ML17226A146
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RBS USAR TABLE 9.1-1 TOOLS AND SERVICING EQUIPMENT Revision 16 1 of 1 March 2003 Fuel Servicing Equipment In-Vessel Servicing Equipment165Channel handling boom Control rod grapple Fuel preparation machines Control rod guide tube grapple New fuel inspection stand Fuel support grapple Channel bolt wrenches Grid guide Channel handling tool Control rod latch tool Fuel pool sipper Control rod guide tube seal Fuel transfer system Incore guide tube seal Channel gauging fixture Blade guides General purpose grapples Fuel bundle sampler
Fuel handling platform Blade guide rack with 2 blade Refueling Equipment guides Refueling platform 5 Auxiliary and vessel platform Servicing Aids Portable radiation shield 16Pool tool accessories Actuating poles Storage EquipmentGeneral area underwater lights Local area underwater lights Spent fuel storage racks Drop lights Channel storage racks Underwater TV monitoring Control rod storage racks system Defective fuel storage Underwater vacuum cleaner containers Viewing aids In-vessel racks Light support brackets Defective fuel storage racks Underwater viewing tube New fuel storage racks Reactor Vessel Servicing Under-Reactor Vessel Servicing Equipment EquipmentReactor vessel servicing tools Control rod drive servicing Steam line plugs and tools installation tools CRD hydraulic system tools Shroud head bolt wrenches Water seal cap Head holding pedestals Control rod drive handling Head stud rack equipment Dryer-Separator Strongback Equipment handling platform Head Strongback/Carousel Thermal sleeve installation (incl. stud tensioners) tool Incore flange seal test plug Key bender RBS USAR___________________________________
(1) NE - Nonessential PE - Passive essential Revision 21 1 of 1 Table 9.1-2 FUEL SERVICING EQUIPMENT Component Identification Essential Classification (1)Safety Classification Seismic Category6 Fuel prep machine PE NNS II 6New fuel inspection stand PE 2 I Channel bolt wrench NE NNS NA Channel handling tool NE NNS NA Fuel pool sipper NE NNS NA Channel gauging
fixture NE NNS NA General purpose
grapple PE UNC I10 Jib crane 10PE 2 I Channel handling
boom NE NNS NA5 Blade guide rack
with two blade
guides NE NNS NA 5 RBSUSAR1of2August1987TABLE9.1-3FUELTRANSFERSYSTEMCOMPONENTSEssentialSafety ComponentClassifi-Classifi-SeismicNo.Identification cation (1)cation Category1Winch NE NNS NA2HydraulicpowerNENNSNA supply3FluidstopNENNSNA4VentpipeNENNSNA 5CableenclosuresNENNSNA 6Tophoriz.guideNENNSNA arms7UpperpoolupenderNENNSNA 8TrunnionboxNENNSNA 9HydrauliccylinderNENNSNA 10UpperpoolframingNENNSNA 11SheaveboxcoverNENNSNA 12HydrauliccylinderNENNSNA 13FillvalveNENNSNA 14SheaveboxNENNSNA 15SheavepipeNENNSI 16HydrauliccylinderNENNSNA 17ManualgatevalveNENNSI 18ContainmentisolationPE2I 19ContainmentbellowsPE2I 20TransfertubeNE/PENNS/2I 21HydraulicpowerNENNSNA supply22Mid-supportNENNSI 23Wirerope(cables)NENNSNA 24CarriageNENNSNA 24ATilttubeNENNSNA 24BFollowerNENNSNA 25GatevalveNENNSI 26BellowsNENNSNA 27DrainvalveNENNSNA 28HorizontalguideNENNSNA arms RBSUSAR (1)NE-NonessentialPE-Passiveessential2of2August1987TABLE9.1-3(Cont)FUELTRANSFERSYSTEMCOMPONENTSEssentialSafety ComponentClassifi-Classifi-SeismicNo.Identification cation (1)cation Category29Valvesupport NE NNS I structure30LowerpoolframingNE NNS NA31LowerpoolupenderNENNSNA32PivotarmframingNENNSNAcontrolsystem RBSUSARTABLE9.1-4REACTORVESSELSERVICINGEQUIPMENT1of1August1987EssentialSafety ComponentClassifi-Classifi-Seismic Identification cation (1)cation CategoryReactorvesselserv.toolsNE NNS NASteamlineplugs NE UNC NAShroudheadboltwrenchNE NNS NAHeadholdingpedestal PE NNS IHeadstudrack NE NNS NADryerandseparator PE 2 I (2)strongbackHeadstrongbackcarouselPE 2 I_______________________________
(1)NE-NonessentialPE-Passiveessential (2)Dynamicanalysismethodsforseismicloadingarenotapplicable, asthisequipmentissupportedbythereactorbuildingpolar crane.Liftingdeviceshavebeendesignedwithaminimumsafety factorof5andundergoprooftesting.
RBS USAR Revision 23 1 of 2 TABLE 9.1-5 DESIGN PARAMETERS OF FUEL POOL COOLING AND PURIFICATION SUBSYSTEMS
Cooling Subsystem 14 8A 8 Fuel Building Fuel Storage Pool Max Normal Temp 139.8 F Max Abnormal Temp 1 (Full Core Off Load) 155.6 F Max Abnormal Temp 1 (Temporary Loss of Cooling) 170.0 F 14 Containment Fuel Storage Pool Max Normal Temp (0.32 cores) 126.9 F Max Abnormal Temp (0.32 cores) 134.6 F (Temporary Loss of Cooling) 170.0 F 8 8A Cooling Water Temperature RPCCW 105 F (maximum)
SSW 95 F (maximum)
Pump Capacity 2 @ 100% Type Horizontal Centrifugal
2,500 gpm Design Flow 87.6 ft HO Design Total Head 87.6 ft Shell Side Tube Side Cooler Fluid RPCCW Fuel Pool Water Flow 1,000,000 lb/hr 1,250,000 lb/hr Design Pressure 150 psig 150 psig Normal Heat Load 2,3 17.07 x 10 6 Btu/hr Temp, in 105.0 F 140.0 F Temp, out 122.1 F 126.3 F Abnormal Heat Load 3 28.63 x 10 6 Btu/hr Temp, in 105.0 F 163.3 F Temp, out 133.7 F 140.5 F 11 8A 8A 11 RBS USAR Revision 23 2 of 2 TABLE 9.1-5 (cont)
Purification Subsystem
Demineralizer Flow 300 gpm Filter Flow 600 gpm (each) Filter Design Maximum Particle Size 6 microns
Pumps Capacity 2 @ 50% Type Horizontal Centrifugal Design Flow 600 gpm (each) Design Total Head 260 ft HO Pool Water Quality Conductivity
= 3 umho/cm @ 25 C Chloride = 0.5 ppm pH 5.3 to 7.5 @ 25 C Heavy Elements
< 0.1 ppm (Fe, Cu, Hg, Ni)
Total Insolubles
< 1 ppm
_____________________________
1 Design Limits 2 Heat loads shown are for the fuel building fuel storage pool only. These values are the limiting case numbers for the fuel
storage pools.
3 These values calculated using SRP 9.1.3 method. Offload rate to the fuel building fuel storage pool is constrained to ensure the temperature design limit is maintained.
KEY: RPCCW - Reactor Plant Component Cooling Water SSW - Standby Service Water RBS USAR Table 9.1-6 FUEL DISCHARGE HEAT LOAD FOR NORMAL OPERATION (24-MONTH REFUELING CYCLE)
Revision 23 1 of 1 14 Discharge Number Number of Fuel Assemblies Decay Time (days) 1 260 400 2 260 365 3 260 150 hours0.00174 days <br />0.0417 hours <br />2.480159e-4 weeks <br />5.7075e-5 months <br /> 14 RBSUSARRevision151of2May2002TABLE9.1-715LIGHTLOADSOVERTHESPENTFUELPOOLFUELBUILDING 15Distance(ft)
Kinetic Item Above Pool Surface Total Above Rack Dry Weight (lb)Energyat Impact (2)(topofrack)(ft-lb)Channelboltwrench 4 31 15 465Channelhandlingtool11.5 (1)38.5 (1)25 963Channelgaugingfixture 17.8 (1)210 3738Generalpurposegrapple3.6 (1)30.6 (1)45 1377Actuatingpole 4 31 61 1891Droplight 4 31 25 775Localareaunderwater
light 4 31 35 1085Viewingaid 27 13 351Controlrod 12 (1)218 2616Handrail,removable 4 31 122 3782UnderwaterTVcamera 4 31 50 15501Defect.fuelcontainerwithfuelassembly5.4617(4)3332Fuelchannel 24 (1)99 237615Dummyfuelassembly 5.79 (9)617 (4)3573 (3)Fuelbundle 5.79 (9)580 (4)3358 (3)2Fuelbundleandchannel 5.79 (9)664 (4)3752 (3)(5)NewFuelBundleand Channel (6)51.7 (7)744 27680 210MiscellaneousLight Loads (8)36.831200 (8)44200 (8)15101 RBSUSAR TABLE 9.1-7 (CONT)Revision152of2May20021 (1)Distancefromcenterofgravitytotopoffuelstoragerackandpool surface.(2)Kineticenergycalculatedwithoutcredittakenforbuoyancyanddrag forconservation,exceptfordefectivefuelcontainerandspentfuel
assembly.(3)SeeUSARSection15.7.4forfuelassemblyfuelhandlingaccident.
Kineticenergyvaluesdifferbecauseofrounding-offoffactors.
(4)Creditwastakenforbuoyancy.2 (5)Creditwastakenforfluiddragforces.
1(6)Nocredittakenforbuoyancyorfluiddragforces.Thetopofafuel channelornewfuelbundlealone,isboundedbytheanalyzeddropof anewfuelbundleandchannel.15(7)Distancefromtopofnewfuelbundletouppertieplateofspentfuelstoredinspentfuelracks.Foractualenergyimpactcalculation,avalueof37.2ftisusedwhichisconservativetotheheightspecified(442in,36.83ft)whichrepresentsthedistancefromthe bottomofanewfuelbundletotheuppertieplateoffuelstoredinthespentfuelrack.
15210 (8)Miscellaneouslightloadshavebeengenericallyboundedbyevaluation.Specificweightversusheightcriteriahasbeenanalyticallydevelopedtoensurethatconsequencesareboundedbyregulatorylimits.
1015(9)Distancefrombottomofnewfuelbundletotopofspentfuelrack.
RBSUSARRevision51of2August1992TABLE9.1-8LIGHTLOADSOVERTHEUPPERCONTAINMENTPOOL TotalDistanceDistanceKineticEnergyAboveAboveDry (2)atImpact (2)HWLRack (1)Weight(topofrack)
Item(ft-in)(ft-in)(lb)(ft-lb)Channelboltwrench16-241-9 15 626Channelgauging fixture 0 15-7 210 3272Generalpurpose
grapple1-827-3 45 1226Utilitymanipulator19-845-3 45 2036Actuatingpole 0 15-0 61 9155Fuelbundlesampler0 12-0 600 7200 5Droplight4-229-9 25 7441Spentfuelassembly0 5-10 664 3220 1Viewingaids 0 25-7 13 333Lightsupportbracket4-229-9 110 3273Channelhandlingtool12-237-9 25 944Underwaterviewing tube4-229-9 20 595Fuelsupportgrapple19-244-9 147 6578Peripheralfuelsupportplug20-245-9 16 732Controltubegrapple16-241-9 45 1879 RBSUSARRevision102of2April1998TABLE9.1-8(Cont)LIGHTLOADSOVERTHEUPPERCONTAINMENTPOOL1 TotalDistanceDistanceKineticEnergyAboveAboveDry (2)atImpact (2)HWLRack (1)Weight(topofrack)
Item(ft-in)(ft-in)(lb)(ft-lb) 1Controlrodlatch tool 0 21-9 74 1610Bladeguide 0 21-9 180 3915Gridguide 0 21-9 32 696Removablehandrails2-227-9 122 3386Magneticretriever4-229-9 2 605Bladeguiderackwithtwobladeguides09-113/4400 3992 510MiscellaneousLight Loads (3)(3)1200 (3)(3)10________________________
(1)Alldistancesaremeasuredfromthecenterofgravityofthe droppedobjecttothetopoftherack.
(2)Forconservatism,allkineticenergiesarecalculatedwithout credittakenforbuoyancyanddragforcesforthedistance travelledthroughwater.Thekineticenergiesaretherefore calculatedasiftheentiredropoccursthroughaironly.
(Buoyancyeffectswereconsideredforthespentfuelassembly.)10 (3)Miscellaneouslightloadshavebeengenericallyboundedby evaluation.Specificweightversusheightcriteriahasbeen analyticallydevelopedtoensurethatconsequencesareboundedby regulatorylimits.
10 RBSUSAR1of2August1988TABLE9.1-9LIGHTLOADSOVERTHEREACTORVESSELCORE(DURINGREFUELING,VESSELHEADOFF)1 TotalDistanceDistance (2)KineticEnergyAboveAboveDryatImpact (2)HWLCore (1)Weight(topofrack)Item(ft-in)(ft-in)(lb)(ft-lb)1Generalpurpose17-271-745 3221 grappleUtilitymanipulator20-274-745 3356 grapple Fuelbundle040-10600 24500 sampler Clamshellretriever3-057-525 1435Peripheralfuel20-274-716 1193supportplug Droplight20-274-725 1865UnderwaterTV18-873-125 1827Viewingaid054-513 7071Spentfuelassembly034-0664 22576 1Fuelsupportgrapple19-273-7147 10817Peripheraloffice17-271-745 3221 grappleCRDguidetubeseal20-274-760 4475In-coreguidetube052-756 2945 seal Peripheralorifice20-274-7130 9696 holder Bladeguide052-1180 9375 RBSUSARTABLE9.1-9(Cont)Revision72of2January19951 TotalDistanceDistance (2)KineticEnergyAboveAboveDryatImpact (2)HWLCore (1)Weight(topofrack)
Item (ft-in)(ft-in)(lb)(ft-lb)1Fuelbailcleaner15-069-5100 6917Gridguide051-532 1645Fuelgrapple9-263-745028613Controlrodgrapple19-273-717 1251CRDguidetube19-874-135 2593 grappleStudhandlingtool17-271-7135 9664RPVstud18-272-7500362927Shroudheadbolt18-272-742030486 wrench 7Steamlineplug13-267-772 4866installationtoolLocalareaunder-20-274-735 2610waterlight Generalarealight20-274-750 3729Steamlineplug19-273-737527594Headstudrack18-272-720014517 (empty)Magneticretriever5-059-52 1191 In-vessel31-283-8405 33882controlrodstoragerack (empty)1 RBSUSARTABLE9.1-9(Cont)2aof2August19881 TotalDistanceDistance (2)KineticEnergyAboveAboveDryatImpact (2)HWLCore (1)Weight(topofrack)
Item (ft-in)(ft-in)(lb)(ft-lb)1In-vessel032-11623 20506controlrodstoragerack (loadedwithacontrolrod)(1)Alldistancesaremeasuredfromthecenterofgravityofthedroppedobjecttothetopofthecore.(2)Forconservatism,allkineticenergiesarecalculatedwithoutcredittakenforbuoyancyanddragforces,forthedistancetraveledthroughwater.Thekineticenergiesare thereforecalculatedasiftheentiredropoccursthrough aironly.(Buoyancyeffectswereconsideredforthespent fuelassembly.)
1 RBS USAR TABLE 9.2-1 NORMAL SERVICE WATER SYSTEM MAJOR COMPONENT DESIGN DATA Total Operating Design Data Quantity Heat Load for Each Operating/
(Btu/hr Component Description Available x 10 6) (gpm) Revision 16 1 of 3 March 2003 Normal Service Water Pumps 2/3 - 31,500 (1) (approx) 14 12TPCCW Heat Exchangers 2/3 26.28 9,250 Turbine Building Air-Condi- 2/3 38.70 4,000 tioning Water Chillers 9RHR Heat Exchangers 0/4 0.00 (2) 5,800 (5)9RPCCW Heat Exchangers 2/3 48.65 5,000 10 SPC Heat Exchangers 1/1 60 (6) 2,500 1016157Drywell Unit Coolers 5/6 13.4 334 7 15 163Control Building Air-Condi- 2/4 5.70 630 tioning Water Chillers 3Lube Oil Coolers 1/2 0.14 1,200 Hydrogen Coolers 4/4 23.44 916 Alternator Cooler 1/1 0.42 240 Standby Diesel Generator 0/2 0.00 (2) 700 Jacket Water Coolers 2HPCS Diesel Generator 0/1 0.00 (2) 800 Jacket Water Cooler 2 12Turbine EHC Coolers 1/2 0.14 50 Fuel/Radwaste Building 2/3 12.90 1,200 Chilled Water Chillers 14Steam Bypass Hydraulic 1/2 0.00 40 Power Units RBS USAR TABLE 9.2-1 (Cont) NORMAL SERVICE WATER SYSTEM MAJOR COMPONENT DESIGN DATA Total Operating Design Data Quantity Heat Load for Each Operating/
(Btu/hr Component Description Available x 10 6) (gpm) Revision 16 2 of 3 March 2003 Auxiliary Building Unit Coolers 16 14RWCU Pump and Heat 1/1 0.187 50 Exchanger Room Unit Cooler 12 RPCCW Pump and Heat 1/1 0.318 100 Exchanger Area Unit Cooler El 114' Area Unit Cooler 1/1 0.293 90 HPCS Pump Room Unit Cooler 1/1 0.722 185 Switchgear, LPCS Pump, and 1/1 0.928 235 RHR Pump A Area Unit Cooler Switchgear Room and Electric 1/1 0.486 150 Terminal Boxes Unit Cooler Main Steam Pipe Tunnel, 1/1 0.405 120 North End, Unit Cooler RHR Heat Exchanger, RHR 1/1 0.692 210 Pumps B and C, and RCIC Pump Area Unit Cooler El 95'-9" HPCS Hatch and 1/1 0.118 37 Elevator Area Unit Cooler Upper Auxiliary Building 2/1 1.012 410 Levels Unit Coolers 12 16Annulus Ventilation 2/2 0.0002 9 Radiation Monitors RHR Heat Exchanger 2/2 0.00 (3) 9 Radiation Monitors 14 RBS USAR TABLE 9.2-1 (Cont) NORMAL SERVICE WATER SYSTEM MAJOR COMPONENT DESIGN DATA Total Operating Design Data Quantity Heat Load for Each Operating/
(Btu/hr Component Description Available x 10 6) (gpm) Revision 14 3 of 3 September 2001 14 Steam Jet Air Ejector 1/2 0.78 131 Intercoolers Turbine Building Sample 1/1 0.22 60 Room Chiller Condensing Unit 146Normal Service Water 7/8 164/444 (4) 9,000 Plate/Frame Heat Exchangers 6____________________________
(1)This number represents 50 percent capacity at 211 ft total head (2)Does not operate during normal plant operation.
(3)Does not have a heat load until RHR heat exchangers operate. 14 6 (4)Normal heat load is 164 Btu/hr x 10 6, while design peak heat load is 444 Btu/hr x 10 6.6 1412 9 9 1210 (6) This number represents design heat load when providing Alternate Decay Heat Removal. Heat load during normal plant operation is negligible.
10 RBSUSAR1of1August1987TABLE9.2-2 REACTORPLANT COMPONENTCOOLINGWATERSYSTEMCOMPONENTDESCRIPTIONRPCCWPumps(1CCP-P1A,P1B,P1C)
Quantity 3Type Horizontal,centrifugalCapacity,each,gpm(%)3,000(50)TDH,ft 177Driver,hp 200RPCCWHeatExchangers(1CCP-E1A,E1B,E1C)
Quantity 3Type TEMA-CEN Duty,each,Btu/hr25.0x10 6ShellSide:
FluidDemineralizedcoolingwaterNo.ofpasses 1Flowrate,gpm2,337(50%capacity)Temperaturein/out,°F 126°/105TubeSide: FluidServicewaterNo.ofpasses 1Flowrate,gpm5,022(50%capacity)Temperaturein/out,°F 95/105RPCCWSurgeTank(1CCP-TK1)Capacity,gal 2,300Designpressure,psig 150Designtemperature,°F 150 RBS USAR TABLE 9.2-3 REACTOR PLANT COMPONENT COOLING WATER SYSTEM MAJOR COMPONENT DESIGN DATA
_________________________
(1) One fuel pool heat exchanger in operation at any one time.
(2) Supplied with RPCCW following a LOCA if adequate RPCCW pressure is
available.
(3) Supplied with SSW following a LOCA if adequate RPCCW pressure is not available.
Revision 14 1 of 1 September 2001 Description Quantity Operation Design Data/Each
Component (gpm) Total Heat Exchange Rate
@ 105 o F Inlet Temp. (10 Btu/h) 14 Fuel pool heat
exchangers (1) 14 (1SFC*E1A, E1B) 2 Normal/
Accident (2,3) 2,000 16.62/24.68 Control rod drive pump
lube oil cooler (1C11-
PC001A, PC001B) 2 Normal (2) 15 0.05 RHR pump seal coolers
(1ETZ*PC002A, PC002B) 2 Normal/
Accident (2,3) 20 0.20 8 Reactor water cleanup
pumps seal coolers
(1G33-PC001A,PC001B) 2 Normal/
Abnormal (2) 25 0.36 8 Reactor water cleanup
non-regenerative HX
(1G33-EB002A, EB002B) 2 Normal 627 14.0 Drywell equipment drain
sump cooler (1DER-E1) 1 Normal 45 1.01 Reactor plant sample
station (1G33-PNLZ020) 1 Normal 25 0.01 Reactor recirculation
pump seal, bearing and
winding coolers
(1G33*PC001A, PC001B) 2 Normal 252 2.5
RBS USAR Revision 14 1 of 1 September 2001 TABLE 9.2-4 DECAY HEAT RATES DUE TO FISSION PRODUCTS AND HEAVY ELEMENTS FOLLOWING A DBA 14 Time (min/hr/days)
Time (sec)
Combined Decay Heat Rate (x 10 6 Btu/hr) 10 1 x 10 1 522.35 50 5 x 10 1 364.61 100 1 x 10 2 353.63 200 2 x 10 2 309.40 500 sec 5 x 10 2 260.81 1000 sec 1 x 10 3 222.28 30.0 min 1.8 x 10 3 188.77 1 hr 3.6 x 10 3 153.77 1.5 hr 5.4 x 10 3 134.60 2.0 7.2 x 10 3 123.54 2.5 9.0 x 10 3 116.17 3.0 1.08 x 10 4 110.97 4.0 1.44 x 10 4 102.69 5.0 1.80 x 10 4 97.05 6.0 2.16 x 10 4 93.01 8.0 2.88 x 10 4 87.65 10.0 3.60 x 10 4 82.29 12.0 4.32 x 10 4 78.04 16.0 5.76 x 10 4 72.33 20.0 7.20 x 10 4 68.16 24.0 8.64 x 10 4 64.56 2 days 1.73 x 10 5 52.73 3 2.59 x 10 5 46.07 4 3.46 x 10 5 41.62 5 4.32 x 10 5 38.31 6 5.18 x 10 5 35.91 7 6.05 x 10 5 33.56 8 6.91 x 10 5 31.93 9 7.78 x 10 5 30.30 10 8.64 x 10 5 28.98 15 1.29 x 10 6 24.78 20 1.73 x 10 6 21.70 25 2.16 x 10 6 19.83 30 2.59 x 10 6 18.18 14 RBS USAR Revision 24 1 of 1 TABLE 9.2-5 14 DECAY HEAT REJECTION* AND CONTAINMENT UNIT COOLER HEAT LOAD TO STANDBY SERVICE WATER FOLLOWING A LARGE BREAK OF A MAIN STEAM LINE DBA-MSL 12 12 (HEAT Removal Rates: Btu/Hr)
Time After Shutdown Time(sec) RHR HVR Total Pump Adjustment Adjusted Total Integral Heat load (BTU) 0.00 hr 0.00E+00 0.000E+000.000E+000.000E+00 0.000E+000.000E+000.000E+0010.00 min 6.00E+02 0.000E+00 0.000E+00 0.000E+00 1.071E+07 -1.071E+07 1.79E+06 0.50 hr 1.80E+03 7.960E+07-7.809E+047.952E+07 1.132E+076.819E+07 5.56E+061 hr 3.60E+03 9.114E+07-1.996E+049.112E+07 8.142E+068.297E+079.63E+061.5 hr 5.40E+03 9.460E+07-1.076E+049.459E+07 8.142E+068.645E+071.37E+072 hr 7.20E+03 9.799E+076.315E+039.799E+07 8.142E+068.985E+071.78E+072.5 hr 9.00E+03 1.011E+081.150E+041.011E+08 8.142E+069.294E+072.18E+073 hr 1.08E+04 1.033E+082.653E+041.034E+08 8.142E+069.522E+072.59E+074 hr 1.44E+04 1.061E+084.983E+041.061E+08 8.142E+069.799E+073.41E+075 hr 1.80E+04 1.070E+086.911E+041.071E+08 8.142E+069.895E+074.22E+076 hr 2.16E+04 1.070E+088.672E+041.071E+08 8.142E+069.892E+075.03E+078 hr 2.88E+04 1.054E+081.045E+051.055E+08 8.142E+069.732E+076.66E+0710 hr 3.60E+04 1.019E+081.000E+051.020E+08 8.142E+069.383E+078.29E+0712 hr 4.32E+04 9.774E+071.329E+059.787E+07 8.142E+068.973E+079.92E+0716 hr 5.76E+04 9.116E+071.310E+059.129E+07 8.142E+068.315E+071.32E+0820 hr 7.20E+04 8.572E+071.564E+058.587E+07 8.142E+067.773E+071.64E+0824 hr 8.64E+04 8.088E+071.353E+058.102E+07 8.142E+067.288E+071.97E+082d1.73E+056.581E+071.055E+056.592E+07 8.142E+065.777E+073.92E+083d2.59E+055.749E+079.215E+045.759E+07 8.142E+064.944E+075.88E+084d3.46E+055.195E+078.327E+045.204E+07 8.142E+064.389E+077.83E+085d4.32E+054.780E+077.662E+044.788E+07 8.142E+063.974E+079.79E+086d5.18E+054.480E+077.181E+044.487E+07 8.142E+063.673E+071.17E+097d6.05E+054.187E+076.711E+044.194E+07 8.142E+063.379E+071.37E+098d6.91E+053.984E+076.385E+043.990E+07 8.142E+063.176E+071.56E+099d7.78E+053.780E+076.059E+043.787E+07 8.142E+062.972E+071.76E+0910d8.64E+053.617E+075.798E+043.623E+07 8.142E+062.809E+071.96E+0915d1.30E+063.091E+074.954E+043.096E+07 8.142E+062.282E+072.93E+0920d1.73E+062.709E+074.342E+042.714E+07 8.142E+061.899E+073.91E+0925d2.16E+062.474E+073.966E+042.478E+07 8.142E+061.664E+074.89E+0930d2.59E+062.268E+073.636E+042.272E+078.142E+061.458E+075.86E+09 14 RBS USAR TABLE 9.2-6 14PLANT AUXILIARIES HEAT LOAD (BTU/hr)
INPUT TO STANDBY SERVICE WATER FOLLOWING A DBA evision 25 1 of 1 12 12 Component 0 - 30 min 30 min - 1 hr 1 hr - 2 hr 2 hr - Day 1 Day 1- Day 10 Day 10 - Day 30 SDG Jacket Wtr Cooler 'A' 1.203E+07 1.203E+07 1.203E+07 1.203E+07 1.203E+07 1.203E+07 HPCS DG Jacket Cooler 8.580E+06 8.580E+06 8.580E+06 8.580E+06 8.580E+06 8.580E+06 Control Room
Chillers 2.803E+06 2.803E+06 2.803E+06 2.803E+06 2.803E+06 2.803E+06 Fuel Pool Coolers 0.000E+00 0 0 2.392E+07*
1.465E+07*
1.297E+07* 16 Aux Building Unit Coolers HVR-UC2 8.789E+04 8.789E+04 8.789E+04 8.789E+04 8.789E+04 8.789E+04 HVR-UC3 1.708E+05 1.708E+05 1.708E+05 1.708E+05 1.708E+05 1.708E+05 HVR-UC5 5.396E+05 5.396E+05 5.396E+05 5.396E+05 5.396E+05 5.396E+05 HVR-UC6 6.108E+05 4.073E+05 4.073E+05 4.073E+05 4.073E+05 4.073E+05 HVR-UC7 2.948E+05 2.948E+05 2.948E+05 2.948E+05 2.948E+05 2.948E+05 HVR-UC8 2.424E+05 2.424E+05 2.424E+05 2.424E+05 2.424E+05 2.424E+05 HVR-UC11A 16 5.576E+055.576E+055.576E+055.576E+055.576E+055.576E+05RHR Pump Cooler 'A' 0.000E+00 0.000E+00 0.000E+00 5.360E+04 5.360E+04 5.360E+04 PVLCS Air Compressor 1.200E+05 1.200E+05 1.200E+05 1.200E+05 1.200E+05 1.200E+05 14 RMS-RE15A 1.118E+05 1.118E+05 1.118E+05 1.118E+05 1.118E+05 1.118E+05 RMS-RE11A 2.000E+02 2.000E+02 2.000E+02 2.000E+02 2.000E+02 2.000E+02 NOTE: These heat rates assume a coincident loss of offsite power.
- Fuel Pool Loads decrease from the value shown through the remaining time period shown.
RBS USAR Revision 25 1 of 1 TABLE 9.2-7 PLANT AUXILIARIES HEAT INPUT TO STANDBY SERVICE WATER Time Time (sec) SPC Heat Rejection Rate (Btu/hr) x 10 7 Other Auxiliaries Heat (Btu/hr) x 10 7 Integrated Heat (Btu) 16 14 12 0.0 hr 0.0 2.640 0.0 0.5 1.8 x 10 32.620 1.320 x 10 71.0 3.6 x 10 32.620 2.630 x 10 71.5 5.4 x 10 32.620 3.940 x 10 72.0 7.2 x 10 3 2.3922.620 5.249 x 10 72.5 9.0 x 10 3 2.363 2.625 7.750E+073.0 1.08 x 10 4 2.334 2.625 1.024E+084.0 1.44 x 10 4 2.277 2.625 1.517E+085.0 1.80 x 10 4 2.219 2.625 2.004E+086.0 2.16 x 10 4 2.162 2.625 2.486E+088.0 2.88 x 10 4 2.047 2.625 3.431E+0810.0 3.60 x 10 4 1.931 2.625 4.354E+0812.0 4.32 x 10 4 1.816 2.625 5.254E+0816.0 5.76 x 10 4 1.586 2.625 6.984E+0820.0 7.20 x 10 4 1.469 2.625 8.645E+0824.0 8.64 x 10 4 1.465 2.625 1.028E+092 days 1.73 x 10 5 1.449 2.625 2.007E+09 3 2.59 x 10 5 1.426 2.625 2.982E+09 4 3.46 x 10 5 1.405 2.625 3.952E+09 5 4.32 x 10 5 1.385 2.625 4.917E+09 6 5.18 x 10 5 1.366 2.625 5.877E+09 7 6.05 x 10 5 1.347 2.625 6.832E+09 8 6.91 x 10 5 1.330 2.625 7.784E+09 9 7.76 x 10 5 1.313 2.625 8.731E+09 10 8.64 x 10 5 1.297 2.625 9.674E+09 15 1.30 x 10 6 1.225 2.625 1.434E+10 20 1.73 x 10 6 1.165 2.625 1.892E+10 25 2.16 x 10 6 1.114 2.625 2.343E+10 30 2.59 x 10 6 1.070 2.625 2.789E+10 12 14 16 RIVER BEND STATION UPDATED SAFETY ANALYSIS REPORT CONTAINMENT UNIT COOLER HEAT REJECTION TOSTANDBY SERVICE WATER FOLLOWING A LARGERECIRCULATION LINE BREAK TABLE 9.2-8REVISION 14SEPTEMBER 2001 THIS TABLE HAS BEEN DELETED RBS USAR Revision 24 1 of 1 TABLE 9.2-9 HEAT REJECTED BY OPERATING PUMPS FOLLOWING DBA Time Time (sec) Heat Rejection Rate (Btu/hr) x 10 6 Integrated Heat (Btu) 14 12 0.0 hr 10.850 0.000 14 0.5 1.8 x 10 3 8.354 5.427 x 10 6 1.0 3.6 x 10 3 8.354 9.604 x 10 6 1.5 5.4 x 10 3 8.354 1.378 x 10 7 2.0 7.2 x 10 3 8.354 1.796 x 10 7 2.5 9.0 x 10 3 8.682 2.230 x 10 7 3.0 1.08 x 10 4 8.682 2.664 x 10 7 4.0 1.44 x 10 4 8.682 3.352 x 10 7 5.0 1.80 x 10 4 8.681 4.400 x 10 7 6.0 2.16 x 10 4 8.681 5.268 x 10 7 8.0 2.88 x 10 4 8.681 7.005 x 10 7 10.0 3.60 x 10 4 8.681 8.741 x 10 7 12.0 4.32 x 10 4 8.681 1.048 x 10 8 16.0 5.76 x 10 4 8.680 1.395 x 10 8 20.0 7.20 x 10 4 8.680 1.742 x 10 8 24.0 8.64 x 10 4 8.679 2.089 x 10 8 2 days 1.73 x 10 5 8.676 4.172 x 10 8 3 2.59 x 10 5 8.673 6.254 x 10 8 4 3.46 x 10 5 8.671 8.335 x 10 8 5 4.32 x 10 5 8.668 1.042 x 10 9 6 5.18 x 10 5 8.665 1.25 x 10 9 7 6.05 x 10 5 8.662 1.458 x 10 9 8 6.91 x 10 5 8.659 1.665 x 10 9 9 7.76 x 10 5 8.656 1.873 x 10 9 10 8.64 x 10 5 8.653 1.081 x 10 9 15 1.30 x 10 6 8.468 3.104 x 10 9 20 1.73 x 10 6 8.456 4.119 x 10 9 25 2.16 x 10 6 8.445 5.133 x 10 9 30 2.59 x 10 6 8.433 6.146 x 10 9 12 RBS USAR Revision 25 1 of 1 TABLE 9.2-10 TOTAL INTEGRATED HEAT INPUT TO STANDBY SERVICE WATER FROM RHR HEAT EXCHANGERS, CONTAINMENT UNIT COOLER, PUMPS, SPC, AND PLANT AUXILIARIES
Total Integrated Heat (Btu)
Time Time (sec) RHR Heat Exchangers and
Containment Unit Cooler Pumps SPC and Plant Auxiliaries Total Integrated Heat 16 14 12 6 0.0 0.0 0.0 0.0 0.0 0.0 0.5 hr 1.8 x 10 3 8.687 x 10 6 5.427 x 10 6 1.320E+07 2.731E+07 1.0 3.6 x 10 3 4.648 x 10 7 9.604 x 10 6 2.630E+07 8.238E+07 2.0 7.2 x 10 3 1.329 x 10 8 1.796 x 10 7 5.249E+07 2.034E+08 24.0 8.64 x 10 4 2.059 x 10 9 2.089 x 10 8 1.028E+09 3.296E+09 5 days 4.32 x 10 5 7.037 x 10 9 1.042 x 10 9 4.917E+09 1.300E+10 10 8.64 x 10 5 1.102 x 10 10 2.081 x 10 9 9.674E+09 2.277E+10 30 2.59 x 10 6 2.059 x 10 10 6.146 x 10 9 2.789E+10 5.463E+10 6 12 14 16 RBS USAR TABLE 9.2-11 STANDBY COOLING TOWER PERFORMANCE FOLLOWING A LARGE BREAK OF A MAIN STEAM LINE (DBA-MSL)
Revision 25 1 of 1 16 14 12 Time Time (sec) Total SSW Heat Load (Btu/hr) SSW Flow (gpm) Cold Water Temp (o F) Hot Water Temp (o F) 0.5 hr 1.80E+03 1.027E+08 13210 88.51 104.15 1 hr 3.60E+03 1.175E+08 13210 89.55 107.43 2 hr 7.20E+03 1.487E+08 15370 91.91 111.36 3 hr 1.08E+04 1.535E+08 15368 92.10 112.18 4 hr 1.44E+04 1.557E+08 15365 92.17 112.54 5 hr 1.80E+04 1.561E+08 15363 92.18 112.60 6 hr 2.16E+04 1.555E+08 15361 92.16 112.50 8 hr 2.88E+04 1.527E+08 15356 92.07 112.06 10 hr 3.60E+04 1.481E+08 15351 91.88 111.27 12 hr 4.32E+04 1.428E+08 15346 91.67 110.37 16 hr 5.76E+04 1.339E+08 15337 91.31 108.86 20 hr 7.20E+04 1.273E+08 15328 91.04 107.74 24 hr 8.64E+04 1.225E+08 15318 90.84 106.91 2 d 1.73E+05 1.072E+08 15262 88.27 102.39 3 d 2.59E+05 9.947E+07 15205 87.88 101.03 4 d 3.46E+05 9.349E+07 15149 87.56 99.97 5 d 4.32E+05 8.897E+07 15092 87.32 99.17 6 d 5.18E+05 8.564E+07 15036 87.14 98.59 7 d 6.05E+05 8.248E+07 14979 86.97 98.04 8 d 6.91E+05 8.018E+07 14923 86.83 97.64 9 d 7.78E+05 7.796E+07 14867 86.71 97.25 10 d 8.64E+05 7.613E+07 14810 86.59 96.93 15 d 1.30E+06 6.986E+07 12046 85.32 96.98 20 d 1.73E+06 6.539E+07 11834 85.02 96.13 25 d 2.16E+06 6.249E+07 11634 84.80 95.60 30 d 2.59E+06 5.997E+07 11441 84.66 95.19 12 14 16 RBS USAR Revision 25 1 of 1 TABLE 9.2-12 AVAILABLE SCT BASIN VOLUME FOLLOWING DBA WITH EVAPORATION, DRIFT AND PVLCS COMPRESSOR LEAKAGE (MAXIMUM EVAPORATION CASE)
Time Available Basin Mass
[lbm] Available Basin Volume
[gal] 0 hr 5.338E+07 6.415E+06 0.5 hr 5.334E+07 6.410E+06 1 hr 5.327E+07 6.402E+06 2 hr 5.314E+07 6.386E+06 3 hr 5.300E+07 6.369E+06 4 hr 5.285E+07 6.351E+06 5 hr 5.271E+07 6.334E+06 6 hr 5.256E+07 6.316E+06 8 hr 5.228E+07 6.282E+06 10 hr 5.201E+07 6.250E+06 12 hr 5.175E+07 6.220E+06 16 hr 5.128E+07 6.163E+06 20 hr 5.084E+07 6.110E+06 24 hr 5.044E+07 6.062E+06 2 d 4.810E+07 5.780E+06 3 d 4.606E+07 5.535E+06 4 d 4.408E+07 5.297E+06 5 d 4.216E+07 5.066E+06 6 d 4.028E+07 4.840E+06 7 d 3.850E+07 4.626E+06 8 d 3.679E+07 4.422E+06 9 d 3.508E+07 4.216E+06 10 d 3.343E+07 4.018E+06 15 d 2.534E+07 3.045E+06 20 d 1.772E+07 2.129E+06 25 d 1.037E+07 1.247E+06 30 d 3.272E+06 3.932E+05
RBSUSAR______________________________
(1)LoopAonlyisassumedtooperatefollowingDBA.8A8 88ARevision 221of1TABLE9.2-13STANDBYSERVICEWATERSYSTEM SAFEGUARDEQUIPMENTSTATUSFOLLOWINGADBA9 Component (1)0-20min20min-1hr1hr-24hr24hr-30day 9RHRPumpA O perating O perating O perating O peratingRHRHeatExchA Off Operating Operating OperatingHPCSPumpOperatingOperating Operating OperatingLPCSPumpOperatingOff Off OffSSWPumpAOperatingOperating Operating OperatingSSWPumpCOperatingOperating Operating Operating8A8SCTFansA-E Off Off Operating OperatingSCTFansL-P Off Off Operating Operating 88ASDGAOperatingOperating Operating OperatingHPCSDGOperatingOperating Operating Operating RBSUSARNOTES:NSW-NormalServiceWaterRPCCW-ReactorPlantComponentCoolingWaterHPCS-HighPressureCoreSprayRHR-ResidualHeatRemovalA/C-Air-Conditioning CST-CondensateStorageTank(formakeuponly)*SSWservesthesecoolersonlyifRPCCWdischargepressureis
low.1of1August1987TABLE9.2-14 ESSENTIALC OMPONENTSSERVEDB YS TANDBYSERVICEWATERSY STEMComponentLocationComponent'sNormal Component (Building)CoolingSupplyStandbyDiesel Generator1ADieselGenerator NSWStandbyDiesel Generator1BDieselGenerator NSWHPCSDieselDieselGenerator NSW GeneratorControlBuildingA/CChillerA Control NSWControlBuilding A/CChillerB Control NSWRHRHeat Exchanger sA&C Auxiliary NSWRHRHeat Exchanger sB&D Auxiliary NSWFuelPoolMakeup Fuel CSTFuelPoolCooling*Fuel RPCCWUnitCoolerCoils ContainmentChilledWaterUnitCoolerCoils Auxiliary NSWPenetrationValve LeakageControl
Compressor Auxiliary NSWRHRPumpSealCoolers*Auxiliary RPCCW RBSUSARRevision141of2September2001TABLE9.2-15STANDBYSERVICEWATERSYSTEMMAJORCOMPONENTDESIGNDATADesignDataforEachComponent Description Quantity (gpm)StandbyServiceWaterPumps 4 7,690 (1)1214StandbyDieselGenerator JacketWaterCoolers 2 7002High-PressureCoreSpray DieselGeneratorJacket WaterCooler 1 800 2*3ControlBuildingAir-ConditioningWaterChillers 4 630 3*98A8ResidualHeatRemovalHeat
Exchangers 4 5,800 (3)88A9ContainmentUnitCoolers 2 540AuxiliaryBuildingUnitCoolersRWCUPumpandHeat ExchangerRoomUnitCooler1 50RPCCWPumpsandHeat ExchangerRoomand CRDTransferandWork AreasUnitCooler 1 100El95'-9"Area UnitCooler 1 90HPCSPumpRoomUnitCooler1 185 12RCICPumpRoom,LPCSPump Room,andRHRPumpAand HeatExchangersAandC RoomUnitCooler 1 235 14 RBSUSAR (1)Thisnumberrepresents50-percentcapacityat170fttotalhead.
(2)Thisnonessentialequipmentcanbesupplied bySSWifavailable.9 (3)TheSSWflowtotheRHRHeatExchangerswillbethrottledto 3,000gpmwhentheSCTBasinwaterleveldropstoanelevation of90 ftfollowingaLOP-LOCA.
9*8A888ARevision122of2December1999TABLE9.2-15(Cont)DesignDatafor EachComponent Description Quantity (gpm)NormalSwitchgearand ElectricTerminalBox AreaUnitCooler 1 1501MainSteamPipeTunnel, NorthEndUnitCooler 1 120 1RHRPumpBandHeat ExchangersBandDRoom andRHRPumpCRoomUnitCooler1 210Elevation114'HPCSHatch andElevatorAreaUnit
Cooler 1 3712UpperAuxiliaryBuilding LevelUnitCoolers 2 410 12 RHRPumpSealCoolers 2 15FuelPoolHeatExchangers 2 2,000PenetrationValveLeakage ControlCompressor 2 65DrywellUnitCoolers (2)6 334ReactorPlantComponent CoolingHeatExchangers (2)3 5,000AnnulusVentilation RadiationMonitors 2 5RHRHeatExchanger RadiationMonitors 2 9 RBSUSARRevision8A1of1October1996TABLE9.2-16STANDBYSERVICEWATERSYSTEMSINGLEPASSIVEFAILURECRITERIONANALYSISSinglePassiveFailure ConsequenceFailureofUHSThisisnotacrediblecoolingtower.failureduetothedesignrequirementsforthetower.Failureofplantmake-AdequateUHSwaterinventory upwatersystemmakeupisprovidedtomakeupfor linetostoragebasin.driftandevaporativelossesovera30-dayperiod.FailureofHPCSdieselHeadercanbeisolatedby generatorjacketcool-motor-operatedvalves.
erorareaunitcoolerPlantcooldowncanbeaccom-servicewaterheaders.plishedusingRHRpumps.FailureofacoolingThisisnotacredibletowerbasin.failureduetothedesignrequirementsforthebasin.FailureoftheSSWThestandbyservicewatersys-pressureboundaryfortemredundancyandintercon-anysingleloopduetonectionprovideavailability piperupture,heattoperformtherequiredcoolingexchangertubingrup-function.
ture,orpipefitting (elbowtoe,reducer, etc)rupture.FailureofanymanualThestandbyservicewatersys-valve,i.e.,valvetemredundancyandintercon-failsopenedorclosed,nectionprovideavailability contrarytoitsnormaltoperformtherequiredcooling
position.function.8A8 88A RBS USAR Revision 17 1 of 1 TABLE 9.2-17 LIST OF COOLERS SERVICED BY TURBINE PLANT COMPONENT COOLING WATER SYSTEM Component Coolers Quantity Generator Stator Coolers (including one spare) 2 8 8Condensate Pump Motor and Thrust Bearing Coolers 3 Heater Drain Pump Lube Oil and Motor
Bearing Coolers (including two spares) 4 12 Air Removal Pump Coolers (used during plant startup) 2 Reactor Feed Pump Lube Oil and Motor Bearing Coolers 3
Off Gas Glycol Condensers 3 ** Waste Evaporator Overhead Condenser 1 ** Regenerant Evaporator Overhead Condenser 1 ** Waste Evaporator Distillate Cooler 1 Regenerant Evaporator Distillate Cooler 1 Off Gas Vault Refrigerant Condenser 2
- Auxiliary Boiler Recirculation Pump Gland Cooler 2
- Waste Evaporator Vent Gas Cooler 1 Regenerant Evaporator Vent Gas Cooler 1 Isolated Phase Bus Duct Cooler 4
- Auxiliary Boiler Sample Cooler 1 Turb. Bldg. Sample Coolers 6 Reactor Feed Pump Gear Increaser Lube Oil Coolers 3 Reactor Feed Pump Seal Water Heat Exchangers 3 ** Instrument Air Comp. Water Jackets and Intercoolers 3
- Intrument Air After Coolers 3
- Turb. Plant Sampling Fdwtr Corrosion Monitor Sample Cooler 1
- Turb. Plant Sampling Refrigerating Units 1 13 Sample Precoolers (SST-PNL205B/ 206B/ 207B) 3 13Reactor Feed Pump Seals 6* These components are not used during Normal Operation.
- These components are not connected.
12 RBS USAR Revision 12 1 of 2 December 1999 TABLE 9.2-18 DESIGN DATA FOR VENTILATION CHILLED WATER SYSTEM System Equipment and Design Data Turbine Building Subsystem Radwaste Building Subsystem
- 1. Centrifugal Liquid Chillers Equipment Mark No. 1HVN-CHL1A,B&C 1HVN-CHL2A,B&C Three 50-percent centrifugal
liquid chillers for each building 12 Capacity 1250 tons 400 tons Entering chilled water
temperature 72°F 65°F Leaving chilled water
temperature 57°F 50°F Maximum chilled water capacity 2000 gpm 640 gpm Condenser cooling water
requirements 3625 gpm 1200 gpm
- 2. Chilled Condenser Cooling Water Pumps Equipment Mark No. 1SWP-P4A,B&C 1SWP-P5A,B&C Three 50-percent pumps for each
building Capacity 4000 gpm 1200 gpm Total head 31 ft 30 ft 12 2. Chilled Water Recirculation Pumps Equipment Mark No. 1HVN-P1A&B 1HVN-P4A&B Two 100-percent pumps for each
building Capacity 3750 gpm 1550 gpm Total head 231 ft 115 ft RBS USAR 2 of 2 August 1987 TABLE 9.2-18 (Cont)
System Equipment and Design Data Turbine Building Subsystem Radwaste Building Subsystem
- 4. Secondary Pumps Equipment Mark No.
1HVN-P2A&B Two 100-percent pumps for the fuel
building Capacity 400 gpm Total head 161 ft 5. Compression Tank Equipment Mark No. 1HVN-TK1 1HVN-TK2 One 100-percent compression tank
for each building Working capacity 665 gal 230 gal Design pressure 150 psig 150 psig
RBS USAR Revision 12 1 of 1 December 1999 TABLE 9.2-19 DESIGN DATA FOR THE CONTROL BUILDING CHILLED WATER SYSTEM Equipment Design Data 12 3 1 Centrifugal liquid chillers (Equipment Mark No.
1HVK*CHL1A, B, C, and D)
Capacity: 189 ton (100%)
Entering chilled water temperature: 67.5°F
Leaving chilled water temperature: 52.5°F
Chilled water capacity: 330 gpm/chiller
Condenser cooling water requirements: 630 gpm/loop 12 Condenser cooling water
pumps (Equipment Mark No.
1SWP*P3A, B, C and D)
Capacity: 630 gpm (100%)
Total head: 34 ft 1 Chilled water recirculation
pumps (Equipment Mark No.
1HVK*P1A, B, C and D)
Capacity: 330 gpm (100%)
Total head: 145 ft 3 Compression tank (Equipment Mark No.
1HVK*TK1A and B)
Working capacity: 125 gal
Design pressure: 150 psig
RBS USAR Revision 14 1 of 1 September 2001 6 TABLE 9.2-20 SERVICE WATER COOLING SYSTEM MAJOR COMPONENT DESIGN DATA 14 Description of Component Quantity Operating/
Available Total Operating 10 6 BTU/HR Design GPM for Each Component 14 Service Water Cooling
Pumps (1) 2/3 -- 31,500 Service Water Cooling
System Flushable Filters 7/8 -- 9,000 Service Water Cooling
System Cooling Tower 1/1 444 63,000
NOTES: (1) Approximate flow at 211 ft. developed head 6
RBS USAR TABLE 9.3-1 PROCESS SAMPLING SYSTEM Measured
Description Sample Station Location Purpose ParameterRevision 16 1 of 8 March 2003 Reactor Steam Supply SystemReactor Water 1G33-PNL Z020, Recirculation Pump Reactor Water CE & CP 1SSR-PNL 121 Discharge (Grab Sample Quality at the Sample Panel) Main Steam 1SST-PNL 80 Main Steam Line (Grab Carryover/ CE Sample at the Sample Moisture Panel) Standby Liquid Control System NA Borated Water Storage Borate Borate Tank (Local Grab Sample) Concentration Concentration Reactor Water Cleanup SystemFilter/Demineralizer Influent 1G33-PNL Z020 Inlet Line (Grab Sample Reactor Water CE At the Sample Panel) Quality Filter/Demineralizer Effluent 1G33-PNL Z020 & Outlet Line (Grab Sample Filter CE & CP 1SRR-PNL 121 at the Sample Panel) Efficiency Fuel Pool Cooling and Cleanup System16Purification Pump 1SSR-PNL 120 Discharge (Grab Sample Fuel Pool CE at the Sample Panel) Water Quality Filter Effluent 1SSR-PNL 120 Outlet Line (Grab Sample Filter CE at the Sample Panel) Efficiency Demineralizer Effluent 1SSR-PNL 120 Outlet Line (Grab Sample Demineralizer CE At the Sample Panel) Efficiency 16 RBS USAR TABLE 9.3-1 (Cont.) Measured Description Sample Station Location Purpose ParameterRevision 16 2 of 8 March 2003 Reactor Plant Component Cooling WaterCooling Water Sample 1SST-PNL 80 Outlet of Each Major Monitor Heat CE Heat Exchanger (Grab Exchanger Tube Sample at the Sample Leaks Panel) Turbine Plant Component Cooling WaterCooling Water Sample 1SST-PNL 80 Outlet of Each Major Monitor Heat CE Heat Exchanger (Grab Exchanger Tube Sample at the Sample Leaks Panel) Residual Heat Removal SystemHeat Exchanger Outlet 1SST-PNL 80 Outlet of Each Heat Water Quality CE Exchanger (Grab Sample at the Sample Panel)
Control Rod Drive SystemCRD Supply 1G33-PNL Z020 & Inlet Line (Grab Sample Water Quality CE & CP 1SRR-PNL 121 at the Sample Panel)
Radwaste System16Waste Collector Tank 1SSW-PNL 130 Effluent (Grab Sample Process Data CE at the Sample Panel) Demineralizer 1SSW-PNL 130 Effluent (Grab Sample Demineralizer CE at the Sample Panel) Efficiency Filtrate Pump 1SSW-PNL 130 Effluent (Grab Sample Process Data CE at the Sample Panel) 16 RBS USAR TABLE 9.3-1 (Cont.) Measured Description Sample Station Location Purpose ParameterRevision 16 3 of 8 March 2003 16Demineralizer 1SSW-PNL 130 Influent (Grab Sample Process Data CE at the Sample Panel) Demineralizer NA Acid Influent (Local Acid Concentration pH,CE Grab Sample) Demineralizer NA Caustic Influent (Local Caustic pH,CE Grab Sample) Concentration Recovery Sample Tank 1SSW-PNL 130 Effluent (Grab Sample Water Quality CE at the Sample Panel) Floor Drain Collector Tank 1SSW-PNL 130 Effluent (Grab Sample Process Data CE at the Sample Panel) Discharge Control 1SSW-PNL 130 Final Discharge (Grab Water Quality CE Sample at the Sample Panel) Monitor Station RAD Liquid Activity Releases (Continuous) Radwaste Filter 1SSW-PNL 130 Effluent (Grab Sample Filter CE at the Sample Panel) Efficiency Regenerant Waste Tank 1SSW-PNL 130 Effluent (Grab Sample Process Data CE at the Sample Panel) Regenerant Evaporator Bottoms 1SSW-PNL 130 Effluent (Grab Process Data CE Sample at the Sample Panel) 16Phase Separator Tank NA Pump Discharge Process Data CE (Local Grab Sample)
RBS USAR TABLE 9.3-1 (Cont.) Measured Description Sample Station Location Purpose ParameterRevision 16 4 of 8 March 2003 16Waste Evaporator Bottoms 1SSW-PNL 130 Effluent (Grab Sample Process Data CE at the Sample Panel) Waste Evaporator Distillate Cooler NA Effluent (Local Grab Process Data CE Sample) Regenerant Evaporator Distillate NA Effluent (Local Grab Process Data CE Cooler Sample) Radwaste Demineralizer Waste 1SSW-PNL 130 Effluent (Grab Sample Process Data CE Header At the Sample Panel)
TABLE 9.3-1 (Cont) 16Water Treating SystemCation Exchanger Unit 1SST-PNL 78 Influent (Grab Sample Process Data CE at the Sample Panel) Cation Exchanger Unit 1SST-PNL 78 Effluent (Grab Sample Demineralizer CE at the Sample Panel) Efficiency Anion Exchanger Unit 1SST-PNL 78 Influent (Grab Sample Process Data CE at the Sample Panel) Anion Exchanger Unit 1SST-PNL 78 Effluent (Grab Sample Demineralizer CE,Si at the Sample Panel) Efficiency Mixed-Bed Exchanger Unit 1SST-PNL 78 Influent (Grab Sample Process Data CE at the Sample Panel) Mixed-Bed Exchanger Unit 1SST-PNL 78 Effluent (Grab Sample Demineralizer CE,Si at the Sample Panel) Efficiency Dilute Acid NA Effluent (Local Grab Acid Concentration pH Sample)
RBS USAR TABLE 9.3-1 (Cont.) Measured Description Sample Station Location Purpose Parameter5 of 8 August 1988 Dilute Caustic NA Effluent (Local Grab Caustic pH Sample) Concentration Wastewater NA Effluent (Local Grab Process Data CE Sample)
Condensate Demineralizer SystemDemineralizer (Train) 1SST-PNL 72 Influent Header (Grab Process Data CP,TU,O-,CE Sample at the Sample Panel) Demineralizer (Train) 1SST-PNL 72 Effluent Header (Grab Demineralizer CP,TU,O-,CE Sample at the Sample Efficiency Panel) Resin Hold Tank 1SST-PNL 72 Effluent (Grab Sample Process Data CE at the Sample Panel) Demineralizers (10) 1SST-PNL 72 Effluent (Grab Sample Process Data CE,CP at the Sample Panel) Ultrasonic Resin Cleaner NA Effluent (Local Grab Process Data CE Sample) Resin Mix Tank 1SST-PNL 72 Effluent (Grab Sample Process Data CE at the Sample Panel) Cation Regeneration Tank 1SST-PNL 72 Effluent (Grab Sample Process Data CE at the Sample Panel) Anion Regeneration Tank 1SST-PNL 72 Effluent (Grab Sample Process Data CE at the Sample Panel) Recovered Acid Tank NA Effluent (Local Grab Acid Concentration pH,CE Sample) Dilute Acid NA Effluent (Local Grab Acid Concentration pH,CE Sample)
RBS USAR TABLE 9.3-1 (Cont.) Measured Description Sample Station Location Purpose Parameter6 of 8 August 1988 Recovered Caustic Tank NA Effluent (Local Grab Caustic pH,CE Sample) Concentration Dilute Caustic NA Effluent (Local Grab Caustic pH,CE Sample) Concentration Recovered Water Sump NA Pump Discharge (Local Process Data pH,CE Grab Sample)
Condensate Makeup and Drawoff System1Condensate ISSR-PNL 120 Pump Discharge (Grab Condensate CE Sample at the Sample Quality Panel) 1Makeup Water SystemDemineralizer Water 1SST-PNL 80 Transfer Line (Grab Demineralizer CE Sample at the Sample Water Quality Panel) Wastewater Treatment SystemWaste Neutralizing Tank NA Effluent (Local Grab Process Data CE Sample)
Condensate SystemCondensate 1SST-PNL 80 Condensate Pump Condensate Quality CE Discharge (Grab Sample and Condenser Tube at the Sample Panel) Leaks Condenser NA Hotwell (Local Sample Condenser Tube CE Probe and Monitor) Leaks Heater Drains 1SST-PNL 80 Third Point Heater Water Quality and CP,TU,O- Drains (Grab Sample - Concentration at the Sample Panel)
RBS USAR TABLE 9.3-1 (Cont.) Measured Description Sample Station Location Purpose ParameterRevision 13 7 of 8 September 2000 Reactor Feedwater SystemFeedwater 1SST-PNL 80 and After Last Heater (Grab Feedwater Quality CE,pH,O-, 1BZ1-PNL Z001 Sample at the Sample and Check Corrosion TU,CP 13 SST-PNL207** Panel) 13Circulating Water SystemEffluent NA Blowdown Line (Local Monitor Station CE,RAD Online Monitor) Liquid Activity Releases Auxiliary Steam SystemAuxiliary Boiler 1SST-PNL 78 Steam Outlet (Grab Water Quality CE Sample at the Sample Panel) Feedwater 1SST-PNL 78 Feedpump Discharge Water Quality CE,O- (Grab Sample at the Sample Panel) Auxiliary Boiler NA Blowdown (Local Water Quality CE Conductivity Element)
Sealing Steam SystemSealing Steam Evaporator 1SST-PNL 80 Evaporator Effluent Steam Quality CE (Grab Sample at the Sample Panel) 9*Note: 1BZ1-PNLZ001 does not measure turbidity 913**SST-PNL207 is for corrosion products sample collection 13 RBS USAR TABLE 9.3-1 (Cont.) Measured Description Sample Station Location Purpose Parameter 8 of 8 August 1988 Radwaste Steam SupplyRadwaste Steam Reboiler 1SST-PNL 80 Reboiler Discharge Steam Quality CE (Radwaste Auxiliary Steam) (Grab Sample at the Sample Panel)
Containment SumpsEquipment Drain Sumps N/A Equipment Drain Sump Water Quality As Required Pump Discharge (Local Grab Sample) Floor Drain Sumps N/A Floor Drain Sump Pump Water Quality As Required Discharge (Local Grab Sample) Key to Sample Stations: Key to Measured Parameters: 1G33-PNL Z020 - Reactor Plant Sample Station CE - Conductivity 1SSR-PNL 121 - Reactor Plant Corrosion Product Monitor pH - pH 1SSR-PNL 120 - Fuel Building Sample Station TU - Turbidity 1SST-PNL 72 - Condensate Demineralizer Area Sample Station O 2 - Dissolved Oxygen 1SST-PNL 78 - Water Treatment Building Station Si - Silica 1SST-PNL 80 - Turbine Building Sample Station CP - Corrosion Products 1SSW-PNL 1 - Radwaste Building Sample Station RAD- Radiation (See Section 11.5 for 1B21-PNL Z001 - Feedwater System Corrosion Product Monitor monitors that specifically measure radiation levels of radioactive samples)
RBSUSARTABLE9.3-1aEQUIPMENTANDFLOORDRAINAGESYSTEMSCOMPONENTCAPACITIES1of1August1987 PumpSumpMarkSumpPumpDataNominalSumpCapacityNumberPump1Pump2Capacity(gal)(gpm,each)1DFT-TK1A1DFT-P1A1DFT-P1D65050 1DFT-TK1B1DFT-P1B1DFT-P1E83050 1DFT-TK1C1DFT-P1C1DFT-P1F71050 1DFT-TK2A1DFT-P2A1DFT-P2C71050 1DFT-TK2B1DFT-P2B1DFT-P2D77050 1DFT-TK31DFT-P3A1DFT-P3B59050 1DET-TK1A1DET-P1A1DET-P1D71050 1DET-TK1B1DET-P1B1DET-P1E71050 1DET-TK1C1DET-P1C1DET-P1F83050 1DFT-TK71DFT-P7A1DFT-P7B95050 1DFM-TK41DFM-P4A1DFM-P4B71050 1DFM-TK71DFM-P7None40050 1DFM-TK81DFM-P8None40050 1DFM-TK91DFM-P9None40050 1DFM-TK111DFM-P11None37050 1DFM-TK11DFM-P1None26050 1DFM-TK21DFM-P2None26050 1DFM-TK31DFM-P3None26050 1DFM-TK51DFM-P5A1DFM-P5B34050 1DFM-TK61DFM-P6A1DFM-P6B49050 1DFW-TK1A1DFW-P1A1DFW-P1C71050 1DFW-TK1B1DFW-P1B1DFW-P1D71050 1DFW-TK21DFW-P2A1DFW-P2B95050 1DFA-TK41DFA-P4A1DFA-P4B71050 1DER-TK11DER-P1A1DER-P1B95050 1DER-TK21DER-P2A1DER-P2B77050 1DER-TK31DER-P3A1DER-P3B77050 1DFR-TK11DFR-P1A1DFR-P1B83050 1DFR-TK21DFR-P2A1DFR-P2B59050 1DFR-TK3A1DFR-P3A1DFR-P3G53050 1DFR-TK3B1DFR-P3B1DFR-P3H59050 1DFR-TK3C1DFR-P3C1DFR-P3J53050 1DFR-TK3D1DFR-P3D1DFR-P3K53050 1DFR-TK3E1DFR-P3E1DFR-P3L53050 1DFR-TK3F1DFR-P3F1DFR-P3M53050 1DFR-TK5A1DFR-P5A1DFR-P5D65050 1DFR-TK5B1DFR-P5B1DFR-P5E65050 1DFR-TK5C1DFR-P5C1DFR-P5F65050 1DFR-TK61DFR-P6A1DFR-P6B35050 RBS USARTABLE 9.3-2STANDBY LIQUID CONTROL SYSTEM OPERATING PRESSURE/TEMPERATURE CONDITIONSSLCS Modes(1)Standby Mode(1)Circulation Test Injection Test(2) Operating Mode(1)¸Revision151of2May2002PressureTempPressureTempPressureTempPressureTempPiping(psig)(3)(°F)(psig)(3)(°F)(psig)(3)(°F)(psig)(3)(°F)12PumpMakeup70/100Test Tank70/100Test Tank70/100Storage70/110SuctionWater (4)Static (4)Static (4)Tank (4)PressureHead(5)Head(5)Static Head15Pump Dis-Makeup70/1000/125070/10070 Plus70/100(70 Plus70/110 charge toWaterReactorReactor ExplosivePressureStaticStatic Valve InletHeadHead) To 1,250 12ExplosiveReactor70/100Reactor70/100<70 Plus70/100(<70 Plus70/110Valve Outlet StaticStaticReactorReactorto but notHead ToHead ToStaticStatic Including1,180(6)1,180(6)HeadHead) ToFirst Iso-
<1,250lation Check ValveFirst Iso-Reactor70/565Reactor70/565Reactor125(2)Reactor70/560lationStatic (7)Static (7)StaticStatic (7)Check ValveHead ToHeadHead(2)Head Toto the1,180(6)1,180(6)Reactor 15 RBSUSARRevision152of2May2002TABLE 9.3-2 (Cont)Notes to Table 9.3-2:(1)The pump flow rate is zero (pump not operating) during the standby mode and at rated capacityduring the test and operating modes.(2)Reactor to be at 0 psig and 125°F before changing from the standby mode to the injection test mode.(3)Pressures tabulated represent pressure at the points identified below. To obtain pressure atintermediate points in the system, the pressures tabulated must be adjusted for elevation difference and pressure drop between such intermediate points and the pressure points identified below:Piping Pressure Point Pump suction Pump suction flange inlet Pump discharge to ex- Pump discharge flange plosive valve inlet outlet Explosive valve outlet to but not including first isolation check valve Explosive valve outlet First isolation check valve to the reactor Reactor sparger outlet(4)During chemical mixing, the liquid in the storage tank is at a temperature of 150°F maximum.(5)Pump suction piping is subject to demineralized water supply pressure during flushing and filling ofthe piping and during any testing where suction is taken directly from the demineralized water supply line rather than a test tank.15(6)Maximum reactor operating pressure is 1,180 psig at reactor standby liquid control sparger outlet.(7)565°F represents maximum sustained operating temperature.
15 RBSUSARTABLE9.3-3Revision101of1April1998PVLCSPROCESSLINEINFORMATIONTHISTABLEHASBEENDELETED RBSUSAR*Basedonmanufacturer'srequirements.3**SeeSection9.3.1.1.2forclarificationforCategory2actuatorsonCategory1valves/dampers.
3Revision31of1August1990TABLE9.3-43SAFETY-RELATEDEQUIPMENTSUPPLIEDBYINSTRUMENTAIRSYSTEM**
3MaximumAllowableParticleSize*Description(microns)Air-operatedventilation175shutoffvalvesTestablecheckforinboard175andoutboardcontainment isolationvalvesAir-operatedventilation155shutoffdampersDrywellpenetration40isolationvalvesStandbyliquidcontrolstoragetanksHydrauliccontrolunitforCRDsScramdischargevolume5ventanddrainvalves RBSUSARTABLE9.3-5POST-ACCIDENTSAMPLINGSYSTEMANALYSESINSTRUMENTATIONDesignDesignDesignParameterMethodBasesRangeBasesAccuracyBasesTime1of1August1987Grossacti-Gammaspectroscopy0.1Ci/mlto+50percent<3hoursvitygamma10Ci/ml
spectrumBoronPlasmaspectometry0-6000ppm+5percent<3hoursTitrimetry(manitol)1-100ppmChlorideOffsiteanalysisN/AN/A<96hoursTotaldis-GEdissolvedgasprocedure25cc/kgto+50percent<3hourssolvedgas50cc/kggreater+30percentthan50cc/kgpHMicroelectrode1-13pHunits+0.3pHunits<3hours HydrogenGaschromatograph50-2000cc/kg+10percent<3hours0-50cc/kg+5percentDissolvedViadissolvedhydrogenVerifiesthatN/A<3hoursoxygenconcentrationatgreaterdissolvedthan10cc/kgoxygenislessthan0.1ppm RBS USAR TABLE 9.4-1 ENVIRONMENTAL AND SYSTEM DESIGN PARAMETERS FOR HVAC 16 (See note 27 on page 5 of 5) Operates Provision Degree of Under for Rad Temperature (°F) Pressure (in W.G.) Rel. Humidity (%) ESF Redundancy Post- Monitor at Normal Post Normal Post Normal Post Power (Major Accident Release Range LOCA Range LOCA Range LOCA Reqd. Components) Condition Point 16129Revision 18 1 of 5 Control building 75 max 80 max 0.125 min 0.125 min 20-70 20-70 Yes 2-100% Yes Yes, at main control 65 min 65 min (18) (18) intake
room 9Control building A.C. equipment 90 max 90 max 0.125 min 0.125 min 20-60 20-60 Yes 2-100% Yes Yes, at room (for main 60 min 60 min (18) (18) intake
control room equipment) 12Control building 90 max 90 max Atmos Atmos 20-85 20-85 Yes 2-100% Yes Yes, at battery rooms 60 min 60 min intake Control building switchgear, refrig 104 max 104 max Atmos Atmos 20-90 20-90 Yes 2-100%(5) Yes Yes, at machinery rooms, 40 min 40 min intake
inverter rooms
and cable vaults Control building 104 max 104 max Atmos Atmos 20-90 20-90 Yes 2-100% Yes Yes, at general areas 40 min 40 min intake 3141384Fuel building 96 max 125 max Equal or Equal or 20-90 20-90 (6) 2-100% (6) Yes general areas 40 min less than less than 0.00 -0.25 (21)(22)13Fuel Pool 96 max 125 max Equal or Equal or 20-100 20-100 (6) 2-100% (6) Yes area 40 min less than less than 0.00 -0.25 (21)(22)Cubicles 120 max 13 8 max Equal or Equal or 20-90 20-90 (6) 2-100% (6) Yes 40 min less than less than 0.00 -0.25 (21)(22)4 8 14 RBS USAR TABLE 9.4-1 (Continued) 16 (See note 27 on page 5 of 5)
Operates Provision Degree of Under for Rad Temperature (°F) Pressure (in W.G.) Rel. Humidity (%) ESF Redundancy Post- Monitor at Normal Post Normal Post Normal Post Power (Major Accident Release Range LOCA Range LOCA Range LOCA Reqd. Components) Condition Point Revision 18 2 of 5 128Auxiliary building NA Uncon- NA -0.25 min NA Uncon- Yes 2-100% Yes Yes SGTS system trolled trolled Auxiliary building 122 max 132 max Atmos -0.25 min 20-90 20-100 Yes 2-100% Yes Yes general areas 40 min 40 min (19) (19) Auxiliary building 122 max 127 max Atmos -0.25 min 20-90 20-100 Yes 2-100% Yes Yes cubicles (17) (17) (19) (19) 40 min 40 min 8 12 16Radwaste building 96-104 NA 0.00 NA 20-90 NA No (7) No Yes all areas max 40 min Turbine building 96-120 NA 0.00 NA 20-90 NA No 3-50% No Yes all areas max Exh fans 40 min Offgas, condensate, 75(8)- NA -0.125 NA 20-90 NA No 2-100% No Yes and demineralizer 120 max buildings 40 min Offgas char vault -40 min NA -0.125 NA 0 NA No 2-100% No Yes 16159 Diesel-gen bldg: operating area 12 0 max 12 0 max Atmos Atmos20-100 50 Yes 2-100% Yes Yes 40 min(23) 40 min(23) 2 min(24) 2 min(24) 9control room 104 max 104 max Atmos Atmos20-100 50 Yes 2-100% Yes Yes area 40 min(23) 40 min(23) 2 min(24) 2 min(24) 15Standby service 109 max 109 max Atmos Atmos20-100 20-100 Yes 2-100% Yes No water cooling 40 min 40 min
tower; swgr, transfmr, and pump
rooms RBS USAR TABLE 9.4-1 (Continued) 16 (See note 27 on page 5 of 5)
Operates Provision Degree of Under for Rad Temperature (°F) Pressure (in W.G.) Rel. Humidity (%) ESF Redundancy Post- Monitor at Normal Post Normal Post Normal Post Power (Major Accident Release Range LOCA Range LOCA Range LOCA Reqd. Components) Condition Point Revision 18 3 of 5 Standby service 104 max 104 max Atmos Atmos 95 max 95 max Yes 2-100% Yes No water cooling 3 5 min 3 5 min tower; remote air intake
roomStandby service 102 max 106 max Atmos Atmos 40 100 Yes 10-100% Yes No water cooling 25 min
tower; fan deck 12Reactor building 90 max NA(9) NA 20-50(13) NA Yes 3-50% Yes Yes containment 70 min +/-8.3 (25) 2Reactor building 145 max NA +41.7 to NA 20-50(13) NA (10) 6-25% No Yes drywell 70 min 0.0 (26) 2 1614Reactor building 120 max NA -3.0 min -0.50 min 12-100 NA Yes 2-100% Yes Yes annulus 40 min (14) (20) (15) (20) 12143Control building 90 max 90 max Atmos Atmos 20-60 20-60 Yes 2-100% Yes Yes, at remote shutdown 40 min 40 min intake
panel rooms 315Fire pumphouse 104 max NA -0.125 NA 100 max NA No None No No 40 min 15Water treatment 104 max NA 0.125 NA 100 max NA No None No No building 60 min Makeup water 120 max NA Atmos NA 100 max NA No 2-100% No No intake structure 65 min
and switchgear
houseMotor generator 120 max NA 0.125 NA 100 max NA No None No No building 25 min Demineralized 104 max NA -0.125 NA 100 max NA No None No No water pumphouse 40 min RBS USAR TABLE 9.4-1 (Continued) 16(See note 27 on page 5 of 5)
Operates Provision Degree of Under for Rad Temperature (°F) Pressure (in W.G.) Rel. Humidity (%) ESF Redundancy Post- Monitor at Normal Post Normal Post Normal Post Power (Major Accident Release Range LOCA Range LOCA Range LOCA Reqd. Components) Condition Point 16Revision 16 4 of 5 March 2003 Normal switchgear 104/80 NA 0.25/ NA 90/20 NA No 2-100%(11) No No building max -0.125 75/25 min Auxiliary boiler 104 max NA -0.125/ NA 100 max NA No None No No building 40 min -0.25 Cooling tower 109 max NA 0.125 NA 85 max NA No None No No switchgear house 40 min 2Electrical and 122 max (17)122 max (17)-0.125 NA 100 max 50 max No (12) No No piping tunnels 40 min 2Circ H20 pH and 104 max NA 0.125 NA 100 max NA No None No No switchgear room 60 min Auxiliary control 72/104 NA -0.125/ NA 100 max NA No 2-100% No No building max -0.25 60/72 min Clarifier area 104 max NA 0.125 NA 100 max NA No None No No switchgear house 40 min Hypochlorite area 104 max NA 0.125 NA 100 max NA No None No No switchgear house 25 min Blowdown pit NA max NA NA NA 95 max NA NA NA NA NA NA min (16)
RBS USAR TABLE 9.4-1 (Continued) Revision 16 5 of 5 March 2003 (1) Outside design conditions: Summer: 96°F dry bulb, 81°F wet bulb Winter: 25°F dry bulb (2) Normal conditions: Those operating conditions that exist during routine plant operation or testing, including normal plant operation, shutdown, and hot standby.
(3) No heating is provided to maintain a minimum of 40°F following LOCA and loss-of-offsite power.
(4) Conditions list are essentially steady state and do not reflect transients.
(5) Refrigeration machinery room: 1-100% normal 2-100% accident (6) Normal supply and exhaust system operates only in normal mode. Charcoal filtration system operates only in accident mode. ESF required only in accident mode.
(7) 3-50% exhaust fans 2-100% filter units and exhaust fans (8) Sample room only.
(9) During accident one unit cooler runs as part of containment heat removal system.
(10) ESF power provided on loss-of-offsite power only.
(11) Plus 1-100% battery and computer rooms.
(12) (2) systems 2-100%; (8) systems 1-100%. 129(13) During shutdown conditions elevated relative humidities may be present. Humidity is maintained to prevent condensation.
914(14) Negative pressure of at least -3" W. G. provided by annulus pressure control system. (15) -0.50" W. G. min negative pressure with respect to outside atmosphere provided by standby gas treatment system post accid ent.(16) Limiting relative humidity only.
14162(17) Normal and post LOCA maximum temperature in the main steam tunnel (north) is 135°F.
213(18) A pressure up to +5.0" W. G. may result with Control Room Fresh Air System train(s) operating. (19) A pressure up to -9.0" W. G. may result with SGTS train(s) operating.
(20)A pressure up to -14.0" W. G. may result with SGTS train(s) operating.
(21)A pressure up to -2.0" W. G. may result with Fuel Building Charcoal filter train(s) operating.
12 1314 (22)Fuel Building integrity is only credited during fuel handling accidents involving recently irradiated fuel.
1415 (23)Diesel Generator in standby (24)Diesel Generator running during winter minimum temperature 15(25)Normal pressure range for reactor building containment is equivalent to +/-0.3 psig. (26)Normal pressure range for reactor building drywell is equivalent to +1.5 psig to 0.0 psig (+1.2 psid to -0.3 psid).
(27)The design parameters (Temperature, Pressure, Relative Humidity) represent the range of environmental design parameters for general areas or buildings. Refer to design specification 215.150, Environmental Design Criteria, for the requirements of
specific areas.
16 RBS USAR TABLE 9.4-2 DESIGN DATA FOR THE AUXILIARY BUILDING HVAC SYSTEM Equipment Design DataRevision 3 1 of 4 August 1990 1. Main Control Room Air-Conditioning UnitsEquipment Mark No. 1HVC*ACU1A&B This system includes two 100-percent
units and two 100-percent electric
duct heaters 3a. Air-Conditioning Units: Air flow capacity 38,200 scfm Cooling capacity 980 mbh Leaving air temperature 60.6°F dB Chilled water flow 101 gpm 3b. Heating Coils: Equipment Mark No. 1HVC*CH1A&B Type Electric, finned tubular Heating capacity 65 kW 2. Standby Switchgear Room Air-Conditioning UnitsEquipment Mark No. 1HVC*ACU2A&B This system includes two 100-percent
units, two 100-percent return air fans, and six battery rooms exhaust fans (two 100-percent fans for each room) 3a. Air-Conditioning Units: Air flow capacity 29,330 scfm Cooling capacity 950 mbh Heating capacity 50 kW Leaving air temperature 66.2°F dB Chilled water flow 62.3 gpm 3b. Return Air Fans: Equipment Mark No. 1HVC*FN2A&B
Type Vaneaxial Air flow capacity 25,330 scfm Static Pressure 4.5 in W.G.
Equipment Design DataRevision 3 2 of 4 August 1990 c. Battery Rooms Exhaust Fans: Equipment Mark No. 1HVC*FN3A,B,C,D, E,F Type Centrifugal, non-sparking Air flow capacity 1,430 cfm Static pressure 2.6 in W.G. 3. Chiller Equipment Room Air-Conditioning UnitsEquipment Mark No. 1HVC*ACU3A&B This system includes two 100-percent
units, one ventilation supply fan, and
one ventilation exhaust fan 3a. Air-conditioning units: Air flow capacity 3,500 scfm Cooling capacity 165 mbh Leaving air temperature 90.0°F dB Chilled water flow 28 gpm 3b. Supply fans: Equipment Mark No. 1HVC-FN6
Type Centrifugal Air flow capacity 1,100 scfm Static pressure 2 in W.G. c. Exhaust fan: Equipment Mark No. 1HVC-FN11
Type Centrifugal Air flow capacity 1,100 scfm Static pressure 1 in W.G. 4. Main Control Room Charcoal Filter TrainsEquipment Mark No. 1HVC*FLT3A&B This system includes two 100-percent
filter trains with associated boosters
and decay heat removal fans a. Charcoal filter trains: (1) Charcoal filters: Type Deep bed, RBS USAR TABLE 9.4-2 (Cont)
Equipment Design DataRevision 17 3 of 4 Capacity 4,000 cfm Media Impregnated coconut shell charcoal Radioiodine removal 9 8% elemental iodine and 9 8% methyliodine, test at 70% relative humidity Depth of each bed 4 in Face velocity 40 fpm Ignition temperature 340°C Density 30 lbs/ft 3(2) HEPA filters: Type High efficiency, dry Capacity 4,000 cfm Media Fiberglass U.L.
Class I Efficiency, based on 99.97% with
0.3 micron
DOP test (MIL-STD-282) DOP aerosol Pressure drop, clean 1.0 in W.G.
(3) Prefilter: Type Medium efficiency, dry Capacity 4,000 cfm
Media Fiberglass Efficiency 80% NBS dust spot test Pressure drop, clean 0.45 in W.G.
(4) Heater: Type Finned tubular Capacity 23 KW
Stages One (5) Moisture separator: Type Multiple bed Capacity 4,000 cfm 7Media Louvers and Glass or Stainless steel pads 7
Equipment Design Data 4 of 4 August 1987 Pressure drop, clean 1.0 in W.G. b. Booster fans: Equipment Mark No. 1HVC*FN1A&1B
Type Centrifugal Air flow capacity 4,000 cfm Static pressure 20 in W.G. c. Decay heat removal fans: Equipment Mark No. 1HVC*FN8A&B
Type Centrifugal Air flow capacity 100 cfm Static pressure 1.0 in W.G. 5. Smoke Removal Fans Main Control Room Equipment Mark No. 1HVC-FN9
Type Vaneaxial Air flow capacity 13,200 cfm Static pressure 5.7 in W.G.
Standby Switchgear Rooms Equipment Mark No. 1HVC-FN10
Type Centrifugal Air flow capacity 4,000 cfm Static pressure 11 in W.G.
RBSUSARTABLE9.4-3DESIGNDATAFORTHEFUELBUILDINGHVACSYSTEMEquipmentDesignData1of5August19871.SupplyAirSystemAirConditioningUnitEquipmentMarkNo.1HVF-ACU1Totaldesignairflow(outside),cfm9,000Thissystemconsistsofabuiltupair-conditioningunitwithtwo100-percentcapacitysupplyfans.Thefollowingarethemajor componentswithdesigndata:a.FiltersTypeHorizontal,roll Airflowcapacity,cfm9,000 Filterpressuredrop(dirty),inW.G.1.5Facevelocity(Max),fpm475 Filterefficiency(average)20%min(ASHRAEdustspottest)b.HeatingcoilTypeElectricfinned tubeHeatingcapacity,kW57 Numberofstages4c.CoolingcoilDesignpressure/temppsig/°F200/300 TypeChilledwater Totalcoolingcapacity,mbh740.1 No.ofcoils1 No.ofcircuitspercoil30d.SupplyairfanTypeVaneaxial Airflowcapacity,cfm9,000 Totalpressurecapability,inW.G.5.58 Speed,rpm3,500 Motor,hp15 TypeofdischargeHorizontal RBSUSARTABLE9.4-3(Cont)EquipmentDesignDataRevision152of5May20022.UnitCoolersa.CRDWaterPumpAreaEquipmentMarkNo.1HVF-UC1 Coolingcapacityofcooler,mbh190.5 Coolerairflow,cfm7,200 FantypeVaneaxial Motor,hp15 FiltertypeDisposable Filterefficiency(average)20%min(ASHREdustspottest)15b.GeneralAreaEl.70'-0"EquipmentMarkNo.1HVF-UC2 Coolingcapacityofcooler,mbh214.5 Coolerairflow,cfm5,500 FantypeVaneaxial Motor,hp5 FiltertypeDisposable Filterefficiency(average)20%min(ASHRAEdustspottest)c.NewFuelReceivingAreaEquipmentMarkNo.1HVF-UC3 Coolingcapacityofcooler,mbh121.2 Coolerairflow,cfm3,600 FantypeVaneaxial Motor,hp3 FiltertypeDisposable Filterefficiency(average)20%min(ASHRAE)dustspottest) 15d.GeneralAreaEl.113'-0"EquipmentMarkNo.1HVF-UC4 Coolingcapacityofcooler,mbh304.2 Coolerairflow,cfm8,700 FantypeVaneaxial Motor,hp10 FiltertypeDisposable Filterefficiency(average)20%min(ASHRAEdustspottest)e.GeneralArea&FanRoomEquipmentMarkNo.1HVF-UC5 Coolingcapacityofcooler,mbhLTR Coolerairflow,cfm4,200 RBSUSARTABLE9.4-3(Cont)EquipmentDesignData3of5August1987FantypeVaneaxialMotor,hpLTR FiltertypeDisposable Filterefficiency(average)20%min(ASHRAEdustspottest)f.FuelReceivingandCaskWashdownArea EquipmentMarkNo.1HVF-UC6 Coolingcapacity,mbh261.9 Coolerairflow,cfm7,700 FantypeVaneaxial Motor,hpLTR FiltertypeDisposable Filterefficiency20%min(ASHRAEdustspottest)g.GeneralAreaandElectricEquipmentArea EquipmentMarkNo.1HVF-UC7 Coolingcapacityofcooler,mbh342.0 CoolerAirFlow,CFM10,250 FantypeVaneaxial Motor,hpLTR FiltertypeDisposable Filterefficiency(average)20%min(ASHRAEdustspottest)h.CharcoalFilterRoomsEquipmentMarkNo.1HVF-UC8 Coolingcapacityofcooler,mbhLTR Coolerairflow,CFM4,500 FantypeVaneaxial Motor,hpLTR FiltertypeDisposable Filterefficiency(average)20%min(ASHRAEdustspottest)3.ExhaustAirSystemExhaustFansEquipmentMarkNo.1HVF-FN8A&8BTypeVaneaxial Airflowcapacity,cfm10,000 Totalpressurecapability,inW.G.4 Speed,rpm3,500 Motor,hpLTR RBSUSARTABLE9.4-3(Cont)EquipmentDesignData4of5August1987TypeofdischargeHorizontal4.CharcoalFiltrationSystemEquipmentMarkNo.1HVF*FLT2A&2BTotaldesignairflow,cfm10,000Thissystemconsistsoftwo100-percentfilterunitswithtwo100-percentcapacityexhaustfans.Eachfilterunitconsistsof followingcomponents:a.MoistureseparatorsFlowrate,cfm(max)10,000 Pressuredrop,inW.G.1.0 Facevelocity,fpm40b.ElectricheatingcoilCapacity,kW57 Pressuredrop,inW.G.0.5 TypeFinned,tubularc.PrefiltersPressuredrop,inW.G.(dirty)1.0 Filterefficiency80-85%NBSdustspottestDustholdingcapacity300gm FiltermediaFiberglassd.HEPAfiltersEachcell,airflowcapacity,cfm1,000 Filterefficiency99.97%
Pressuredrop,inW.G.1.0 Eachfiltercellsize24"x24"x111/2"e.CharcoalfiltersTypeDeepbed, rechargeableCapacity10,000cfm MediaImpregnatedcoconutshell
charcoalRadioiodineRemoval99%elementaliodineand99%
methyliodine, testat70%
relative RBSUSARTABLE9.4-3(Cont)EquipmentDesignData5of5August1987 humidityDepthofeachbed4in Facevelocity40fpm Pressuredrop,clean1.0inW.G.
Ignitiontemperature340°C Density30lbs/ft³f.ExhaustfanEquipmentMarkNo.1HVF*FN3A&3B TypeCentrifugal Airflowcapacity,cfm10,000 Staticpressure,inW.G.16 Speed,rpm1,720 Motor,hp40g.DecayheatremovalexhaustfanEquipmentMarkNo.1HVF*FN7A&7B TypeCentrifugal Airflowcapacity,cfm100 DriveDirect Staticpressure,inW.G.2.5 Motor,hp0.5h.HeatingcoilsEquipmentMarkNo.1HVF-CH1 TypeFinnedtubular Heatingcapacity,kW8 EquipmentMarkNo.1HVF-CH2 TypeFinnedtubular Heatingcapacity,kW3 RBS USAR Revision 16 1 of 4 March 2003 TABLE 9.4-4 DESIGN DATA FOR THE AUXILIARY BUILDING HVAC SYSTEM Equipment Design Data1. Standby Gas Treatment Units Equipment Mark No. 1GTS*FLT1A & 1B Refer to Section 6.5 for design data of SGTS 16 14 82. Unit Cooler Equipment Mark No. 1HVR*UC2 Cooling capacity (mbh) 187.46 Cooler air flow (cfm) 6,700 Fan type Vaneaxial Motor (hp) 5 Cooling medium Standby service water Flow rate (gpm, max) 50 Leaving air temp dry/wet bulb (°F) 98.03/80.4 15 53. Unit Cooler Equipment Mark No. 1HVR*UC3 Cooling capacity (mbh) 318.22 Cooler air flow (cfm) 13,000 Fan type Vaneaxial Motor (hp) 7.5 Cooling medium Standby service water Flow rate (gpm, max) 100 Leaving air temp dry/wet bulb (°F) 97.87/81.3 4. Unit Cooler Equipment Mark No. 1HVR*UC4 Cooling capacity (mbh) 293.22 Cooler air flow (cfm) 11,800 Fan type Vaneaxial Motor (hp) 7.5 Cooling medium Standby service water Flow rate (gpm, max) 90 Leaving air temp dry/wet bulb (°F) 97.6/81.2 5 8 14 15 16 RBS USAR TABLE 9.4-4 (Cont) Revision 16 2 of 4 March 2003 Equipment Design Data1614 8A 5. Unit Cooler Equipment Mark No. 1HVR*UC5 Cooling capacity (mbh) 721.91 Cooler air flow (cfm) 24,000 Fan type Vaneaxial Motor (hp) 50 Cooling medium Standby service water Flow rate (gpm, max) 185 Leaving air temp dry/wet bulb (°F) 97.35/80.0 8A6. Unit Cooler Equipment Mark No. 1HVR*UC6 Cooling capacity (mbh) 927.68 Cooler air flow (cfm) 31,000 Fan type Vaneaxial Motor (hp) 40 Cooling medium Standby service water Flow rate (gpm, max) 235 Leaving air temp dry/wet bulb (°F) 97.53/80.0 1615 57. Unit Cooler Equipment Mark No. 1HVR*UC7 Cooling capacity (mbh) 486.08 Cooler air flow (cfm) 19,800 Fan type Vaneaxial Motor (hp) 15 Cooling medium Standby service water Flow rate (gpm, max) 150 Leaving air temp dry/wet bulb (°F) 97.85/81.3 5 1538. Unit Cooler Equipment Mark No. 1HVR*UC8 Cooling capacity (mbh) 405.38 Cooler air flow(cfm) 18,000 Fan type Vaneaxial Motor (hp) 15 Cooling medium Standby service water Flow rate (gpm, max) 120 Leaving air temp dry/wet bulb (°F) 97.95/81.3 3 8 14 RBS USAR TABLE 9.4-4 (Cont) Revision 16 3 of 4 March 2003 Equipment Design Data1615 14 859. Unit Cooler Equipment Mark No. 1HVR*UC9 Cooling Capacity(mbh) 692.07 Cooler air flow (cfm) 27,400 Fan type Vaneaxial Motor (hp) 30 Cooling medium Standby service water Flow rate (gpm, max) 210 Leaving air temp dry/wet bulb (°F) 97.16/81.1 10. Unit Cooler Equipment Mark No. 1HVR*UC10 Cooling Capacity(mbh) 118.66 Cooler air flow (cfm) 4,900 Fan type Vaneaxial Motor (hp) 5 Cooling medium Standby service water Flow rate (gpm, max) 37 Leaving air temp dry/wet bulb (°F) 98.06/81.3 11. Unit Cooler Equipment Mark No. 1HVR*UC11A & 11B Cooling Capacity(mbh) 1011.82 Cooler air flow (cfm) 53,000 (11A) and (11B)
Fan type Vaneaxial Motor (hp) 75 Cooling medium Standby service water Flow rate (gpm, max) 410 Leaving air temp dry/wet bulb (°F) 96.94/82.5 5 15 1612. Unit Cooler Equipment Mark No. 1HVR-UC14 Cooling Capacity(mbh) 68.2 Cooler air flow (cfm) 4,570 Fan type Centrifugal Motor (hp) 10 Cooling medium Chilled water Flow rate (gpm, max) 11 Leaving air temp. dry/wet bulb (F°) 62.6/61.7 8 14 RBS USAR TABLE 9.4-4 (Cont) Revision 15 4 of 4 May 2002 Equipment Design Data13. Supply Fans Equipment Mark No. 1HVR-FN6A & 6B Type Vaneaxial direct drive Air flow capacity (cfm) 10,000 Total pressure capability (in W.G.) 6 Speed (rpm) 3550 Motor (hp) 15 Type of discharge Horizontal 14. Roll Type Air Filter Equipment Mark No. 1HVR-FLT2 Total air capacity (cfm) 10,000 Filter pressure drop (dirty) (in W.G.) 1.5 Face velocity (max, fpm) 475 Filter efficiency (average) 85% NBS Filter media thickness (in) 2 15 15. Extended Surface Type Filters Equipment Mark No. 1HVR-FLT7 Total air capacity (cfm) 10,000 Filter pressure drop (dirty)
(in W.G.) 0.7 Face velocity (max, fpm) 475 Filter efficiency (average) 95 ASHRAE 52-76 Filter media thickness (in) 22 1516. Exhaust Fans Equipment Mark No. 1HVR-FN7A & 7B Air flow capacity (cfm) 10,000 Total pressure capability (in W.G.) 6 Speed (rpm) 3550 Motor (hp) 20 Type of discharge Horizontal 17. Electrical Duct Heater Equipment Mark No. 1HVR-CH1 Type Finned tubular Capacity 80 kW Stages 4 RBSUSAR1of4August1987TABLE9.4-5DESIGNDATAFORTHERADWASTEBUILDINGHVACSYSTEMEquipmentDesignData1.IntakeFilterPlenuma.RolltypeairfiltersEquipmentMarkNo.1HVW-FLT4A&B Totalaircapacity(cfm)39,200 Filterpressuredrop(dirty)(inW.G.)1.5Facevelocity(max,fpm)475 Filterefficiency(average)85%NBS Filtermediathickness(in)2b.ExtendedsurfacetypefiltersEquipmentMarkNo.1HVW-FLT5A&5B Totalaircapacity(cfm)39,200 Filterpressuredrop(dirty)(inW.G.)0.7Facevelocity(max,fpm)475 Filterefficiency(average)95ASHRAE52-76 Filtermediathickness(in)222.UnitCoolerSampleRoom,LaundryRoom,andFormaldehyde AreasEquipmentMarkNo.1HVW-UC5A&5BCoolingcapacity(mbh)600 Coolerairflow(cfm)6,300 FantypeVaneaxial Motor(hp)7.5 CoolingmediumChilledwater Leavingairtempdry/wetbulb(°F)59.2/58.9Flowrate(gpm,max)80 Heatingcoil30kW3.UnitCoolerEquipmentMarkNo.1HVW-UC1Coolingcapacity(mbh)612.4 Coolerairflow(cfm)13,700 FantypeVaneaxial Motor(hp)20 CoolingmediumChilledwater Leavingairtempdry/wetbulb(°F)74/70.5Flowrate(gpm,max)80 RBSUSAR2of4August1987TABLE9.4-5(Cont)EquipmentDesignDataHeatingcoil70kW4.UnitCoolerEquipmentMarkNo.1HVW-UC2Coolingcapacity(mbh)1421.8 Coolerairflow(cfm)31,800 FantypeVaneaxial Motor(hp)30 CoolingmediumChilledwater Leavingairtempdry/wetbulb(°F)73.9/70.5Flowrate(gpm,max)187 Heatingcoil160kW5.UnitCoolerEquipmentMarkNo.1HVW-UC3Coolingcapacity(mbh)585.7 Coolerairflow(cfm)13,100 FantypeVaneaxial Motor(hp)15 CoolingmediumChilledwater Leavingairtempdry/wetbulb(°F)74.1/70.5Flowrate(gpm,max)76 Heatingcoil63kW6.UnitCoolerEquipmentMarkNo.1HVW-UC4Coolingcapacity(mbh)603.6 Coolerairflow(cfm)13,500 FantypeVaneaxial Motor(hp)20 CoolingmediumChilledwater Leavingairtempdry/wetbulb(°F)74/70.5Flowrate(gpm,max)78 Heatingcoil65kW7.CharcoalFiltrationUnitEquipmentMarkNo.1HVW-FLT1A&1B Eachfilterunitconsistsofthefollowingcomponents:
a.MoistureSeparator(Demister)Flowrate(cfm)4,000 RBSUSAR3of4August1987TABLE9.4-5(Cont)EquipmentDesignDataPressuredrop(inW.G.)1.0Facevelocity(fpm,max)250b.ElectricheatingcoilCapacity(kW)57 Pressuredrop(inW.G.)0.5 TypeFinned,tubularc.PrefiltersPressuredrop(inW.G.,clean)0.45 Filterefficiency78%average ASHRAE 52-68dustspot
testDustholdcapacity300gm FiltermediaFiberglassd.HEPAFiltersEachcellairflowcapacity(cfm)1000 Filterefficiency(DOPtest)99.97 Pressuredrop(inW.G.)1.0 Eachfiltercell(size)24"x24"x111/2"e.CharcoalFiltersTypeRechargeable Filterefficiencyforremovalofelementaliodine(at90%rh)95%
methyliodine(at90%rh)95%Filterpressuredrop(inW.G.)(clean/dirty)1.0/2.0f.CharcoalFilterExhaustFansEquipmentMarkNo.1HVW-FN4A&4B TypeCentrifugal Airflowcapacity(cfm)4,000 Staticpressure(inW.G.)19 Speed(rpm)3,550 Motor(hp)Ltrg.DecayHeatRemovalExhaustFanEquipmentMarkNo.1HVW-FN5A&5B TypeCentrifugal Airflowcapacity(cfm)100 Staticpressure(inW.G.)2.2 RBSUSARRevision154of4May2002TABLE9.4-5(Cont)EquipmentDesignDataSpeed(rpm)3,450Motor(hp)0.5158.MainExhaustFansEquipmentMarkNo.1HVW-FN1A,1B,&1C TypeVaneaxial Airflowcapacity(cfm)38,200 Staticpressure(inW.G.)6 Speed(rpm)1750 Motor(hp)50 159.ExhaustFilterPlenuma.RollTypeAirFiltersEquipmentMarkNo.1HVW-FLT7&8 Totalaircapacity(cfm)38,200 Filterpressuredrop(dirty)(inW.G.)1.5Facevelocity(max,fpm)475 Filterefficiency(average)85%NBS Filtermediathickness(in)2b.ExtendedSurfaceTypeFiltersEquipmentMarkNo.1HVW-FLT9&10 Totalaircapacity(cfm)38,200 Filterpressuredrop(dirty)(inW.G.)0.7Facevelocity(max,fpm)475 Filterefficiency(average)95ASHRAE52 Filtermediathickness(in)22 RBS USAR TABLE 9.4-6 COMPARISON OF NORMAL CHARCOAL FILTRATION SYSTEMS WITH REGULATORY GUIDE 1.140 REQUIREMENTS Radwaste Building Air Removal Tank Exhaust Containment Purge Hogging Pump
Paragraph No. Filtration System Filtration System System C-1 "Environmental Design Criteria" 1.a In compliance In compliance In compliance 1.b In compliance In compliance In compliance 1.c In compliance In compliance In compliance 1.d In compliance In compliance In compliance C-2 "System Design Criteria" 2.a In compliance In compliance In compliance 2.b In compliance In compliance In compliance 2.c In compliance In compliance In compliance 2.d In compliance In compliance In compliance 2.e In compliance In compliance In compliance 2.f (1) (1) (1)
C-3 "Component Design Criteria and Qualifications Testing" 3.a In compliance In compliance In compliance 3.b In compliance In compliance In compliance 3.c (2) (2) (2) 3.d In compliance In compliance In compliance 3.e In compliance In compliance In compliance 3.f In compliance In compliance In compliance 3.g (3) (3) (3) 3.h (4) (4) (4) 3.i (5) (5) (5) 3.j In compliance In compliance In compliance 3.k (6) (6) (6) 3.l (7) (7) (7) 3.m In compliance In compliance In compliance C-4 "Maintenance" 4.a In compliance In compliance In compliance 4.b In compliance In compliance In compliance 4.c In compliance In compliance In compliance 4.d In compliance In compliance In compliance C-5 "In-Place Testing Criteria" 5.a In compliance In compliance In compliance 5.b In compliance In compliance In compliance 5.c In compliance In compliance In compliance 5.d In compliance In compliance In compliance
C-6 "Laboratory Testing Criteria for Activated Carbon" 6.a (9) (9) (9) 6.b (10)(10)(10)
______________________________(1) Exception is taken to the amount of allowable air leakage in HVAC non-ESF charcoal filtration systems set by ANSI N509, 1980. See Table 1.8-1, Regulatory Guide 1.140 position. (2) For HEPA filters and adsorber mountings, requirements of ANSI N509-1980 Section 5.6.3 are complied with except for the tolerance requirements. Tolerances for HEPA filters and adsorber mounting frames are sufficient to
pass the bank leak tests of paragraphs 5.c and 5.d of the guide. (3) Bed depths of charcoal adsorber units at RBS are 4 in, with a minimum residence time of 0.5 sec. Verification of filter efficiency is the objective; thus HEPA filters are tested in the shop and in the field for
efficiency. Upon installation, and periodically thereafter, the filters are DOP tested in accordance with
ANSI N510-1980. (4) Exception is taken to Section 5.2.2.4 of ANSI N509-1980 which calls for a means of compaction to uniform density. Where uniform compaction can be demonstrated, compacting means are not required. (5) 1. System resistances are determined in accordance with Section 5.7.1 of ANSI N509-1980 except that fan inlet and outlet losses are not calculated in accordance with AMCA 201. 2. Exception is taken to Section 5.7.2 of ANSI N509-1980. Copies of fan ratings or test reports are not necessary when certified fan performance curves are furnished. 3. Exception is taken to Section 5.7.3 of ANSI N509-1980. Balancing techniques specified need not be followed. Maximum permissible vibration velocity level method need not be complied with. 4. Exception is taken to Section 5.7.5 of ANSI N509-1980. Where AMCA certification ratings are submitted, documentation is not furnished. (6) Airflow distribution is within +/-20 percent of the average airflow as tested in accordance with ANSI N510-1980.
Turning vanes are provided only where a uniform air distribution cannot be achieved.
RBS USAR TABLE 9.4-6 (Cont) Revision 17 3 of 3 (7) Exception is taken to Section 5.9 of ANSI N509-1980: 1. Dampers are not designed to the specification of ANSI B31.1.
- 2. Butterfly valves are not used.
- 3. Leakage rates for construction Class B, Leakage Class II and III are determined for one damper of each type instead of for every damper. 4. Dampers with shaft lengths of 24 in have a minimum shaft diameter of 1/2 in. Dampers with shaft lengths
>24 in and 48 in have a minimum shaft diameter of 3/4 in. (Note: Items 1 and 2 do not pertain to containment penetrations.)
(8) Deleted.
(9) Exception is taken to the requirement that new activated carbon meets the physical property specification given in Table 1 of Regulatory Guide 1.140, 1979. The charcoal adsorbent now commercially available does not meet
the physical requirements of Table 1, but does meet the requirements of ANSI/ASME N509-1980.(10)Exception is taken to the requirements of conducting laboratory tests of representative samples as indicated in Table 2 of Regulatory Guide 1.140. Representative samples will be tested in accordance with ASTM D3803-1979.
RBSUSAR1of11 August1987TABLE9.4-7DESIGNDATAFORTURBINEBUILDINGVENTILATIONSYSTEMEquipmentDesignData1.MainSupplySubsystemAir-ConditioningUnitEquipmentMarkNo.1HVT-ACU1Totaldesignairflow,cfm34,000Thissubsystemconsistsofabuilt-upair-conditioningunitwithtwo50-percentcapacitysupplyfans.Thefollowingarethemajor componentswithdesigndata:a.FilterTypeHorizontal,roll Airflowcapacity,cfm34,000 Filterpressuredrop(dirty)inW.G.1.5Facevelocity(max),fpm500 Filterefficiency(average)20%min(ASHRAEdustspottest)b.HeatingcoilTypeElectric,finned tubeHeatingcapacity,kW200 Numbersofstages7c.CoolingcoilTypeChilledwater Totalcoolingcapacity,mbh1,335 No.ofcoils/No.ofcircuitspercoil2/27Designpressure/temp.,psig/°F200/300d.Supplyairfans,two50-percent capacityTypeVaneaxial Airflowcapacityeach,cfm17,000 Totalpressurecapability,inW.G.7.56Speed,rpm35 Motor,hp30 TypeofdischargeHorizontal RBSUSARTABLE9.4-7(Cont)EquipmentDesignData2of11August19872.UnitCoolersSubsystema.Unitcooler-generalareaNEEquipmentMarkNo.1HVT-UC1A Coolingcapacity,mbh244.7 Coolerairflow,cfm8,000 FantypeVaneaxial Motor,hp10 CoolingmediumChilledwaterb.Unitcooler-generalareanorthEquipmentMarkNo.1HVT-UC1B Coolingcapacity,mbh244.7 Coolerairflow,cfm8,000 FantypeVaneaxial Motor,hp10 CoolingmediumChilledwaterc.Unitcooler-aircompressorareaEquipmentMarkNo.1HVT-UC2 Coolingcapacity,mbh576.9 Coolerairflow,cfm18,000 FantypeVaneaxial Motor,hp7.5 CoolingmediumChilledwaterd.Unitcoolers-reactorfeedpumpareaEquipmentMarkNo.1HVT-UC3A,3B,3C
&3DCoolingcapacity,mbh576.9 Coolerairflow,cfm18,000 FantypeVaneaxial Motor,hp7.5 CoolingmediumChilledwatere.Unitcoolers-reactorfeedpumpareaEquipmentMarkNo.1HVT-UC4A,4B Coolingcapacity,mbh244.7 Coolerairflow,cfm8,000 FantypeVaneaxial Motor,hp5 CoolingmediumChilledwater RBS USAR TABLE 9.4-7 (Cont)
Equipment Design DataRevision 15 3 of 11 May 2002 f. Unit coolers - condenser and CCW pump area Equipment Mark No. 1HVT-UC5A&5B Cooling capacity, mbh 576.9 Cooler airflow, cfm 18,000 Fan type Vaneaxial Motor, hp 7.5 Cooling medium Chilled water g. Unit cooler - chiller area Equipment Mark No. 1HVT-UC6 Cooling capacity, mbh 576.9 Cooler airflow, cfm 18,000 Fan type Vaneaxial Motor, hp 7.5 Cooling medium Chilled water h. Unit coolers - chiller area Equipment Mark No. 1HVT-UC7&8 Cooling capacity, mbh 244.7 Cooler airflow, cfm 8,000 Fan type Vaneaxial Motor, hp 5 Cooling medium Chilled water i. Unit cooler - condenser tube withdrawal area Equipment Mark No. 1HVT-UC9 Cooling capacity, mbh 244.7 Cooler airflow, cfm 8,000 Fan type Vaneaxial Motor, hp 5 Cooling medium Chilled water 15 j. Unit cooler - condenser cubicle north Equipment Mark No. 1HVT-UC10 Cooling capacity, mbh 244.7 Cooler airflow, cfm 3,600 Fan type Vaneaxial Motor, hp 5 Cooling medium Chilled water 15 RBSUSARTABLE9.4-7(Cont)EquipmentDesignData4of11August1987k.Unitcooler-steamtunnelEquipmentMarkNo.1HVT-UC11 Coolingcapacity,mbh1452.5 Coolerairflow,cfm24,000 FantypeVaneaxial Motor(2),hp40 CoolingmediumChilledwaterl.Unitcooler-lubeoilpurifierroomEquipmentMarkNo.1HVT-UC12 Coolingcapacity,mbh244.7 Coolerairflow,cfm8,000 FantypeVaneaxial Motor,hp10 CoolingmediumChilledwaterm.Unitcooler-switchgearareaandheaterbayEquipmentMarkNo.1HVT-UC13 Coolingcapacity,mbh244.7 Coolerairflow,cfm8,000 FantypeVaneaxial Motor,hp10 CoolingmediumChilledwatern.Unitcooler-heaterbayareaEquipmentMarkNo.1HVT-UC14A&B Coolingcapacity,mbh1217.5 Coolerairflow,cfm24,000 FantypeVaneaxial Motor,hp50 CoolingmediumChilledwatero.Unitcooler-generalareaEquipmentMarkNo.1HVT-UC15 Coolingcapacity,mbh244.7 Coolerairflow,cfm8,000 FantypeVaneaxial Motor,hp10 CoolingmediumChilledwater RBSUSARTABLE9.4-7(Cont)EquipmentDesignData5of11August1987p.Unitcooler-generalandairremovalpumpareaandgeneral areasouthEquipmentMarkNo.1HVT-UC16A,B,C&17 Coolingcapacity,mbh244.7 Coolerairflow,cfm8,000 FantypeVaneaxial Motor,hp16A,B,C5 1710CoolingmediumChilledwaterq.Unitcooler-airejectionandPRVcubicleEquipmentMarkNo.1HVT-UC18A,B&C Coolingcapacity,mbh68.3 Airflowcapacity,cfm1,300 FantypeCentrifugal Motor,hp1.5 CoolingmediumChilledwaterr.Unitcooler-moistureseparator/reheaterareaeastEquipmentMarkNo.1HVT-UC19A&B Coolingcapacity,mbh741.4 Airflowcapacity,cfm14,000 FantypeVaneaxial Motor,hp20 CoolingmediumChilledwaters.Unitcooler-turbinewellEquipmentMarkNo.1HVT-UC20 Coolingcapacity,mbh1541.4 Airflowcapacity,cfm(2fanseach20,000cfm)40,000FantypeVaneaxial Motor(2),hp30 CoolingmediumChilledwatert.Unitcooler-moistureseparator/reheaterareawestEquipmentMarkNo.1HVT-UC21A&21B Coolingcapacity,mbh1057.3 RBSUSARTABLE9.4-7(Cont)EquipmentDesignData6of11August1987Airflowcapacity,cfm22,000FantypeVaneaxial Motor,hp30 CoolingmediumChilledwateru.Unitcooler-generalareanorthEquipmentMarkNo.1HVT-UC22 Coolingcapacity,mbh244.7 Airflowcapacity,cfm8,000 FantypeVaneaxial Motor,hp16A,B,C5 1710CoolingmediumChilledwaterv.Unitcooler-steamseal evaporator/radwaste reboilerareaEquipmentMarkNo.1HVT-UC23A&B Coolingcapacity,mbh68.3 Airflowcapacity,cfm1300 FantypeCentrifugal Motor,hp1.5 CoolingmediumChilledwaterw.Unitcoolers-generalareael123'-5"EquipmentMarkNo.1HVT-UC24A,B,C&D Coolingcapacity,mbh244.7 Airflowcapacity,cfm8,000 FantypeVaneaxial Motor,hp10 CoolingmediumChilledwaterx.Unitcooler-generalareaiodinefilterroomEquipmentMarkNo.1HVT-UC25A&B Coolingcapacity,mbh244.7 Airflowcapacity,cfm8,000 FantypeVaneaxial Motor,hp5 CoolingmediumChilledwatery.Unitcooler-roofabovemoistureseparator RBSUSARTABLE9.4-7(Cont)EquipmentDesignData7of11August1987EquipmentMarkNo.1HVT-UC26Coolingcapacity,mbh1217.5 Airflowcapacity,cfm24,000 FantypeVaneaxial Motor,hp50 CoolingmediumChilledwater3.Off-gasarea/condensatedemineralizerareaareaventilationsubsystema.Unitcooler-condensatedemineralizertankareaEquipmentMarkNo.1HVT-UC27 Coolingcapacity,mbh72.0 Airflowcapacity,cfm1,300 FantypeVaneaxial Motor,hp1 CoolingmediumChilledwaterb.Unitcooler-condensatedemineralizersolutionareaEquipmentMarkNo.1HVT-UC28 Coolingcapacity,mbh79 Airflowcapacity,cfm2,600 FantypeVaneaxial Motor,hp1.5 CoolingmediumChilledwaterc.Unitcooler-condensatedenimeralizertankcubicleEquipmentMarkNo.1HVT-UC29 Coolingcapacity,mbh374.7 Airflowcapacity,cfm7,000 FantypeVaneaxial Motor,hp7.5 CoolingmediumChilledwaterd.Unitcooler-glycoltankandpumpareaandhydrogen analyzerareaEquipmentMarkNo.1HVT-UC30 Coolingcapacity,mbh345.9 Airflowcapacity,cfm11,400 FantypeVaneaxial Motor,hp7.5 CoolingmediumChilledwater RBSUSARTABLE9.4-7(Cont)EquipmentDesignData8of11August1987e.Unitcooler-regenerator/desiccantdryercubicleEquipmentMarkNo.1HVT-UC31A&B Coolingcapacity,mbh39.5 Airflowcapacity,cfm1,300 FantypeVaneaxial Motor,hp1 CoolingmediumChilledwaterf.Unitcooler-off-gascondenser cubicleEquipmentMarkNo.1HVT-UC32 Coolingcapacity,mbh237.2 Airflowcapacity,cfm6,000 FantypeVaneaxial Motor,hp5 CoolingmediumChilledwaterg.Off-gasrefrigerationunitsEquipmentMarkNo.N64B012A&B Coolingcapacity,Btu/hrattemperature-40°F72,000Airflowcapacity,cfm6,500 Airhandlingunitexternalstaticpressure,inW.G.2.0Temperatureofcondensingwater°F105Maximumwaterheadloss,ft15 Watersidedesignpressure,psig150 Foulingfactor,waterside0.0005 Condenserwaterflowrate,gpm42 RefrigeranttypeR-224.ExhaustAirSubsystema.MainexhaustfansEquipmentMarkNo.1HVT-FN1A,B&C Airflowcapacity,cfm22,000 Totalpressurecapability,inW.G.11.75Speed,rpm3,500 Motor,hp60 TypeofdischargeHorizontalb.Off-gasareaexhaustfansEquipmentMarkNo.1HVT-FN2A&B RBS USAR TABLE 9.4-7 (Cont)
Equipment Design DataRevision 15 9 of 11 May 2002 15 Airflow capacity, cfm 7,700 Total pressure capability, in W.G. 9.25 Speed, rpm 3,500 Motor, hp 20 Type of discharge Horizontal 155. Charcoal Filtration Subsystem Equipment Mark No. 1HVT-FLT1 Each filter unit consists of the following components: a. Moisture separator (demister) Flow rate, cfm 5,000 Pressure drop, in W.G. 1.0 Face velocity, fpm (max) 40 b. Electric heating coil Capacity, kW 25 Pressure drop, in W.G. 0.5 Type Finned, tubular c. Prefilters Pressure drop, in W.G. (clean) 0.45 Filter efficiency 78% average ASHRAE 52-68 dust spot test Dust holding capacity, gm 300 Filter media Fiberglass d. HEPA filters Each cell, airflow capacity, cfm 1,000 Filter efficiency, DOP test 99.97% Pressure drop, in W.G. 1.0 Each filter cell size 24"x24"x11 1/2" e. Charcoal Filters Type Rechargeable Filter efficiency for removal of Elemental iodine (at 90% RH) 95%
Methyl iodide (at 90% RH) 95%
Filter pressure drop, in W.G.
(clean/dirty) 1.0/2.0 RBSUSARTABLE9.4-7(Cont)EquipmentDesignData10of11August1987f.CharcoalfilterexhaustfanEquipmentMarkNo.1HVT-FN3 TypeCentrifugal Airflowcapacity,cfm5,000 Staticpressure,inW.G.16.5 Speed,rpm3,500 Motor,hp30g.DecayheatremovalexhaustfanEquipmentMarkNo.1HVT-FN4 TypeCentrifugal Airflowcapacity,cfm100 Staticpressure,inW.G.3.8 Speed,rpm3,500 Motor,hp1/36.SampleRoomAir-ConditioningSystema.AirConditioningUnitEquipmentMarkNo.1HVT-ACU2 Airflowcapacity,cfm4,000 FiltertypeDisposableCoolingcoilTypeDirectExpansion Coolingcapacity,mbh222.1 Enteringairtemp,db/w.b.°F81.8/69.5 Leavingairtemp,db/w.b.°F55/53.5SupplyFanAirflow,cfm4,000 Totalpressurecapability,inW.G.1.0TypeofdischargeHorizontal HeatingTypeElectricOpen-TypeCapacity,kW40b.WaterCooledCondensingUnitEquipmentMarkNo.1HVT-CUR2 Capacity,mbh222.1 Enteringcondenserwatertemp,°F96 Leavingwatertemp,°F106 RBSUSARTABLE9.4-7(Cont)EquipmentDesignData11of11August1987c.HeatingSystemUnitHeaterGeneralArea SouthEquipmentMarkNo.1HVT-UH1 TypeElectric Capacity,kW40UnitHeaterGeneralArea Heating BayEquipmentMarkNo.1HVT-UH2 TypeElectric Capacity,kW30UnitHeaterFireProtection RoomEquipmentMarkNo.1HVT-UH3andUH4TypeElectric Capacity,kW5HeatingCoilAreaAbove Moisture SeparatorEquipmentMarkNo.1HVT-CH1 TypeElectric-Finned TubularCapacity,kW89.4HeatingCoilOffgasBldgGlycolTank andPumpAreaEquipmentMarkNo.1HVT-CH2 TypeElectric-Finned TubularCapacity,kW12 RBSUSARTABLE9.4-7(Cont)EquipmentDesignDataRevision411aof11August199147.SteamTunnelAirConditioningSystemA.AirConditioningUnitEquipmentMarkNo.1HVT-ACU4AAirFlowCapacity,CFM14,000 CoolingCoilTypeDirectExpansion CoolingCapacity,BTUs/Hr300,000B.AirConditioningUnitEquipmentMarkNos.1HVT-ACU4B,4CAirFlowCapacity,CFM7,000each CoolingCoilTypeDirectExpansion CoolingCapacity,BTUs/Hr150,000eachC.AirCooledCondensingUnitEquipmentMarkNos.1HVT-CUR4and5 Capacity,BTUs/Hr600,000each RBS USAR Revision 15 1 of 3 May 2002 TABLE 9.4-8 DESIGN DATA FOR THE ENGINEERED SAFETY FEATURES VENTILATION SYSTEMS
Equipment Design Data
Diesel Generator
Rooms Exhaust Fans 15 Equipment Mark No. 1HVP*FN2A & B Type Vaneaxial Capacity 110,000 cfm Static pressure 1.75 in W.G.
Motor 100 hp
Equipment Mark No. 1HVP*FN3A Type Vaneaxial Capacity 131,000 cfm Static pressure 3.5 in W.G.
Motor 100 hp
Diesel Generators 1A & B
Control Room Supply Fans
Equipment Mark No. 1HVP*FN6A & B Type Centrifugal Capacity 3,500 cfm Static pressure 1.7 in W.G. (FN6A) 2.8 in W.G. (FN6B)
Motor 2 & 3 hp
Diesel Generator 1C Control
Room Supply Fan
Equipment Mark No. 1HVP*FN6C Type Centrifugal Capacity 2,000 cfm Static pressure 0.75 in W.G.
Motor 1 hp 15 Diesel Generator Rooms Unit Heaters
Equipment Mark No. 1HVP-UH1A, B, & C 1HVP-UH2A, B, & C Type Electric unit heater Capacity 7.5 kW
Equipment Mark No. 1HVP-UH3A, B, & C 1HVP-UH4A, B, & C RBS USAR TABLE 9.4-8 (Cont)
Equipment Design Data Revision 16 2 of 3 March 2003 Type Electric unit heater Capacity 5 kW
Pump House Pump Rooms Supply Fans 16 Equipment Mark No. 1HVY*FN1A, 1B, 1C, & 1D Type Vaneaxial Capacity 15,000 cfm (NOTE 1)
Static pressure 2 in W.G.
Motor 7.5 hp 6 SSW Cooling Tower Pump House Pump Rooms Unit Heaters
Equipment Mark No. 1HVY-UH17 & 18 Type Electric unit heater Capacity 10 kW
Switchgear Rooms Supply Fans
Equipment Mark No. 1HVY*FN2A, 2B, 2C, & 2D Type Vaneaxial Capacity 6,200 cfm (NOTE 2)
Static pressure 1.5 in W.G.
Motor 3 hp 16 SSW Cooling Tower Switchgear Rooms Unit Heaters
Equipment Mark No. 1HVY-UH15 & 16 Type Electric unit heater Capacity 10 kW 6 SSW Cooling Tower Remote Air Intake Room Supply Fans 15 Equipment Mark No. 1HVY*FN32A & 32B Type Vaneaxial Capacity 3,600 cfm Static pressure 1.25 in W.G.
Motor 5 hp 15 RBS USAR TABLE 9.4-8 (Cont)
Equipment Design Data Revision 16 3 of 3 March 2003 SSW Cooling Tower Remote Air Intake Electric Duct Heaters
Equipment Mark No. 1HVY*CH6A & 6B Type Finned tubular Capacity 12 kW
16 Notes: 1.The ventilation system capacity for pump room is ~20000 cfm when both fans (HVY-FN1A&C or HVY-FN1B&D) operate
simultaneously.
2.The ventilation system capacity for switchgear room is ~10000 cfm when both fans (HVY-FN2A&C or HVY-FN2B&D) operate
simultaneously.
16 RBSUSARTABLE9.4-9DESIGNDATAFORREACTORBUILDINGVENTILATIONSYSTEMEquipmentDesignData1of5August19871.ContainmentVentilationSystema.ContainmentunitcoolersEquipmentMarkNo.1HVR*UC1A,1B&1HVR-UC1CEachcontainmentunitcoolerconsistsofthefollowing
components:
FiltersTypeDisposable, fiberglassAirflowcapacity,cfm50,000 Filterpressuredrop(dirty),inW.G.0.50Facevelocity(max),fpm480 FilterEfficiency(average)ASHRAE52-6820CoolingcoilsDesignpressure,psig200Designtemperature,°F300 TypeChilledwater/servicewaterTotalcoolingcapacity,normal,mbh2,543 LOCA,mbh23,000Flowratenormal,gpm350 LOCA,gpm540SupplyairfanTypeVaneaxialAirflowcapacity,cfm50,000 Totalpressurecapability,inW.G.7.5Speed,rpm1,750 Motor,hp150b.RecirculationfansEquipmentMarkNo.1HVR-FN1A,1B,1C&1DTypeVaneaxial RBS USAR TABLE 9.4-9 (Cont)
Equipment Design DataRevision 16 2 of 5 March 2003 Airflow capacity, cfm 7,400 Total pressure capability, in W. G. 1.01 Speed, rpm 1,170 Motor, hp 2.0 2. Drywell Ventilation SystemDrywell coolers Equipment Mark No. 1DRS-UC1A, B, C, D, E, & F
Each drywell cooler consists of the
following components:
Filters Type Disposable, fiberglass Airflow capacity, cfm 28,000
Filter pressure drop (dirty), in W.G. 0.5 Face velocity (max), fpm 480
Filter efficiency (average)
ASHRAE 52-68 20 Cooling coils1615Total cooling capacity, mbh 2680.6 Design pressure, psig 200 Design temperature, °F 300 Type Chilled water Flow rate, gpm 334 Leaving air temp db/wb, °F 114/111.7 15 1610 Supply air fan Type Vaneaxial Airflow capacity, cfm 28,000 Total pressure capability, in W.G. 8.78 Speed, rpm 3,500 Motor, hp 60 3. Annulus Pressure Control System (Exhaust Fans)Equipment Mark No. 1HVR-FN16A & 16B Type Centrifugal Airflow capacity, cfm 2,000 10 RBSUSARTABLE9.4-9(Cont)EquipmentDesignDataRevision153of5May2002Totalpressurecapability,inW.G.8.20Speed,rpm1,750 Motor,hp54.ContainmentandDrywellPurgeSystem15a.SupplyfanEquipmentMarkNo.1HVR-FN8 TypeVaneaxial Airflowcapacity,cfm12,500 Totalpressurecapability,inW.G.8.43Speed,rpm3,535 Motor,hp50 15b.SupplyfanEquipmentMarkNo.1HVR-FN13 TypeCentrifugal Airflowcapacity,cfm7,000 Totalpressurecapability,inW.G.2.0Speed,rpm1,150 Motor,hp5c.CharcoalfilterunitEquipmentMarkNo.1HVR-FLT6 Thecharcoalfilterunitconsistsofthefollowing
components:Moistureseparator(demister)Flowrate,cfm7,000Pressuredrop,inW.G.1.0 Facevelocity,fpm(max)40ElectricheatingcoilCapacity,kW32.0Pressuredrop,inW.G.0.5 TypeFinned,tubular PrefilterPressuredrop,inW.G.(clean)0.45Filterefficiency78%averageASHRAE52-68 dustspottest RBS USAR TABLE 9.4-9 (Cont)
Equipment Design DataRevision 18 4 of 5 Dust holding capacity, gm 300 Filter media Fiberglass d. HEPA filters Each cell airflow capacity, cfm 1,000 Filter efficiency DOP test 99.97%
Pressure drop, in W.G. 1.00 Each filter size 24" x 24" x 11 1/2" e. Charcoal filters Type Rechargeable
Filter efficiency for
removal of elemental iodine (at 90% RH) 95 Methyl iodide (at 90% RH) 95
Filter pressure drop, in W.G.
(clean) 1.0 (dirty) 2.0 f. Charcoal filter exhaust fan Equipment Mark No. 1HVR-FN14
Type Centrifugal Airflow capacity, cfm 7,000 Static pressure, in W.G. 16.25 Speed, rpm 3,600 Motor, hp 30 g. Decay heat removal exhaust fan Equipment Mark No. 1HVR-FN15
Type Centrifugal Airflow capacity, cfm 100 Static pressure, in W.G. 2.9 Speed, rpm 1,750 Motor, hp 1 5. Annulus Mixing System (Disabled)Equipment Mark No. 1HVR*FN11A & 11B Type Centrifugal Airflow capacity, cfm 52,500
Total pressure capability, in W.G. 12 Speed, rpm 1,180 Motor, hp 150 RBSUSARTABLE9.4-9(Cont)EquipmentDesignData5of5August19876.ContainmentHeatingEquipmentMarkNo.1HVR-CH2TypeElectricFinned TubeCapacity,kW130 RBS USAR TABLE 9.4-10 DESIGN DATA FOR THE MISCELLANEOUS BUILDINGS' HVAC SYSTEMS Revision 15 1 of 5 May 2002 1. Fire Pump House
- a. Exhaust Fans Equipment Mark Nos. 1HVY-FN3, 4, and 6 1HVY-FN5 and 7 Type Vaneaxial Vaneaxial Airflow capacity, cfm 8,000 25,080 Total pressure capability, in W.G. 0.375 0.375 Speed, rpm 1,750 875 Motor, hp 3 7.5 Type of Discharge Horizontal Horizontal
- b. Unit Heaters Equipment Mark No. 1HVY-UH1, 2, 3, 4, and 5 Capacity, kW 10 Air volume, cfm 750 Minimum throw, ft 27
- 2. Normal Switchgear Building 15 a. Air Conditioning Units Equipment Mark Nos. 1HVY-ACU2 1HVY-ACU3A and B Filter type Disposable Disposable Airflow capacity, cfm 4,860 37,100 15 Cooling coil Type Direct Exp. Direct Exp. Cooling capacity, mbh 401 1476 Entering air temp., db/wb o F 88/74 96/81 Leaving air temp., db/wb o F 56/54 74/72 Supply fan Airflow, cfm 6,100 37,100 Total pressure capability, in W.G.
1.2 2.7 Type of discharge Vertical Horizontal Motor, hp 10 30 b. Air-Cooled Condensing Units Equipment Mark Nos. 1HVY-CUR2 1HVY-CUR3A and B Capacity, mbh 401 1476 Entering air temp, condenser o F 96 96 Number of unloading steps 3 3 Refrigerant type R-22 R-22 Starting and operating low ambient temp o F 30 30 RBS USAR TABLE 9.4-10 (Cont)
Revision 15 2 of 5 May 2002 c. Exhaust Fans 15 Equipment Mark No.
1HVY-FN19A and B Type Vaneaxial Airflow capacity, cfm 27,230 Total pressure capability, in W.G.
2.5 Type of Discharge Horizontal
- d. Battery Room Exhaust Fan Equipment Mark No. 1HVY-FN21 Type Centrifugal Airflow Capacity, cfm 3,750 Total pressure capability, in W.G. 1.5 Type of discharge Top horizontal 15 3. Auxiliary Boiler Building
- a. Switchgear Room Air Conditioning Unit Equipment Mark No. 1HVI-ACU1 Filter type Disposable Airflow capacity, cfm 8,400 Cooling coil, type Direct Expansion Cooling capacity, mbh 30.05 Leaving air temp.
o F db/wb 74/73 Entering air temp.
o F db/wb 96/81 Supply fan, type Airfoil Airflow, cfm 8,400 Type of discharge Horizontal
- b. Air Cooled Condensing Unit Equipment Mark No. 1HVI-CUR1 Entering air temp, condenser o F 96 Number of unloading steps 3 Refrigerant type R-22 Starting and operating low ambient temp o F 30 c. Exhaust Fan 15 Equipment Mark No.
1HVI-FN3 Type Vaneaxial Airflow capacity, cfm 7,850 Type of discharge Horizontal 15 d. Boiler Room Exhaust Fans Equipment Mark No. 1HVI-FN1 and 2 Type Roof Ventilator Airflow capacity, cfm 4,600 Type of discharge Up, Vertical
Revision 15 3 of 5 May 2002
- 4. Water Treatment Building
- a. Air Handling Unit Equipment Mark No. 1HVJ-AHU1 Filter, type Roll Max. face velocity, fpm 500 Heating coil, type Electric Capacity, kW Supply fan, type Airfoil Airflow capacity, cfm 22,850 Total pressure capability, in W.G.LTR Type of discharge Horizontal
- b. Exhaust Fan 15 Equipment Mark No.
1HVJ-FN1 Type Vaneaxial Airflow capacity, cfm 22,430 Type of discharge Horizontal
- 5. Makeup Water Intake Structure and Switchgear House
- a. Supply Fans Equipment Mark No. 1HVY-FN23A and B Type Vaneaxial Airflow capacity, cfm 42,350 Type of discharge Horizontal
- b. Exhaust Fans Equipment Mark No. 1HVY-FN22A and B Type Vaneaxial Airflow capacity, cfm 42,250 Type of discharge Horizontal 15 8 c. Heating and Ventilation Unit - Switchgear Area Equipment Mark No.
1HVY-ACU1 Filter type Disposable Airflow capacity, cfm 550 Cooling Coil Type N/A Cooling Capacity, mbh N/A Entering air temp o F db/wb 96/81 Supply Fan Airflow, cfm 550 Type of discharge Horizontal 8 RBS USAR TABLE 9.4-10 (Cont)
Revision 15 4 of 5 May 2002 6. Electrical and Piping Tunnels
- a. Supply Fans 15 Equipment Mark Nos.
1HVY-FN11 and 14 1HVY-FN18 1HVY-FN12 Type Vaneaxial Vaneaxial Vaneaxial Airflow capacity, cfm 3,800 (FN11) 2,500 15,000 5,000 (FN14) Total pressure capability, in W.G. 1.5 1.0 1.0 Type of discharge Horizontal Horizontal Horizontal
- b. Supply Fans Equipment Mark Nos. 1HVY-FN8 1HVY-FN9 and 10 Type Vaneaxial Vaneaxial Airflow capacity, cfm 7,500 4,600 Total pressure capability, in W.G. 1.0 2.0 Type of discharge Horizontal Horizontal/Vertical 15 8 Equipment Mark No.
1HVY-FN17 Type Vaneaxial Airflow capacity, cfm 7,500 Total pressure capability, in W.G. 1.5 Type of discharge Horizontal 8 c. Exhaust Fans 9 Equipment Mark Nos.
1HVY-FN15A and B 1HVY-FN16A and B Type Vaneaxial Vaneaxial Airflow capacity, cfm 30,500 28,000 9 d. Heating Coils Equipment Mark Nos. 1HVY-CH12 1HVY-CH13 Type Elec Finned Tube Elec Finned Tube Capacity 39.2 30 Equipment Mark Nos.
1HVY-CH17 1HVY-CH15 Type Elec Finned Tube Elec Finned Tube Capacity 39.2 26.2 Equipment Mark Nos.
1HVY-CH16 1HVY-CH11 Type Elec Finned Tube Elec Finned Tube Capacity 26.2 13.1 Equipment Mark Nos.
1HVY-CH10 1HVY-CH14 Type Elec Finned Tube Elec Finned Tube Capacity 78.4 14.1 Equipment Mark Nos.
1HVY-CH18 Type Elec Finned Tube Capacity 14.1 RBS USAR TABLE 9.4-10 (Cont)
Revision 8 5 of 5 August 1996 8 e. Inlet Filters Equipment Mark Nos. 1HVY-FLT8 1HVY-FLT9 1HVY-FLT10 1HVY-FLT12 Fan (1HVY-) FN8 FN9 FN10 FN12 Filter area (in. x in.) 48x48 48x48 48x24 72x72
Equipment Mark Nos. 1HVY-FLT14 1HVY-FLT17 1HVY-FLT18 Fan (1HVY-) FN14 FN17 FN18 Filter area (in. x in.) 48x48 48x48 24x48 8
1of1August1988TABLE9.5-1POWERSOURCESFORCOMMUNICATIONSYSTEM1EquipmentPowerSourceDescriptionVolts Ph IdentificationPP/PA120ac11VBN-PNL01A11VBN-PNL01B1 Maincontrolroom 136"-0",andlocal non-class1Epower 1Portableintercom--IndependentbatterysystemsuppliesPBX120ac11VBN-PNL04,El110'Healthphysicsbldg localnon-class1E
power1Onsiteradio--Independentbattery(hand-heldsuppliesandlocal portableradionon-class1Epower, system)1VBN-PNL(LTR),and1IHS-PNLO1formain controlroomconsoles andbasestationsPlant-to-offsite--Switchyardbatteryradio1VBN-PNL(LTR),and 1IHS-PNL01 1GSUmicrowave--Switchyardbatterysystem1VBN-PNL(LTR)
RBSUSARTABLE9.5-2ILLUMINATINGLEVELANDTYPEOFFIXTURESUSEDINPLANTAREASNECESSARYFORSAFESHUTDOWNOREVACUATIONOFPERSONNEL
______________________________(a)20percentoffixturesconnectedtoUPS(b)20percentoffixturesconnectedtostandbysourceandswitchabletoothersourcesbyadministrativecontrol (c)Meansofegressandexit
- Arealightingrequiredforsafeshutdown.1of1August1987NormalLightingEmergencyLightingAreaFixture FC Source Fixture FC1.MaincontrolFluorescent75(Mainconsole)UPSFluorescent20(a)room75(Computer)Standby*Fluorescent20(b)BatterypackIncandescent0.5(c)2.Standbyswitch-Fluorescent35BatterypackIncandescent3gearrooms3.Class1EFluorescent20BatterypackIncandescent3Batteryrooms(enclosed&
casketed)4.StandbydieselFluorescent20BatterypackIncandescent3generatorareas5.StandbyserviceFluorescent20BatterypackIncandescent3waterpumphouse6.StandbyMCCsFluorescent20BatterypackIncandescent3andload centers7.RemoteshutdownFluorescent30BatterypackIncandescent5panelroomsStandby*Fluorescent308.MeansofegressFluorescentor5BatterypackIncandescent0.5andexitincandescent (allbuildings)
RBSUSARTABLE9.5-3STANDBYDIESELENGINELUBRICATIONSYSTEMCOMPONENTS1of2August1987ElectricMotor-Engine-DrivenDrivenLubeOil LubeOilPumpCirculatingPump1.PumpsQuantity1perdiesel1perdieselTypeGearScrew Capacity,gpm34540 Head,psig75152.LubeOilCoolerQuantity1perdiesel Duty,Btu/hr1,613,000 DesignConditionsTubeSide-JacketWater a.Inlettemp,°F145.4b.Outlettemp,°F149.4 c.Flow,gpm800ShellSide-LubeOila.InletTemp,°F182.4b.Outlettemp,°F160.0 c.Flow,gpm3203.LubeOilSumpTankQuantity1perdiesel TypeBuiltinaux.skid Capacity,gal514galhighlevel RBSUSARTABLE9.5-3(Cont)2of2August19874.LubeOilHeaterCirculatingPumpQuantity1perdieselCapacity,gpm40 Head,psig155.LubeOilHeaterQuantity1perdiesel Output,kW20kW RBSUSARTABLE9.5-4DESIGNDATAFORDIESELGENERATORCOMBUSTIONAIRINTAKEANDEXHAUSTSYSTEM1of1August1987HPCSDieselStandbyDieselGeneratorComponentGenerators(FilterOnly)IntakeAirFilter/SilencerTypeDisposablecartridgeDisposable cartridgeCapacity(scfm)14,19410,700 Pressuredrop(inW.G.)(max)6.53.3Media(packing)MineralwoolHighefficiencyand14gaugefilterpaper hot-rolledsteelPressure(psia)14.714.7ExhaustSilencerCapacity(acfm)31,60023,000 RBS USAR TABLE 9.5-5 STORAGE OF GAS UNDER PRESSURE Container Stored Gas Maximum Est. Est. Tank Design Pressure Pressure (1) No. Vol.
Gas (psig) (psig) (psig) Tanks (cu ft)Ea.
LocationRevision 20 1 of 3 Carbon Dioxide (3)Fire Protection 1,800 850 1,000 64 3 Turbine Bldg, Basement Generator Purge (5) 450 300 357 1 308.7 Yard - approximately 90 ft from southeast corner of bldg
Nitrogen11Nitrogen 3,360 2,400 3,200 20 1.88 Turbine Bldg (5 tanks) Blanketing Auxiliary Bldg (7 tanks) Radwaste Bldg (2 tanks)
Auxiliary Boiler Bldg 11 (6 tanks) Nitrogen 3,360 2,400 3,360 3 1.88 Containment el 114' Storage for CRD Accumulators CRD Accumulators 2,000 (4) 2,000 2,000 145 2 16 Hydrogen (Generator Cooling - Backup Source) 16Tube Trailer 4,000 2,400 3,800 30 7.7 Yard - approximately 90\ft southeast of building Reserve Skids(2) 4,000 2,400 3,800 56 4.5 AirInstrument Air 135 120 135 3 96 Turbine Bldg ReceiversAir Damper 150 120 135 6 8 Control, Auxiliary, and Accumulator Fuel Bldg Instrument Air 159 120 135 1 75 Radwaste Bldg Accumulator Radwaste Air 150 120 135 1 29 Radwaste Bldg Receivers1412 12 14 RBS USAR TABLE 9.5-5 (Cont) Container Stored Gas Maximum Est. Est. Tank Design Pressure Pressure (1) No. Vol.
Gas (psig) (psig) (psig) Tanks (cu ft)Ea.
LocationRevision 20 2 of 3 13Instrument Air System 4000 2400 2640 16 1.75 Control Building Air Bottles 13Penetration Valve 200 120 150 1 212 Auxiliary Bldg Leakage Control 1 72 Auxiliary Bldg Isolation Valve 150 120 135 4 5.5 Auxiliary Bldg Accumulators23512023545.5 Reactor Bldg ADS Accumulators 300 150 300 7 8.8 Reactor Bldg Safety Relief 300 150 300 9 1.7 Reactor Bldg Valve Accumulators HPCS Diesel 275 250 275 2 64 Diesel Generator Bldg Generator Receiver Standby Diesel 275 250 275 8 76 Diesel Generator Bldg Generator Receiver Service Wtr Air 150 120 150 2 36.8 Reactor Bldg Accum HalonFire Protection 3,000 360 1,000 54 0.26 Main Control Room Fire Protection 3,000 360 1,000 2 1.9 Aux Cont Bldg, el 123'-6" Fire Protection 3,000 360 1,000 6 3.5 Aux Cont Bldg, el 123'-6" Fire Protection 3,000 360 1,000 2 0.13 Norm Swgr Bldg, el 123'-6" Fire Protection 3,000 360 1,000 2 0.15 PAP Bldg Fire Protection 3,000 360 1,000 2 1.4 Services Bldg, Rm 305 Fire Protection 3,000 360 1,000 2 1.4 Services Bldg, Rm 353 Fire Protection 3,000 360 1,000 2 2.7 Services Bldg, Rm 302 Fire Protection 3,000 360 1,000 2 0.4 Services Bldg, Rm 302 Fire Protection 3,000 360 1,000 2 0.75 Services Bldg, Rm 205 Fire Protection 3,000 360 1,000 2 1.5 Services Bldg, Rm 206 RBS USAR TABLE 9.5-5 (Cont) Container Stored Gas Maximum Est. Est. Tank Design Pressure Pressure (1) No. Vol.
Gas (psig) (psig) (psig) Tanks (cu ft)Ea.
Location (1)Safety valve or cylinder rupture disk set point (2)Deleted (3)Stored as liquified gas (4)Maximum working pressure (5)Liquid carbon dioxide in a low-pressure cryogenic storage unit 12 (6)Evaluation of effects due to failure of hydrogen and oxygen storage vessels for this system performed in accordance with EPRI Report NP-5283-SR-a, "Guidelines for Permanent BWR Chemistry Installations - 1987 Revision."
12Revision 20 3 of 3 Fire Protection 3,000 360 1,000 2 0.44 Met Instr Bldg Fire Protection 3,000 360 1,000 2 0.23 Met Utility Bldg Hydrogen in NitrogenHydrogen Analyzer 3,360 2,400 3,000 2 1.88 Auxiliary Bldg Calibration Gas Bottle OxygenHydrogen Analyzer 3,360 2,400 3,000 4 1.88 Auxiliary Bldg Reagent Gas Bottle12 Hydrogen Water Chemistry (6)Cryogenic Hydrogen NA (6)Cryogenic Oxygen NA (6)Bottled Hydrogen NA (6)12 RBSUSAR1of2August1987TABLE9.5-6STANDBYDIESELGENERATORCOOLINGWATERSYSTEMCOMPONENTSJacketWaterPumpsTypeCentrifugalQuantity1perdieselengine(enginedriven)Capacity900gpm NPSH15ft TDH110ftJacketWaterCoolerTypeTEMAClassRASMESectionIII,shellandtubeDuty12,030,000Btu/hrDesignConditions(Plant)TubeSide-CoolingWaterInletTemperature95°F OutletTemperature129°F Flow:700gpmShellSide-EngineJacket
Water*InletTemperature175°F OutletTemperature144.9°F Flow:800gpmHeatRemovalDesignOverloadMargin110percentJacketWaterStandpipeQuantity1perdieselengineTypeVertical Capacity225gallonstofill Engine500gallonstofillfromjacketwaterinlettojacketwater
outletJacketWaterHeaterTypeFlangedimmersionQuantity1perstandpipe Output48kw(3phase/60Hz/460V)
RBSUSAR2of2August1987TABLE9.5-6(Cont)JacketWaterKeepwarmSystemCirculatingPumpTypeCentrifugalQuantity1perdieselengine Capacity50gpm NPSH15ft TDH50ftTurbochargerAfter-CoolersDuty3,695,000Btu/hrJacketWaterFlow450gpm JacketWaterInletTemperature150°FJacketWaterOutletTemperature165°FHeatRemovalDesignMargin10percent
_________________*Datalistedisforengineatfullloadoperation,stabilizednominalfullloadtemperature.
RBS USAR TABLE 9.5-7 HYDROGEN WATER CHEMISTRY SYSTEM ALARMS AND ISOLATIONS Revision 23 1 of 1 Parameter Alarm Isolation Hydrogen Flow Setpoint error High Loss of Signal Hydrogen Pressure Low High Oxygen Pressure High Low Oxygen Flow Setpoint error Hydrogen Area High Monitor Malfunction High-High H 2/O 2 Supply Systems Trouble System Trip Offgas Monitor Trouble Low O 2 High O 2 Isolation Local Manual Control Room Manual Reactor Power Loss of Signal Reactor Scram Note: The SCRAM contacts are wired into the Control Room Manual Shutdown switch circuit.
Full SCRAM