ML20203J400
| ML20203J400 | |
| Person / Time | |
|---|---|
| Site: | Crystal River  |
| Issue date: | 02/04/1972 |
| From: | Kowal G AFFILIATION NOT ASSIGNED |
| To: | |
| Shared Package | |
| ML20203J289 | List:
|
| References | |
| NUDOCS 9712190201 | |
| Download: ML20203J400 (50) | |
Text
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- 1. E' n '
g.43 CRYSTAL RIVER UNIT 3 FLORIDA POWER CORPORATION .
. l i
l 4
ANALYSIS AND DESIGN OF l
THE PRESSURIZER QUENCH TANK l
r h
l r
George M. Kowal- .
+
f
~
r V
r P
GILBERT ASSOCIATES, INC.
Reading, Pennsylvania 2/4/72-e
. .e en ~
.y v- -y e w- a- y e qm- v -
xvi- A-3 1.0 SCOP.E.
l The purpose of this sudy was to design and analyze the pressurizer quench (relief) tank subject to conditions of its operation during a pressurizer relief transient. 1 2.0 INTRODtfCTION
'n the flow stream of a nucicar primary system exists a tank commonly referred to as a drain tank (or sometimes as a pressurizer quench tank). The function of this tank is to quench the steam effluent from safety valves of the pressurizer, should the safety valves ever actuate.
Ihis study deals with the sizing and design of this tank, particularly for two coiditions of operation, i.e.
- a. nomal actuation of the pressurizer safety valves,
- b. condition of stuck safety valves.
Because of the complexity of this whole system with respect to geometry and conditions of two phase mixtures, a direct mathemacical solution is entrczely cumbersome and, hence numerical techniques have to be employed.
In this analysis, a cot puter program for the digital simulation of a multinode reactor plant during loss-of-coolant FLASH-251) , was used for all calculations.
3.0 COMPirtER MODEL -
To take advantage of the FLASH-2 Program, the entire system (i.e. pres-surizer, drain tank and containment) was conveniently divided into several lumped volumes. Each volume was defined by its exact dimensions and was referenced at an elevation from the bottom of the containment (datum 0).
(1) J. A. Redfield, J. H. Hurphy and V. C. Davis, " FLASH-2-A FM.TRAN IV PRO-GRAM for the Digital Simulation of a Multinode Reactor Plant during Loss-of-Coolant", WAPD TM-666 (April 1967).
1
'.IHI-A-3 The control volumes were connected by two principal types of paths i.e.,
simple pipe (specified flow)- and ' leak path. The flow direction of each i path was specified according to the physical understanding of the system behavior. !
Details of the mock up of the whole system by control volumes (nodes) i and the paths connecting each is shown _in Figure 1. For comparison pur- '
pose, the actual physical situation is shown in Figure 2.
, 4.0 - ASSUMPTIONS The criteria
- sed in this study as a basis for the design of the quench tank are _ the followingt
- a. The safety valves lif t at the high pressure reactor trip (2,355 psig). (This assumption imposes slightly more severe conditions than for thn actual relief value of 2,255 psis),
- b. During the transient until the pressurizer safety valves resent-
- a total of 3030(2) lbs of steam is dumped into the quench tank.
The tank must therefore be designed to quench this mass of steam under the normal operation transients.
- c. All three safety valves are assumed to lift simultaneously.
- d. In case of a failure of the safety valves to rescat, the tank must be able, upon rupture of-the pressure disc, to sustain a continued blowdown from the pressurizer.
$.0 PROCEDURE, The calculational procedure was performed in two steps, i.e. first, de-termining the volume of the tank necessary to absorb 3030 lbs of steam in less than one minute, .and second, its capability to sustain a con-tinual blowdown throu'gh.a two (2) sq. ft. vent area (rupture disc).
_(2)
- Hemorandum from C._ E. - Thomas to; E. R. Hottenstein, subject: Reacter
- Coolant Drain Tank, Memo No. CAI-48, March 12.11968.
- 2
Yvi-A-3 In each case the solution was obtained utilizing the FLASil-2 computer program.
The initial known conditions, excepting the design basis, are the thermo-dynamic properties (summard red in Table 1), pipe lengths and sizes and general geometric configuration. Thus, it is possible to represent the actual geometry an shwon in Figure 1 with a three node mock-up (Figure
- 2) to be input to che FLASH-2 program. With this information, a para-4 metric study was made using the size and water volume in the quench tank as variables.
Tne first estimate of the quench tank volume was obtained by applying the principle of a jet condenter, i.e. amount of water required to con-dense 3030 Ita of stea:n. The heat balance equation is as follows (see sketch below).
W(1, + hs) + W(hwo - hq) =
QC(Te - Tw) where W = Weight of steam to be condensed, Ib/hr To = saturation temperature of steam ( 'tring, F Ls = Latent heat of vaporization at To, Stu/lb h, = Superheat in steam above To , Btu /lb hw = Total heat in exit condensate, Btu /lb hw, a Tota". heat in liquid wat'er at To, Btu /lb Ty = Temperature of water at condenser inlet, OF Te = Temperature of water at condenser exit, F
(
- Water used, Ib/hr C = Specific heat of water,~1 Btu /lb F F
3
vvt- A -3 W{oL t hs [CONDEliSER 7 m h w T:, .
r l
\
l Q Ty Sulving the above equation for Q, with the assumption of the known value of steam flow, the equation becomes:
W (L, + hs ) + W (hw, - hu)
Te - Tw and substituting the following initial assumptions:
W = 3030 lb To =
472 F at 525 psia (saturated)
L, =
749.2 Btu /lb at 4720F h, = 0 T, = 212 F Tw
=
120 F hw =
180.17 Btu /lb hw -
455 Btu /lb q yg , 3030 (749.2 + 0) + 303 (455 - 180,2) 212 - 120 Q(1b) = 31'1 x 105 = 3,38 x 104 lb 9
or 0
,9 ,
3.38 x 10 lb 62.4 lb/ft3
=
542 ft 3 Thus, this volums of water was the initial value used for the FIASH-2 4
TVI- A -3 run. The initial total tank volume was 25 percent greater than the water volume, i.e. Vtotal = 680 ft3 Proceeding in like manner a net volume of 750 it3 was arrived at which gave realistic results. Of this net volume 562 ft3 was taken to be water. A contingency factor of 6.57.
of the net volume was then subtracted to account for volume taken by the downcomers, supports, etc. Thus, although the free tank volume is 750 ft3, the volume used in the calculations was 700 ft3 to account for the above contingency and introduce s ee conservatism.
Once the volume was obtained, a simple calculation was performed to arrive at the number and size of nozzles (or orifices) required in the three downcomer lines (two 6" and one 4"). From the second assumption above and with the additional criterion of 15 see blowdown, the total flow into the tank becomes:
y steam , 3030 lb = 202 lb/see total 15 sec ..
or 73 lb/see for each of the 6" lines and 56 lb/sec for the 4" line.
Knowing the thermodynamic co..ditions upstream and downstream, the t .. ital required relief area for one downcomer becomes:
A =
W -f"
=
W T 2
, ft
'F 223.8C/h1-h2 where W = flow, Ib/sec T = specific volume, ft /lb I = velocity ft/sec h,h2=
t enthalpy upstream and downstream, Btu /lb C = discharge coefficient 5
.nl- A - 3 For the 6" line g, (73)(7.407*) , 540 223.8 x /12404.2-1150** 223.8 (54)h (.50)
A= 0.672 ft2 = 97 in2 and the number (n) of 1.5" nozzles required is:
A 97 in2'
- 97 T r2 3.14(.75 in)2 1.76 n = 56 Saturated steam in downcomer at 58 psia Assuming maximum expansion (i.e. tank remains at 14.7 psia)
A similar calculation was made for the 4" line, where the requirement was found to be 42 nozzles.
6.0 RESULTS A!.'D DISCUSSION Figures 1 and 2 represent the mock-up and actual geometry respectively used in this analysis. As was previously mentioned, two conditions of blowdown were analyzed, i.e. a controlled mass of steam released and a continuous blowdown with stuck safety valves. Figures 3a and 3b show the maximum pressure and temperature in the tank for conditions of normal blowdown, which are, 43 psig and 210 F respectively, Figure 4 shows the pressure history in the tank for the condition of stuck safety valves. For this case the assumption was made that the rupture disc severs when the tank reaches 100 psig. It is evident from the figure that the pressure is rapidly dissipated after the disc ruptures and it is adequate to sustain a continuous blowdown. Figures 5 through 7 show details of the tank, downcomers and nozzles (orifices).
In sumary, the design and operating criteria of the tank are given in Table 1.
6
l l Wl- A -3 TABLE - 1 QUENCil TANK PARAMETERS DESIC' Pressure -
100 psig Temperature -
300 F OPERATING: (To relleve 3030 pounds of steam)
Peak Presi.ure - 43 psig
- Peak Temperature -
210 F Minimum Water Level -
G'-3" -
Maximum Water Level -
10'-6" -
Water Volume (Normal) -
562 ft3 TANK DIMENSIONS:
lieight -
13'-0" Diameter - 8'-6" Volume -
750 ft3
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- CRYSTAk RIVER IDrIT 3 rage 3dio" 34 ENHANCED DESIGN BASIS DOCtMENT -
, LIQUID WASTE DISPOSAL SYSTEM-i-7 5-i 4.01 -REFERENCES
.1 : . MAR t/o. 77 03-02A, "Wasto Transfer Pumps . WOP 5 A, B, C," dated 9/28/78.
- 2. _ MAR 82 05 02 01, " Installation of Ultrafiltration System," dated 12/2/82.
~
4 - gal Calculation, XIV B 3, " Decay Heat Pit Sump Ptmp," dated 6/3/69.
5, GAI Calculation, XIV B 2, " Auxiliary Building Sump Pump," dated 5/26/69; 6.- gal Calculation, XIV A 1, " Waste Transfer Pump," dated 5/27/69.
- 7. - MAR 8010-618 " Waste Disposal Pumps WDP 6A and 68," dated 11/5/C1.
~8.- gal _ Calculation, XIV 18, " Neutralizer Pump," dated 5/29/69.
9.' gal Calculation,-XIV A 11 " Decant Pump Head Cales," dated 5/29/69.
10, gal Calculation, XIV A 10, " Slurry Pump Head Cales," dated 5/28/69.
11, gal Calculation, XIV A 7, " Concentrated Radioactive Liquid Waste Pump," datec 5/29/69.
- 12. gal Calculation, XIV A 9, " Boric Acid Recycle Pump Head Cales," dated 5/26/69.
- 13. - Calculation M910049, " Effluent Release. Hydraulic Calcualtions," dated 2/14/92.
- 14. . gal Report, " Analysis and Design of RC Drain Tank," dated 2/4/72.
-15. Gilbert Commonwea emorandudi, from H, t:. vaugnn to v. A. eum, " Quench Tank Heat Exchanger," dated 10/15/82.
- 16. MAR No. 77 0719, "LRWD System Modification," dated 7/14/80.
- 17. GAI-Letter from M. J. Cambrin to Dr. R. Englehart,? Design Cycle for Waste Disposal System," dated 7/29/71.
- 18. .G Al Letter to B&W, from L. Sace to C. E. Thomas, B&W 82, " Boric Acid Storage Tank,"
dated 8/7/68.
- 19. s MAR No. 80 02 71, " Crc 4stie RC Drain and RCDT Pumps, dated 10/10/84.
20.' -
. MAR 78 0612-00A, 'Second part of MAR 78 06 12".
__ 21;_ : MAR 821016-01 A',
- Disconnect One Platecoil Cooler From RC Drain Tank WDT 5,"
- dated 3/28/85. .
.- 2 2.- ; Maximum Hypothetical' Accident Analysis Basis Document B&W (Proprietary) 51-1172973 00.
A-
-O
I i
CRYSTAL RTVER tnTIT 3 page 3* cf 34 EN} LANCED DESIGN BASIS DOCUMElfT LIOUID WASTE DISPOSAL SYSTEM
.f". >,
- 23. Calculation M90 0030, " Containment isolation Valves Stroke Times."
- 24. gal Calculation, XIV A 6, "RC Drain Tank Pump & RC Drain Pump Head Calculations."
dated 9/17/70.
- 26. Calculation M91 1012. "RB/AB Sump Pump Flow and Structural Calculations," dated 4/30/91. .
- 27. G/Cl Document No. DC 5520148 01.00-ME, " Reactor Coolant Drain Tank .jperational Levels." dated 4/7/93, FPC Document No. M 93 0009.
- 28. MAR 92 0418 01, "WDP 6A/6B Impeller Modification," dated 12/11/92.
~
- 29. MAR 52 02 20-01 A, "RC Drain Tank Level Setpoint Change", dated 9/17/93.
- 30. Calculation 191-0018, "RC Drain Tank (Liquid) Level Loop Accuracy", dated 3/06/96.
- 31. " Optimized Replacement Filter Element Fur WDFL 1 A and WDFL 18," PEERE #1190/ Ref:
REA 35-0039.
E'PSD /, // cf l
-1
. l Page13:_cf 34, l]
CRYSTAL *tIVER tThIT 3 - l
= ENHANCED DESIGN BASIS DOCUMINI. -l LIQUID WASTE DISPQSAL SYSTEM
- 4. '. -
i
~-
3.Oo iCOMPONENT PARAMETERS .
COMPONENT / PARAMETERS - REASON /SOtTRCE INTERFACE-4
- Motor:
[460VA C, 3 phase, 60Hz, 7.5hp Motor phase and fres.:tency are
= based on standard US ' electrical 4dOVAC Reactor A1CC '
3A2, Unit SAR -
l ;
systems. ' Vcitage rating specified is
- for use on nop safety bus 3A2.
Horsepower rating is based on head l requirements andpump design flow. r Reference 2
~ln9erlocks:
- Pump starts on high levelin the ' Automatically processes the oily Waste Neutralitation Tank. waste water through the ultrafiltration system.
- Pump stops on high temperature "or high pressure at the inlet of. Prevents damage to the permsate
- W CFL.S. filters.
WDT 3A.- WDT 33, WDT 3C: Reactor Designed Volume (Liquid):
- Coolant Bleed Tanks 10j 50 ft' '
(1700 Ge! e3 h) Previds 30 day holdup capacity for DW provides normal operation based on bleed - demineralized water for volume required to accommodate: flushing of the tanks and
- 1) two cold startups at beginning of filling loop seals, core lite:
- 2) three ccid startups thereafter at CA provides flow path for 77.5 day intervals with continuous sampling tanks, shim bleed during operation: and 3).
- boron removal during the last 55 MU the LWD provides days of core life and shutdown for purified primary coetant refueling, back to MU System for Reference 17 recycle back to the primary system.
FSAR L FSAR Table 115 WDTM:' Miscellaneous Radioactive -
Waste Storage Tank (20.000. gal) Designed Volume (Liquid):
2750 ft*
This volume is based on the DW - provides estimated monthly accumulation of damineralized water for
- misgellaneous . radioactive waste. filling loop seal.
-FSAR FSAR Table 115 WDT-S: Reactor Coolant Drain Tank l Required Tank Volume:
- (6220 gal' 831 ft' (total) '
a -
f
-Fage.i3 cf 34 CRYSTAL RIVER UNIT 3-EmtANCED DESIGN BASIS DoCUME}rt - ^
-LIQUID WASTE DISPOSAL SYSTEM q ';
3,0' ' COMPONENT PARAMETERS.
?' (~ COMPONENT /PARAMITERS REASON / SOURCE INTERFACj t
561 ft 3'(liquid) -
Based on volume required to quench. .RC collects primary
- steam resulting from lif ting of coolant from the RC pressurizer relief valves, system and provides -
References 14,27 quenching for steam during a pressurizer safety valve lift.
FSAR FSAR Table 115 NG provides nitrogen for purging.
CF - collects water from
- the core flood tank drains.
DW - provides demineralized water for fushing of the RC Drain Tank.
0:. cling Ca:acity: Designed to cocl 610 ft3 of water from 240F to 150F in 2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br />.
Provides cooling plus margin for sw . provides cooling normal RC system leakage to ensure water.
RC Drain Tank is capable of quenching sta am during pressurizer relief valve lift. One platecoil has been removed from service due to a cooling water leak with adequate recerve cooling capacity being maintained.
Reference 15 WDT 6: Spent Rosin Storage Tank Required Volume (Liquid):
(120 Gal.) 860 ft*-
Volume based on nominal resin DW provides capacity of 800 ft' or two years' demineralized water for retention capacity, flushing of piping and the spent resin tank and filling the tank loop seal.
FSAR FSAR Table 115 SF col:ects resin from the Spent Fuel Coolant ...
Demineralizers.
MU collects resin from the Makeup Systern
. ' TABLE 5 4 (Continued)-
' list of Methods of Seismic Analysis For Class 1 Structures.-Systems, and Comoonents Design Reference or Codes Seismic Desian RB Fire Service ANSI /ASME III Seismic I* in RB Standpipe NFPA-14 Seismic ! at Penetration (see.
Section 5.1.2.2)
Nitrogen pressi-ization system FSAR 6.1.2.1.3 Modal Analysis far core flood tanks ANSI B31.1 Response Spectrum I. Radioactive Waste F Disoosal System Reactor coolant FSAR Table 11-5, Static bleed tanks ASME III-c Miscellaneous waste- FSAR Table 11-5, Static >
storage tank ASME III-c Reactor coolant FSAR Table 11-5, Static drain tank ASME III-c Spent resin storage tank' '
FSAR Table 11-5, Static ASME III-c Con:entrated radioactiv wasts F3AR Table 11-5, Static storage tank ASME III-c Concentrated boric acid tanks FSAR Table 11-5, Static ASME III-c Neutralizer tank FSAR Table 11-5, Static ASME III-c Waste gas decay tanks FSAR Table 11-7, Static Nozzles and flanges USAS (ANSI)- 150 lbs.
Reactor building sump pumps ASME III-c Dynamic and Static Auxiliary building sump pumps ASME III-c Static 5-123 (Rev.8)'
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