ML17226A100

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Revision 25 to the Updated Safety Analysis Report, Chapter 10, Section 10.1-1 Table - Steam and Power Conversion Systems Principal Design and Performance Characteristics
ML17226A100
Person / Time
Site: River Bend  Entergy icon.png
Issue date: 07/28/2017
From:
Entergy Operations
To:
Office of Nuclear Reactor Regulation, Office of Nuclear Material Safety and Safeguards
Shared Package
ML17226A087 List:
References
RBG-47776, RBF1-17-0089
Download: ML17226A100 (5)


Text

RBS USAR TABLE 10.1-1 Revision 25 1 of 3 STEAM AND POWER CONVERSION SYSTEMS PRINCIPAL DESIGN AND PERFORMANCE CHARACTERISTICS Item Design and Performance Characteristics

Turbine-Generator Unit (Section 10.2) 14 Turbine 1,047,301 kWe (@ 2 in. absolute exhaust back pressure) nameplate rating; 1,060,928 kWe (@ 3 in. absolute exhaust pressure) for

rated flow conditions, 1,800 rpm, tandem compound, 4-flow, 43-in, last-stage buckets, at single-stage reheat 3.0 in Hg

absolute exhaust pressure and 0 percent

makeup 14 Generator 1,151,100-kVa, 1,800-rpm, direct-connected, 3-phase, 60-Hz, 22,000-V, liquid-cooled stator, hydrogen-cooled rotor, rated at 0.90 pf, 0.58 short circuit ratio and 75

psig hydrogen pressure

Exciter 2960-kW, 500-V, compact Alterrex type with static regulation

Control Digital Electrohydraulic control (EHC)

Overspeed protection Redundant speed control systems

a. Normal and transient DEHC speed control system
b. Diverse electrical overspeed system
c. Backup overspeed system

Main Steam Supply Piping and valves including branch lines System between Second up to first valve in branch line Isolation to and Safety Class 1, Seismic Category I including the First Field Weld Outside the Impingement Wall (Section 10.3)

RBS USAR TABLE 10.1-1 (Continued)

Revision 17 2 of 3 Item Design and Performance Characteristics Main Steam Supply Piping and valves including branch lines System between the up to first valve in branch line First Weld outside the Safety Class 2, Seismic Category I Impingement Wall up to and including the Third Isolation Valve (Section 10.3)

Main Steam Supply Piping and valves: ANSI B31.1 or as System Downstream of designated in Table 3.2-1, Item XXXII the Third Isolation (Section 10.3)

Condenser Twin-shell, single-pass 616,750 ft 2 surface (Section 10.4.1) area, 27°F tube rise, equalizing ducts between steam sections and hotwell sections Condenser Air Two half-capacity air removal pumps for Removal System initial shell-side air removal; two (Section 10.4.2) full-capacity steam jet air ejectors for maintaining vacuum. Steam and noncondensibles go to the radwaste off gas system for the air ejectors and through charcoal filters to the atmosphere for the air removal pump. Piping and valves: ANSI B31.1 7 Turbine Gland Sealing Steam supplied from the steam seal System (Section 10.4.3) evaporator. Noncondensibles go to condenser. Piping and valves either ANSI B3l.l or General Electric's standard that parallels ANSI B31.1 7Turbine Bypass System Flow capacity equal to

9.5 percent

of the (Section 10.4.4) reactor design steam flow. Piping and valves up to but not including bypass valves: ANSI B31.1 and ANSI B31.1 downstream of the bypass valves. Bypass valves are as designated in Table 3.2-1, Item XXXII RBS USAR TABLE 10.1-1 (Continued) 3 of 3 August 1987 Item Design and Performance Characteristics Circulating Water Four 25-percent capacity circulating System (Section 10.4.5) water pumps, 4 multicell water cooling towers, and a fabricated-steel piping system Condensate Demineralizer a. Two trains each of 5 ion exchangers, System (Section 10.4.6) with 8 ion exchangers normally operating, external cleaning, and regeneration facilities, acid and caustic dilution systems, and waste recovery system b. Piping: ANSI B31.1 Pressure vessels: ASME Section VIII Condensate and Feedwater a. Three half-capacity motor-driven con-System (Section 10.4.7) densate pumps, 2 full-capacity air ejector intercondensers, 1 full-cap-acity steam seal condenser, 5 stages of low-pressure regenerative feed-water heaters including 2 separate drain coolers all divided into 2 strings of half-capacity heaters, 3 one-third capacity, motor-driven through step-up gear reactor feed pumps and 1 stage of 2 half-capacity high-pressure feedwater heaters

b. Piping and valves from the hotwell up to but not including the feed-water shutoff valve outside: the containment structure: ANSI B31.1.

Piping and valves from the first containment isolation valve to the reactor: ASME Section III, Code Class l. Feedwater heaters: ASME Section VIII. Feedwater shutoff valve and piping up to but not including containment isolation valves: ASME Section III, Code Class 2

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NOTE: The systems listed above are not safety-related unless otherwise noted.

RBS USARRevision 17 1 of 1 TABLE 10.4-1 DESIGN AND PERFORMANCE PARAMETERS FOR THE CONDENSER 15 Surface (sq ft) 616,746 Number of passes 1 Number of tubes (per shell):

Admiralty 32,790 70-30 Cu-Ni 2,116 15Effective length of tubes (ft in) 45-0 Tube outside diameter (in) 0.75 Tube material: Condenser main body Admiralty Tube bundle impingement

& air core area 70-30 Cu-Ni 14 Design Tube velocity (fps)

7.0 Condenser

duty at maximum 6.9 6 x 10 9 expected load (Btu/hr) Circulating water flow (gpm) 508,470 Maximum expected circulating 96 water inlet temperature (°F) Circulating water temperature 27 rise at maximum expected

load (°F) Condenser vacuum at rated power with 4.

8 maximum expected circulating water temperatures (in Hg abs) 14 RBS USAR Revision 17 1 of 1 TABLE 10.4-2 EXPECTED CONDENSATE DEMINERALIZER SYSTEM INFLUENT CONCENTRATIONS Normal Operation (1) Startup Temperature (°F) 100-130 81-175 Specific conductivity

@ 25°C, uS/cm 0.20 1.00 Chlorides, ppb 20 100 Silica as Si02, ppb 50 2000 pH @ 25°C, S.U.

6.5-7.5 5.8-8.0 Dissolved oxygen, ppb 200 1000 Total metals, ppb (2)<5<5Total organic carbon, ppb 300 1000 (1) Extended normal operation concentrations are defined as those occurring during full-power operation without condenser tube

leaks.(2) Includes soluble and insoluble iron, copper, and nickel.

Based on operation of prefiltration equipment, Section 10.4.7.5.2.