System.is also i'ntended to be used as a source of flush water for=the SDS. l I

                                                                                                        -]

l 0430B/LC' 1

SD 3527-005 Source Tank Receiving Tank WDL -1A, IB, 1C EPICOR II WDL-T-2' DH-T-1 MDCT WDL-T-1A, 1B, 1C I i HDL-T-2

                                                                                         ~

EPICOR II l WDL-T-1A, 18, 1C I WDL-T-5 WDL-T-8A, b3 l j SDS-T-1A, IB EPICOR II PW-T ~, 2 SDS Recycle SDS Flush WDL-T-1A, 18, 1C WDL-T-2 i i 1 I l l - l l l l l - 89'- 04308/LC j

1 i SD 3527-005 I i

                                   .3.6. Staffing levels 1

3.6.1 System Operations 1 1 l During system operation, the staffing levels will be as follows: i

1. Operat' tons Department One (1) Operator )

L l 2. Chemistry Department One (1) Chemistry _ Technician as d i needed , , 3. Radcon Department One (1) Health Physics Technician 1 as needed 1 1 (

                                                                                                                         )

In addition, during vessel movement evolutions, a fuel handling { building crane operator will be supplied by the Maintenance Department. l l I These manpower levels are subject to change as a result of lessons l l learned from the operation of-the system.

                                                                                                                         ]

4

                                                                                                                         )

System Outages I 3.6.2 i During outages, the system will be routinely surveyed by at least one operator and one health physics technician. 0430B/l.C

SD 3527-005 4.0 Abnormal Operating Conditions and Emergency Events l 4.1 Types of Events Considered Design and operating parameters of the SDS have included consideration of abnormal operating conditions and emergency events which might arise. The-following are noted as situations which may occur: Abnormal Operating Conditions Loss of SDS Off-Gas System ) 1

                                                                                                          \

Leakage of the SDS into the Spent Fuel Pool I J Loss of Instrument Air j 1 Loss of Electric Power i Emergency Events Fire Vessel Drop in the Spent Fuel Pool  ; l Cask Drop . Han in the Spent fuel Pool  ; l 4.2 Abnormal Operating Conditions l 4.2.1 Loss of SDS 0#f-Gas System 0430B/LC

A

                                                                        .SD 3527-005   ,

i 4.2.1.1? ' Design Criteria to Hitigate Effects Upon' failure'of.thetoff-gas. system such that flow through.the

                                                                                              )
              .sy' stem is lost, CN-V-IX-24' automatically closes. This action
             . interrupts process flow throughithe SDS, thereby' precluding:             :]

processing operations with.the off-gas system not functioning. , 1 This design feature has beentintorporated to enable control.over the possible.' generation of airborne radionuclides particulate:and. -

.ga se s .

J

                                                                                            'l 4.2.1.2      Response l

1 Upon loss of the 505 Off-Gas System,.the SDS will-be. shut down 1 and its components isolated until the off" gas system is restored. q to service. The Unit II Control Room will be notified  !

                                                                                           .i immediately. Any unnecessary personnel will be evacuated from                Ll l

the area until such time'as Health-Physics personnel determine the area is safe. Self-contained breathing apparatus or respirators will be used by remaining essential personnel , if required, during implementation of. corrective action.- 4.2.2 Leakage from SDS Into the Spent Fuel, Pool  ; 1 l l

                                                                                           'i
                                        -                              0430B/LC'        I u

SD 3527-005 4.2.2.1 De, sign Criteria to Hitigate Effects , l The SDS has been designed to minimize the possibility of leakage. Metallic piping has been designed and fabricated using all welded construction to the maximum extent possible. Process components, the ion exchange vessels, are located within containment enclosures to restrict the spread of radioactive ' contamination within the Spent Fuel Pool in the event that a  ! Hansen coupling to a vessel should leak. Radiation detector RE-LC-05 is provided to detect such a leak. -Valve enclosures are l drained as described in Table 2 to control radioactive liquids shou'd a valve leak occur; airborne radioactive contamination is controlled by ventilating the valve enclosures to the off-gas  ! system. Area radiation monitors will provide indication and k alarm of increases in the general area radiation levels.

                                                                                                                                                               ]

l l 4.2.2.2 Response l If a leak in the submerged piping of the SDS is either detected 1 or suspected, the processing operations will be suspended. The Unit II Control Room will be notified immediately. Area l 1 radiation monitoring, in addition to the monitoring in place, I will commence. Continuous air samples will be taken to determine - the existence of increased airborne radiation levels. Should it ) be necessary, personnel will be evacuated from the area.  ! Causative factors will be defined; corrective action will be

                                                                                                                                                             )

i planned and implemented. i f i 04308/LC , l 4

                                                                           'SDL3527-005-4.2.3 : Loss of fnstrument! Air' T

4.2.3.1 Design' Criteria to Hitigate Effects CN-V-IX-24 automatically shuts ~upon loss of instrument air ca'using termination'of the. feed to SDS. Resogg}g Any loss of system air Will' be reported to the Unit'II Control Room. SinceLthis abnormal operating condition-does not require

                  'immediate corrective action,.an-action plan-will be developed and implemented to correct the causative factor, i

4 2.4 Loss of Electric Power 4.2.4.1 Design Criteria to Hitigate Effects

                                                                                          ;l,
                                                                                         .j Upon loss of electric power.SDS' processing will be automatically.

terminated; feed pump operation will be_ terminated, off-gas; system operation will be' terminated,-CN-V-IX-24'will close. 4.2.4.2 Response Implement those actions that.may be necessary for loss of the SDS off-gas system.  ! l - 94 - 0430B/LC l i t

i SD 3527-005 4.3' Emeroency Events 4.3.1 Fire 4.3.1.1 Desion Criteria to Mitigate Effects Many of the SDS components remain submerged while in operation. Futhermore, the use of: flammable substances'has been minimized in-the above-water; portion'of the system.- Fire. fighting equipments is;available in the SDS operating area. .The. probability for fire in the area of the "B" Spent Fuel Pool, the location of the SDS, is extremely. low. q 4.3.1.2 Response 1 i i

                                                          ~

Upon detection of . fire in.the Fuel: Handling Building, processing operatins of-the SDS will'be terminated.and the system shut ~ j a down. Unnecessary personne1~will be evacuated from the area. If possible, personnel in the area will fight the fire'with available fire fighting equipment. The. Station Fire Brigade will . be assembled. 1 l 4.3.2 Vessel Drop in the Spent Fuel Pool i

                                                                                         )

i h 0430B/LC

g i-

                                                                 +                      '      i SD 3527-005 l

1

                                                       ~
                             ~4.3.2.1.      ' Desion Criteria' to Mitiaate ' Effects
                                                                                                                           ~l 1

SDS vessel handling will be done only underwater. ' Hovement. of -: l

                                            .the-vessels will occur under stringent observation of: operators.

Vessel handling 4 tools are.of the original; vendor. design as i modified by GPU: engineering.in accordance with' ANSI /ASME' N45.2.15. ' Testing and periodic maintenance'are performed in-accordance.with approved procedures. The SDS' vessels have been'

                                                                                                                           .q designed with sufficient strength to discourage' rupture if..
                                              . dropped within..the' pool. If component (vesselLor piping) damage           .
                                                                                                                 ~

were to occur, such'that smail. amounts ofLradioactive' water is. . released to the Spent. Fuel-Pool,.the. pool and.its' cleanup systems

                                                                                                     ^

will limit dispersal of radionuclides and provide cleanup-capability for the_ contaminated pool water. Crane operators tvill , l receive training' prior.to handling,the spent vessels, q a 4.3.2.2 Response SDS processing operations will be terminated,; The operator will immediately notify the Unit-II' Control Room in the event of a dropped vessel. An immediate visual inspection of. system-components and instrumentation will then be made to note any. indication of possible damage. If damage lhas'occured to any system components, the operator will take corrective action as

                                              .necessary.
                                                                                                                           -q q

0430B/LC ,

e SD-3527-005 ,

                                                                                              -1 4.3.3 . Cask Drop-I Cask drop analysis"is provided in the SDS'TER, Section 7.5.      This.

analysisyleidstheconclusion'that,whiletheunlikelyprobabilityl exists that a cask drop could result.in a significant cleanup effort, the public health'and safety.is not compromised. j

      '4.3.3.1        Design Features!to Hitigate Effects Should a' cask drop occur, the fuel ~ Handling Building Ventilation 1 System will be operated to limit: radionuclides dispersion.to the atmosphere to within Technical Specification limits. The' cask-        !

handling procedures strictly.. limit the.are'a above which the l l  : shipping casks will be. handled and ensure that a cask drop willt l .. y not damage essential plant hardware. u l l 4.3.3.2- Response' .l SDS processing operations will.be terminated'. .All unnecessary , personnel will be immediately evacuated from the area ~in order to l-minimize personnel exposure. Any injured personnel will'be l 1 removed from the area via proper emergency techniques. The Unit I I and Unit II Control Roceas shall .then be notified, in addition 1 to Health Physics personnel. The Control Room will periodically l announce that unnecessary personne1~are to remain clear of the: l accident site. Once the damage and/or danger is assessed, follow-up actions will be-initiated to recover from the effects of this accident'. 0430B/LC l

SDi3527-005 s

                                                                                                                                                                                                                .t
                                    '4.3.4 Man in the                                         "B". Spent Fuel Pool                                    ,

i 4.3.4.1 Design-Criteria to Mittaate Effects.

                                                                                                                                                                                                                >j SDS operation will--be performed with as requ' ired Health. Physics:

support.. These personnel have knowledge ~of. required actionsLin' , the event'of gross-contamination of the worker'due to~ falling in ,; the' Fuel Pool. Eye wash stations'are available in the operating. 1 area. Plant showers and other. services.necessary-to I. ' decontaminate workers are'available. , H 4.3.4.2 Response < i

                                                                                       .If a man falls into.the."B" Spent Fuel Pool..the man will'.be retrieved from the' pool and' processing'and equipment handling.

will be stopped. Unit II Control Room'and Health. Physics personnel will be notified. 1 1 i t 'l 04308/LC. .

SD 3527-005 o

1. 1'
                                                               .. 5.0 -

Maintenance. a 5.1 Maintenance Approach j q The>SDS has been designed specifically'to be virtually m6tntenance free; however, some minimal maintenance requirements are expected. '.To. j provide ALARA radiation exposure during maintenance all system piping,. glove boxes and. manifolds are provided with flush' conn'ections. All l j components will'be' flushed prior to maintenance work'.if necesssry. l Maintenance requirements'for the SDS can be. categorized into the q following broad general' areas: ]i

1. Instrument maintenance and calibration. I 1
2. Pump maintenance. 1
3. Valve maintenance.

l

4. Hansen coupling maintenance.

l S. Off gas. filter-system maintenance.  : The maintenance approach'for each of these areas is described below, 5.1.1 Instrument Maintenance-and Calibration Approach l Instrumentation calibration will be performed on a routine basis.in ' j' accordance with the normal site calibration frequency in accordance with 4221-ADM-3620.01 1027 Preventive Maintenance. Maintenance on l electronic portions of instrumentation outside the pressure boundary will be 0430B/LC-

        ,                                                       n                         >
s ,-' y

't . , ,

                                                                  ,               . SD '3527-005'-'        ';

performedLin.accordanceeithvendorsmanuali;asr'quiredandLwill' e generally present no-special requirements. Pressure.-indicating ' devices'  : which communicate with the process fluid are'of'thel isolation:diaphram 4 ti and filled capillary tube type and are located withi'n'the various H

                                                        ~

fi;anifold boxes. These.instrume.nts would normally not require?  ; maintenance and are:' intended to be replaced. remotely should problems develop. -

                                                                                                           .l 5.1.2 Pump Maintenance,                                                                              g d

5.1.2.1  : Jet Pump (SWS.P-1) & Off Gas Bottoms Pump-The SDS Jet pump and.cff'. gas-bottoms submerged pumps are' intended to be replaced rather than repaired.

                                                                                                           'j 5.1.2.2        'SDS Manifold and Glove Box Sump' Pumps                                           ;j i
                                     .(

The manifold and glove box pumps'will be' replaced rather than repaired. 1 I

1 i

l l 1

                                                   - 100 -                                  0430B/LC 4

SD 3527-005 5.1. 2 .'3 ' leakage Containment System Pump. . l. , The leakage containment sys' tem' pump'is. located in an accessible. area at the north end of'the~"B" Fuel Pool and just west'of'the' ion: exchanger manifold. It is not' expected to become' highly contaminated during'SDS operation'. Normal plant m'aintenance:

                  . practices will be utilized should repair become necessary..

5.1.2.4 Monitor Tank Transfer Pumps: l: The monitor tank system transfer pumps are located'in~an accessible area of the'model room. They are not expected'to beccme highly contaminated as they are' planned to handle SDS, flush water. Normal plant maintenance practices wil'l.be utilized <

                  'should repair'become.necessa'ry.

5,1.3 Valve Maintenance All key system valves communicating with.' contaminated process fluidiare located within the various manifold boxes. These valves a're accessible 1 through ports in the manifold box covers'. The valves are of the top entry type for use of maintenance. The manifold boxes can be flushed and drained to minimize surface contamination prior,to commencing 1 maintenance activities. Existing generic'. plant maintenance. procedures will be used where possible. Special procedures will be developed for  ; equipment which is unique to the SDS. 1 1

                                              - 101 -

0430B/LC

                                                                                                                                    ,                    .SD 3527 005-I 5.1.4   Hansen Couplina Maintenance The female Hansen couplings, which are.part of the flexible' hoses.
                                                                                                                                               ~

connect 1.ng the- system.to the vessels, cont'a iri?"0" rings which could i become worn orfdamaged through T continued use; .These.may.be replaced-underwater either manually or.through.the'use'of remote tools.

                                                                                       . Experience with'the system willL dictate. frequency of replacement.                                          !

1 5.2 Corrective Maintenance. -l

                                                                                      ' Prior to performing any maintenance activity on SDS components
                                                                                                                                 ~

l associated with the pressure boundary or other' contaminated portions, the system wi.ll be flushed using"either demineralized water or low q activity processed water if necessary. The' system will then be drained l and the necessary surveys and swipe! samples..taken to. determine thel appropriate work procedure to maintain ALARALconditions. When work is to be accomplished within the manifold boxes, a survey and .! swipe samples will'be taken in: the box and .the box: will be. flushed if contamination is detected. Photographs which were taken of~the. boxes prior to installation of the covers will be used as iequired to-determine wcsrk space and' component. location. For removal of isolation diaphram type pressure instruments'a special tool as described in Section 1.8 will be utilized to allow the remote l- removal and replacement of the instrument. l-

                                                                                                                       --102 -                               0430B/LC-

_ - _ _ _ _ - - _ _ _ _ _ - - - - - _ - _ _ - - - _ - _ - _ . - - - - - _ -- _ - _ - - . - . . _ - - - _ - . .. a

SD 3527-005 3.2.1 Retesting Requirements Repairs, maintenance and system modifications which violate the integrity of the pressure boundary will require post-maintenance testing at normal operating pressure and temperature'. This will be accomplished using low level processed water or demineralized water. Replacement of the off gas system HEPA or charcoal filters will require the performance of a DOP or Freon 2 Test, respectively, to verify filter efficiency, in accordance with Regulatory Guide.l.140. I i l 5.3 Preventive Maintenance and Inservice Inspection l 5.3.1 Preventive Maintenance ' The pool clean-up system pump will be checked to ensure that oil is visible in the oil reservoir at regular intervals. I Periodic surveys of the manifold boxes will be performed to determine leak integrity of valve stem packing. This will be accomplished when  ! the system is shut down for vessel change out and can be performed by removing a valve access plug and taking a swipe sample of the drain sump.

                                                                                            .l l

1

                                      - 103 -                           0430B/LC               j
                                                                                ---------___d

I SD 3527-005 5.3.2 Inservice inspection Inservice inspection consists of periodic physical inspection of components. Valves, pumps, instrument connections, motors and other active components will be routinely inspected to determine degradation and to spot potential. problem areas. Instrument readings will be taken daily and compared to previous data to develop trend information which may indicate system degradation or potential problem areas. This information will be evaluated by the engineering staff and corrective measures recommended as deemed appropriate. l l l l l 1 l l 1 l 4

                                            - 104 -                            04308/LC

l ISD:3527-005 1 6.0 " Acceptance Testina '

                                                                                    ,l l

The SDS testing.can be: subdivided into.'threefgeneral catagories:

                                                                                    ]  1
      .1.      Construction Testing' l

i

2. " Cold" Functional Testing,
3. " Hot" Functional Testing. 1 o

' 6' 1

   . Construction Testina-                                                           1 Constructionitestingwill.consistoffluidsystemflushing,: flow.

verification'and' pressure testing and' continuity testing and' alarm set point checks of all' electrical and instrument circuits. Additionally, all' instruments (which were' purchased initially with' factory .; calibration certification) will be recalibrates. DOP and Freon 2 testing has been performed on the off gas HEPA and charcoal filters, respectively in accordance with Regulatory Guide l.140. Initial equipment. mechanical checkout, including vibration testing, lubrication checks and initial run in have been completed. Vessels will be. required to pass a hydrostatic test'in accordance with the ASME Boiler and Pressure Vessel Code, Division 1, The test criteria for the HEPA I and charcoal filters is that they meet a 99.95 percent efficiency for. removing the test media employed.

                                       - 105 -                            04308/LC-1
                                                                                 ,SD 3527-005 6.2 " Cold" Functional Testing               i The system was alig'ned in its normal operating mode and filled with               i demineralized water. System operating procedures were proof tested (red lined) and baseline data was taken from system instrumentation.

This information was'conpared with the design points to verify system performance to be in accordance wit 1 the design. The system was  ! required to perform to the design points specified in this do; ament (Appendix 7). The system Will be required to perform operations which are described in Section 3 of this document. Set points, alarm points j a and system trip points were verified. Tank level indication was- j verified. Remote tool operability was demonstrated. Filter and ion l exchanger handling operations was demonstrated. j l 6.3 " Hot" Functional Testi.ng l l The initial operation of the system is planned to be used as a part of l the system testing program. The initial processing wili utilize water l contained in the Reactor Coolant Bleed Tanks which is of low specific activity. This information will allow additional data to be taken l including surveys of pipe and tank shielding areas to determine potential " shine" areas. Instrument readings will be taken and some DF (decontamination factor) verification can be expected. l l l i

                                              - 106 -                                 04308/LC i

SD 3527-005 6.4 Ancillary Testing The following ancillary testing has also been performed'both on and off site

1. Dewatering testing of ion-exchange columns.
2. Dewatering testing of filter vessels.
3. Ion-exchanger column testing.
4. Distribution header testing of ion-exchange vessels.
5. Channeling testing of ion-exchange vessels.

l

6. Polishing system column testing.
7. Filter loading testing.

l l l l l l l l l l l i

                                   - 107 -                          0430B/LC

SD.3527-005 This page. Intentionally left blank 1 l.. l 1

                - 108 -                       04308/LC

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SD 3527-005

                                           -TABLE 2 SDS' COMPONENT VENTS AND DRAINS SDS COMPONENT      VENTS TO           DRAINS TO Ion Exchange Manifold           Offaas Filters     Offgas Separators Beta Monitoring Manifold           Offoas Filters     Offaas Separators-RCS Cleanup Manifold           Offgas Filters     Offgas Separators-High Rad filter
  -Sample Glovebox     Offaas Filters-    Offaas Separators High Rad feed
  . Sample Glovebox    Offaas Filters     Offaas Separator Intermediate Level Sample
  'Glovebox            Offaas Filters     Offgas Separator Ion Exchange Trains             Offgas Separator   Leakace Containment Final Filter       Offgas Filter      Leakage Containment Pre Filter         Offgas Filter      Leakage Containment SDS Post filter                        Lined with Herculon Enclosure-         Offaas Filters      NO DRAIN Common Vent to Offgas Filters /

Hi Rad Filter Sample Glovebox; Vessel Line Drainable-Storage Racks To Pool Pool SDS Monitor Existing F.H.B. l Tanks Exhaust Existina 81da. Drain

  • Offaas Separator Offoas Filters RCS manifold Offoas Filters Building Stack N/A

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                                         - 113 -                      04308/LC        q l

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SD 3527-005 .,

                                                                                                 .l I

1 Appendix No. I j to Submerged Demineralized System l System Design Description

i 1

1 i l l Titie S.O.S. Pumps / Blowers

SD 3527-005 Appendix 1 SDS PUMPS / BLOWERS 1 Pump Details l Identification SHS-P-1 . Noun Name Reactor Building Basement Jet Pump Manufacturer Goulds Pumps Inc. Model No. GHISD j Type Deep Well Jet Pump with Packer assembly Standard Material Designation Cast Iron l Rated Speed 3450 RPM Rated Capacity 25 GPM Rated Total Dynamic Head 113 ft. Design Temperature 40*C i Lubricant Water Packer Goulds - FP2-14 Well Head Adapter Goulds - AHJ-2 l l Motor Details Manufacturer Wagner Type C Rated Horse Power 1 1/2 HP S Rated Speed 3450 RPM Lubricant / Coolant 011/Alr . Power Requirements 115/230 Volts, Phase 60 Hz, 17.5/8.75 Amps l Power Source PDP-2B 428B/LC f __ - - - _ _ - - ~

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  • 15 gpm l Design Temperature 100*F (140'F max.)

Lubricant Water Motor Details Manufacturer Franklin Electric Model 2341272003 Enclosure Stainless Steel Rated Horse Power 5 HP Rated Speed 3450 RPM l Lubricant / Coolant Water / Air Power Requirements 460 Volts, 3 Phase 60 Hz, 8.7 Amps Power Source PDP-6A 4288/LC

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SD 3527-005 Appendix 1 SDS PUMPS / BLOWERS_ 4 Pump Details Identification FCC-P-1 Noun Name Fuel Transfer Canal Drain Pump Manufacturer Goulds Pumps Inc. Model No. 45J05434 Type. Submersible Standard Material Designation Stainless Steel Rated Speed 3500 RPM  ! l Rated Capacity 45 GPM l Rated Total Dynamic Head 280 ft a 45 GPM Design Temperature 100*F Lubricant Water Motor Details l Manufacturer Franklin Electric  ! Model 2341272003 Enclosure Stainless Steel Rated Horse Power 5 HP Rated Speed 3450 RPM Lubricant / Coolant Water / air Power Requirements 460 Volts, 3 Phase 60 Hz, 8.7 Amps Power Source PDP-6 -A o 428B/LC l 1

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SD 3527-005 Appendix 1 l SDS PUMPS / BLOWERS Pump Details l Identification SDS-P-1A and SDS-P-1B Noun Name Monitor Tank Transfer Pumps Manufacturer Goulds Pumps Inc. , i Model No. 3196 "ST"  ; Type Double Mechanical Seal - Centrifugal , Standard Material Designation Stainless Steel l Rated Speed 3500 RPM Rated Capacity 50 GPM I Rated Static Pressure 111 ft. Design Temperature 500*F Lubricant Water Motor Details Manufacturer Reliance l Type P Enclosure ODP Rated Horse Power 5 HP Rated Speed 3500 RPM Lubricant / Coolant 011/ Air l Power Requirements 460 Volts, 3 Phase 60 Hz, 6.6 Amps Power Source SDS-STR-1 and SDS-STR-2 Reference Drawing No. 2-M080A, Rev. 0 4288/LC

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1 SD 3527-005 Appendix 1 SDS PUMPS / BLOWERS Pump Details Identification CN-P-LC06 Noun Name Leakage Containment System Pump Manufacturer Goulds Pumps Inc. Model No. 3196 MT-A-60 Type Centrifugal q Standard Material Designation 316 S.S. Rated Speed 1750 RPM - Rated Capacity 120 GPM 2 l Rated Static Pressure 55 Ft. Design Temperature 100*F i Lubricant Water Motor Details Manufacturer Westinghouse Type Type S , Enclosure TEFC l Rated Horse Power 3 HP Rated Speed 1750 RPM j Lubricant / Coolant Oil / Air Power Requirements 460 Volts, 3 Phase 60 Hz, 4.8 Amps Power Source SDS-PDP 6A Reference Drawing No. DS-527-G-05, Rev. 2 428B/LC -j

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SD 3527-005 1 l Appendix 1 SDS PUMPS / BLOWERS f Pump Details i Identification CN-P-VA04 Noun Name Off Gas Bottom Pump , 1 Mar ':facturer Goulds Pumps Inc. Model No. WP 3870 Type Submersible Standard Material Designation 400 Series Stainless Steel j Rated Speed 3450 RPM Rated Capacity 30 GPM Rated Static Pressure 65 ft. l Design Temperature 100*F l Lubricant Water  !

                                                                                               )

Motor Details Manufacturer Franklin -l

l. Type Submersible Enclosure Hermetically Sealed Rated Horse Power 1 HP l

l Rated Speed 3450 RPM '

                                                                                               .)

Lubricant / Coolant 011 l Power Requirements 460 Volts, 3 Phase 60 Hz, 3.5 Amps Power "ource SDS-PDP 6A i l Reference l Drawing No. DS-527-G-05, Rev. 2 11 - 428B/LC

SD 3527-005 SPECIFICATIONS j o,e.,uo. l s, _ y,,,, j ,,,,, l,,, jeono,!g lWt. l Volts Phase RPM Solids  ; Wt. 70 l oro,r No. HP WPH1012El 1 l 230 - l 1 l3450l%" l 11.0 WP0311E 1/3 Its 1 1750 E" 9.4 56 3 3450  %* 7 70 l WPH10'J2El 1 l20a730 PERFORMANCE RATING (GPM) 60 l WP03 (% HP) TDH GPM i N I I, l l 1 I I I i Total go 33 50 l 15 l 62 I I g-l Feetto E, e 40 I Il l l l l l Water 20 l 36  ! I l l I i MI  ! I I

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                                                                                   !                                tio            go     j   73 II                      I        I        i    iI              l 0      20       40       60        80         100               120         140    160 Capacity--Gallons Per Minute                                                                       60     l'1a Model 3870 Packaged                                                                   $ggiyy      t ee'55 GPM S" Solids Handling Capability Effluent E)*ector System                                                               2" NPT Discharge Connection l         Goulds packaged effluent                                -
                                                                .,         El                   Package includes:

I ejector system offers both -  ! E Submersible Sewage Pump l ease of ordering and instal- (WPO311E)or (WPH1012E) lation. A smgle ordering a Mercury Level Control Switch

             "    8 f                        -  or 1 H P.' package) o    , den       nd commer;lat sump and effluent pump applications.

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E Ma netic Contactor (AL 3-1 with 1 H.P. units only), j The ease of installation is 41 w,Lh 5 Polyethylene Basin enhanced by plug-in power P$,((- i (ALS7-1801P) fevel controfswi cwhch j ' E Basin Cover (ALSB-1822S) eliminates the need for  ! E Check Valve (ALS9-2) additionalwir Except t for 1 H.P. units ch have  ! Order No. SWP0311E 115 Volts, bare leads f or connection to , 95 lbs. magnetic contactor. Order No. SWPH1012E 230 Volts.109 Lbs. 7A. GOULDS PUMPS,INC. m a ix 1 Form No. A 478A.Ws M 59ECA FAus tEW YDAK Bu:S sp3 spo cH. P- VA 0 4

1 l SD 3527-005 j Appendix 1 SDS PUMPS / BLOWERS i Pump Details Identification CN-E-VA05 Noun Name Off Gas Blower i Buffalo Forge Corp.

                                                                                  )

Manufacturer q Model No. SE Type Radial Flow Centrifugal Type "E" Standard Material Designation Sheet Steel i Rated Speed .3510 RPM Rated Capacity 1000 CPM Rated Static Pressure 12" W.G. Design Temperature 104*F Lubricant 011 Motor Details i j Manufacturer Westinghouse Type K Enclosure TEFC l l Rated Horse Power 5 HP l l Rated Speed 3510 RPM Lubricant / Coolant Oil / Air l Power Requirements 460 Volts, 3 Phase 60 Hz, Amps l Power Source SDS-PDP 6A l r Reference - Manual MSA Off Gas Air Filtration System Instruction Manual ' 428B/LC

SD 3527-005 "E" and "RE" BLOWERS and EXH AUSTERS CAPACITIES and STATIC PRESSURES SIZE 5 E BLOWERi?!!! ^ (F.S.)

      '1                                                                                                                                    TM.i- . 37-D _,i.$d.I'3500 R.P.MJ '.-[dh:[ 7f
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                                                                                                                                                                            .                          17.0* Wheel' ~15.0* Whe:..I S.P.           B.H.P.       S.P.            B.H.P.

l Ratings are for standard air at.0751bs per , C.F.M.,Q 5.P. B.H.P. S.P. B.H .P. g cubic feet density at 70*F 29.92" Hg. Per- ggm 23.5 3.0 20.3 ~2.6 15.1 1.9 10.2 1.3 q formance dain in the tables and curves 2.2 10 1 1.5 is for standard wheel diameters which T~500Y -- 23.6 3.4 20.4 2.9 15.2 i,,, d are carried in stock. When suitable. .600 1 23.5 3.7 20.3 33 15.1 2.5 10.0 1.7 select a stock site for fastest delivery. [700 5 23 3 4.2 20.1 37 14.9 2.9 9.7 2.0 Ej Special wheel diameters to meet inter. 3 mediate ratings can be deiermined upon ja00,4 23 0 4.6 19.8 4.0 14.5 3.2 S.2 2.3

       $                    request to your Buffalo Sales Engineer.                                                                          -900 --                  22.5                E.0          19.3            4.5           14.0              3.5           8.7          2.6
                                                                                                                                                              ~

1 --- .- - r1000.2 22.0 5.5 18 6 4.9 13.3 3.8 8.0 2.8 4100M 21.0 6.0 17.7 5.3 12.3 4.2 7.1 3.1 j - "-'#" l1300 2 19.0 6.9 15 8 6.1 10 4 7.9 4.9 5.5 5.0 2.4 3.5 4.0 l 1 1500 J' 16.7 7.9 13.3 6.9 l l l l 3500 R.P.M. PERFORMANCE CHART ii! , e i e i i e i i i  ! i . i i i.iii i . I ii, e i,i i i i i . e i a t 6 i i i i i;ii ii6 .ii 6 i .) 6 ii i .i i i i i

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                 -- a00                  - 400                    600                000           *1e00                    1200                  1400                1600 - 1e00                            a000               1200               a400          3600               teo0 CAPACTff = Wel Af'PE N DI A 1 503                                                             SDD                          CN- E- VA 05 14 -
                                                                                                                                                   /

l 1

                                                                                                            ~SD 3527-005.

Appendix 1 q SDS' PUMPS / BLOWERS i Pump Details . Identification CN-P-FLO7 Noun Name High Rad Fiiter.. Manifold

                                                                                    ~

Manufacturer Cole Parmer Instrument. Company .] Model No. C-7144-70

           -Type-                                                            2-Gear Magnetic Drive Standard Material Designation'                                   316 Stainless steel / Teflon /Ryton..             ]

Rated Speed 3000-1 Rated Capacity 0.50 GPM at 95 psig Rated'. Static Pressure 300' psi l j l Design Temperature 180*F. Lubricant Water i Motor Details , Manufacturer Cole Parmer Instrument Cortpany i Type Ir. duction Enclosure TEFC.

                                                                                                                                     )

Rated Horse Power 0.18 HP.(135 watts)- Rated Speed 3000 i Lubricant / Coolant 011/ Air i 1 Power Requirements 115 Volts, 2 Phase 60 Hz, 1.3 Amps.

                                                                                                                                    ]

Power Source HP-CN-1 1 Reference Drawing No. DS-527-G-06, Rev. 3 DS-527-G-07 Rev. 3,- DS-527-G-08, Rev.;L 428B/LC-

-______ _ = - - _ - - _ _ _ _ _ _ _ = _ _ _ _ _ _ _ _ _ _ _ = - _ __ . - . ._ .:

EMEnnsEMe@MMHiMara WMnsMad, AC, DC, and air motor magnetic drive pumps se asn-oos Seal-less pumps operate at temperatures from -100oF to +275oF {

                                   -.s.--
             . Exceptional che'mical and
                                                          - 3 . gy.,;. ) _.. , ,. ,     ,

Magnetically coupled rear pumps are des ped for metering not.-

n. abrasne fluids at te=peratures from -100 to +275'T. Dry lia. 6 feet
              . corrosion resistances AA;E..;.%'y                         +

of water, and when the geen are wetted self prune up to 26 inches or

                                                                                                    . .: .y '.7-                   Hg. Because the puznp is magnetically Coupled to the motor, there att g      Self-prirning-pa-[i-'Ofc1*4how
                                           -            -A
                                                                                                      ~ E. .. continttNf. . . no shaft seals     ..N.'to sear. leak or generate heat. Tnis makes it ideal for    -

g;! most systems, espec2 ally those that cannot tolerate contamination. yl.W:Li r'run dry y ;- - g .J , --

                                                                                       -e$

py . gy. Gear pump desip produces a steady, pulse-free flow at the outJet. E.[R-p- -q' '_ ( ,.. M; ik@$[M.MZc Flow continuity is c1%, as long as the differentia] pressure, Duid vinosity and line voltage remain constant. Construction is of high grade 316 stainless steel. TeDon' and car-

     ;M*:,                    .
                                         -~~                ] f$-

M bon to make pumps exceptionally chemical and corrosion resistant, e.9  ; .

                                                                                     .                          c                                                                                                 ;

and to insure long, maintenance-free service life. Adetaced pump p$%" ~" F, '

                                                                                                                      'g          head design prmdes excellent loyto high pressure aM Dow per-ggi.                                                         qq,,                      ,
                                                                                                          ,-g                     formance, and permits safe operatson with syrtem pressuns up to
      ;, ;.2.M                                                                                            '

600 psi. 9p

     .f 9.E*."                                                       '
                                                                       'g                     '

N..

      /rS.9
     ;DCrfwa, h M w.v.            YQ                                               - -

1cg Pumps are compact and very lightweight-many models weigh less than 1% lbs. Side ports are %* (T)NFT. Each pump is fuljy factory tested prior to shipment and includes installation, operation, and

                                                   .i            d y'                                A       .W.#.l'm)           maintenance instructions. (Service k.its a vailable.)

1eflon-Res TV E.t Duperit ce Nemou s & Co.

       ' Catalog -             S951 m5"q-" M)4ype                 r.Wm45t'o rg,'.f. ]'                         Maumum'
         . eiumber           " W escinremersts'*                                                               rnow rpm
                                                                                                                               . Amps'           N0* ~    : - ##'""'#"   -- N      I1         W* MS
                                                                                          . .                                                 -frd/mm         .pressre -          <I     tat. n c. l p ne,'

C.M 450 113 VAO. 60 m.; Vananie speed 9.600 1.1 0400 100 ps $322.o0 115 CO *. - C M4447 $37.50 urnersa: AO/D0 C 71455 115/230 VA0060/60 H Exposen troo" 2.150 2.3 265 175 ps. 468.00 C 71460 115 *230 VAO.50/60 Hr 3.15; C M4447 37.50 inexmon TETO if 26E 175 os 282.00 C M4447 C 714445 37.50 Anmow 6.00: 6 - C5% i 175es 328.00 C 714447 37.50 C 714440 O tc24 VDC Brunn 10.000 C-C.5 C25-E 40 ps C.M 644 5 Onc24VDC Bv.n 228.00 C-71442 37.Sc 10.C00 C C.5 1.5 30 45 ps; 228.00 C-7144-47 C 71443 0 to 24 VD0 Bvr5 10.0 % 37.50 0 C.5 50 600 60 ps; 228.00 C M4447 C 7144 45 Cto24VD0 Evsh 37.5C 10.C00 0-C 5 6 4 C30 175 os' 250.00 C.M 444 ' 37.50 Magnetic drive 2 and 3 gear pumps... with patented suction-shoe design Uniquely desiped suction shoe acts as a sealing member to sepa.

                                                                                                       .WFO h                        rate the inlet aide from the pressure side of the pump. The uayor design advantage is its size: the suction shoe is a fraction of the size f                                                            -

of a conventional cavity plate housing. This makes the pump bghter and more compact, and-most importantly-perzrJts the use of a third gear. The S gear roodel doubles the Dow of the 2-gear model, while ocupying the same amount of space. Gears and suction shoes are all contained within a stepped snarnet cup which is pressurized

                                                                                    .ieo aW O'

d by the surrounding Duid. The iluid forces the gears together from all

                                                        "-                                                                      angles for efficient pressure loading.

b r ...leW Dk3 Construction is of 316 cast stainless steel for a durable, corrosion

3. . . . m resistant housing. gears and suction shoes are of Rpon* for out.

w, A y . . .; .g nmr; ~d f_n sta.nding the=jeal resistance, high thermaj stability. and a low coef. s q .1 m .- r$;- ficient of friction. All other parts that contact the work.tng Duid are of 1, r. r . .' . c,. :

        '-                                                                                                                     Teflon' and stainless steel-selected to provide marimum corrosion efa'w            d            resistance and minimt.m wear, Laarve                                                                          An i.nternal by pass valve pertnits rectreulation of the Guld at the 1    *8              8          8                   5                                 preset pressure, preventing system over pressure and motor over.
                                                             ,;                                                                load. By pass valve is externally stustable--even while the pump is

{ 6: , , . , , - 3.. a . w. ,'!4+

                                                                        ;',,,,                  4                              operating. Magnetic coupling provides leak proof, contarrii nation.

e '4 -s sc free service and reduces main;enance. Driven magnet is Ryton'.

\L M f coated to prevent thermal abock and contamination. Pumps are all lao MYI.1'-+M ; ' ' :T; ;: "d". 4,-2  ;.

y 1- -3

  • field ocrvicable-see table below for service kits.

6 . C ,, Pump dry lift capabilities: 3 feet of H,0; vacuum down to the vapor "ri 4 :'!? Y' -1 pressure of the Duid being purnped. Differential pressure to 95 psig; e oi c: ca e4 os e.e c.7 c4 cs in i.i 12 system prearure to 300 psig. Tenen hen Tw E.L 0#ces ce hemars & Co Ryton has 7w Ptahos peroseum Ce Catalog .

  • Ar iber,cy p {p.,, , rnctor rpm ' % h' ~y ,yfEF%Mu.h no g]g -roouremeru
                                                     ' Power ~Ns-'5 m."H_'                                                 MaxynumJ                    *n   fQg,. i                             CC '

number goa. s . < m. Mow -- seenge ' ~ ,,pm

 \     c 7144 70               2_pna s           115 VAO. 50 /60 Hz                          anoscoon TEFC                  3000         1.6 CJ
                                                                                                                                                         % go_m to 100ps    3177.00      C-M 64._7L ._H 1.DC C 71w75                  3 pia :          115723m",10760 Kz                                         -

E.xpicson DreF"~~"MDC 2.3 1.05 I gom to Wps C 71 4 80 S pea s i ts/230 VAC. 54/60 Hz 390M~"_C M477 55.00 enosetron TEFO 3400 231.50 1 Dom to 60 tw 236.00 C M44-77 45.00 1

SD 3527-005-Apper.d1x.1 (Cont'd) SDS PUMPS / BLOWERS Pump Details Identification CN-P-SA08,'CN-P-RC09 i Noun Name High' Rad _ Filter. Sample, and RCS Manifold Sump Pumps . .- Manufacturer Gormann-Rupp' Industries  ! .Model No. 20501-000. l Type Nutating. 1 Standard Material Designation Polypropylene and.Polyphenosulfide l Rated Speed 1550 Rated Capacity 0.50 GPM Rated Static Pressure 80.85 ft. Design Temperature 180*F I Lubri. cant . Water Motor Details Manufacturer Gormann-Rupp Industries Type PSC Enclosure TEFC Rated Horse Power 0.18 HP-(135 Watts)- Rated Speed 1550 Lubricant / Coolant 011/ Air Power Requirements 115 Volts, 2 Phase 60 Hz, 1.3 Amps Power Source MP-CN-1

                                                                                      ,[

Reference ) Drawing.No. DS-527-G-06,.Rev. 3 DS-527-G-07,'Rev. 3 DS-527-G-08, Rev. 1- i

                                    - 17    -

428B/LC 1

SD 3527-005 1 1 i Appendix No. 2 I to Submerged Demineralized System ) System Design Description 4 l Title

     -SDS Filter Vessels 1

i

50 3527-005 APPENDIX NO. 2 PREFILTER/ FINAL FILTER . Vessel Details l Identification (Prefilter) F-10001 Series j

                                       .(Final Filter)                 F-20001 Series                        j Number Installed                               Two (o                                 j i

Manufacturer APC0

                                                                                                            )

1 Installation Vertical j Outside Diameter / Height, ft. in. 2 Ft. 1/2 In./4 ft. 5 1/2 Inch I Shell Thickness 3/16 Inch Shell Material Stainless Steel (304)' Design Pressure / Temperature 150 PSIG/100'F Volume 10 Cubic Feet Prefilter Media 125 Micron Cuno or Layered Sand Final Filter Media 10 Micron Cuno or Layered Sand 0414B/LC

o SD 3527-005 APPENDlX NO. 2 PREFILTER/ FINAL FILTER-4 Vessel Details. Identification (Prefilter) D-00001 Series (Final Filter) i Number Installed Two (2) I Manufacturer APCO Installation Vertical j

Outside Diameter / Height, ft. in. 2 ft. 1/2 In./4 Ft.~5 1/2 Inch l

l Shell Thickness 3/16 Inch Shell Material Stainless Steel (304) Design' Pressure / Temperature 350 PSIG/100'F Volume 10 Cubic feet Prefilter Media Layered Sand i Final Filter Media Layered Sand l l 1 0414B/LC

SD 3527-005 APPENDIX NO. 2 PREFILTER/ FINAL FILTER Vessel Details Identification (Prefilter) 0-2003X Series (Final filter) Number Installed Two (2) Manufacturer Buffalo Installation Vertical Outside Diameter / Height, ft. in. 2 ft. 1/2 In./4 ft. 5 1/2 Inch Shell Thickness 3/8 Inch Shell Material Stainless Steel (316L) Design Pressure / Temperature 350 PSIG/100*F Volume 10 Cubic Feet Prefilter Media Layered Sand

                                                                                                                          .l Final Filter Media                             Layered Sand 1

i 4 l 1 l l l l 1 l l l  ; l i 0414B/LC i i

SD 3527-005 APPENDIX NO. 2 PREFILTER/ FINAL FILTER /" CATION" SAND FILTER Vessel Details

                         . Identification (Pref! Iter)                     U-00001 Series (Final filter)

Number Installed Two (2) Manufacturer APC0/ Buffalo  ! Installation Vertical-Outside Diameter / Height, ft. in. 2 f t.1/2 In./4 f t. 5 1/2 Inch - She'l Thickness 3/8 Inch  ! Shell Material Stainless Steel (316L) Design Pressure / Temperature 350 PSIG/100*F Volume 10 Cubic Feet Pre 91ter Media Layered Sand l Final Filter Media Layered Sand

                         " Cation" Sand Filter Media                      layered Sand i

0414B/LC i

SD 3527-005

                                                        ~ .1 l

l Appendix No. 3 to submerged Demineralized System System Design Description l  ! i A i i l l l I l Title l SDS Demineralized Vessels l l

SD 3527-005

                                      ~'

APPENDIX NO. 3 i iff0 LITE DEMIN VESSELS j 1 i Vessel Details Identification D-100ll through D-10018 (Permutit) l D-20021 through D-20042 (Buffalo Tank)' J U-00001 through U-00047 (Buffalo /APCO) l Number Installed Six (6) Manufacturer Permutit/ Buffalo Tank /APC0 Installation Vertical l Outside Diameter / Height, ft. in. 2 ft. 1/2 In./4 Ft 5 1/2 Inch Shell Thickness 3/8 Inch Shell Material Stainless Steel (316L) t Design Pressure / Temperature 350 PSIG/400*F Volume 10 Cubic feet j

                                                                             .                                                              1 i

l l l l l l l l l 0415B/LC l l

SD 3527-005 l l Appendix No. 3 (Cont'd) J i LEAKAGE CONTAINMENT ION EXCHANGE VESSELS { i Vessel Details Identification D-00001 through 0-00010 Number Installed Two (2) i Manufacturer APC0 Installation Vertical Outside Diameter / Height, ft. in. 2 Ft. 1/2 In./4 ft. 5 1/2 Inch Shell Thickness 3/16 Inch l Shell Material Stainless Steel (304) Design Pressure / Temperature 150 PSIG/100*F Volume 10 Cubic Feet l l I 0415B/LC

SD 3527-005 l l l Appendix No. 5 to Submerged Demineralized System System Design Description i Title .l l SDS Monitor Tanks

SD 3527-005 APPENDfX NO. 5 SDS MONITOR TANKS l Vessel Details 4 Identification SDS-T-1A through SDS-T-1B  ! Manufacturer Buffalo Tank Number Installed Two (2) l I Design Capacity, Gallons 12,000 Gal. Each > Installation Vertical l Outside Diameter / Height, ft, in. 8 Ft./32 Ft. Shell Material Stainless Steel (304) . Shell Thickness, In. 3/16 Inch l 1 i Design Temperature, 'F Amb. l Design Pressure, PSIG Atmospheric Corrosion Allowance, In. None 1 Design Code API-650, Appendix J ' Code Stamp Required API-650, Appendix J 1 04178/LC

S0 3527-005 i l Appendix No. 5 (Cont'd)

                                                                                      .]

MONITOR TANK 1A/1B VOLUME VERSUS LEVEL 1 Level Tank Level Tank Level Tank Indication Volume Indication Volume Indication Volume 0 156 135 4353 270 85;0 187 136 4384 { 1 271 8561 2 218 137 4415 272 8612 3 249 138 4446 273 8643 4 280 139 4477 274 8674  ; 5 311 140 4509 275 8705  ! 6 342 141 4539 276 8736 373 142 4570

                                                                                       ]

7 277 8767 ) 8 404 143 4601 278 8799 9 435 144 4632 279 8830 l

                                                                                      .i 10       466            145         4664           280      8861 11       498            146         4695           281      8892

{ 12 529 147 4726 282 -8923 j 13 560 148 4757 283 8954 j 14 591 149 4788 284 8985 J l 15 622 150 4819 285 9016 j l 16 653 151 4850 286 9047 ( 17 684 152 4881 287 9078 18 715 153 4912 288 9109 ,

              ~19      746            154         4943           289      9141          {

20 777 155 4974 290 9172 l 21 808 156 5006 291 9203 { 22 840 157 5037 292 9234 J 23 871 158 5068 293 9265 24 902 159 5099 294 9296 25 933 160 5130 295 .9327 26 964 161 5161 296 9358 27 995 162 5192 297 9389 28 1026 163 5223 298 9420- ) i 29 1057 164 5254 299 9451 1 30 1088 165 5285 300 9483 l 31 1119 166 5316 301 9514 i 32 1150 167 5348 302 9545 33 1181 168 5379 303 9576 34 1213 169 5410 304 9607 35 1244 170 5441 305 9638 36 1275 171 5472 306 9669 37 1306 172 5503 307 9700 l 38 1337 173 5534 308 9731 39 40 1368 1399 174 5565 309 9762  ! 175 5596 310 9793 1 41 1430 176 5627 311 9824  : 42 1461 177 5658 312~ 9856 I 43 1492 178 5690 313 9887 h l l l 0417B/LC i q

SD 3527-005 Appendix No. 5 (Cont'd) MONITOR TANK 1A/18 VOLUME VERSUS LEVEL (Cont'd) Level Tank Level Tank Level ' Tank Indication Volume Indication Volume Indication Volume 41 1523 179 5721 314 9918 4:5 1555 180 5752 315 9949 46 1586 181 5783 316 9980 47 1617 182 5814 317 10011 48 1648 183 5845 318 10042 49 1679 184 5876 319 10073 50 1710 185 5907 320 10104 51 1741 186 5938 321 10135 52 1772 187 5969 322 10166 I 53 1803 188 6000 323 10198 1 54 1834 189 6032 324 10229 55 1865 190 6063 325 10260 56 1897 191 6094 326 10291 57 1928 152 6125 327 10322 i l 58 1959 193 6156 328- 10353 59 1990 194 6187 329 10384 60 2020 195 6218 330 10415 61 2052 196 6249 331 10446 l 62 2083 197 6280 332 10477 63 2114 198 6311 333 10508 64 2145 199 6342- 334 10539 65 2176 200 6374 335 10571 66 2207 201 6405 336 10602 l l 67 2239 202 6436 337 10633-68 2270 203 6467 338 10664  ! 69 2301 204 6498 339 10695  ; 70 2332 205 6529 340 10726  ! 71 2363 206 6560 341 10757 72 2394 207 6591 342 10788 ] 1 73 2425 208 6622 343 10819 74 l 2456 209 6653 344 10850 j 75 2487 210 6684 345 10882  : I 76 2518 211 6715 346 10913  ! 77 2549 212 6747 347 10944 i 78 2581 213 6778 348 10975 l a 79 2612 214 6809 349 11006 80 2643 215 6840 350 11037  ? l 81 2674 216 6871 351 11068 l 82 2705 217 6902 352 11099 83 2736 218 6933 353 11130 84 2767 219 6964 354 11161 85 2798 220 6995 355 11192 86 2829 221 7026 356 11224 0417B/LC L - - __o

SD 3527-005 Appendix No. 5 (Cont'd) MONITOR TANK 1A/1B VOLUME VERSUS LEVEL (Cont'd) Level Tank Level - Tank Level Tank Indication Volume Indication Volume Indication Volume 87 2860 222 7057 357 11255 88 2891 223 7089 358 11286 89 2923 224 7120 359 11317 90 2954 225 7151 360 11348 91 2985 226 7182 361 11380 92 3016- 227 7213 362 11410 93 3047 228 7244 363 11441 94 3078 229 7275 364 .11472 95 3109 230 7306 365 11503 96 3140 231 7337 366 11534 97 3172 232 7368 367 11566 98 3202 233 7389 368 11597 99 3283 234 7431 369 11628 100 3265 235 7462 370 11659. 101 3296 236 7493 371 11690 102 3327 237 7524 372 11721 L 103 3358 238 7555 373 11752 104 3389 239 7586 374 11783 105 3420 240 7617 375 11814 106 3451 241 7648 376 11845 107 3482 242 7679 377 11876 108 3513 243 7710 378 11908 109 3544 244 7741 379 11939 110 3575 245 7773 380 11970 111 3606 246 7804 381 12001 112 3638 247 7835 382 12032 113 3669 248 7866 383 12063 114 3700 249 7897 384 12094 115 3731 250 7928 385 12125 116 3762 251 7959 386 12156 117 3792 252 7990 387 -12188 118 3824 253 8021 388 12219 119 3855 254 8052 389 12250 120 3886 255 8083 390 12281 121 3917 256 8115 391 12312 , 122 3948 257 8146 392 12343 123 3980 258 8177 393 12374 - 124 4011 259 8208 394 12405 , 125 4042 260 8239 395 12436 1 126 4073 261 8270 396 12467 127 4104 262 l 8301 397 12498 128 4135 263 8332 398 12529 129 4166 264 8363 399 12561 130 4197 265 8394 400 12592 I 1 04178/LC

l
   - _                                                                             1

j SD 3527-005 Appendix No. 5 (Cont'd) MONITOR TANK 1A/1B VOLUME VERSUS LEVEL-(Cont'd) l Level Tank Level Tank Level Tank l Indication Volume Indication Volume Indication Volume  ! 131 4228 266 8425  ! 132 4259 267 8457 133 4290 268 8488 i 134 4322 269 8519 i 1 s I l I

                                                       '0417B/LC'

_ -___ _ _ - w

SD 3527-005 i j l 1 1 1 I 1 l  ! 1 l Appendix No. 6 I 1 to i l Submerged Demineralized System 1 j System Design Description j i

                                              '1 l

i

                                               )

O Title SOS Off Gas Separator Tank 1

SD 3527-00S APPENDIX NO. 6 SDS OFF GAS SEPARATOR TANK Vessel Details Identification CN-T-VA02 Manufacturer APC0 No. Installed One (1) Design Capacity, Gallons 590 Ga1. Each Installation Vertical i Outside Diameter / Height, ft. in. 36 In./10 ft. Shell Material Stainless Steel (304) Shell Thickness 3/16 Inch Design Temperature, 'F 100*F Design Pressure, PSIG 16 PSIG Corrosion Allowance, In. None Design Code ASME Section VIII, Div. 1 Code Stamp Required ASME Section VIII, Div. 1 l l l 0418B/LC

SD 3527-005 Appendin No. 6 (Cont'd) I OFF GAS SEPARATOR TANK VOLUME VERSUS LEVEL Level Tank Level. Tank Level Tank l Indication Volume Indication Volume Indication Volume I (percent) (gallons) (percent) (gallons) (percent) (gallons)- l i 0 25.8 40 198.5 80 371.7  ! 1 30.2 41 202.8 81 375.3 l 2 34.5 42 207.1 82 379.7 l l 3 38.8 43 211.4 83 383.9 l ! 4 43.2 44 215.7 84 388.3 5 47.5 45 220.0 85 392.6 f 6 51.8 46 224.3 86 396.9 7 56.1 47 228.7 87 401.2 8 60.4 48 232.9 88 405.5 9 64.7 49 237.3 89 469.9 10 69.0 50 241.6 90 414.2 11 73.4 51 245.9 91 418.5  ; 12 77.7 52 250.2 92 422.3 13 82.0 53 254.5 93 427.1 > 14 86.3 54 258.9 94 431.4 15 90.6 55 263.2 95 435.7 16 94.9 56 267.5 96 446.1 17 99.2 57 271.8 97 444.4 18 103.5 58 276.1 98 448.7 19 107.9 59 280.4 99 453.0 20 112.2 60 284.7 100 457.3 21 116.5 61 289.1 22 120.8 62 293.4-  ; 23 125.1 63 297.7 ' 24 129.4 64 302.0 25 133.7 65 306.3 26 138.1 66 310.6 27 142.4 67 314.9 28 146.7 68 319.3-29 151.0 69 323.6 L 30 155.3 70 327.9 J 31 159.6 71 332.2 J 32 163.9 72 337.5 33 168.3 73 340.8 34 172.6 74 345.1 35 176.9 75 349.5 i 36 181.2 76 353.8 37 185.5 77 358.1 38 189.8 78 362.4 l 39 194.1 79 366.7 NOTE: The above values represent tank volus.e versus' level-and do not include corrections for water in the standpipe. The standpipe has a linear relationship of 0.81 gallons per percent. l 04188/LC

SD 3527-005-l

                                                                               .]

Appendix No. 7 to Submerged Demineralized System System Design Description l l l l

                                                                                 .j I

1 I i l l l i 1 . l Title 1 S.D.S. Instrument List  ! i i i I l l l

                                          --.---------.-.-.-._.a,.,x__,

DI A NTL M UAO E - CRM R I I I I I I I I I EI TR DDNA - ONOL T CICA N

           - - -     I LICA          O A             P N :

OS T A A A A A A A A A I K E / / / / / / / / / TR S N N N N N N N N N CA NM UE E FR NL AA PC i i i i i i i i i SS s s s s s s s s s

                 / /          p      p        p        p      p       p         p       p       p TT UU         0      0        0        0      0       0         0       0       0 PP         6      6        6        6      6       6         6      6        6 NT         1      1        1        1      1      1          1      1        1 I U           -      -        -        -      -       -         -       -       -

D 0 0 0 0 0 0 0 0 0 O N L 5 S 5 5 S 5 S S S E 9 9 9 9 9 9 9 9 9 D 7 7 7 7 7 7 7 7 7 O 2 2 2 2 2 2 2 2 2 M 1 1 1 1 1 1 1 1 1 R t t t t t t t t t X E f f f f f f f f f E I o o o o o o o o o D L r r r r r r r r r 7 N P c c c c c c c c c I P h h h h h h h h h U s s s s s s s s s o T S A A A A A A A A A N N E x M i U d R x x n T d ro d d d ro e S l eB l l l eB p p N I f o t l e f o f o f o t l e A i i v i i i i v d d d S n F o n n n F o l l l D a l a a a l o o o S N M dG M M M dG f f f O a a i i i I r R e r r r R e n n n T e l e e e l a a a A t h p t t t h p M M M C l gm l l l gm O i i a i i i i a X X X L F HS F F F HS I I I e e e e e g l t l g g a p n p t a a dG m e m n G G l a t t u a e oe S n n l S u "A e "B e fr e e f l " r " r iu t u u f t f u u ns n l l E n n Xs Xs as ee f e f e e ee I e I s I s Me ug ng f g rg ug g e e r l a I a E a ea l a da 1 r 1 r nP o fG n r G r G tG l fG f l G o .P .P i t I e ee ee i e E e f e ot ot E t n r t r t r F r r i r N n N n C ae ru l u 1 u u ru nu e e I ru es i s 1 s l s es as nu nu V tl t s f s f s as t s Ms il i l R l f l e ee ee ne l e e af af E i n i r rr rr i r i r X r rf rf S FI FP PP PP FP FP IP TE TE l 2 3 4 S 6 8 9 0 O O O O O O 0 0 1 L L L L L L X X X F F F F F F I I I I I I I I I I I I P P P P P P P P P G . - - - - - - - - - AO N N N N N N N N N TN C C C C C C C C C

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                                                                                   ~

SD 3527-005 Appendix No. 8 to Submerged Demineralized System System Design Description l I l i 1

                                                                                                                             -l ;

1 Typical Analysis of Water Processed s u__________________.________..____.__________________.____._.___ _ _ _ _ . . _ .

SD 3527-005-Appendix 8 i Typical Analysis of Water Processed RCS RB Sump RB Sump Decon '

                                      -!sotope      RCS            RCS 6/85              5/86             9/80                  7/83 2/81 0.07uCi/mi        0.085uC1/mi      0.97uCi/mi     0.12uCi/mi H-3        0.066uC1/mi not detectable    not detectable   0.18uci/m1     not detectable Sr-89        0.25uci/mi 2.3uC1/mi          2.4uCi/mi       2.64uCi/mi     1.6uct/mi Sr-90        23uci/mi 0.055uCi/ml        0.013uCi/mi     9.1x10-3uCi/ml 0.023uCi/mi Sb-125       1.6x10-3uCi/ml 5.8x10-3uCi/mi     0.01uci/mi      27.7uC1/ml     0.14uci/mi Cs-134       3.4uCi/mi 25uC1/ml       0.14uC1/ml         0.35uCi/ml      172uC1/mi      2.luci/ml Cs-137 pH           7.6            7.55              7.58            8.6            7 5230 ppm          5460 ppm         2000 ppm      3193 ppm Boron        3800 ppm 1420 ppm          1500 ppm         1100 ppm      240 ppm Na           1240 ppm

) l 35,000 625,000 20,000 Volume 88,000 --- l (gallons) 1 0408B/LC

SD 3527-005 RCBT RCS RCS RCS RB Sump 471/87 RB Sump Decon 2/2/87- 3/15/87 12/18/86 2/10/87 1 H3 l 3.8x10-2uCi/mi 0.13uCi/ml 0.15uCl/ml  ! 0.luci/ml 0.12uCi/mi Sr-90 1. luc 1/mi 1.6x10-20Ci/ml 0.18uCi/ml 1.2uCl/mi 1. luc 1/ml Sb-125 3.9x10-2uC1/ml 3.9x10-2uCl/ml f-2.7x10-2uci/ml 4.1x10-2uCl/ml 1.5x10-2uCl!ml Cs-134 3 1x10-3uC1/mi 7.4x10-5uci/ml Cs-137 3.9x10-4u ci/mi 3.8x10-3uC1/mi 8.2x10-2uC1/m1-0.16uci/ml 2.2x10-3uCi/ml 2.3x10-2uC1/ml 0.19uC1/ml 3.5uCi/mi pH 7.61 7.54 7.67 7.6 7.48 Boron 5340 5015 4948 5145 3297 Na 1560 1420 1420 1375 548 3 \ Volume 35,000 73,950 71,710 50,372 40,506 i l

l 1

I l 4 l l l 04088/LC l l 1

SD 3527-005 I l i j l

                                                  .l i

l l j l l K i Appendix No. 9

                                                ~
                                                   \

to ) I Submerged Demineralized. System l l System Design Description l i I i l 1 l l l Title S.D.S. Drawing List l l l' l l l

SD 3527-005 Appendix No. 9 S.D.S. DRAWING LIST DRAWING NO. TITLE 1 CNSI-TMI Supply Manifold Submerged Ion l 527D-A-5001 l Exchangers P and ID l CNSI-TMI P and ID Contaminated Feed Water System 527D-A-5002 CNSI-THI P and ID Off-Gas and Liquid Separation 527D-A-5004 System CNSI-THI lon Exchange flow Sheet 527D-A-5005 CNSI-TMI 527-A-03/ Intermediate Sampling System 5270-A-5006 527D-A-5007 General Layout Plan Ion-Exchange Equipment CNSI-THI 527A-02 P and ID Beta Monitoring 5270-A-5009 Manifold 527D-A-5010 lon Exchanger Support Assembly Drawing 527C-A-5Dil CNSI-TMI Dewatering Station P and ID 5270-A-5013 P and ID RCS Clean-Up Manifold 527D-A-5014 Pool Floor Equipment Base-Locations Installation Dimensions 5270-D-5002 Prefilter 125 Micron 527D-D-5003 Final filter 10 Micron i 527D-D-5004 Prefilter/ Final Filter Details ( i J 0409B/LC 1

SD 3527-005-Appendix No. 9'(Cont'd). S.D.S. DRAHING LIST i DRAWING No. TITLE-5270-D-5007 Off-Gas Separator Item No.- 5270-01 527D-D-5008 Off-Gas Pump Stand Pipe 5270-0-5009 Exchanger Skirt and Lifting Lugs 527D-D-5011 Pref 11ter 141th Agitator > 5270-D-5012 Ion Exchanger, Final Filter and Prefilter '

                       . Details 527D-D-5013     Ion Exchanger and final Filter 527D-D-5014     Prefilter                                                 '

527D-J-5001 Beta Monitoring Housing Details 527C-J-5002 Beta Monitor Mounting Detail for L527-65 l RE527-13 527D-3-5003 , l Radiation Monitor Panel RMP-1 Arrangement 527D-J-5004 \ Radiation Monitors Holder and Weight Assy and Det for Ion Exchange filters Radiation Monitors ' l 5270-J-5005 Radiation Moni:: ors Holders and Weight Assembly l and Details for Ion Exchanger 5270-L-5001 Filter Manifold Piping Plan and Elevations 527D-L-5002

                     -Ion-Exchanger Support. Rack Piping 527D-t-5003    Ion-Exchanger Support Rack Piping 527D-L-5004 Filter and Leakage Containment Exchanger Rack Piping 5270-L-5005 Intermediate Level Sampling Glove Box Layout l

and Details 527A-03 l l l l l 0409B/LC

                                                                                                                                                                                                                                       ~
                                                                                                                                                                                                              ~SD 3527-005' g                                                                                           Appendlx.No.9(Cont'd)l S.D.S. DRAWING LIST DRAWINGNOi                                                                     TITLE (
                                                                                                                                                                                                                                    .i 5270-L-5008                                                                 . Unit (I) Support. Rack"and Exchanger PipingL Manifold Interconnecting,Pipi_ng Plan.and                                                                          i Section "A-A" 527D-L-5009                                                                    Unit-(I) Support Rack and Exchanger: Piping Manifold Interconnecting Piping Plan and Section "B-B"'
                                    '527D-L-50'10                                                                    Unit (I) Support Rack and Exchanger. Piping Manifol_d Interconnecting ~ Piping Plan'and Section "C-C'?

5270-L-50ll. P1 ping P1an'and~ Elevation Exchanger Manifold 527D-L-5012 Piping. Sections Exchanger Manifold-

                                                                                                                                                                                                                                    .i 5270-L-5014                                                                    filter Manifold and Filter Rack Interconnect-Piping <

527D-L-5015 Filter Manifold and filter Rack. Interconnect Piping. , 527D-L-5016 Piping Arrangement Su.rge Chamber Area-- 527D-L-5017 Piping Section Surge Chamber Area 527D-L-5018 Piping.Section Surge Chamber Area ~ f i 5270-L-5021 Piping Arrangement - Plan Off-Gas System 'l 1 5270-L-5022 Filter Manifold and Hi-Rad Filter Box  ? (527-A-01) _ Interconnect Piping I 5270-L-5023 Piping Arrangement - 527A-02 Beta Monitoring Manifold I l l 0409B/LC l l l L___ _ _ _ _ _ _ . ------ - - - - - - - - __ - - _ _ _ - - _______:--------------__-----.----_ - - - - _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ - - - - - - - - - - - - . - _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ ___ o

SD 3527-005 Appendix No. 9 (Cont'd) S.D.S.' DRAWING LIST , DRAWING NO. TITLE 1 5270-L-5026 Utility Piping Arrangement Plan - Unit II "B" I Tuel Pool l 1 5270-L-5027 Utility Piping Arrangement Details - Unit II -

               "B" Fuel Pool 5270-L-5028   Piping Arrangement - Sections Off-Gas System 527D-L-5029   Piping Arrangement - Dewatering Station 527D-L-5030   Piping Arrangement RCS Clean-Up Manifold 5270-L-5031   Composite Piping Arrangement Ion Exchanger, l               Polish Manifold, Filter Manifold.and RCS           j Clean-Up Manifold                                  i 527D-L-5032   Composite Piping Elevation Ion Exchanger, Polish Manifold, Filter Manifold and RCS Clean-Up Manifold l

527D-L-5033 Composite Piping Arrangement Surge Chamber Area l Plan Column AM to AP 5270-L-5034 Composite Piping Arrangement Surge Chamber Area Elevations 5270-M-5003 Filter Manifold Assembly Plan and Elevation 527D-M-5004 Filter Manifold' Assembly Sections 527D-M-5005 Filter Manifold Assembly Details I 5270-M-5006 Filter Manifold Assembly Details 527D-M-5007 CNSI-THI lon Exchanger Support Unit la 527D-M-5008 CNSI-TMI lon Exchanger Support Units Ib, Id and Ie 5270-M-5009 CNSI-TMI lon Exchanger Support Unit Ic i l 0409B/LC. l

4 SD 3527-005 Appendix No. 9 (Cont'd) S.D.S. DRAWING LIST l DRAWING NO. TITLE ;l 5270-M-5010 CNSI-TMI. Ion Exchanger Support Unit II 5270-M-50ll CNSI-TMI Ion Exchanger Support Unit III 527D-M-5012 Ion Exchanger Support Data 11s 5270-M-5013 Off-Gas Separator and. Stand Pipe - Skid Detail 270-H-5015 Cask Support Platform Plan, Section and Detail 5270-M-5016 Surge Chamber Cover Plan and Details i l 5270-M-5017 Exchanger Manifold Plans and Sections l 527D-M-5018 Exchanger Manifold Sections and Details 5270-M-5019 Cask Support Platform Filter Manifold Shielding Details 527D-M-5020 Ion Exchanger Lifting Yoke Guide Details 527D-M-502'l Spent Ion Exchanger Storage Rack 5270-M-5022 Beta Monitoring Manifold Plans and Sections 5270-M-5023 1-13C Shipping Cask Support Platform 527D-M-5024 Yoke Hanger Detail 5270-M-5025 Plans and Details Dewatering Station 5270-M-5026 Fipe Containment and Restraint Details 527D-M-5027 Moveable Spent Ion Exchanger Storage Rack-5270-M-5028 Spent Ion Exchanger Storage Rack - Unit 3 527D-M-5029 Spent Ion Exchanger Storage Rack - Unit 4a 0409B/LC

SD'3527-005 Appendix No. 9.(Cont'd) 5.D.S. DRAHING LIST DRAHING NO. TITLE ) 5270-M-5030 RCS Clean-Up Manifold Assembly, Plan, Elevation and Details jl 5270-M-5031 RCS Clean-Up Manifold Assembly, Sections and Details i' 527D-M-5032 Spent Ion Exchanger Storage Rack - Unit'4b 527D-M-5033 Shielded Pipe Chase for RCS' Clean-Up Manifold Arrangement Assembly and Details 527D-M-5034 Radiation Shielding Between RCS Clean-Up Manifold and Pipe Chase Assembly and Details ' I 527D-M-5035 Personnel Crane Basket Assembly 5270-M-5036 Personnel Crane Basket Details 5270-M-5037 Storage Rack Lifting Device Plan, Sections and Details

                                                                    )

527D-P-5002 CNSI-TMI Electrical Hiring Diagrams 460 Volt Motors,-Etc. 527C-P-5003 CNSI-TMI Electrical Hiring Diagrams 120 Volt Sump Pumps 1 527D-P-5004 CNSI-TMI Electrical Plan Power and' Lighting j 527D-P-5005 CNSI-TMI Electrical Details and Bill of Materials 1 I 527D-P-5006 CNSI-THI Electrical Sections 5270-P-5007 Loop Diagram F1/FQ1 - 527-07. -09, -10 L1-527-01 527D-P-5008 Electrical Connection Diagram Annunciator Panel No. I and Single Point Annunciators 527D-P-5009 Instrument and Electrical Plan and Details 1 j l 0409B/LC

SD 3527-005 Appeadix No. 9 (Cont'd) j 5.0.S. DRAWING LIST i 1 DRAWING NO. TITLE 527C-P-5010 Loop Diagram LC/LSH-527-03, LC-527-04, LSH-527-04, LC/LSH-527-43 l 5270-P-5011 Instrument and Electrical Sections 527D-P-5012 Loop Diagram Area and Off-Gas Gamma Monitors 527D-P-5013 Interconnection Wiring Diagram Radiation j Recorder RJR-527-01 527D-P-5014 Loop Diagram Beta Monitoring System 5270-P-5016 Loop Diagram Underwater Radiation Monitoring- ) System 1 527D-P-5017 Loop Diagram Pressure Instr., Temperature Instr., Demineralized Water Flow Control 527C-R-1003 Unit IIB Structural Bracing for Rigging  ; 527C-R-1004 Unit IIA Structura'l Bracing for Rigging 527C-R-1005 Unit IIIA Structural Bracing for Rigging 527C-R-1006 Unit IIIB Structural Bracing for Rigging l 527C-R-1007 Load Transfer Triangle and Spreader Bar Details 527D-R-1008 Unit IIIA P,igging Details 527D-R-1009 Unit IIIB Rigging Details 527C-R-1010 Arrangement for Mating Unit IIIB to IIIA 527D-R-1011 Unit IIA Rigging Details 527D-R-1012 Unit IIB Rigging Details ) l 0409B/LC

SD 3527-005 Appendix No. 9 (Cont'd) S.D.S. DRAWING LIST- :1 DRANING NO. TITLE I 527C-R-1013 Arrangement for Mating Unit IIB to IIA 5270-R-1014 Unit ID/IE Rigging 527C-R-1015 Load Transfer Triangle and Adjustable Spreader Bar 5270-R-1016 Unit IC Rigging 527D-R-1017 Unit IB Rigging 527D-R-1018 Ur,1 t IA' Rigging 527C-R-1019 Compression Rigging Lug Details i 527D-R-1020 Alignment and Compression Rigging Assemblies for Unit IA, IB, IC, ID, IE . 527D-R-1021 Filter Manifold Rigging 527D-R-1022 Shipping Cask Support Platform Rigging 527D-R-1024 Beta Manifold Rigging and Pad Eye Details 527D-R-1025 Ion Exchanger Manifold Rigging Details 5270-R-1026 Ion Exchanger Manifold Rigging Sections 527C-R-1027 Intermediate Glove Box Table 527A-03T Swivel Shackle Bolt Hole Location Details 527C-R-1028 Hi-Rad filter Glove Box Support Table 527A-01T Rigging Support Details 527D-R-1029 Intermediate Level Glove Box Assembly Rigging 5270-R-1030 Hi-Rad filter Sample Box and Support Rigging Details i i

                       -B-                            04090/LC t

SD 3527-005 l Appendix No. 9 (Cont'd) ~ S.D.S. DRAWING LIST DRAWING NO. TITLE 527C-R-1031 Lightweight Padeye Test Rig Assembly (Torque) 527C-R-1032 Lightweight Padeye Test Rig Assembly (Hydraulic) 4

                                                                                                                                                                                        -l 5270-R-1033      Off-Gas Air filtration System Rigging 527C-R-1034      Hi-Rad Feed Glove Box Rigging Support Details 5270-R-1035       Hi-Rad Feed Sample Glove Box Assembly Rigging l

5270-R-1036 Surge Chamber' Cover Rigging for Covers 1A, 2A, 3A, 4A (typ) l 5270-R-1037 Off-Gas Separator and Standpipe Rigging Phase II i 527D-R-103B Off-Gas Separator and Standpipe Rigging Phase I - and III 527D-R-1041 Ion Exchanger Transport Cask 14-195-H Assembly J Rigging .] 5270-R-1044 Dewatering Station Structural Bracing Required for Rigging l 5270-R-1045 Dewatering Station Rigging Phase I and Phase II i 527C-R-1046 Dewatering Station Rigging Phase III 5270-1-5001 Assembly and Details Remote Disconnect for Hansen Coupler 1 527D-T-5002 Intermediate Level Sampling Glove Box 527A-D3 1 527D-T-5003 Intermediate Level Sampling Glove Box 527A-03 527C-T-5004 Intermediate Sampling Manifold Bottle Lifting Mechanism Details 527A-03 I 5270-T-5008 Hi-Rad feed Sample Glove Box 527A-04 i 04090/LC I

d. . <

SD 3527-005' A Appendix No. 9 (Con't'd)

                                                         .S.0.5. DRAHING LIST a

DRAWING NO. TITLE

           '5270-T-5009                                    Lifting Yoke Assembly.for Exchanger Tanks 527D-T-5010                                   Remote' Disconnect Guide and Supports 5270-T-5011-                                  Exchanger Yok'         e Details.
            .527D-T-5012'                               -Hi-Rad filter Sample Glo've Box:527A-01 5270-T-5014'.                                 Hi-Rad Feed Sample Glove Box Layout and. Details:

527A-04: 527D-T-5015 Hi-Rad filter Glove Box' Layout and Details 527 5270-T-5016 , Lifting'. Yoke Assembly for CNS-1600 Shipping Cask

           ~5270-T-5017_                                ~Hi-Rad filter Glove Box Piping and Sectlons.

527A-01 527DhT-5018 Hi-Rad Feed Sample Glove' Box Piping and i' Sections 527-04 527D-T-5019 Liftitg Yoke Details 5270-T-5020 Support. Table 527A-03T and'527A-04T'for Intermediate Level Glove Box and Hi-Rad Feed Glove Box 5270-T-5022 Lifting Yoke Assembly for Unspent Exchanger Tanks 5270-T-5023 Exchanger. Yoke Details for-Unspent Exchanger Tanks 5270-T-5024 Support Table 527A-01T for Hi-Rad Filter Glove Box 527A-01 5270-T-5025' Cask and Exchanger Tank Alignment F1xture 5270-T-5026 Shielded Pipe Chase 527A-01C for Hi-Rad Filter Glove: Box 527A-01 Arrangement, Assembly and Details

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SD 3527-005 Appendix No. 9 (Cont'd) S.D.S. DRAHING LIST DRAWING NO. TITLE 5270-T-5027 Assembly and Details Remote Disconnect for Hansen Coupler at Dewatering Station 527D-T-5028 Dewatering Station Remote Disconnect Guide and Supports 527D-T-5029 Valve Stem Extensions and Shielding, Assembly and Details for Glove Boxes and Manifolds 527D-T-5030 Valve Stem Extensions and Shielding, Assembly and Details for Manifolds 527D-T-5031 Hansen Coupler Remote Connector Assembly and Details for Prefilter Nozzle A 5270-T-5032 Manipulator and Recovery Tool DD-527A-J-5001 Sht. 1 of 3 Installation Design Detail Material List , l DD-527A-3-5001 Sht. 2 of 3 Installation Design Detail Material List DD-527A-J-5001 Sht. 3 of 3 General Notes for Fabrication and Installation of Instruments and Supports DD-527C-J-5002 Installation Design Detail Level Control Panel Off-Gas Separator DD-527A-J-5004 Installation Design Detail Flow Indicator / Totalizer and Liquid Vortex Flow Element DD-527A-J-5007 Installation Design Detail Flow Indicating U-Tube Manometer and Orifice { DD-527A-J-5008 Installation Design Detail Flow Indicating Manometers Orientation - Ion / Cation Exch. Sys. DD-527A-J-5013 Installation Design Detail Pressure Differential Indicator / Switch l 0409B/LC l

SD 3527-005 Appendix No. 9 (Cont'd) S.D.S. DRAHING LIST DRAWING NO. TITLE ' DD-527A-J-5016 Installation Design Detail Feed Temp. Indicator I TI-527-07 and TI-527 DD-517C-3-5017 Installation Design Detail Mounting Support for-l l Annunciator Panel No. 1 and Hi-Rad Alarm ' ) DD-527A-J-5018 Installation Design' Detail Electronic Level

                                          ' Switch LC and LSH-527-04 DD-527A-J-5019        Installation Design Detail Electronic Level       i Switch LC/LSH-527-03 and LC/LSH-527-43 DD-527A-J-5020         Installation Design Detail Hi Rad. Alarm RAH-527-ll DD-527A-J-5021      ' Installation Design Detail Hi Rad. Alarm l

RAH-527-01

                                                                                              ]

DD-527A-J-5022 Installation Design Detail Underwater Gamma Radiation Monitors f DD-5270-3-5023 Installation Design Detail Sample System Piping Off-Gas Radiation Monitor DD-527A-3-5024 Installation Design Detail Mounting Support for Relay Panel RP-1 DD-527A-J-5025 Installation Design Detail Support Stand for Filter Radiation Monitors l l 1 0409B/LC

SD 3527-005  ! Appendix No. 9 (Cont'd) 5.D.S. DRAWING LIST , DRAWING NO. TITLE l l RW3501-012C-14 Filter Manifold and Filter Rack Interconnect Piping RW3501-012C-14-01 Filter Manifold and Filter Rack Interconnect Piping - Piping Detail RW3501-012C-14-02 Filter Manifold and Filter Rack Interconnect-Piping - Piping Detail RW3501-012C-14-03 Filter Manifold and Filter Rack Interconnect Piping - Piping Detail I RW3501-012C-14-04 Filter Manifold and Filter Rack Interconnect Piping - Piping Detail  ! RW3501-012C-14-05 Filter Manifold and Filter Rack Interconnect Piping - Piping Detail RW3501-012C-14-06 Filter Manifold and Filter Rack Interconnect Piping - Piping Detail RW3501-012C-14-07 Filter Manifold and Filter Rack Interconnect  ! Piping - Piping Detail RW3501-012C-15 Filter Manifold and Filter Rack Interconnect { Piping d l l l 0409B/LC -- _ __-_-_ _ _ _ _ _ = _ _ _ _ _ _ _ _ _ _ - _ _ _ _ _ _ - _ _ _ _ _ _ _ _ _ _ _

SD 3527-005 Appendix No. 9 (Cont'd) S.D.S. DRAHING LIST DRAHING NO. TITLE RH3501-012C-22 Filter. Manifold and Hi-Rad Filter Box.(527A-01) Interconnect Piping l RH3501-012A-08 Unit (1) Support Rack and Exchanger Piping Manifold Interconnecting Piping Plan sad Section "A-A" j RH3501-012A-08-01 Unit (1) Support Rack and Exchanger Piping. Manifold Interconnecting Piping - Piping Detail RH3501-012A-08-02 Unit (1) Support Rack and Exchanger Piping

                                                  .                                       i i                                       Manifold Interconnecting Piping - Piping Detail ~  l RH3501-012A-08-03  ' Unit (1) Support Rack and Exchanger Piping i                                       Manifold Interconnecting Piping - Piping Detail l

RH3501-012A-08-04 Unit (1) Support Rack and Exchanger Piping . Manifold Interconnecting Piping - Piping Detail- ) ( RH3501-012A-08-05 Unit (1) Support Rack and Exchanger Piping Manifold Interconnecting Piping - Piping Detail RH3501-012A-08-06 Unit (1) Support Rack and Exchanger Piping ) Manifold Interconnecting Piping - Piping Detail ' RH3501-012A-08-07 Unit (1) Support Rack and Exchanger Piping Manifold Interconnecting Piping - Piping Detail RH3501-012A-08-08 Unit (1) Support Rack and Exchanger Piping Manifold Interconnecting Piping - Piping Detail RH3501-012A-08-09 Unit (1) Support Rack and Exchanger Piping i Manifold Interconnecting Piping - Piping Detail l RH3501-012A-08-10 Unit (1) Support Rack and Exchanger Piping Manifold Interconnecting Piping - Piping Detail RH3501-012A-08-11 Unit (1) Support Rack and Exchanger Piping Manifold Interconnecting Piping - Piping Detail 04098/LC l

i SD 3527-005-1 Appendix No. 9 (Cont'd): 1 S.D.S. DRAHING LIST DRAHING NO. TITLE RH3501-012A-08-12: Unit (1) Support Rack and Exchanger Piping .. Manifold Interconnecting P.iping '. Piping Detail l RH3501-012A-08-13. Unit (1) Support Rack and Exchanger Piping s  : Manifold Interconnecting Piping'- Piping. Detail RW3501-012A-08-14 Unit-(1) Support Rack and Exchanger. Piping... '

                                                                                                                ~ Manifold Interconnecting Piping -' Piping Detail RH3501-012A-08-15          . Unit (1) Support. Rack.and Exchanger Piping.

Manifold Interconnecting Piping . Piping' Detail.

                                                                                                                                                                                    )
                                                                                                                                                                                  -l RH3501-012A-08-16             Unit ~-(1) Support Rack and Exchanger Piping           .

Manifold. Interconnecting Piping;- Piping'_ Detail. ] RH3501-012A-08-17 Unit (1) Support Rack and Exchanger Piping- .. Manifold Interconnecting Piping : Piping' Detail i RH3501-012A-08-18 Unit (1) Support Rack and Exchanger. Piping. Manifold Interconnecting Piping - Piping Detail-RH3501-012A-08-19 Unit:(1) Support Rack and. Exchanger Piping-Manifold Interconnecting Piping - Piping Detail RH3501-012A-09 Unit (1) Support Rack and Exchanger Piping Manifold Interconnecting Piping - Section "B-B" RH3501-012A-10 Unit (1) Support Rack and Exchanger. Piping Manifold Interconnecting Piping - Section "C-C" RH3501-005-03 Intermediate Level Sample Layout and Details l RH3501-005-03-01 Air Filter Ass'y i RH3501-005-04 Intermediate Level Sampling Glove' Box 527A-03 Details i RH3501-005-05 Intermediate Level-Sample Layout'and Detaiis i RH3501-005-06 Tubing. Loop Sheet j I l

                                                                                                                                                                                 .I a

0409B/LC i

1 50'3527-005 Appendix No. 9 (Cont'd) S.D.S. ORAHING LIST DRAHING NO. TITLE RH3501-005-07 Support Table 527A-03T for Intermediate Level Glove Box RH3501-007-01 Hi-Rad Filter Glove Box Piping and Sections 527A-01 1 RH3501-007-02 Hi-Rad filter Glove Box Layout and Details 527A-01 RH3501-007-03 Hi-Rad filter (01) Glove Box Details RH3501-007-04 Hi-Rad Filter Sample Glove Box 527A-01 RH3501-007-05 Hi-Rad Filter Sample Glove Box 527A-01 RH:501-007-06 Support Table for Hi-Rad Filter Glove Box RH3501-007-07 Misc. Details for Support Table. RH3501-007-08 Misc. Details for Support Table and Piping Shield RH3501-008-01 Hi-Rad Feed Sample Glove Box Piping and Sections 527A-04 1' RH3501-008-02 Hi-Rad Feed Sample Glove Box Layout and Details 527A-04 RH3501-008-03 Hi-Rad Feed Sample (-04) Glove Box Details RW3501-008-04 Hi-Rad Feed Sample Glove Box 527A-04

RH3501-008-05 Hi-Rad Feed Sample Glove Box Details (04) l RH3501-008-06 Support Table 527A-04T for Hi-Rad Feed Glove Box RH35CJ -009-01 Beta Monitor Mounting Detail for L527-65
       ;                      RE527-13 RH3541-010-04 Sht.1 of 2  Off-Gas Separator and Standpipe, Piping Rack 1

0409D/LC

SD 3527-005 Appendix No. 9 (Cont'd) 'I 5.D.S. DRAHING LIST J DRAHING NO. TITLE RH3501-010-04 Sht. 2 of 2 Off-Gas Separator and Standpipe' Piping Rack RH3501-002-01 Filter Manifold Piping Plan and Elevations RH3501-002-02 Filter Manifold Assembly Details RH3501-002-03 Filter Manifold Assembly Plan and Elevation RH3501-002-04 Fiiter Manifold Assembly Seetions RH3501-002-05 Filter Manifold Assembly Details j l RH3501-002-06 Filter Manifold Assembly Details i l RH3501-002-07 Filter Manifold Assembly Box and Details l .

                                                                                                            \

RH3501-003-01 Exchanger Manifold , RH3501-003-02 Exchanger Manifold Sections and Misc. Details RH3501-003-03 Exchanger Manifold Misc. Details RH3501-003-04 Exchanger Manifold Containment Plates Details RH3501-003-05 Coping Details for Exchanger Manifold I RH3501-003-06 Beta Monitor Housing Details Type B RH3501-003-07 Exchanger Manifold Structure Assembly RH3501-003-11 Piping Plan and Elevation Exchanger Manifold i RH3501-003-12 Piping Sections Exchanger Manifold RH3501-004-01 Beta Monitoring Manifold RH3501-004-02 Beta Monitoring Manifold Misc. Details l RH3501-004-03 Beta Monitor Housing Details Type "A" 0409B/LC

50:3527-005' i ['  ; Appendix'No.'9 (Cont'd)' S.D.S. ORAWING LIST 1 1 DRAWING NO. TITLE. RW3501-004A-23 Piping Arrangement - 527A-02 Beta Monitoring- a Manifold' ' RW3501-005-01  : Intermediate Level SampletGlove: Box j RW3501-005-02 Intermediate' Level' Sampling Glove Box 527A-03. RW3501-012E-16 Piping Arrangement Surge Chamber. Area- - RW3501-012E-16-01 Surge. Chamber Area Piping Detail.  ! RW3501-012E-16 ' Surge Chamber Area Piping Detail: RW3501-012E-16-03 . Surge' Chamber Area Piping. Detail-RW3501-012E-16-04 Surge Chamber Area Piping. Detail RW3501-012E-16-05 Surge. Chamber Area Piping Detal1 RW3501-012E-16-06 Surge Chamber-Area Piping Detail RW3501-012E-16-07 Surge Chamber Area Piping Detail RW3501-012E-16-08 Surge Chamber Area Piping Detail RW3501-012E-16-09 Surge. Chamber Area Piping Detail RW3501-012E-16-10 Surge Chamber. Area Piping Detail i RW3501-012E-16-11 Surge Chamber Area' Piping Detail RW3501-012E-16-12 Surge Chamber Area.Pipin'g Detail RW3501-012E-16-13 Surge Chamber Area Piping Detail-RW3501-012E-16-14 Surge Chamber Area Piping Detail nW3501-012E-16-15 Surge Chamber Area Piping Detall' RW3501-012E-16A Off-Gas Separator and Standpipe Skid P.iping Arrangement { l

                                                                  - 18   -

0409B/LC

SD 3527-005 Appendix No. 9 (Cont'd) S.D.S. DRAWING LIST DRAWING NO. TITLE RW3501-012E-17 Piping Sections Surge Chamber Area RW3501-012E-18 Piping Sections Surge. Chamber Area e RW3501-012F-ML-01 Sht. 1 of 2 Bill-of Material RW3501-012F-ML-01 Sht. 2 Of 2 Bill of Material RW3501-012F-26 Utility Piping and Polish Manifold Piping'Plece Mark Dwgs. RW3501-012F-27 Utility Piping Arrangement Details Unit No. 2 -

                                                                              "B" Fuel Pool RW3501-012L-31                      Composite Piping Arrangement Ion Exchanger, Polish Manifold, Filter Manifold and RCS Clean-Up Manifold RW3501-012L-32                      Composite Piping Arrangement Ion Exchanger, Polish Manifold, Filter Manifold and RCS Clean-Up Manifold RW3501-012L-33                      Composite Piping Arrangement Surge Chamber Area Plan - Column AM to AP RW3501-012L-34                      Composite Piping Arrangement Surge Chamber Area Elevations RW3501-012N-21-01                   Off-Gas System Piping RW3501-012N-21-02                   Off-Gas System Beta Manifold Piping RW3501-012N-21-03                   Off-Gas System Hi-Rad Feed Sample Glove Box l                                                                              Piping Connection RW3501-012N-21-04                   Off-Gas System Piping from Hi Rad Filter Sample Glove Box i

RW3501-012N-21-05 Off-Gas System Exchanger Manifold Exhaust Piping l l l 04098/LC l

SD 3527-005 Appendix No. 9 (Cont'd) S.D.S. DRAWING LIST DRAWING NO. TITLE ' RW3501-012N-21-06 Off-Gas System Piping ., RW3501-012N-21-07 Off-Gas System Piping RW3501-012N-21-08 Off-Gas System Piping RW3501-012N-21-09 'Off-Gas System Piping RW3501-012N-21-10 Off-Gas System Piping ' RW3501-0120-1 Plate Layout for Pipe Supports 527-PS-1-49 3 RW3501-015-B1 RCS Clean-Up Manifold Pipe Bend i RW3501-015-01 Sht. I of 7 RCS Clean-Up Manifold Assembly RW3501-015-01 Sht. 2 of 7 RCS Clean-Up Manifold Assembly RW3501-015-01 Sht. 3 of 7 RCS Clean-Up Manifold Assembly i RW3501-015-01 Sht. 4 of 7 RCS Clean-Up Manifold Assembly i RW3501-015-01 Sht. 5 of 7 RCS Clean-Up Manifold Assembly I RW3501-015-01 Sht. 6 of 7 RCS Clean-Up Manifold Assembly i RW3501-015-01 Sht. 7 of 7 RCS Clean-Up Manifold Assembly  ! RW3501-015-02 RCS Clean-Up Manifold Brick Placement Layout RW3501-015-30 Piping Arrangement RCS Clean-Up Manifold RW3501-015-30-01 RCS Clean-Up Manifold Piping RW3501-015-30-02 RCS Clean-Up Manifold Piping RW3501-015-30-03 RCS Clean-Up Manifold Piping RW3501-015-30-04 RCS Clean-Up Manifold Piping 0409B/LC I

SD 3527-005 Appendix No. 9 (Cont T S.D.S. DRAHING LIST DRAHING NO. TITLE RH3501-015-30-05 RCS Clean-Up Manifold Piping RH3501-015-30-06 RCS Clean-Up Manifold Piping RH3501-015-30-07 RCS Clean-Up Manifold Piping RH3501-015-30-08 RCS Clean-Up Manifold Piping RH3501-015-30-09 RCS Clean-Up Manifold Piping RH3501-015-30-10 RCS Clean-Up Manifold Sump Pump Piping RH3501-015-30-11 RCS Clean-Up Manifold Sump Pump Piping RH3501-031-00-01 Ion Exchanger, Filter and Leakage Containment Exchanger Rack Piping RH3501-031-00-02 Ion Exchanger, Filter and Leakage Containment Exchanger Rack Piping RH3501-031-00-03 Ion Exchanger, Filter and Leakage Containment Exchanger Rack Piping RH3501-031-02 Ion Exchanger Support Rack Piping Bundle Piping RH3501-031-03 Ion Exchanger Support Rack Piping i RH3501-031-03-09 Ion Exchanger Support Rack Piping Details RH3501-031-04 Filter and Leakage Containment Exchanger Rack l Piping 1 l l RH3501-031-04-07 Leakage Containment Exchanger Rack Piping I Details RH3501-031-04-08 Leakage Containment Exchanger Rack Piping Details RH3501-031-04-09 Leakage Containment Exchanger Rack Piping Details 1 0409B/LC

, .\

., oF :SD 3527-005 Appendix No. 9.(Cont'd) ' S.D.S. DRAWING LIST d d DRAWING NO. . TITLE-RH3501-031-04-10 -Leakage Containment' Exchanger' Rack Piping Details .i

                                        ~

RW3501-031-04-11 . Leakage' Containment' Exchanger Rack Piping Details RW3501-031-04-12 iLeakage Containment. Exchanger l Rack Piping Details 'i 3 1 RH3501-031-04A . Filter and Leakage. Containment Exchanger ~ Rack Piping-RH3501-031-07A Sht. 1 of 3 CNSI-TMILIon Exchanger Support Unit '1A.- I RH3501-031-07A Sht. 2 of 3-

                                                                                           'l CNSI-TMILIon~ Exchanger Support Unit 1A
                                                                            ~

q RW3501-031-07A Sht. 3 of 3 CNSI-TMI lon' Exchanger Support Unit 1A I RH3501-031-088 Sht. 1 of 2 CNSI-TMI~ Ion Exchanger Support Unit 18 RW3501-031-08B Sht. 2 of 2 CNSI-TMI Ion Exchanger Support Unit 18 RW3501-031-08D-01 CNSI-TMI lon Exchanger Support-Unit.1D RH3501-031-080-02 CNSI-TMI lon Exchanger Support Unit 1D RW3501-031-08E-01 CNSI-TMI Ion Exchanger Support Unit 1E RH3501-031-08E-02 CNSI-TMI lon Exchanger Support Unit 1E. RH3501-031-09 Sht. 1 of 7 CNSI-THI lon Exchanger Support Unit'IC RW3501-031-09 Sht. 2 of 7 CNSI-TMI. Ion Exchanger Support Unit IC l RW3501-031-09 Sht. 3 of 7 CNSI-TMI Ion: Exchanger Support Unit 1C RW3501-031-09 Sht. 4 of 7 CNSI-THI lon Exchanger. Support Unit 1C RH3501-031-09 Sht. 5 of 7 CNSI-THI-Ion Exchanger Support Unit 1C' l 0409B/LC.

50 3527-005: ) l

                                               . Appendix No. 9 (Cont'd)l                                        i S.D.S. DRAHING LIST DRAHING NO.                        TITLE RH3501-031-09 Sht.'6 of'7:         CNSI-TMI Ion. Exchanger Support Unit 1C RH3501-031-09 Sht. 7'of 7         CNSI-TMI' Ion. Exchanger Support Unit.1C
                .RH3501-031-10A Sht. 1.of 2        CNSI' THI Iori Exchanger Support Unit IIA TRH3501-031-10A Sht 2 of 2         CNSI-TMI' Ion. Exchanger Support Un.it IIA RH3501-031-10C Sht. 1:of.3        CNSI-THI. Ion Exchanger Support Unit IIB RH3501-031-10C.Sht. 2 of 3L       CNSI-TMI Ion Exchanger Support Unit IIB l

RH3501-031-10C Sht. 3 of 3 CNSI-TMI-Ion Exchanger Support Unit IIB RH3501-031-11A Sht. 1:of'2 CNSI-TMI Ion Exchanger Support Unit IIIA. RH3501-031-11A Sht. 2 of 2 CNSI-TMI Ion Exchanger: Support Unit.IIIA RH3501-031-11B Sht. 1 of 3 CNSI-TMI.lon Exchanger Support Unit IIIB RH3501-031-118 Sht. 2 of 3- CNSI-TMI lon Exchanger Support Unit IIIB RH3501-031-118 Sht. 3 of 3 CNSI-THI lon Exchanger Support Unit IIIB  ; RH3501-031-12 Ion Exchanger Support Detiils Noveable ' Personnel Bridge. RH3501-031-12A Ion Exchanger Support Details Hoveable. Personnel Bridge II-RH3501-031-13 Ion-Exchanger Support Details Cross Bracing- , RH3501-031-14 Ion. Exchanger Remote Valv'e Operators RH3501-031-15 Sht.1 Of 2 Ion Exchanger Piping Rack Details j RH3501-031-15 Sht. 2 of 2 Ion Exchanger Piping Rack Details) l RH3501-031-16 . Cask Support Connection' Unit IIIA i i i 1 l l  !

                                                                                                              'i 0409B/LC         l l

_ - _ _ - - __ - _ - _ _ - - _ _ _- _ - - . =2 .-

 ,                                                                              i 50 3527-005' Appendix No. 9 (Cont'd)-

S.D.S. DRAHING LIST DRAHING NO. TITLE RW3501-031-17' ' Pipe Containment Stand RH3501-031-18 Load Transfer Triangle and-Spreader Bar Details RW3501-031-19 Unit IIA Structural Bracing for Rigging RW3501-031-20 Unit IIB Structural Bracing for Rigging ) i RW3501-031-21 Unit IIIA Structural Bracing for Rigging l RW3501-031 Unit IIIB Structural Bracing for Rigging RW3501-031-23 Pipe Chase for Unit I RH3501-031-24 Restraints for Unit 1 and Unit 2 Rw3501-031-25 Strut Rod Orientation Assembly and Details RW3501-031-28 Load Transfer Triangle and Adjustable Spreader Bar RH3501-031-29 Compression Rigging Lug Details l l RW3501-031-30 Unit lA Rigging

                                                                                 )

l RW3501-031-31 Unit 1C Rigging RW3501-031-32 Remote Valve Operator (Diaphram Valve) RW3501-032-01 Assembly and Details - Remote Disconnect for Hansen Coupler RW3501-032-02 Remote Disconnect Guide and Supports RW3501-032K-31 Sh'. 1 of 2 Hansen Coupler Remote Connector Assembly and Details for Pref 11ter Nozzle "A" RW3501-032K-31 Sht. 2 of 2 Hansen Coupler Remote Conn. Bill of Haterial for Prefilter Nozzle "A" 04098/LC

I SD'3527-005 Appendix No. 9-(Cont'd) S.D.S. DRAWING LIST-DRAWING NO. TITLE RH3501-033-01 . Cask Support: Platform. Plan,. Sections and Details RH3501-033-06 ShieldedPipeChaseRCSClean-UpfManifold Arrangement and Assembly RH3501-033-07 Shielded Pipe Chase RCS Clean-Up Manifold RH3501-033-08 Radiation Shielding Between RCS Clean-Up l Manifold.and Pipe Chase Assembly and Details [ RW3501-033-09 Field Fabrication Details RW3501-034-01 Sht. 1 of 3 Metal Forms for Surge Chambe'r Cover i

                                                            ~

RW3501-034-01 Sht. 2 of 3' Metal. Forms for Surge Chamber. Cover Details I RW3501-034-01 Sht. 3 of 3 . Surge Chamber Cover Plan and Details - 1A RW3501-034-02 Sht. 1 of 3 Metal Forms for Surge. Chamber' Cover RW3501-034-02 Sht. 2 of 3 Metal Forms for Surge Chamber Cover Details RH3501-034-02 Sht. 3 of 3 Surge Chamber Cover Plant and Details --2A I RW3501-034-03 Sht. 1 of 3 Metal forms for Surge Chamber Cover RH3501-034-03 Sht. 2 of 3 Metal Forms.for Surge Chamber' Cover Details RW3501-034-03 Sht. 3 of 3 Surge Chamber Cover Plan and Details - 3A-RH3501-034-04 Sht. 1 of 3 Metal forms.for Surge Chamber Cover RH3501-034-04 Sht. 2 of 3 Metal forms for Surge Chamber Cover Details RH3501-034-04 Sht. 3 of 3 Surge Chamber Cover Plan and Details - 4A j RH3501-034-06 Surge Chamber Cover Brick RW3501-035-01 Sht. 1 of 2 Spent Ion Exchanger Storage Rack Unit 1 j i

                                                                                              .i I

l l i 0409B/LC

                                                                                                                                                  .i l

SD 3527-005 Appendix No. 9 (Cont'd) 5.D.S. DRAHING LIST , DRAHING NO. TITLE RH3501-035-01 Sht. 2 of.2 Spent Ion Exchanger Storage Rack Unit 1 RH3501-035-02 Sht. 1 of 2 Moveable Spent Ion Exchanger Storage Rack RH3501-035-02 Sht. 2 of 2 Moveable Spent Ion Exchanger Storage Rack RH3501-035-03 Spent Ion Exchanger Storage Rack - Unit 3 RH3501-035-04a Spent Ion Exchanger Storage Rack - Unit 4a RH3501-035-04b Spent Ion Exchanger Storage Rack - Unit 4b RH3501-037-01 Sht. I of 2 Cask Support Platform RH3501-037-01 Sht. 2 of 2 Cask Support Platform

RW3501-038-01 Assembly and Details - Remote Disconnect for Hansen Coupler at Dewatering Station RH3501-038-01 Sht. 1 of 2 Plans and Details Dewatering Station RH3501-038-01 Sht. 2 of 2 Plans and Details Dewatering Station RH3501-038-02 Dewatering Station Remote Disconnect Guide and  !

Support RH3501-038-03 Dewatering Station and Ion Exchanger Station i Lanyards RH3501-038-04 Dewatering Station Structural Bracing Required for Rigging RH3501-038-05 Lead Shielding for Dewatering Station Piping RH3501-038B-29 Piping Arrangement Dewatering Station RH3501-038B-29-Al Dewatering Station Pipe Bending Details RH3501-0388-29-A2 Dewatering System Pipe Bending Details l 0409B/LC

                                                                         'SD 3527-005 Appendix No. 9 (Cont'd)'-

S.D.S.~ DRAWING LIST

     ' DRAWING NO.                 TITLE ~

RW3501-0388-29-A3 Dewatering Station' Pipe Bending Details RW3501-038B-29-01 . Dewatering Station-Ion Exchanger Vessels - Air /N2/. Emergency Demineralized Water Supply RW3501-0388-29-02 ~ Dewatering _ Station Air /N2/ Emergency. Demineralized Water-Inlet-RW3501-038B-29-03 Dewatering Station Filter Vessels Air /N2 / Emergency Demineralized Water Supply RW3501-038B-29-04. Dewatering Station Demineralized Water From Ion Exchanger Vessels to Off-Gas Separator RW3501-0388-29-05 Dewatering Station Filter Vessel Outlet

    'RW3501-0388-29-06            Dewatering Station Demineralized Water. Supply RW3501-038B-29-07            Dewatering Station Remote Discon.nect Tool Pipe Extensions RW3501-038B-29-08          ' Dewatering Station Remote Disconnect Tool Pipe Extensions RW3501-051-05 Sht. 1 of 3    Prefilter 125 Micron Assembly RW3501-051-05 Sht. 2 of 3    Prefilter 124. Micron, Filter Cylinder Details l

l RW3501-051-05 Sht. 3 Of 3 Prefilter 125 Micron, Head Details RW3501-051-06 Sht. 1 of 3 Final filter, 10 Micron-RW3501-051-06 Sht. 2 of 3 . final filter, 10 Micron,. Misc. Details RW3501-051-06 Sht. 3 of 3 Final Filter, Filter Subassembly and Misc. Details. RW3501-052-01 Sht. 1 of 3 Ion Exch' anger Assembly w/o Agitator RW3501-052-01 Sht. 2 of 3 Top Head Assembly and Details l

                                          - 27  .

0409B/LC

50 3527-005 Appendix No. 9 (Cont'd) S.O.S. DRANING LIST DRAWING NO. TITLE RW3501-052-01 Sht. 3 of.3 Bottom Skirt and Assembly RH3501-058-02 Shielding Cylinder.for Feed Pump Removal and for Gas. Pump Removal { RH3501-059-01 Personnel Crane Basket Assembly l

 ' RH3501-081-01               Valve Extension 1" Rising Stem Diaph. Valve                           '

RW3501-081-02 Valve Stem Extensions 1/2", 3/4", 1" and 1 1/2" ITT Grinnel Ball Vaives RW3501-081-03 Valve Stem Extensions 1/4"-Ball, 1/4" Needle and 3/8" Ball Whitey Series 43, 44 and IRS 4  ! Resp. 1 RW3501-081-04 Valve Stem Extension Pneumatic Operator ! RH3501-081-05 Valve Stem Extensions 1" ITT Grinnell Ball l Valves RH3501-081-06 Valve Stem Extensions 1" Rising Stem Diaph. l Valve j RH3501-082-02 Rack IIA Wirl'ng Diagram j l RW3501-082-02-02 Ion Exchanger Rack IIA Electrical (Instrumentation) Plan and Elevations  ! RH3501-082-03 Rack IA Wiring Diagram RH3501-082-03-01 Rack IA Elementary RW3501-082-03-02 Ion / Cation Exchanger Rack I Electrical l (Instrumentation) Plan and Elevations RW3501-082-04 Filter Manifold Hiring Diagram RW3501-982-04-01 Filter Manifold Elementary l l 0409B/LC 1

l 50 3527-005 Appendix No. 9 (Cont'd) S.D.S.' DRAWING LIST ] 1 ORAHING NO. TITLE RH3501-082-04-02 Filter Manifold. Electrical (Instrumentation) 1 Plan and Elevations- l RH3501-082-05 Exchanger Manifold Hiring Diagram Exchanger Manifold Elementary j RH3501-082-05-01 RH3501-082-05-02 Exchanger Manifold Electrical (Instrumentation) Plan and Elevations RH3501-082-07 Intermediate Level Sampling Glove Box RW3501-082-07-02 Intermediate Level Sample Glove Box.(Electrical Instrumentation) Plan and Elevations l RH3501-082-08 RCS Clean-Up Manifold Hiring Diagram' RH3501-082-08-01 RCS Clean-Up Manifold Elementary RH3501-082-08-02 RCS Manifold Electrical (Instrumentation) Plan and Elevation , RH3501-082-09 Hi-Rad Filter Glove Box Hiring Diagram RH3501-082-09-01 Hi-Rad Filter Glove Box Elementary RH3501-082-09-02 Hi-Rad Filter Sample Glove Box Electrical (Instrumentation) Plan and Elevations RH3501-082-10 Hi-Rad Feed Sample Glove Box Wiring Diagram RH3501-082-10-02 Hi-Rad Feed Sample Glove Box Electrical (Instrumentation) Plan and Elevations i 0409B/LC

, , r . 7 SD 3527-005 Appendix No. 9 (Cont'd)' S.D.S. DRAWING LIST DRAWING NO. TITLE t, RW3501-082-11 Beta Monitor Manifold Wiring Diagram RW3501-082-11-02 . Beta Monitoring Manifold-Electrical

                                       '(Instrumentation)' Plan andTElevations RW3501-082-11-03            ; Beta Monitor. Manifold Megohmmeter Readings RW3501-082-12                  Dewatering Station Wiring Diagram RW3501-084-01 Sht. 1.of 2-  . Shielded Pipe _ Chase. Assembly.527A-01-C' RW3501-084-01-Sht. 2 of 2      Shielded Pipt: Chase Details:

RW3501-IDX-01 Filter Manifold'Index-RW3501-IDX-02 Filter Rack Piping Index FSK-1743-3060' Off-Gas. Air Filtration System; Arrangement (MSA' Drawing)~ PI-35675 Mine Safety, Appliance Contactor Panel (Chromalox Dwg.) 106-057080-999 Duct Heater.(Chromalox Dwg.)~ 3475-E019 480V motor controlicenter aux, one.1'ine diagram 3475-E031

                                    .480V unit sub sta, one line' diag.

3475-E032 Misci PWR PNL schedules for' Submerged Demineralized System 3475-E119 fuel Handling Bldg. ele. 347'6" conduit plan-for SOS-(SH 1)' ' 3475-E125 FHB ele. 347.'6" conduit plan for SDS (SH 2) 3475-E796 Block diag. 480V USS 2-32< 3475-E798 Ext. conn, for 480V USS 2-32

                                             -                            0409B/LC

J

                                                     'SD 3527-005 Appendix No. 9 (Cont'd) 5.D.S. DRAWING LIST ll DRAHING NO. TITLE 3475-E799     Int, and ext, conn. for MCC 2-328 (section 5 rear)-

3475-E800 Int. conn. for USS 2-32 Unit.12 i 3475-E804 Block diag. mist. SDS 3475-E805 Block diag. misc. SDS 3475-E806 Block diag mise. SDS 3475-E807 Block diag. misc. SDS k i 3475-E808 Block diag, misc. SDS j I 3475-E809 Inter, and ext. conn. for 2-32B (section 1 front) j i 3475-E810 Conn. diag. for ann. PNL No. 1 \ 3475-E811 Conn. diag. Hi-Rad. Filter Sample Glove Box l 527-A-01 , i 3475-E812 Conn. diag. Hi-Rad Filter Sample Glove Box , 527-A-01 1 3475-E813 Conn. diag. Off-Gas Separator LVL inst. rack 3475-E814 Conn. diag, for Unit 3A of SDS 3475-E815 Conn. diag. for Unit IIA of SDS 3475-E816 Conn. diag. for Unit lA of SDS 3475-E817 Conn. diag for Filter Manifold of 505 l l l 0409B/LC

l SD 3527-005 Appendix No.19 (Cont'd) S.D.S. DRAHING LIST l DRAWING NO. TITLE 3475-E820 Conn. diag. for local starter CN 60 for leakage containment pump 527 GM-05 3475-E821 Conn. diag. for local starter CN 58 for Off-Gas Blower pump 527 GM-04 I 3475-E822 Conn. diag. for local starter CN 55 for Off-Gas ') Bottoms Pump 527 GM-02 q l 3475-E823 Conn. diag. Hi-Rad Feed Sample Glove Box 527-A-04 l l 1 3475-E824 Conn. diag. Ion Exchanger Manifold

                                                                   ~

3475-E825 Conn. diag. Int. Iv1. Sample Glove Box 527-A-03 3475-E826 Conn. diag.BetaMonitorManifold52h-A-02

3475-E827 Conn. diag. "Off-Gas HDR"' Term. Box CN 70 and 'i l PI/PSH/PSHH-527-18 and RE-527-18 3475-E828 Elem. diag. SDS 480V Feed Pump 527 GM-01 3475-E829 Elem. diag. SDS 480V Off-Gas Blower and Leak Cont. pump 3475-E830 Elem. diag. SDS Off-Gas Bottom pump 527 GM-02 3475-E831 Elem. diag. SDS 480V Off-Gas HTR 527-E-01 l 3475-E832 Conn. diag. HTR cont. PNL for Off-Gas HTR l 527-E-01 3475-E833 Conn. diag. rad. mon. PNL RMP.1 (Sh. 1 of 3) 3475-E834 Conn. diag. rad. mon. PNL RMP.1 (Sh. 2 of 3) 3475-E835 Conn. diag. rad, mon. PNL RMP.1 (Sh. 3 of 3) 1 3475-E836 Conn. diag. for RCS Clean-Up Manifold 0409B/LC

SD 3527-005 Appendix No. 9 (Cont'd) S.0.S. DRAWING LIST j DRAWING NO. TITLE 3475-E837 Block diag. misc. SDS 3475-E838 Conn. diag. dewatering station

                                                                               )

3475-E839 Elem.. diag. Rad. Monitor PNL RMP-1 control and I alarm 3475-E840 Conn. diag. for RE-527-ll, 12 and 13 and i RAH-527-ll 3475-E852 Elem. diag. R.B. Haste Pump WG-P-1 3 1 3475-E853 Elem. diag. sol . valve AV-01, AV-02 and SV-13 3475-E886 Block diag. SDS misc. Rad. Monitor i Conn. diag. Filter Containment. Rad. det. inst. 3475-E887 rack 3475-E892 Int. and ext. conn. for LCL cont. PNL WMG 149 3475-E893 Elem. diag. alarms - cont. PNL CN-PNL-1 ] 1 3475-E894 Int. and ext. conn, for cont. PNL CN-Pt'L-1 (Sh. I i 1 of 2) l 1 3475-E895 Int. and ext. conn. for cont. PNL CN-PNL-1 (Sh. 2 of 2) 3475-E903 Conn. diag. for hoist 527-T-04 3475-BM-E819 Bill of material for local starter CN 52 3475-BM-E820 Bill cf material for local starter CN 60 3475-BM-E821 Bill of material for local starter CN 58 l A 1 0409B/LC

1 l SD 3527-005. l Appendix No.- 9 (Cont'd) S.0.S. DRAWING LIST DRAWING NO. TITLE l 3475-BM-E822 Bill of material for local starter CN 55 2-M74-SDS01 Piping and Instrument Diagram, SDS Feed and Monitor Tank System i 2-M74-DWO1 Piping and Instrument Diagram, Demineralized ] Service Water l 1 2-M74-DHCO3 Piping and Instrument Diagram, DWC Auxiliary Systems j 2-M74-PW01 Piping and Instrument Diagram, Processed Water Storage and Recycle System.- 2-P0A-6201 . General Arrangement, SDS Monitor Tanks,' Fuel Handling Building, El. 305'0" 2-C0C-6201 FHB, E1. 305'0", SDS Equipment, Foundations and Misc. Support Steel ]; 2-COR-6201 FHB, El. 305'0", SDS Equipment, Foundations Reinforcing Details 2-C21-008 Civil Structural Standards, Anchor Bolt 1 Schedule and Details 2-C8R-6201 FHB, SDS Equipment Foundations Reinforcing Bar List 2-E21-005 One Line Diagram SDS Admin. Building 2-E38-DHC01 Connection Diagram, DHC-STR-1 & Terminal Box 2-E38-DWC02 Connection Diagram, DHC-HS-1266 & DHC-HS-1. i 2-E38-RC02 Connection Diagram, RC-LCPI 2-E38-SDS01 Connection Diagram, Local Control Panel SDS-LCP1 1 2-E38-SD502- Connection Diagram, Local Control Panel SDS-LCP2 2-E38-SDS03 Connection Diagram, SDS Monitor. Tank Transfer Pump Local Starters 2-E38-SDSO4 Connection Diagram, SDS Misc. Devices 2-E38-SDS05 Connection Diagram, SDS Misc. Term Boxes l 2-E76-DHC01 DWC Pump i 0409B/LC I l I ____,__._---_-__m_m---

I SD 3527-005 4 Appendix No. 9 (Cont'd) S.D.S. DRAWING LIST { l DRAWING R NO. TITLE

                                                                                                                      'l 2-E76-DHC02              Isolating Valve WDL-V40
                                                                                                                      ]

2-E76-DWC03 IIF Level Alarms j 2-E76-SDS01 Schematic Diagram, SDS Monitoring Tank Transfer I Pump (PIA) 1 2-E76-SD502 Schematic Diagram, SDS Monitoring Tank Transfer j Pump (PlB) i I 2-E76-SD503 Schematic Diagram, SDS Monitor Tank Inlet Valves j 2-E76-SDSO4 Schematic Diagram, SDS Misc. Instrumentation and Alarms  ; i 2-E76-SDS05 Schematic Diagram, SDS Misc. Instrumentation f and Alarms J I 2-E80-SDS01 Bill of Materials, Local Control Panel, I SDS-LCP-1 1 2-E80-SD502 Bill of Materials, Local Control Panel, l SDS-LCP-2 1 2-E81-DWC-01 DHC Pull Slips 2-E81-RC-02 RCS water level monitoring pull slips I i 2-E81-SD501 SDS Pull Slips i i 2-J23-001 Instrument Piping Class Specification 2-J25-002 Installation Details 2-J25-003 Installation Details l 2-J25-005 Installation Details < 2-J25-007 Installation Details 2-J25-Oll, Sht. 1 Installation Details, Reactor / Refueling Canal Water Level Monitoring System 2-J25-013 Installation Details, IIF Water Level Monitoring System 2-J71-SD501 Instrument Rack Layout, Instrument Rack SDS-R-1 l 2-J71-SDS02 Instrument Rack Layout, Instrument Rack SDS-R-2 0409B/LC

 ..                _-             - - _ _ -                         _                  _---____..---_.___-__________a

SD 3527-005 { Appendix'No. 9.(Cont'd) S.D.S. DRAWING LIST DRAWING NO. TITLE 2-J73-SD501 Panel-Drawing, SDS feed and Monitor Tank, Panel SDS-LCP-1 2-J73-50502 Panel Drawing, SDS feed and Monitor Tank, Panel SDS-LCP-2 2-J73-5D5-03 Panel Drawing, SDS Control Panel-CN-PNL-1 2-J74-SD501 Instrument Installation Detail, SDS Monitor Tank Transfer Pump P-1A Discharge 2-J74-5D502 Instrument Installation Detail, SDS Monitor Tank Transfer Pump P-1B Discharge 2-J74-SDS03 Instrument Installation Detail, SDS Monitor Tank T-1A 2-J74-SDSO4 Instrument Installation Detail, SDS Monitor Tank T-1B 2-J75-RCO2 Loop Diagram, RC System Water Level Montoring System 2-J75-SD501 Loop Diagram, SDS Monitor Tank T-1A Level 2-J75-SDS02 Loop Diagram, SDS Monitor Tank T-18 Level 2-J75-SD503 Loop Diagram, SDS Monitor Tank, P-1A Discharge 2-J75-SDSO4 Loop Diagram, SDS Monitor Tank, P-1B Discharge 2-J75-SD505 Loop Diagram, SDS Monitor Tank T-1A Low Level , Trip  ! 2-375-SD506 Loop Diagram, SDS Monitor Tank T-1B Low Level Trip l 2-J77-SD501 Logic Diagram, SDS Feed and Monitor Tank . Transfer Pumps I 2-J77-SD502 Logic Diagram, SDS feed and Monitor Tank Inlet  : Valves 2-J77-SD503 Logic Diagram, SDS Feed and Monitor Tank Alarms  ; 2-J78-SDS01 Level Setting Diagram, SDS Monitor Tank, T-1A-2-J78-SD502 Level Setting Diagram, SDS Monitor Tank, T-1B 0409B/LC

SD 3527-005' .j Appendix No. 9 (Cont'd) S.D.S. DRAWING LIST 4 q DRAWillG NO. TITLE l 2-P0H-001 HVAC, Partial Plans 2-P15-001 Wall and Floor Penetration Schedule- l 2-P15-002 Wall and floor Penetration Schedule 2-P60-DWOI Piping Isometric, Demineralized Water System, # FHB, Unit 1/ Unit 2 Corridor 2-P60-SD501 Piping Isometric, SDS, Aux and fuel Handling Building 2-P60-SDS02 Piping Isometric, SDS-, Aux and fuel Handling Building 2-P60-SDS03 Piping Isometric, SDS, Aux and Fuel Handling Building 2-P64-DW01 Hanger Details, Demineralized Water System, FHB, Unit 1/ Unit 2 Corridor I 2-P64-SD501 Hanger Details, SDS feed and Monitor Tank System, Aux and fuel Handling Bldg. 2-P64-SD502 Hanger Details, SDS Feed and Monitor Tank System, Aux and fuel Handling Bldg.  ! 2-P64-SD503 Hanger Detal?s SDS Feed and Monitor Tank l System, Aux and fuel Handling Bldg. 2-E21-SDS01 SDS-One Line Diagram 2-M100A-00001-01 Two 12,000 Gallon, 96" 0.D. x 32'0", Straight Shell Water Storage Tanks, Buffalo Tank 2-EOR-6201 Grounding and Raceway, Submerged Demineralized System  ;

                                                                                                           \

JSOB2080 SDS Graphic Display 2D-950-29-001 Sht. I of 2 SDS Demineralized Liner 20-950-29-001 Sht. 2 of 2 SDS Demineralized Liner i 2D-950-29-002 SDS Spray Header Assembly 2E-950-02-001 SDS Plan View 0409B/LC l i _ _ _ _ _ _ _ . . - _ _ __ ___ _ _ . - - _ o

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SD 3527-.005

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95,0;-29-003 l Sht, 1 of) 3,'" SDS Prt. filter 125 Micron s s emb'ly _ c t _

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                                                                                                                              #o                                                                                 'l 20450 C9-003' Sht s Vof. 3                                                              SDS Pr(filter 125 Micron Filter Cylinder Details                                                      1 2b950-25-004       j p y 5 4 1 ofL3             y                                                   ,
                                                                                                                                                                                                                 -i a          505 Finh1 Filter 10 Microns dL
                    ' 2D-95tA29-004 EhtI2 of 3,                                                          ~ SDS Final filter 10 Microns Misc.' Details-s t -.s        ;       3-
                    ~ 2D-950-29-004 Sht. 3 of 3                                                            ~SDS Final ~ Filter 10 Microns Filter Sub-Assembly I
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                       ;c450-29-005 Sht;Iof2                                                               ..SDS Plug                       e
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a;2C. 50-29-005 Sht. 2 of.? 'SDS. Plug, Tool n 2C$50-29-006 a /s ' GDS Vent ' Hose Retainer Clip j 2B-950-29007

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i. MJ-950-29-008 A m SDS Ion Exchanger Off-Gas System Connection A S n , 'j . ! Options 1

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2D-950-294009.,;SM.)1of2 SD5' Exchanger Lifting 1 Yoke Replacement' Assembly 2D-950-29-0W Sht. 2 cf 2 SDS Exchanger Lifting Yoke Details

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2D-950'29-010l5ht,l..bNA. SDS_ Unspent Exchanger Lifting Yoke' Replacement-4,\ /, Assembly { Sh%UnspentExchar.geYLiftingYokeDetails 2D-950-29-OlbShO2of?.fj t-y( / as -

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2p-950-29211Sht)1of)((g.. ? changer Retrieval Tool' Assembly

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20-950-11-001 ' "' ~ , Eump Sucker P .wd ID Surface Water Suction feed

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                  "2C-950-21-002                                                                             SDQPandID. Bet 0konitoringManifold
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SD 3527-005 , l EH N i i DRAWING NC. TITLE l i 2-M75-DHC04 Schematic Diagram - Interim Fuel Transfer Canal Processing System 2-P70-DHC01 Piping Composite - Defueling Water Cleanup System - Reactor ~ Building' { i 2-J77-DHC01 Logic Diagram - IIF Fill Isolation Valve WDL-V40 l 2-J77-DHCO2 Logic Diagram - IIF Processing Pump DHC-P-1 Logic Diagram - IIF Level Alarm j 2-J77-DHCO3

                                                                                                  .l 2-377-DWC04               Logic Diagram - IIF Misc. Alarms 2-J78-DHC01 Level Setting Diagram, Internals Indexing Fixture 2-P70-FCCO2 Reactor Building Sump and Fuel Transfer Canal Draining Network 2-J77-FCC01               Logic Diagram - Fuel Transfer Canal Surface                ,

Suction Pump (FCC-P-1) 2-COP-1306 Reactor Building IIF Platform Plans, Sections,  ! Details j 11127718C (B&W) Hiring Diagram - Water Level Sensing System I 1 1 l i l 04098/LC

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                                     -SD 3527-00S 1

1

                                                  -l Appendix No. 10 to Submerged Demineralized System                i System Design Description l

l Title S.D.S Valve List

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