ML17046A489: Difference between revisions

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{{Adams
#REDIRECT [[LR-N17-0034, Salem Generating Station, Units 1 & 2, Revision 29 to Updated Final Safety Analysis Report, Tables 10.4-1, Main Condensate and Feedwater System Components to 10.4-6]]
| number = ML17046A489
| issue date = 01/30/2017
| title = Salem Generating Station, Units 1 & 2, Revision 29 to Updated Final Safety Analysis Report, Tables 10.4-1, Main Condensate and Feedwater System Components to 10.4-6
| author name =
| author affiliation = PSEG Nuclear, LLC
| addressee name =
| addressee affiliation = NRC/NRR
| docket = 05000272, 05000311
| license number = DPR-070, DPR-075
| contact person =
| case reference number = LR-N17-0034
| package number = ML17046A230
| document type = Updated Final Safety Analysis Report (UFSAR)
| page count = 9
}}
 
=Text=
{{#Wiki_filter:TABLE 10.4-1 MAIN CONDENSATE AND FEEDWATER SYSTEM COMPONENTS Condensate Pumps Number of pumps Design Capacity of each Manufacturer Size and Type Speed Motor Size Shutoff Pressure Manufqcturer Horsepower Current Voltage Speed Hertz Upper BRG Cooling Water Space Heater Design Capacity of each Manufacturer Size and Type Number of Stages Speed Maximum Discharge Pressure limited by for discharge Steam Generator Feed Pump Turbines Number of Drive Turbines Rating Manufacturer Number of Stages Exhaust Pressure 3 8,000 gpm at 1,328 feet (575 Ingersoll-Rand 32 APKD 9 stage vertical 1,170 rpm 4,000 hp 693 psig 3 Electric Machinery Co. 4,000 498 amps 4,160 v 1,190 rpm 60 13 gpm 2 kW 240 V (for storage only) 2 18,613 gpm and 2,320 feet (884 psi) at 370°F Worthington 24 WGID-171 single stage Horizontal centrifugal 1 5530 1,620 psig 2 10,970 hp at 5530 rpm DeLaval 9-double flow exhaust 2.0 inches hg. abs. (Except 11C, 21A, 21B & 21C) 3 Flow Rate per Shell Temperature, In Temperature, Out Flow is directed through tube side of exchanger Number of Passes Pressure Drop Design Pressure Tube Channel Material SGS-UFSAR 1 of'4 3,792,475 lb/hr 92. 6°F 164°F 2 12 psi 700 psig A-515-70 Revision 26 May 21, 2012 Tubes: Material Number O.D. Gauge Flow Rate per Shell , In Temperature, Out Flow is directed through tube side of exchanger Number of Passes Pressure Drop Design Pressure Tube Channel Material Tubes: Material Number O.D. Length Flow Rate per Shell Temperature, In Temperature, Out Number of Passes Pressure Drop Design Pressure Tube Channel Material Tubes: Material Number O.D. Length Flow Rate per Shell In Temperature, Out Flow is directed through tube side of exchanger Number of Tube Passes Pressure Drop Design Pressure Tube Channel Material SGS-UFSAR TABLE 10.4-1 (Cant} \ \ 2 of 4 304 SS A-249 1659 5/8 in. 0.035 Ave Wall 43 feet 0 in. 3,792,475 lb/hr 92. 6°F 164°F 2 12 psi 800 psig A-516-70 304 SS SA-688 1570 5/8 in. 0.035 Ave Wall 1 (21B) 41 feet 3-5/8 in. 41 feet 4 in. (21B} 3,548,026 lb/hr 3,792,475 lb/hr 168. 3°F 164°F 202. 8°F 202°F 2 2 19 psi 18.3 psi 700 psig 800 psig A-515-70 A-516-70 304 s.s. A-249 304 s.s. SA-688 1,119 1,090 5/8 in. 5/8 in. 0.035 Ave Wall 0.035 Ave Wall 37 feet 11 in. 36 feet 7 in. 1 2 3,548,026 1b/hr 3,611,136 lb/hr 202. 8°F 202°F 253. 5°F 251. 2°F 2 2 12.8 13.5 700 psig 800 psi A-515-70 SA-516-70 Revision 26 May 21, 2012 I Tubes: Material Number O.D. Gauge Length Fourth Stage Feedwater Heaters Number of Shells Flow Rate per Shell Temperature, In Temperature, Out Flow is directed through tube side of exchanger Number of Tube Passes Pressure Drop Design Pressure Tube Channel Material Tubes: Material Number O.D. Gauge Length Fifth Stage Feedwater Heaters Number of Shells Flow Rate per Shell Temperature, In Temperature, Out Flow is directed through tube side of Exchanger Number of Tube Passes Pressure Drop Design Pressure Tube Channel Material Tubes: Material Number O.D. Gauge Length SGS-UFSAR TABLE 10.4-1 (Cont) Unit 1 304 S.S. A-249 896 3/4 in. 0.035 Avg Wall 43 feet 5 inches Unit 1 3 3,548,026 lb/hr 253. 5°F 307.2°F 2 16.0 psig 700 psig A-515-70 304 SS A-249 782 3/4 in. 0.035 Ave Wall 43 feet 3 inches Unit 1 3 3,548,026 1b/hr 307.2°F 365°F 2 13.6 psig 700 psig A-515-70 304 SS A-249 845 3/4 in. 0.035 Ave Wall 43 feet 7 inches 3 of 4 Unit 2 SA-688-TP316L 840 +;j in. 0.035 in. Avg. Wall 43 feet 8 inches Unit 2 3 3,611,136 lb/hr. 251.2°F 303.7°F 2 17 psig 800 psig SA-516-70 SA688 TP 316L 726 3/4 in. 0.035 Avg. Wall 43 feet 11 inches Unit 2 (258, 25C) 2 3,611,136 lb/hr 303.7°F 364.5°F 2 13.6 psig 700 psig A-515-70 304 SS A-249 845 3/4 in. 0.035 Ave Wall 43 feet 7 inches Revision 28 May 22, 2015 Fifth Stage Feedwater Heaters Number of Shells Flow Rate per Shell Temperature, In Temperature, Out Flow is directed through tube side of Exchanger Number of Tube Passes Pressure Drop Design Pressure Tube Channel Material Tubes: Material Number O.D. Gauge Length Sixth Stage Feedwater Heaters Number of Shells Flow Rate per Shell Temperature, In Temperature, Out Flow is directed through tube side of exchanger Number of Tube Passes Pressure Drop Design Pressure Tube Channel Material Tubes: Material304 Number O.D. Gauge Length SGS-UFSAR TABLE 10.4-1 (Cont) 4 of 4 Unit 1 3 4,995,701 lb/hr 368.1°F 427.5°F 2 20.7 psig 2100 psig A-516-70 FB SS A-249304 1805 3/8 in. 0.055 Ave Wall 39 feet 2 in. Unit 2 (25A) 1 3,792,475 lb/hr 309.3°F 369.4°F 2 13.5 psig 800 psig A-515-70 SA-688 Type 789 3/4 in. 304 0.035 Ave Wall 42 feet 4 inches Unit 2 3 4,982,149 lb/hr 368. 5°F 427°F 2 20.7 psig 2100 psig A-516-70 FB SS A-249 1805 3/8 in. 0.055 Ave Wall 39 feet 2 in. Revision 28 May 22, 2015 
( Transient Scenario {1) Loss of Main FW Loss of Offsite Power Plant Cooldown NOTES: No TABLE 10.4-2 TOTAL AUXILIARY FEEDWATER FLOW Single Failure In Failure of Turbine Failure of 1 Motor AFW System AFW Pump AFW Pump 2:1600 gpm {2} 2:700 gprn (2) gpm {2) gpm ( 2) 2:700 gprn ( 2) gprn (2) gpm {2) gprn ( 2) gprn (2} 1. AFW flows during steam line break transients (both inside and outside Containment) and feed line break transients vary considerably during the event and are summarized in Reference 2 but not included in this table. 2. Flows represent bounding values for steam generator pressures of 1117 PSIA or 1 of 1 SGS-UFSAR Revision 19 November 19, 2001 I SGS-UFSAR TABLE 10.4-3 ASSUMPTIONS USED IN SLOWDOWN WATER TRANSIT TIME CALCULATIONS THIS TABLE INTENTIONALLY LEFT BLANK 1 of 1 Revision 18 April 26, 2000 I 
: . ' SGS-:.iE"SAR TABLE 10.4-4 SLOWDOWN TRANSIT TIMES THIS TABLE HAS BEEN DELETED 1 of 1 Revision 18 April 26, 2000 TABLE 10.4-5 POSTULATED RELEASE C>t LIQUID ACTIVITY THROUGH BLOWDOWN SYSTEM TUIS TABLE HAS BEEN DELETED 1&2 of 2 SGS-UFSAR Revision 18 April 26, ?.000 SGS-UFSAR TABLE: 10.4-6 t-'OSTIIIJ\TI::D ru: LF.l\SE OF Gl\Sf:OIJS A.r:T IV I TY THROUGH CONDENSER AIR REMOVAL SYSTEM THIS TABLE HAS BEEN DELETED Revision 18 April 26, 2000}}

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