ML18018B778
| ML18018B778 | |
| Person / Time | |
|---|---|
| Site: | Harris  |
| Issue date: | 09/21/1984 |
| From: | CUTTER A B CAROLINA POWER & LIGHT CO. |
| To: | DENTON H R Office of Nuclear Reactor Regulation |
| References | |
| NLS-84-322, NUDOCS 8409260110 | |
| Download: ML18018B778 (62) | |
Text
C$k RBGULATO~INFORMATION DISTRIBUTION
~TEM (RIBS)ACCESSION NBR:8409260110 DOC~DATE: 84/09/21 NOTARIZED:
NO FACIL:50-400 Shearon Har ri s Nucl ear Power Pl anti Uni t 1i Carol ina AUTH'AME AUTHOR AFFILIATION CUTTERiA~BE Carolina Power L Light Co.REC IP.NAME RECIPIENT AFF ILIATION DFNTONiH~RE Office of Nuclear Reactor Regulationi Director
SUBJECT:
Forwards resul ts ofl'westinghouse rept re boron injection tank (BIT)concentration/elimination studyiin support of request to reduce BIT boron concentration to 0 ppm,Change would eliminate.
heat tracingireducing maint costs.,DISTRIBUTION CODE: B001D COPIES RECEIVED:LTR ENCL SIZE', TITLE: Licensing Submittal:
PSAR/FSAR Amdts 8, Related Corr espondence NOTES: DOCKET 05000400 RECIPIENT ID CODE/NAME NRR/DL/ADL NRR LB3 LA INTERNAL: ADM/LFMB IE FILE" IF/DEPER/IRB 35 NRR/DE/AEAB NRR/DE/EHEB NRR/DE/GB 28 NRR/DE/MTEB 17 NRR/DE/SGEB 25 NRR/DHFS/LQB 32 NRR'/DL/SSPB NRR/DSI/ASB NRR/DS I/CSB 09 NRR/DS I/METB 12 N R R 22 G F IL 04/MIB EXTERNAL: ACRS 41=-'MB/DSS (AMDTS)LPDR 03 NSIC 05 COPIES LTTR ENCL 1 0 1 0 1 0 1 1 1 1 1 0 1 2?1 1 1 1 1 1 1 0 1 1 1 1 1 1 1 1 1 1 1 0 6 6 1 1 1 1 1 1 RECIPIENT ID CODE/NAME NRR LB3 BC BUCKLEYiB 01 ELD/HDS1 IE/DEPER/EPB 36 IE/DQA SIP/QAB21 NRR/DE/CEB li NRR/DE/EQB 13 NRR/DE/MEB 18 NRR/DE/SAB 24 NRR/DHFS/HFEB40 NRR/DHFS/PSRB NRR/DS I'/AEB 26 NRR/DS I/CPB 10 NRR/DSI/I CSB 16 NRR/DS I/PSB 19 NRR/DSI/RSB 23 RGN2 BNL(AMDTS ONLY)FEMA-REP DIV 39 NRC PDR 02 NTIS COPIES LTTR ENCL 1 0 1 1 1 0 3 3 1 1 1 2 2 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 3 3 1 1 1 1 1 1 1 TOTAL NUMBER OF COPIES REQUIRED: LTTR 54 ENCL 46 I'a e~1 11 W I pt P 0 ii, t U li
@ME Carolina Power 8 Light Company SEP 31 tS84 0 SERIAL: NLS-84-322 Mr.Harold R.Denton, Director Office of Nuclear Reactor Regulation United States Nuclear Regulatory Commission Washington, DC 20555 SHEARON HARRIS NUCLEAR POWER PLANT UNIT NO~1-DOCKET NO.50-400 BORON INJECTION TANK CONCENTRATION REDUCTION
Dear Mr.Denton:
Carolina Power&Light Company hereby submits information to justify reducing the boron concentration in the Boron Injection Tank (BIT)to zero ppm (Attachment 1).Reducing the boron concentration in the BIT eliminates the need for heat tracing of the system.This will translate into considerable maintenance savings and a slight decrease in plant electrical load.Additionally, all technical specifications concerning BIT boron concentrations, temperatures, and associated surveillance/maintenance, exclusive of the Refueling Mater Storage Tank, will be eliminated.
Carolina Power&Light Company is proceeding to implement the subject design modifications.
Therefore, your prompt review and approval of this submittal is appreciated.
Changes to the Final Safety Analysis Report will be submitted in a future amendment.
If you have any questions, please contact Mr.S.R.Zimmerman at (919)836-6242.Your ery tr.B.Cutter-Vice resident Nuclear Engineering
&Licensing GAS/ccc (356GAS)cct Mr.B.C.Buckley (NRC)Mr.L.B.Marsh (NRC)Mr.G.F.Maxwell (NRC-SHNPP)
Mr.J.P.O'Reilly (NRC-RII)Mr.Travis Payne (KUDZU)Mr.Daniel F.Read (CHANGE/ELP)
Chapel Hill Public Library Wake County Public Library Mr.Wells Eddleman Mr.John D.Runkle Dr.Richard D.Wilson Mr.G.O.Bright (ASLB)Dr.J.H.Carpenter (ASLB)Mr.J.L.Kelley (ASLB)Mr.E.C.Marinos (NRC-RSB)SOiiO SeOml OCK 05OOaeOO-A PDR AD 411 Fayettevilte Street o P.O.Box 1551 o Raleigh, N.C.27602 Qo l I
ATTACHMENT I RESULTS OF THE REPORT FOR THE BIT CONCENTRATION REDUCTION/BIT ELIMINATION STUDY FOR THE SHEARON HARRIS NUCLEAR POWER PLANT BY WESTINGHOUSE ELECTRICAL CORPORATION FOR CAROLINA POWER 6 LIGHT COMPANY 1 (356GAS/ccc)
Introduction Westinghouse has developed improved analytical techniques which allow a reduction in the Boron Inj ection Tank (BIT)concentration or bypassing/elimination of the BIT, which removes it from the Safety Inj ection System.This report provides information to substantiate a reduction in the BIT boron concentration for the Shearon Harris Nuclear Power Plant (SHNPP).Back round on Existi Desi n and Anal sis The BIT is a component of the Safety Injection System whose sole function is to provide concentrated boric acid to the Reactor Coolant System (RCS)to mitigate the consequences of postulated steamline break accidents.
Although the BIT acts to mitigate steamline breaks of various sizes occurring from any power level, the cases which serve as the Westinghouse steamline break licensing basis and which define the existing requirements on the minimum BIT boron concentration are as follows: For the"hypothetical" steamline break;i.e., double-ended rupture of a main steamline, the radiation releases must remain within the requirements of 10 CFR 100.This is the ANSI N18.2 criterion for Condition IV events.The SHNPP conservatively meets this criterion by demonstrating that the DNB design basis, the criterion typically used for Condition II events, is met.For the"credible" steamline break;i.e., the failure open of a single steam generator relief, safety, or turbine bypass valve, the radiation releases must remain within the requirements of 10 CFR 20.This is the ANSI N18.2 criterion for Condition II events.Westinghouse has conservatively demonstrated compliance with this criterion for the SHNPP by demonstrating that no return to criticality is achieved.Descri tion of the Anal ses The only accident analyses which are significantly affected by BIT boron concentration reduction are the steamline break transients.
These transients are affected with respect to both core integrity and mass and energy release to containment.
For the SHNPP, the system was analyzed assuming that the BIT remains installed, without heat tracing, and with the boric acid concentration reduced to zero ppm.This combination provides the most limiting case for the analyses.This case is considered because it allows elimination of the presently specified heat tracing associated with the BIT.Additionally, all technical specifications concerning BIT concentrations, temperatures, and associated surveillance, exclusive of the Refueling Water Storage Tank (RWST), can be eliminated.
(356GAS/ccc)
Core Inte rit Anal sis The following cases were reanalyzed for the reduction in the BIT boron concentration with respect to the core integrity: "Hypothetical" steamline break, with and without off-site power available, for the largest double-ended rupture of a steam pipe (1.4 ft2)."Credible" steamline break, with off-site power available, for the largest single failed open steam generator relief, safety or steam dump valve.For the hypothetical breaks, the same criteria is applied as that applied in the FSAR.That is, for the most severe Condition IV break, Westinghouse concluded that the radiation releases were within the requirements of 10 CFR 100 by demonstrating that the DNB design basis is met.The steamline break dose calculations performed for the FSAR use a conservative fuel failure level of one (1)percent.The core analyses however show that no consequential fuel failures are anticipated.
The credible steamline break analysis is performed using a new criterion whereby the plant may return to criticality, but no damage may occur to the fuel.This constitutes a relaxation of the conservative internal Westinghouse criterion for Condition II events.This new criterion is in compliance with the criteria used by the NRC and ANS which require that releases during steamline.break accidents remain within the limits set forth in 10 CFR 20.If it is assured that there is no consequential fuel damage, the limits stipulated in 10 CFR 20 are met with a return to criticality.
Anal sis Method In this analysis, the system transient parameters; i.e., Reactor Coolant System (RCS)pressure, temperature, steam flow, core boron concentration and core power were calculated by using the LOFTRAN System Transient Analysis computex code (Reference 1).This computer code includes models of the reactor core, protection systems, and engineered safeguards system.The change in Safety In)ection System initial concentration and temperatures were introduced into the analysis in the LOFTRAN code.For the"hypothetical" breaks, the plant is initially assumed to be at hot zero power at the minimum required shutdown margin.Following the break, the RCS temperatures and pressures decrease rapidly, and in the presence of a large End of Life (EOL)moderator coefficient of reactivity, the reactor returns critical with the rods inserted, assuming the most reactive RCCA in the fully withdrawn position.The reactor power increases at a decxeasing rate until boron from the Safety In)ection System reaches the coxe and begins to offset the positive reactivity insertion caused by the cool-down.
The core is subsequently brought subcritical with boron inj ection, aided by the abatement and eventual termination of steam flow from the faulted steam generator.
(356GAS/ccc)
The attached Figures 1 through 6 show the transient behavior for the hypothetical breaks.A comparison of these figures with the current FSAR figures reveals only small changes in RCS parameters, with the single exception of core power, which is understandably higher for the cases without the BIT.The effect of the boron on the total reactivity is both delayed and damped in the attached figures because the Safety Injection System must purge more water before inj ecting boron in the cold leg and the fact that the boron source (RWST)is both colder and of a lower boron concentration.
This causes the power to initially rise to a higher peak due to the delay and to subsequent decay at a slower rate after the boron reaches the core.Additionally, with the BIT assumed to be at zero ppm concentration, the BIT acts as a dilution volume for the borated water being inj ected from the,RWST, thereby further delaying the effectiveness of the RWST.After verifying that the case assuming full reactor coolant flow will remain limiting relative to the case without off-site power, DNB analyses were performed using the same design verification procedure that is used for the FSAR cases.The DNB analyses show that the DNB design basis is met, and that no consequential fuel failures are anticipated.
The dose evaluation, which is performed assuming one (1)percent failed fuel, continues to demonstrate that the Condition IV accident criteria are satisfied.
Attached Figures 7 and 8 depict system transient parameters for the Condition II steamline break in the FSAR.This Westinghouse criterion assures that the DNB design basis is met in a very conservative manner.In order to substantiate reduction of the boron concentration in the BIT, the Westinghouse criterion was relaxed to allow a subsequent return to power for the Condition II transients, but in order to meet, the 10 CFR 20 dose requirements, the DNB design basis had to be met.Figure 7 shows that criticality is attained for the assumed BIT elimination.
DNB analyses for this case show that the DNB design basis is met and no fuel failures are predicted.
This conclusion is also consistent with the conclusion drawn on the Condition IV breaks, since no violation of the DNB design basis was calculated for the more extreme Condition IV, double-ended ruptures.Thus, calculations have been performed for the SHNPP which show that for the present NRC criterion for Condition II events, Carolina Power&Light Company (CP&L)may reduce the boron concentration in the BIT to zero ppm.The same criteria for the Condition IV steamline breaks that was used in the FSAR can be met for this elimination.
Hass and Ener Releases A spectrum of break sizes at various power levels were reanalyzed for the'eduction in the BIT boron concentration to zero ppm.The breaks analyzed are listed in Table l.(356GAS/ccc)
~I~Anal sis Method The mass and energy release was analyzed by Westinghouse using the MARVEL Code (Reference 2).The analysis assumptions are essentially identical to the analysis described in the FSAR with the exception of the temperature and boron concentration of the BXT.The mass and energy releases for the break cases indicated in Table 1 are provided as Appendix A.Based upon the Westinghouse analysis, a new containment pressure and temperature analysis was completed.
The results of this analysis are in Appendix B to this report.The new maximum peak containment temperature is 379'F which is 3'igher than the present FSAR value, but still within the 380'P values used for equipment qualification.
Por the pressure, the worst case was found to be the zero power, full double-ended break with a single failure of a feedwater isolation valve.This is different from the present FSAR worst case which is at 30 percent power.The new maximum peak containment pressure is 39.1 psig which is higher than the present FSAR value of 35.4 psig, but well within the containment design limit of 45 psig.CPGL has reviewed and concluded that the new containment peak temperature and pressure, as they related to balance-of-plant design, are acceptable.
Conclusion As a result of these analyses, CPGL proposes to reduce the boron inj ection tank boron concentration to zero ppm.FSAR changes resulting from these analyses will be incorporated in a future amendment to the FSAR.(356GAS/ccc)
REFERENCES l.WCAP-7907, T.W.T.Burnett, et.al.,"LOFTRAN Code Description," October 197 2.2.WCAP-9235, R.Krise and S.Miranda,"MARVEL Code Description," August 1978.(356GAS/ccc)
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~~I i'.25000.22500.20000.17500.15000.12500.10000 ,07500.05000.02500 0.0 Acvg.6 I C CX: ED X C)Ls C)4J La~25000.22500.20000.17500.15000.12500.10000.07500.05000.02500 0,0 2500.0 2250.0.2000.0~1750.0 1500.0 1250.0 1000.00 750.00 500.00 800.00 70C.00 600.00 500.00~on.oo 300.00 200.00 100.00 0.0 100 200 300<00":00 ooG Time (sec)1.4 ft Steamline Ruo".ure 2 Oi'fsite Power.'lot Available I~I\g~~CL X LW 4 600.00 550.00 500.00 F50.00 io0.00 350.00 300.00 250.00 wlTA(.T t OoPS PAO%ED Loo P 600.00 0-SSO.00 soo.oo Iso.00 ioo.00 cD 350.00 300.00 250.00 2500.0 2000.0 X cL 1000.00 0.0 0'-2000.0-2500.0 500.00 ioo.oo 300.00 CD 200, 00 100.00 0.0'.00 200 300~CO":00 Time (sec)1.4 ft SteamIine Ruoture 2 Of f s i te Power Jot Ava i I ah I e 1.0000 80000 60000~%0000'.0 C)~20000 K C)CD 3.5000 3.0000 2.5000 2~0000 1.5000 1.0000.50000 0.0<gVmT Loan~0 0<I~D 1100.0 1000, 00 800.00 600.00 400.00 200.00 0.0 1.2000 1.0000 ,80000.60000.40000.20000 0.0 i00 l&,Ac r ZOO 300 L-oo P F00 Time (sec)1.4 rt Steam)inc Ruoture Offsite Power.'Iot Avai'~able
~~l~~Cg X CD CD X X 4J 3.50GO 3.0000 2.5000 2.0000 l.58X 1.0000.50000 0.0 CD CD CD FIG~RG 7 CD CD CD CD CD CD CD CD C)CD CD Ed 600.Oe 550.OO 5OO.00 i50.00 100.00 a 350.00 300.00 250.OO C7 C7 CD CD CD Cl CD CD~m CD C)CD CD CD Ct CD CD C)CD CD 2500.0 2000.0~f000.OO I 0.0-:ceo.oo~<000.0 MOO.0 CI CD AJ O CD C)m CD CD CD CD CD CD ri6ul2'E'D.l.P-'5 Tii4IE (SEC)FAILURE OF A STIEAi1 GENERATOR SAFETY OR OUMP'IAL'lE 2'"0 a-c'ZCQ Q iQQQ.0 t 7'.Q.0 l500.0 1250.0 1QQO.00 7 0.00 500.00 800.00 700.OO 4 g 600.00 500.aa 400.00 3OO.00 cD 200.00 a.i00.00 0.0 500.00 400.00 300.QO 200.00 i00.00 0.0 a Cl Cl C7 Cl C)Cl AJ CD CI CD CD C)TIHK (SEC)FAILURE OF A STEAM GENERATOR SAFE: Y OR OUMP'lAL'/E TABLE BREAK DESCRIPTIONS FOR iRASS ANO ENERGY Break Size Power Level 1.4 ft Double-Ended Rupture (OER)2 1024 Power.6 ft OER 102%Power.645 ft Split Break 102$Power 1.4 ft OER 705 Power.5 ft OER.681 f t Sp 1 i t Break 705 Power 705 Power 1.4 ft OER 30%Power.4 ft OER 30~Power.7065 ft Split Break 305 Power 1.4 ft OFR.1 ft OER 05 Power 0%Power.3 ft Split Break 2 05 Power 5013/:10/011984 APPENDIX A MASS/ENERGY RELEASE DATA (356GAS/mf)
1.4 FT2 OE RUPTURE AT$02 PC POWER XXX FR0$4 1G24018 T IIIE SEC.0.00.I.00 2.00 3.00 4.00 5.00 6.00 7.00 8:00 9.00 10.00 11.00 12.00 13.00 14.00 15.00$7.50 20.00 22.50 25.00 27.50 30.00 35.00 40.00 45.00 50.00 60.00 70.00 80.00 90.00 100.00 120.00 140.00 I GO.00 180.00 FORWA FLOW LB/SEC 0'liHO-.OO 277 1.26 2531.4 I 2339.49 218$.36 2090.33 2043.88 1998.83 1953.33 1906.04 1857.08 1807.30 1759.11 17 11.87 1664.06 1617.39 1508.59 14 18.17 1338.84 1270.30 1209.84$156.72 1070.77 1009.68 9G5.24 93$.78 884.88 852.72 828.40 809.43 795.53 778.28 766.58 757.56 750.20 RO FLOW ENTIIALPY 8 IU/LB ($,9 64m4-1195.89 1198.14 1199.80 1201.01 1201.39$201.74 1202.07 1202.39$202.7$$203.02 1203.31 1203.56 1203.80 1204.01 1204.20 1204.53 1204.71 1204.79 1204.78 1204.71 1204.60 1204.3 I 1204.01$203.74 1203.50 1203.11 1202.80 1202.55 1202.33 1202.17 1201.95 1201.79 1201.e7 1201.57 PRESSURE PSIA IOOS.81 915.47 843.83 784.83 736.50 720.30 704.72 689.29 673.40 656.83 639.80 622.61 eoe.45 590.05 573.74 557.74 521.$7 490.60 463.64 440.23 419.56 401.41 372.I I 351.31 336.10 324.60 308.39 297.20 288.71 282.09 277.25 271.12 267.03 263.88 261.29 Tl Tl Tl TI TI Tl Tl Tl TI Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl TI Tl+Tl+Tl Tl+T I IIE SEC.0.00 1.00 2.00 3.00 4.00 6.00 7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 17.50 20.00 22.50 25.00 27.50 3O.OO 35.00 40.00 45.00 50.00 60.00 70.00 80.00 90.00 100.00$20.00 140.00 160.00 180.00 REVERSE FLO'W FLOW LB/SEC g t'I 9$.$0-.00 5542.52 5062.81 4679.03 43G3.10 4182.30 4092.18 4006.59 3922.06 3835.42 3745.96 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0,00 0.00 0.00 0.00 0.00 0.00 ENTIIALPY Blu/LB 1192.72 I 195.89 1198.14 1199.80 1201.01 1201.38 1201.72 1202.03 1202.33 1202.62 1202.91 1202.77 1202.21 1201.68 1201.19 1200.75 I 199.85 1199.21 1198.76 1198.38 1198.10 1197.92 1197.69 1197.56 I 197.50 1197.47 1197.45 1197.47 1197.54'1197.65'I 197.78 1198.08 I$98.39 1198.66 1198.91 1.4 FT2 OE RUPTURE AT 102 PC POWER-XXX FROM TG240IB T I ME SEC.200.00 220.00 240.00 260.00 280.00 300.00 FORWARD FLOW FLOW ENTHALPY LB/SEC BTU/LB 743.13 1201.47 735.76-1201.36 670.58 1200.21 571.99 1198.15 506.38 1196.36 436.97 1194.02 PRESSURE PSlA 258.78 256.17 231.49 197.17 173.90 149.41 7 IME SEC.T I+200.00 T I+220.00 T I+240.00 T I+260.00 T I+280.00 T I+300.00 REVERSE FLOW FLOW LB/SEC 0.00 0.00 0.00 0.00 0.00 0.00 ENTIIALPY BTU/LB 1199.12 1199.31 1199.49 I 199.67 1199.84 1199.99
.60 FI2 OE RUPTURE AT 102 PC POWER ORY 5 TEAM I IME SEC.0.00 1.00 2.00 3-00 4.00 5.00 6.00 7.00 8.00 9.00 10.00$1.00 12.00 13.00 14.00 15.00 17.50 20.00 22.50 25.00 27.50 30.00 35.00 40.00 45.00 50.00 60.00 70.00 80.00 90.00 100.00 120.00 140, 00 I GO.00 180.OQ FOR WA F I.OW I.B/SEC l253.(e-.00-$1227.98 1185.98 I 15'I.12 1120.39 1108.69 I I IQ.80 I I 10.13 110G.13 1098.42 1087.35$073.70 1058.27'l04$.77 1024.78 1007.77 974.63 943.38 912.91 884.13 857.76 833.88 794.16 761.21 733.10 709.14 67$.16 64 I.62 618.10 598,82 582.41 557.94 539.63 526.40 516.14 RO FLOW ENTIIALPY BTU/Le I f2,7Ar48-.44
$194.04 I 195.06$195.92 1196.64 1196.56 1196.54 1196.59 1196.74 1196.97 I'I97.28 I 197.63 1198.01 1198.40 1198.79 1199.16 1199.82'1200.46'I 20$,05 I201.57'I202.01.1202.39'1202.98 1203.41'1203.74 1203.99 1204.33 1204.53 1204.65 1204.73 1204.77 1204.79 I204.78 1204.75 1204.71 PRESSURE I SIA'I005.81 969.27 939.96 914.6Q 892.21 894.99 895.57 893.8$889.25 881.85 872.11 860.66 848.08 834.89 821.48 808.19 783.73 759.09 735.12 7$2.60 692.00 673.35 642.31 616.29 594.05 575.24 544.97 521.35 502.48 486.96 473.74 453.57 438.8S 428.25 419.99 Tl Tl Tl Tl Tl Tl Tl TI Tl Tl TI Tl Tl TI Tl TI'll TI II Tl Tl Tl Tl TI Tl Tl Tl Tl TI TI TI Tl$1 T IME SEC.0.00 1.00 2.00 3~00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00'I 2.00 13.00 14.00 15.00+17.50+20.00+22.50 25.00 27.50 30.00 40.00 45.00 50.00 60.00 70.00 80.00 90.00 100.00 120.00 140.00 160.00 180.00 REVERSE FLOW FLOW LB/SEC Igf3.$~1238.7 I 1209.86 1181.62 1154.15 1153.17 I 173.46 1189.54 1201.23 1208.17 12$0.55 1209.00 1204.25 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0,00 0.00 0.00 0.00 0.00 0.00 ENTIIALP Y BIU/LB$192.72 1193.53 1194.32 1195.07 1195.76'I 195.17 1194.69 1194.31 1194.06 1193.93 I'I93.92'I 194.01 I 194.18 1194.$0 1193.82 1193.61 1192.78 1192.20 1191.81'I 191.55 1191.37 I IS I.23 1191.06 1190.97 1190.94 1190.92 I$90.94 1191.06 1191.29 1191.60 1191.96 1192.8 I$193.7 I 1194.59 1195.40 1.4 F I2 DE RUPTURE AT 70 PC POWER-XXX FROM IG340IE I I ME SEC.200.00 220.00 240.00 260.00 280.00 300.00 FORWARD FLOW FLOW ENTIIALPY LB/SEC BIU/LB 7 I I.26 1200.92 680.99 1200.47 660.60 1200.09 634.66 1199.58 599.96 1198.83 560.07 1197.90 PRESSURE PSIA 246.12 236.65 229.30 219.96 207.51 193.58 TIME SEC.T I+200.00 T I+220.00 T I+240.00 T I+260.00 I I i 280.00 T I+300.00 REVERSE FLOW FLOW LB/SEC 0.00 0.00 0.00 0.00 0.00 0.00 ENTIIALPY BTU/LB 1200.02 1200.13 1200.25 1200.38 1200.5'I 1200.65
.5 FT2 OE RUPTURE AT 70 PC POWER ORY 5 TEA14 T I SIE SEC.0.00 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.OO 10.00 11.00 12.00 13.00 14.00 15.00 17 50 20.00 22;50 25.00 27.50 30.00 35.00 40.00 45.00 50.00 60.00 70.00 80.00 90.00 100.00 120.00 140.00 I GO.00 100.00 I 100.73 1070.10 1042.52 1015.40 990.01 967.39 947.37 934.72 927.62 920.09 91'l.54 901.49 889 06 076.92 063.07 040.03 817 06 793.68 771.30 750.69 731.57 697.61 668.91 645.19 624.GB 591.09 565.00 543.04 526.12 511.50 489.73 473.68 461.95 453.00 1191.32 I 192.32 1193.24 1194.12 1194.90 1195.57 1196.16 1196.37 1196.59 1196.03 1197.10 1197.42 1197.77 1198.15 1190.54 1199.09 1199.69 1200.27 1200.79 1201.25 1201.66 1202.33 1202.05 1203.24 1203.55 1203.99 1204.27 1204.4G 1204.59 1204.67 1204.76 1204.79 1204.79 1204.78 FORWARO FLOW FI.OW ENTIIALPY LB/SEC BTU/I.B Illa.I o.Oo IISo Assa-.Gr PRESSURE PSIA 1073.63 1043.01 1016.7 I 991.52 966.98 944.69 924.87 907.27 900.71 093.93 806.47 877.78 867.60 856.01 843.36 830.03 8 10.82 780.84 766.79 745.88 726.47 708.51 676.53 649.54 627.05 607.56 575.71 550.71 530 37 513.29 499.20 471.71 462.31 451.01 442.46 TI Tl TI Tl Tl Tl Tl TI Tl TI Tl Tl Tl TI Tl Tl Tl Tl Tl Tl Tl'T l Tl Tl Tl Tl Tl Tl Tl TI Tl Tl TI T I HE SEC.0.00 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.GO 17.50 20.00 22.50 25.00 27.50 30.00 35.00 40.00 45.00 50.00 60.00 70.00 80.00.90.00 100.00 120.00 140.00 160.00 180.00 REVERSE FLOW FLOW LB/SEC IIIS.]1107.50 1004.13 1059.31 1033.17 1008.06 98S.4O BG5.23 959.22 964.45 960.11 969.93 969.57 966.92 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00'0.00 0.00 0.00 0.00 0.00 ENTIIALPY Bill/LB 1190.12 1190.92 1191.77 1192.66 1193.53 1194.32 1195.0'I 1195.61 1195.42 1195.28 1195.19 1195.17 1195.21 1195.33 1195.10 1194.95 1194.13 1193.63 1193.32 1193.12 1192.97 I 192.88 1192.77 1192.73 1192.72 1192.72 1192.75 1192.07 1193.06 1193.32 1193.62 1194.33 1195.09 1195.01 1196.48
.5 FT2 OE RUPTURE AT 70 PC POWER-ORY STEAM TIME SEC.200.00 220.00 240.00 260.00 280.00 300.00 FORWARD FLOW FLO'W ENTIIALPY LB/SEC BTU/LB 446.30 1204.77 441.14 1204.76 437.03 1204.74 433.54 1204.73 430.33 1204.72 427.25 1204.70 PRESSURE PS1A 435.91 430.93 426.94 423.54 420.41 417.39 TTME SEC.T1+200.00 T1+220.00 T1+240.00 T1 i 260.00 T1 i 280.00 T1 i 300.00 REVERSE FLOW FLOW LB/SEC 0.00 0.00 0.00 0.00 0.00 0.00 ENTIIALPY BTU/LB 1197.08 1197.60 1198.04 1198.43 1198.77 1199.06 70 PERCENT POWER T I ME SEC.FLOM IB/SEC ENTIIAI.PY eTU/LO PRESSURE PSTA ISOLATION AT (SEC)$'$$$$$$$'$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$'$$30 40 50 60 70 80 1.00 2 00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00'I 1.00 12,00 13.00 11.00 15.00 16.00 17.00 18 00 19.00 20, 00 21.00 22.00 23.00 24.00 25.00 26 00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34.00 35 00 503.67 496.38 489.84 483.9 I 478.51 473.57 469.06 464.92 461.13 457.65 154 46 451.55 448.88 446.46 4 14,27 442.30 440.54 438.98 437 59 436.36 435.29 434 35 433 53 432 83 432.22 431.70 431.27 430.90 430.59 430.33 430.'12 429.95 429.82 429, 71 429.63 1190.74 1191.28 1191.76 1192.19 1192.58 1192.93 1193.25 1193.55 1193.81 1194.05 1194.27 1194.47 1194.66 1194.82 1194.97 1195.10 1195.21 1195.32 1195.4 I 1195.48 1195.55 1195.61 1195.67 1195.71 1195.75 1195.78 1195.81 1195.83 1195.85 1195.87 I 195.88 1195.89 1195.90 1195 91 1195 91 1058.02 1044.11 103 I.52 1020.05 1009.57 999,99 991.19 983.12 975.72 968.93 962.69 956.99 951.79 947.08 942.82 939.00 935.60 932.57 929.89 927.53 925.47 923.67 922.11 920.77 919.62 918.64 917.81 917.I I 916.53 916.06 915.67 915.36 915.11 914.92 911 78 1.000 I.000 I.000 1.000 I.000 1.000 1.000 1.000 I.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 I.000 1.000 1.000 1.000 1.000 1.000 1.000 I.000 I.000 1.000 I.000 1.000 I.000 I.000.992.981.976.971.965 1.000 1.000 1.000 1.000 I.000 1.000 1.000 I.000 I.000 I.000 I.000 1.000 1.000 1.000 1.000 I.000 1.000 1.000 I.000 1.000 1.000 1.000 I 000 I.000 1.000 1.000 1.000 I.000 1.000 I.000 1.000 1.000 1.000 I.000 1.000 1.000 I.000 1.000 1.000 I.000 1.000 1.000 I.000 I.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000'.000 1.000 1.000 I.000 I.000 I.000 1.000 1.000 I.000 1.000 1.000 1.000 1.000 1.000 I.000'.000 I.000 1.000 I.000 I.000 I.000 1.000 1.000 1.000 I.000 I.000 I.000 I.000 I.000 1.000 1.000 I.000 I.000 1.000 1.000 1.000 1.000 1.000 I.000 1.000 I.000 I.000 I.000 1.000 I.000 I.000 I.000 1.000 1.000 I.000 1.000 I.000 I.000 1.000 I.000 1.000 I.000 1.000 1.000 I.000 I.000 I 000 1.000 1.000 1.000 I.000 1.000 I.000 I 000 1.000 I.000 1.000 1.000 I.000 1.000 1.000 1.000 1.000 I.000 1.000 1.000 1.000 1.000 1.000 1.000 I.000 1.000 1.000 1.000 1.000 1.000 1.000 I.000 I.000 1.000 I.000 I.000 I.000 I.000 1.000 1.000 1.000 1.000 1-000 I.000 1.000 1.000 I.000 1.000 1.000 1.000 1.000 1.000 I.000 I.000 I.000 1.000 1.000 1.000 1.000 1.000 1.000 70 PERCENT PURER TIME SEC.F I.OM LB/SEC ENTIIAI.PY 8 IU/LB PRESSURE PSIA ISOLATION AT I SEC)$$$$$$$$$$$'$$$$$$$$$$$$$$$$'$$$$$$$$$$$$$$$$$$30 40 50 60 70 80 36.00 37.00 38.00 39 00 40.00 41.00 42.00 43.00 44.00 45.00 46.00 47.00 48.00 49.00 50.00 51.00 52.00 53.00 54 00 55.00 56 00 57.00 58.00 59.00 60.00 61.00 62.00 63.00 64.00 65 00 GG.OO 67,00 68 00 69 00 70.00 429.57 429.53 429 51 429.50 429,50 429.51 429.52 429.55 429.57 429.60 429.64 429.68 429.7 I 429.75 429.80 429.84 429.88 429.92 429.96 430.00 430.05 430.09 430.13 430.17 430.20 430.24 430.28 430.31 430.35 430.38 430.42 430.45 430.18 430.51 430,51 1195.91 1195.92 1195.52 1195.92 I'195.92 1195.92 1195.91 1195.91 1195.91 1195.91 1195.91 I 195.90 1195.90 I 195.90 1195.90 1195.89 1195.89 1195.89 1195.88 1195.88 1195.88 1195.88 1195-87 1195.87 I 195.87 1195.87 1195.86 1195.86 1195.86 1195.86 1195.85 I 195.85 1195.85 1195.85 1195 85 914.68 914.62 914.58 914.57 914.58 914.60 914.65 914.70 914.76 914.83 914.90 914.98 915.0G 915.'l4 915.23 915.31 915.40 915.49 9 IS.57 915.66 915,74 915.82 915.90 915.98 916.06 916.14 916 21 916.28 916,3G 916 42 916.~'I9 916.56 916.62 916,69 916,75.959.950.910.926.912.896.880.BG4.849.836.823.811.800.789.780.771.763.755.747.7 IO.733.726.720.714.708.703.698.693.688.684.679" 675.671.667.663 1.000 I.000 I.000 I.000 1-000.992.982.977.972.967.960.952.941.928.913.897.881.865.850.836.823.811.800.790.781.772.7G3.755 ,748.741.734.727.721.715.709 I.000 I.000 I.000 1.000 I.000 1.000 I.000 I.000 I.000 1.000 1.000 I.000 I.000 I.000 I.000.992.982.977.972.967.960.952.941.927.912.896.880.864.849.835.822.810.799.788.779 I.000 I.000 I.000 I.000 I.000 1.000 1.000 1.000 1.000 1.000 I.000'I.000 I.000 I.000 1.000 1.000 I.000 1.000 1.000 1.000 I.000 I.000 1.000 1.000 1.000.992.982.976.971.966.960.951.940.926.911 I.000 1.000 1.000 I.000 I.000 1.000 1.000 I.000 1.000 1.000 I.000 I.000 1.000 1.000 1.000 I.000 I.000 I.000 1.000 I.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 I.000 I.000 I.000 1.000 1,000 1.000 I 000 1.000 1.000 1.000 1.000 I.000 I.000 1.000 I.000 1.000 I.000 I.000'I.000 1.000 I.000 I.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000'.000 1.000 1.000 1.000 1.000 I.000 1.000 I.000 I.000 I.000 I.000 70 PERCENI POWER TIME SEC.FLOW LB/SEC ENT I IAL P Y B IU/LB PRESSURE PSIA ISOLATION AT (SEC)$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$30 40 50 60 70 80 71.00 72.00 73.00 74.00 75.00 76.00 77.00 78.00 79.00 80.00 81.00 82.00 83.00 84.00 85.00'6.00 87.00 88.00 89.00 90.00 91.00 92.00 93.00 94 00 95.00 96.00 97.00 98.00 99 00 100.00 102.00 104,00 106 00 108 00 110.00 430,57 130.60 430.63 430.66 430.68 430.71 430.74 430.76 430.79 430.8 I 430.84 430.8G 430.89 430.9 I 430.94 430.96 430,98 431.01 431.03 431.05 43'1.08 431.10 431.12 431.14 431.IG 431.19 431.21 431.23 431.25 431.27 431.30 43 I.34 431.37 431.41 431.45 I 195 80 1195.79 1195.79 1195.79 1195.79 1195.78'1195.84 1195.84 1195.84 1195 84 1195.84 1195.83 1195.83 1195.83 1195.83 1195.83 I 195.83 1195.82 I'195.82 I'195.82 1195 82 1195.82 1195.82 1195.81 1195.81 1195.81 1195.81 1195.81 1195.81 1195,80 1195.80 1195.80 1195.80 1195.80 1195,80 916.81 916.87 916,92 916.98 917.03 917.09 917.14 917.20 917.25 917.30 917.35 917.40 917.45 917.50 917.55 917.60 917.65 917.70 917.75 917.79 917.84 917.88 917.93 917.97 918.02 918.0G 918.I I 918.15 918.19 918.23 918.31 918.39 918.47 918.54 918.62.659.655.652.648.645.642.638.635.632.629.626.623.620.617.614.612.609.606.604.601.599.596.594.591.589.586.584.582.580.577.574.570.566.562.558.704.699.694.689.685 ,680.676.672.668.GG4.660.657.653.650.646.639.636.633.630.627.624.621.618.615.613.610.607.605.602.598.593.588.584.579.770.762.754.747.739.733.726.720.714.708.703.698.693.688.684.680.676.671.667.664.660.656.652.649.646.642.639.635.632.629.625.619.613.608.603.895.991.878.982.862.976.847.971.833.966.820.959.808.950.797.939.787.925.777.910.769.893.760.877.752..860.745.845.738.831.731.818.725.806.718.795.713.785.707.775.702.767.697.759.692.751.687.743.683.736.679.730.675.723.670.717.GGG.711.663.706.657.698.650.688.643.680.63G.67 1.630.663 1.000 1.000 I.000 1.000 1.000 1.000 I.000 1.000 1.000 1.000.991.981.976.971.965.959 ,950.938.924.908.892.875.858.843.829.816.804.793.783.774.761.745.731.719.707
.60 FT2 OE RUPTURE AT 102 PC POWER-ORY STEAM TIME SEC.200.00 220.00 240.00 260.00 280.00 300.00 FORWARO FLOW Fl.OW ENTHALPY LB/SEC BTU/LB 507.46 1204.68 500.20 1204.64 493.91 1204.61 488.33 1204.57 482.99 1204.53 477.76 1204.49 PRESSURE PSIA 412.94 407.05 401.95 397.40 393.04 388.77 Tl Tl Tl Tl Tl Tl T IME SEC.+200.00+220.00+240.00+260.00+280.00+300.00 REVERSE FLOW FLOW ENTHALPY LB/SEC 8 IU/LB 0.00 1196.12 0.00 1196.74 0.00 1197.27 0.00 1197.72 0.00 1198.12 0.00 1198.47 102 PC POWER IIME SEC, F I.OW LB/SEC ENTIIAI PY B I U/LB PRESSURE PSIA ISOLATION AT (SEC)$$$$$$$$$$$$$$$$$$$$$$'$$$$$$$$$$$$$$$$$$$$$$$30 40 50 60 70 80 1.00 2 00 3 00 4.00 5.00 6.00 7 00 8.00 9.00 10 00 11.00 12.00 13.00 14 00 15 00 16,00 17.00'18.00 19.00 20 00 21 00 22.00 23.00 24 00 25.00 26.00 27 00 28.00 29.00 30,00 31.00 32.00 33.00 31 00 35 00 445.57 439.33 433,84 428.96 433.11 44 1.69 454.65 462.77 468.7G 472.58 474.51 474.92 471, 18 472.61 470.50 468.06 465,45 4G2.75 460.02 457.28 454 53 451.74 448.92 446.07 4 13.17 4 10.25 437.31 434.38 431.45 428.55 125 67 422.83 420.03 417 2G 411.53 1193.25 1193 70 1194.10 1194.45 1193.50 1192.66 1191.93 1191.35 1190.95 1190.71 I 190.62 I 190.64 1190.74 I 190.89 1191.08 1191.29 1191.51 1191.73 1191.95 1192.18 1192.40 1192.62 1192.85 1193.07 1193.30 1193.52 1193.75 119398 1194,20 1194,42 I 194,64 1194.85 1195.05 1195.26 1195.46 991.37 978.80 967.6G 957.70 984.41 1007.55 1027.00 1042.13 1052.56 1058.60 1060.98 1060.53 1057.99 1054.01 1049.I I 1043,69 1038.00 1032.20 1026.35 1020.47 1014.54 1008.54 1002.45 996.27 990.02 983.72 977.39 97 1.07 9G4.78 958.54 952 37 9 16.27 940.24 934.29 928.12 I.000 I.000 1.000 1.000 I.000 1.000 1.000 I.000 I.000 1.000 000 1.000 I.000 1.000 1.000 I.000 1.000 I.000 1.000 I.000 I.000 1.000 I.000 1.000 1.000 1.000 I.000 1.000 I.000 1.000.971.911.913.888.BG5 I.000 I 000 I.000'.000 I.000 I.000 I.000 I.000 1.000 I.000 I.000 I.000 I.000 1.000 I.000 I.000 I.000 I.000 I.000 I: 000 I.000 I.000 1.000 1.000'I.000 I.000 I.000 1.000'I.000 1.000 I.000'I.000 1.000 1.000 1.000 1.000 1.000 I.000 I.000 I.000 I.000 1.000 1.000 I.000 I.000 I.000 I.000 1.000 1.000 1.000 I.000 1.000 1.000 I.000 1.000 1.000 1.000 1.000 1.000 I.000'I.000 1.000 I.000 1.000 1.000 1.000 1.000 1..000 000 1.000 1.000 1.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 1.000 1.000 1.000 I.000 I.000 1.000 1.000 I.000 1.000 I.000 1.000 1.000 I.000'I.000 I.000 I.000 I.000 I.000 1.000 I.000 I.000 1.000 I.000 I 000 I.000 I: 000 1.000 1.000 1.000 I.000 1.000'I.000 1.000 1.000 1.000 1.000 1.000 000 I.000 1.000 1.000 1.000 I.000 I.000 1.000 I.000 I.000 I.000 I.000 I.000 1.000 I.000 1.000 1.000 1.000 1.000 1.000 I.000 1.000 1.000 I.000 1.000 I.000 1.000 I.000 I.000 I.000 1.000 I.000 1.000 1.000 I.000 I.000 1.000 I.000 I.000 I.000 I.000 I 000 I.000 000 I, 000 1.000 I.000 1.000 I.000 1.000 I.000 I-000 1.000 1.000 I.000 I.000 I.000 102 PC POMER 7 I ME SEC.F LOFTI LB/SEC ENTIIAI P Y Ifru/LO PRESSURE PSIA*ISOLATION Af (SEC)$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$'$30 40 50 60 70 80 3G.OO 37.00 38.00 39 00 40 00 4 1.00~42 00 43 00 00 45.00 46.00 47.00 48 00 49 00 50.00 51 00 52.00 53.00 54.00 55.00 5G.OO 57.00 58 00 59,00 60,00 61,00 62,00 63.00 64.00 65.00 6G.OO 67.00 68.00 69 00 70,00 411.83 409.18 406.55 103.96 101.40 398.87 396.38 39392 391.49 389.09 386.73 384.40 382.11 379.84 377,61 375.40 373.23 371.08 368.97 366,88 364.82 362.79 360.78 358.78 356.79 354.82 352.87 350.93 349.00 347.08 345.17 313.28 341.41 339.5G 337.73 1195.65 1195 F 84 1196.03 1196.21 1196.39 1196.57 1196.74 1196.91 1197.07 1197.24 1197.39 1197.55 1197.70 1197.85 I 198.00 1198.14 1198.28 1198.42 1198.55 1198.68 1198.81 1198 93 1199.06 1199.18 1199.30 1199,42 1199,54 1199.65 1199.76 1199.88 1199 99 1200.09 1200 20 1200.30 1200 4 I 922.62 916.89 911.22 905.62 900.09 894,63 889.24 883.9 I 878 66 873.47 868.35 863.30 858.31 853.39 BIIB.54 843.75 839.02 834.35 829.74 825.19 820.71 816 27 811.86 807.48 803.13 798,82 791.53 790.27 786.02 781.80 777.62 773.47 769.36 7G5,29 7G I 28 843 824 806 789.774.760.717.736.725.715.706.698.690.683.676.669.663.657.652.646.611 ,637.632.G28.624.621.617.613.610.607.604.600.597.595.592 I.000 1.000 1.000 I.000 1.000.973.944.918.894.872.852.833.816.800.785.771.759.748.738.728.720.711 704.696.689.683.677.671.665.660.655.651:e4e.642.638 1.000 1.000 I.000 1.000 I.000 I.000 1.000 1.000 1.000 I.000 I.000 I.000 1.000 I.000 I.000.974.948.923.900.880.860.842.826.810.796.783.771.760.750.74'I.732.724.716.709.702 I.000 I.000 I.000 I.000 I.000 1,000 1.000 I.000 000 I.000 I.000 I.000 I.000 I.000 1.000 1.000 1.000 I.000 1.000 I.000 I.000 1.000 1.000 I.000 I.000.976.950.927.906.886.BG7.850.833.819.805 I.000 I.000 1.000 1,000 I.000 1.000 1.000 I.000 I.000 I.000 1.000 I.000'I.OOO I.000 1.000 I 000 I.000 f.000 I.000 1.000 I.000 I.000 I.000 1.000 I.000 I.000 1.000 1.000 I.000 1.000 1.000 1.000 I.000 1.000 I 000 1.000 I.000 1.000 I.000 1.000 1.000 1.000 1.000 I.000 I.000 1.000 1.000 I.000 I.000 f.000 1.000 1.000 1.000 1.000 I.000 1.000 1.000 1.000 I.000 I.000 1.000 I.000 I.000 I.000 1.000 I.000 I.000 I.000 1.000 1.000 102 PC POWER TIME SEC.F I.OW LB/SEC ENIIIAI PY BTU/LB PRESSURE PSIA ISOLATION AT{SEC)$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$30 40 50 60 70 80 71,00 72.00 73.00 74.00 75 00 76.00 77.00 78.00 79.00 80.00 81.00 82.00 83.00 81 00 85.00 86.00 87.00 88.00 89.00 90.00 91 00 92.00 93.00 94.00 95.00 96.00 97.00 98 00 99.00'100.00 102.00 104.00 106.00 108.00 I I O.00 335.92 334.14 332 40 330.68 329.00 327.35 325.74 324.16 322.62 321.I I 319.63 318.18 316.76 315.35 313.97 312.60 311.25 309.91 308.58 307.27 305.96 304.67 303.40 302.'l4 300.89 299,65 298.43 297.22 296.02 294 84 293.09 290.81 288.58 286.40 284.27 1200.51 1200.60 1200.70 1200.79 1200.88 1200.97 1201.05 1201.13 1201.21 1201.29 1201.36 1201.43 1201.5'I 1201~57 1201.64 1201.71 1201.77 1201.84 1201.90 1201.96 1202.03 1202.08 1202.14 1202.20 1202.26 1202.31 1202.37 1202.42'1202.47 1202.52 1202.62 1202.72 1202.81 1202.90 1202.98 757.32 753.42 749.59 745.83 742.14 738.53 734.99 731.54 728.15 724.84 721.60 718.41 715.27 712.17 709.12 706.09 703.10 700.14 697.20 694.29 691.41 688.55 685.73 682.93 680.16 677.42 674.71 672,02 669.37 666.75 66 1,60 656.57 651.65 64G.83 642.II.589.634.696.792.586.631.689.78 1.584.627.683.770.581.624.6IB.760.579.620.673.75 I.576.6 17.668.742.574.614.663.734.572.6 11.659.727.569.608.654.7 19.567.605.650.7 12.565.602.646.706.562.599.643.700.560.596.639.694.558.594.636.689.556.591.632.684.551.589.629.679.552 ,586.626.675.550.584.623.670.548.582.620.666.546.580.6'17.662.544.577.615.659.542.575.612.655.540.573.6 10.652.539.57 1.607.648.537.569.605.645.535.567.602.642.534.565.600.639.532.563.598'6:IG.530.561.596.634.529.560.594.63 1.526.557.59 1.627.523.554.587.622.520.551.583.617.518.547.579~612.515.544.576.608.973.949.927 ,907 888 870.854.838.824.811.799.788.778.7G9.760.752.744.737.730.723.717.711.706.701.696.691.686.682.678 674.668.661.655.649.643 I.000 I.000 1.000 1.000 I.000 1.000 1.000 1.000 I.000.974.952.932.913.895.878.863.848.835.822.811.800.790.781.772.764.756.749.742.736.727.716.706.697.688 102 PC POWER TIME SEC, FLOW LB/SEC ENTIIAI.PY 8 III/LB PRESSURE PSIA ISOLATION AT (SEC)$$'$$$$$$$$$$$$$$$$$$$$$$$$$$$'$'$$$$$$$$$$$$$$$30 40 50 60 70 80 112.00 114.00 116.00 118.00 120,00 122.00 124.00 12G.00 128.00 130.00 132.00 134.00 136.00 138.00 140.00 142.00 144.00 146.00 In8.00 150.00 160.00 170, 00 180 00 190: 00 20000 282.18 280.14 278.14 276.19 274.28 272.42 270.60 268.83 267.10 265.42 263.78 262.18 260.62 259.03 257.56 256.12 254.72 ,253.36 252.04 250.75 244.81 239,67 235.27 231.49 228.24 1203.06 1203.14 1203.21 1203.28 1203.35 1203.42 1203.48 1203.54 1203.60 1203.65 1203.70 1203 75 1203.80 1203.85 1203.89 1203.93 1203.97 1204.01 1204.04 1204.08 120'4.23 1204.34 1204.43 1204.50 1204.56 637.49 632.97 628 55 624.23'620.01 615.88 611.86 607.94 604.11 600.37 596.74 593.19 589.74 586.37 583.10 579.91 576.81 573.79 570.85 567.98 554.79 5na.a8 533.59 525.18 517.93.5'12.542.572.604.509.539.569.600 507.536.566..596.504.533.562.592.502.530.559.589.500.528.556 585.497.525.553.582.495.523.550.578.493.520.548.575.490.518.545.572.488.5 15.542.569.486.513.540.566.483.510.537.564.481.508.535.561.479.506.532.558.476.504.530.556.474.501.528.553.472.499.525.551.470.497.523.549.468.495.52 1.547.457.486.511.537.448.477.503.528.440.469.496.52 I.432.462.489.514.425.455.484.508.638.681.633.674.628.667.624.661.619.656.615.650.611.645.607.641.G04.636.600.632.597.628.593.624.590.620.587.617.584.613.581.610.579.607.576.604.574.601.57 1.598.56 1.587 552.577.544.5G9.537.562.532.556 1.4 F72 OE RUPTURE AT 70 PC POWER XXX FROM TG340I E TIME SEC.0.00 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 I I.00$2.00 13.00$4.oo 15.00 17.50 20.00 22.50 25.00 27.50 30.00 35.00 40.00 45.00 50.00 60.00 70.00 80.00 90.00 100.00 120.00 140.00 160.00$80.00 RO FLOW ENTIIALPY FORWA FI OW LB/SEC 3I)l.5'OOI 2973.38 27 17.32 2503.35 2318.11 2165.08 2078.36 2002.17 1933.78 1870.49 18 lo.43 1752.70 1703.38 1659.4$1615.20 1571.06 14G4.60$368.20 1287.19'l 220.31 1163.36 1113.47'1030.96 9G7.79 919.75 883.89 834.55 803.95 784.24 770.99 761.86 749.16 7$0.97 734.48 728.21 PRESSURE BTIJ/LB PSIA$/0.il663-.&V
~1073.63 980.31 902.84 835.78 778.52 738.54 710.82 686.18 663.68 642.52 622.24 602.66 587.84 572.61 557.25 542.01 505.51 472.78 445.67 422.88 403.49 386.39 358.09 336.42 319.91 307.6$290.59 280.01 273.18 268.58 265.40 260.87 258.03 255.74 253.52 1193:65 1196.30 1198.37 1199.96 1200.97 1201.61 1202.13 1202.58 1202.97 1203.32 1203.62 1203.83 1204.02 1204.20 1204.36 1204.64 1204.77$204.79$204.73$204.62 1204.47 1204.12 1203.75$203.40 1203.09 1202.6$1202.26 1202.02 1201.85 1201.73 1201.55 120$.44 1201.34 1201.25 Tl Tl Tl Tl Tl Tl TI 71 Tl Tl 7'I 71 71 Tl TI Tl Tl 7$Tl Tl 71 Tl Tl Tl Tl TI Tl Tl Tl Tl Tl 71 Tl Tl TIME SEC 0.00 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 10.00 I 1.00 12.00+13.00+14.00 15.00$7.50 20.00 22.50 25.00 27.50 30.00 35.00 40.00 45.00 50.00 60.00 70.00 80.00.90.00 100.00 120.00 140.00 I GO.OO 180.00 REVERSE FLOW FLOW LB/SEC)al'3.y~5946.77 5434.66 5006.70 4636.67 4331.86 4 162.03 4014.49 3883.71 3764.17 3651.73 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0,00 0.00 0.00 0.00 0.00 0.00 ENTHALPY BTU/Le 1190.12 I 193.65 I 196.30 1198.37 1199.96 1200.95$201.58 1202.09 1202.52 1202.89 1203.22$203.17 1202.72 1202.30 1201.91 1201.56 1200.87 1200.4 I 1200.10 1199.87 I 199.69 1199.56 1199.40$199.31 I$99.26 1199.24 1199.22 1199.22 1199.25 1199.30$199.36 1199.51 1199.65 1199.79 I$99.91 70 PERCENT POWER T I ME SEC.FLOw LB/SEC ENTIIALPY 8 7 II/LB/PRESSURE PSIA ISOLATION AT (SEC)$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$30 40 50 60 70 80 112.00 114.00 I I G.00 118.00 120.00 122.00'12400 126.00 128,00 130.00 132.00 134.00'I 36,00 138.00 140.00 142.00 144.00 146.00 148.00 150.00 160.00 170.00 180 00 190.00 200.00 431.48 431.52 431.55 431.59 431.62 431.65 431.68 431.72 431.75 431.78 431.81 431.84 431.87 431.89 431.92 431.95 431.98 432.00 432.03 432.06 432.15 432.16 432.13 432.09 432.04 1195.78 1195.78 1195.78 1195.77 1195.77 1195.77 1195.77 1195.76 1195 76 1195.76 1195 76 1195.76 1195.75 1195.75 1195.75 1195.75 1195.75 1195.75 1195.74 1195.74 1195.74 1195.74 1195.74 1195.74 1195.74 918.69 918.76 918.83 918.90 918.97 919.03 919.10 919.16 919.23 919.29 919.35 919.41 919.47 919.53 919.58 919.64 919.69 919.75 919.80 919.85 920.02 920.04 919.98 919.89 919.79.554.575.597.624.550.571.592.618.546.567.588.612.542.562.583.607.538.558.579.601.534.554.574.596.531.550.570.591.528.546.566.587.524.542.562.582.52 1.539.557.577.518.535.553.573.515.531.549.569.512.528.545.565.509.525.54 I.560.506.522.538.556.503.5 18.534.552.500.515.531.548.497.512.527.544.494.509.524.540.49 1.506.52 1.536.479.492.505.5 19.467.479.490.504.456.467.478.489.440.452.464.476.4 13.424.436.450.656.697.648.687.641.678.635.670.628.662.622.654.616.647.611.640.605.633.600.627.595.621.590.615.585.610.58 1.604.576.599.572.594.568.589.563.584.559.580.555.575.535.554.518.534.502.517'488.501.464 ,.480
1.4 F T2 Of RupluRE Al 30 pc POWER XXX FROH IG640GC T IHE SEC.0.00 I.00 2.00 3.00 4.00 5.00'6 00 7.00 8.00 9.00 10.00 I I~00$2.00$4.00$5.00 17.50 20.00 22.50 25.00 27.50 30.00 35.00 40.00 a5.00 50.00 60.00 70.00 80.00 90.00 100.00 120.00 140.00 160.00 180.00 763.88 719.22 680.91 647.60 618.10 535.14 521.25 1204.63 1204.77 1204.78 1204.70 1204.56 376.57 360.20 334.44 315.17 300.4 I 289.10 273.69 264.45 259.08 256.00 254.28 252.76 252.14$201.48 IORWARO FLOW FIOW EIITIIALPY PRESSURE LB/SEC BTU/LB PSIA 3 pig.It'0-AN 5~, I 136.48 3165.97 1191.28 1043.97 2908.$4 1194.20 964.92 2680.93 1196.69.890.82 2464.55 1198.77 , 822.10 2276.46 1200.34 2 126.48 1201.42 2005.64 1202.24 190$.75 1202.88 18 10.89$203.38 1729.84$203.78 591.47 1655.83 1204.09 56$.06 1588~16 1204.29 548.85 1549.26 1204 42 1509.50 1204.53 1469.59 1373.$8 1285.05 1208,27 I$42.70 10$$6.5G 1204.37 1038.40$204.15 9G3.10 1203.71 907.01 1203.28 864.$2 1202.90 831.26 1202.56 786.56 1202.04 759.78$201.70 744.19 735.22 1201.35 730i24$20$.28 725.87 1201.2 I 724.07 1201.$9 720~93 1201.14 250.97 716.15 120$.06 249.27 Tl TI'I l Tl Tl Tl Tl Tl Tl Tl Tl TI Tl Tl Tl Tl Tl Tl Tl Tl TI Tl Tl Tl Tl Il Tl Ti'll Tl Tl Tl TI TI T IHE SEC.0.00$.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00$1.00 12.00$3.00$4.00 15.00 17.50 20.00 22.50 25.00 27.50 30.00 35.00 40.00 aS.OO 50.00 60.00 70.00 80.00 90.00 100-00 120.00'I 40.00 160.00 180.00 REVERSE FLOW FLOW LB/SEC t.c79./~633$.94 5816.30 5361.92 4929.56 4554.53 4258.42 4023.65 3823.25 3649.10 3494.53 3353.66 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0,00 0.00 0.00 0.00,.0.00 0.00 ENTHALPY BTU/LB 1187.55 1191.28 1194.20 1196.69 I 198.76 1200.33 1201.38 1202".19$202.81 1203.30$203.68 1203.99 1203.79 1203.53$203.30 1203.08 1202.61 1202.30 1202.11$201.98 1201.88 1201.81 1201.70 1201.64 1201.59$20$.56 1201.5 I 1201.49$201.47 1201.46 1201.44 1201.42 1201.39$201.37 1201.35 1.4 FT2 OE RUPTURE AT 30 PC POWER-XXX FROM IG640GC TIME SEC.200.00 220.00 240.00 260.00 280.00 300.00 FORwARO FLOw FLOW ENTIIALPY LB/SEC BIU/LB 7 10.67 1200.97 704.38 1200.87 697.27 1200.75 657.77 1199.96 537.57 1197.22 477.02 1195.43 PRESSURE PSIA 247.32 245.08 242.54 226.76 184.57 163.54 T IME SEC.T'I+200.00 T I+220.00 T I+240.00 T I+260.00 T I+280.00 Tl+300.00 REVERSE FLOW FLOW LB/SEC 0.00 0.00 0.00 0.00 0.00 0.00 ENIIIALP Y 8 IU/LB 1201.34 1201.34 1201.35 1201.37 1201 41 1201.47
.4 FT2 DE RUPIUHE AT 30 PC POWER STEAN T luE S EC..0.00 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00 l2.00 13.00 14.00 15.00 17.50 20.00 22.50 25.00 27.50 30.00 35.00 40.00 45.00 50.00 60.00 70.00 80.00 90 00 100.00 120.OO 140.OO 160 00 180.00 FOR@A F I.OII IB/SEC gq'l.8 e-.oo 939.66 922.60 903.88 880.30 854.87 I 188.44 1189.25 1190.21 1191.33 1192.42 1193.39 1194.26 1195.04 1195.73 1196.36 1196.95 1197.51 I 198.04 1198.56 1189.0b 1199.90'1200.34 1200,80 1201.23 1201.61 1201.95 1202.51 1202.96 1203.3 I 1203.59 1204.00 1204.26 1204.44 1204.57 1204.65 1204.74 1204.78 1204.79 1204.79 830.80 808.78 788.7 I 770.33 753.29 737.24 721.79 706.65 Gs I.G7 67G.Bb 645.62 631.69 616.41 601.IO 58G,GB 573.47 550.00 529.71 512.22 4J7.09 472.05 452.39 43G.51 412.89 3J7.25 385.88 377.65 371.60 RD FLOM ENTIIALPY BTU/LB IQ~.Sm~PRESSURE PSIA 1136.48 1115.'14 1095.46 1071.39 1042.75 1014.01 987.40 963.07 940.79 920.21 900.95 882.58 864.68 846.98 829.43 812.08 780.74 763.70 745.44 727.34 710.43 694.91 667.22 643.22 622.49 604.5 I 574.79 551.24 532.18 516.59 503.76 484.48 470.85 460.96 453.69 Tl Tl Tl TI Tl 11 Tl Tl Tl TI 11 Tl Tl Tl Tl Tl Tl Tl Tl 1I Tl TI Tl Tl Tl Tl TI Tl 11 TI Tl+++++++++t++++++T IME SEC.~0.00 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 17.50 20.00 22.50 25.00 27.50 30.00 35.00 40.00 45.00 50.00 60.00 70.00 80.00 90.00 100.00 120.00 140.00 160.00 180.00 REVERSE FLOM FLOM LB/SEC/$9,g 0-.60 942.53 926.88 908.49 885.31 860.47 836.83 815.51 796.19 782.61 773.62 764.75 755.78 746.52 736.86 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 ENTIIALPY BTU/LB 1187.55 1188.26>>89.04 1189.99 I 19 I.10 1192.17 1193.12 1193.97 1194.72 I 195.08 1195.44 1195.78 1196.13 1196.49 1196.86 1196.98 1197.04 1196.73 IIS6.58 1196.53 1186.51 1196.51 1196.52 1196.54 1196.56 1196.58 1196.63 1196.72 1196.86 1197.04 1197.25 I 197.70 1198.16 1198.60 1198.99
.4 FT2 OE RUPTURE AT 30 PC POWER-ORY STEAM T I ME SEC.200.00 220.00 240.00 260.00 280.00 300.00 FORWARD FLOW FI.OW ENT'IIALPY I 8/SEC 8 IU/LB 367.13 1204.79 363.66 1204.'78 360.7 1 1204.78 358.03 1204.77 355.46 1204.76 352.92 1204.76 PRESSURE PSIA 448.30 444.10 440.52 437.25 434.11 431.00 TIME SEC.T 1+200.00 I 1+220.00 I 1 t 240.00 I 1+260.00 T I 4 28000'I l i 300.00 REVERSE FLOW FLOW LB/SEC 0.00 0.00 0.00 0.00 0.00 0.00 ENTllALPY 8 IU/L 8 1199.34 1199.64 1199.91 1200.15 1200.37 1200.57 30 PERCENT POMER T I ME SEC.FLOW LB/SEC ENTIIALPY 8TU/LB PRESSURE PSTA ISOLATION AT (SEC)$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$30 40 50 60 70 80 I.00 2 00 3.00 4.00 5.00 6.00 7.00 8.00 9 00 10.00 II 00 12 00 13 00 14.00 15 00 16, 00 17 00 18.00 19.00 20,00 21 00 22.00 23.00 24.00 25.00 26.00 27.00 28.00 29.00 30.00 31.00 32.00 33.00 34,00 35.00 509 505 99 24 500 81 49G.G4 492.71 488 99 485.46 482.08 478.86 475 78 472,83 470.00 4G7.29 464.69 462.20 459 457 80 50 455,30 453.18 451 14 449, 18 44729 445.50 443.79 442.18 440 69 4393 I 438 03 554.92'>46 89 539 53 532.73 526.4 I 520.53 515,07 1188.23 1188.84 1189.39 1189,90 I'190.37 1190.80 1191.20 1191.57 1191.91 1192.23 1192.52 1192.80 1193.05 1193.30 1193.54 1193.76 1193.97 1194.17 1194.36 1194.55 1.194.72 1194.89 1195.05 1195.20 1195.34 1195.48 1195.62 1195.74 I 195.86 1195.98 I 196.09 119G.19 1196.28 1196,37 1196 44 1120.27 I 105 48 1091.82 1079.12 1067.30 1056.30 1046.05 1036.48 1027 53 1019.13 IO I I.22 1003.74 996.64 989.86 983,39 977.20 971.27 965.58 960.13 954.89 949.87 945.05 940.42 935 97 931.GQ 927.57 923.62 919.81 9 IG.16 912.69 909.40 90G.33 903.47 900.83 898 42 I.000 1.000 1.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 1.000 I.000 I.000 1.000 I.000 1.000 1.000 1.000 1.000 1.000 1.000 I.000 I.000 1.000 I.000 I.000 I.000 1.000.985.962.941.922.905 I.000 I.000 I.000 I.000 1.000 1.000 1.000 1.000 I.000 1.000 I.000 I.000 1.000 1.000 1.000 I.000 1.000 1.000 I.000 I.000 1.000 I.000 I.000 1.000 1.000 I.000 1.000 1.000 I.000 I.000 I.000 I.000 I 000 I.000 I 000.I.000 1.000 I.000 I.000 I 000 1.000 1.000 1.000 1.000 1.000'I.000 1.000 I.000 I.000 I.000 1.000 1.000 1.000 I.000 1.000 1.000 1.000 I.000 1.000 I.000 1.000 1.000 1.000 1.000 I.000 I.000 1.000 1.000 1.000 1.000 I.000 I.000 1.000 I.000 1.000 I.000 1.000 1.000 I.000 I.000 I.000 1.000 1.000 I.000 I.000 I.000 I.000 I.000 1.000 1.000 I.000 I.000 1.000 I.000 I.000 1.000 1.000 1.000 I.000 I.000 1.000 1.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000'I.000 I.000 1.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 1.000 I.000 1.000 I.000 I.000 I.000 I.000 I.000 I.000 1.000 1.000 1.000 I.000 000 000 I.000 I, 000 I.000 I.000 1.000 I.000 I.000 1.000 I.000 I.000 I.000 1.000 1.000 I.000 I.000 I.000 I.000 1.000 I.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000 I.000 1.000 I, 000 PERCENt POWER 7 I ME F I.O'W SEC.LB/SEC EN I IIAI P Y 81U/IB PRESSURE PSIA ISOLATION Af (SEC)$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$30 40 50 60 70 80 36.00 37.00 38.00 39 00 40.00 4 1.00 42.00 43.00 44.00 45.00 46.00 47 00 48.00 49.00 50.00 51.00 52.00 53.00 54.00 55 00 56,00 57.00 58.00 59 00 60.00 61.00 62.00 63 00 64.00 65.00 66.00 67 00 68 00 69.00 70.00 436.87 435.,81 434 84 433.97 433.IB 432.48 431,84 431.28 430.79 430.3G 429 98 429 65 429.36 429 12 428.91 428.-74 428,59 428.48 428.39 428.31 428.26 428,23 428.21 428.20 428.20 428.22 428 24 428.27 428.3 I 428.35 428.40 428 45 428 50 428,56 428.62 1196,52 1196.58 1196.64 1196.69 1196.74 1196.78 1196.82 1196.85 1196.88 1196.91 1196.93 I 196.95 1196.97>>96.98 I 196.99 1197.00 1197.01 1197.02 1197.02 1197.02 1197.03 1197.03 1197.03 1197.03>>97.03 1197.03 1197.03 1197.02 1197.02 1197 02 1197.02 1197.01 1197.01 1197.01 1197.00 896.21 894.20 892.37 890.72 889.24 887 91 886.73 885.68 884.76 883,95 883.24 882.63 882.11 881,6G 881.29 880.97 880.7 I 880.50 880.34 880.22 880.13 880.08 880.05 880.05 880.07 880.10 880 16 880.23 880.30 880.39 880.49 880.59 880.7 I 880.82 880.94.889.873.857.842.826.Bl I.796.782 ,769.756.744.733.723.713.704.696.688.680.673.666.659.653.647.642.636.631.626.622.617.613.609.604.601.597.593 1.000 1.000 1.000 1.000 I.000 ,987.966.947.930.914.900.885.870.855.839.824.809.795.78'I ,769.757.746.735.726.717.708.700 693.685 G79.672.66G.660.654.G49 1.000 1.000 1.000 I.000 I, 000 I.000 I.000 I.000 I.000 1.000 I.000 1.000 I.000 1.000.988.968.950.933.918.904.890.875.860.844.829.814.800.786.773.761.750.740.730.721 I.000 I.000 1.000 I.000 I.000 1.000 I.000 1.000 1.000 I.000 1.000 1.000 I.000 I.000 1.000 1.000 1.000 1.000 I.000 1.000 I.000 I.000 I.000 1.000 I.000.989.9GB.950.934.919 ,904.890.875.860.844 I.000 I.000 I.000 I.000 1.000 I.000 1.000 I.000 1.000 1.000 I.000 I.000 1.000 I.000 1.000 1,000 1.000 I.000 1.000 I.000 I.000 I.000 1.000 1.000 1.000 I.000 1.000 I.000 1.000 1.000 I.000 I.000 1.000 I.000 I.000 I.000 I.000 1.000 1.000 1.000 1.000 1.000 1.000 I.000 I.000 I.000 1.000 I.000 I.000 1.000 1.000 1.000 1.000 I.000 1.000 I.000 I.000 1.000 1.000 1.000 1.000 I.000 1.000 1.000 I.000 I.000 I.000 30 PERCENT POWER T I ME~SEC.FLOW LB/SEC ENTIIALP Y B IU/LB PRESSURE PSIA ISOLATION AT (SEC)$$$$$$$$$$$$$$$$$'$$$$$$$'$$$$$$$$$$$$$$$$$$$$$30 40 50 60 70 80 71.00 72.00 73.00 74.00 75.00 76 00 77.00 78.00 79.00 80.00 81.00 82.00 83,00 84 00 85.00 86 00 87,00 88.00 89,00 90.00 91 00 92.00 93.00 94.00 95.00 96.00 97.00 98.00 99.00 100.00 102.00 104 00 106 00 108.00 110 00 428 68 428.74 428 80 428,86 428.93 428.99 429.06 429 12 429.18 429,24 429,3 I 429.37 429 43 429.49 429.54 429.60 429.66 429.7 I 429.77 429 82 429.87 429.93 429.98 430.03 430.08 430.12 430.17 430.22 430.26 430 31 430,37 430 45 430 54 430.62 430 70 1197.00 1196.99 1196.99 1196.99 1196.98 1196.98 1196.97 1196.97 1196.97 1196.96 1196.96 1196.96 1196.95 1196.95 1196.94 1196.9'I 1196.94 1196.93 1196.93 1196.93 1196.92 1196.92 1196.92 I 196.91 1196.91 1196.91 1196.91 1196.90 1196.90 1196.90 I 196.89 1196.89 1196.88 1196.88 1196.87 88 1.06 881.18 881.31 881.44 881.56 881.69 881.81 881.94 882.06 882.19 882.31 882.43 882.55 882.67 882.78 882.89 883.01 883 12 883.22 883 33 883,43 883.53 883.63 883.73 883.83 883.92 884.02 884.II 884, 19 884.28 884.45 88 1.62 884 78 884.91 885 09.589.644.713.829.586.639.705.814.582.634.697.800.579.630.690.786.576.625.683.773.572.621.677.761.569.617.670.750.566.G13.664.740.563.609.659.730.560.605.653.72 1.557.602.648.7 13.554.598.643.705.55 1.595.639.697.549.59 1.634.690.546.588.630.683.544.585.626.677.54 1.58 1.622.670.539.578.6 18.6G4.Sae.S7S.6 14.GS9.534.572.6 IO.654.532.5G9.607.649.530.566.603.644.527.SG3.599.639.525.56 1.596.635.523.558.593.630.52 1.55G.589.626.5 19.553.586.622.517.551.583.618.515.548.580.614~513.546.577.611.5 II.543.572.605.507 538.567.598.504.534.562.592.500 ,530.557.586.497 526 ,552 579.989.9GB.949.933.918.903.889.874.858.843.827.812.798.784.771.759.748.738.728.719.711.703.695.688.681.675,.669.663.657.652.645.636.627.619 ,612 1.000 1.000 I.000 I.000 I.000 I.000 I.000 1.000 I.000 I.000.988.967.948.932.916.901.887.872.856.840.825.810.795.781.768.756.745.735.725.717.704.689.676.664.653 30 PERCENT POwER TINE SEC.FLOW LO/SEC~EN TIIAI PY BIU/LB PRESSURE PSIA ISOLATION AT (SEC)$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$30 40 50 60 70 80 112.00 114.00 116.00 118.00 120.00 122.00 124.00 126.00 128.00 130.00 132.00 134.00 136.00 138.00 140.00 142.00 144.00 14G 00 148 00 150 00 I GO.00 170.00 180.00 190 00 200.00 430.77 430.84 430.91 430.98 431.05 431.12 431.19 431.25 431.31 431.37 431.43 431.49 431.55 431.60 431.66 431.71 431 76 431.81 431.86 431.91 432 13 432.34 432.52 432.27 43 I.73 1196.87 1196.86 1196.86 1196.85 1196.85 119G.84'I 196.84 1196.84 I 196.83 1196.83 I 196.83 1196.82 1196.82 I 196.8 I 1196.81 1196.81 1196.80 I 196.80 119G.BO 1196.80 1196.78 1196.77 1196.76 1196.78 1196.8 I 885.24 885.38 885.52 885.66 885.79 885.93 886.05 886.54 886.65 886.76 886.87 886.98 887.08 887.18 887.28 887.38 887.47 887.92 888.33 888.64 888.07 886.93.494.491.489.486.483.480.478.475.4)2.470.467.465.462.460.458.456.453.451.449.447.438.430.423.416.410.523.548.519.543.515.539.512.535.509.531.506.527.503.524.500.520.497.517.494.513.491.510.489.507.486.504.483.501.480.498.478.495.475.492.473.490.47 1.487..468.484.458.472.448.461.440.452.433.443.426.436.574.568.5G3.558.553.549.544.540.536.532.528.524.520.517 514.510.507.504.501.498.484.472.461.451.443.605.643.598.634.591.625.585.618.579.610.573.603.567.596.562.590.557.584.552.578.548.572 ,543.566.539.SG I.535.556.531.551.527.546.523.542.519.537.516.533.512.529.497.511.483.495.470.481.459.469.450.457 1.4 F l2 OE RUPIURE Ar ZERO POWE R XXX FROM I 64401 A T I ME SEC.0.00 I 00 2 00 3 00 4 00 5 00 6 00 7 00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15, 00 17.50 20.00 22 50 25.00 27.50 30.00 35 00 40.00 45.00 50.00 60.00 70.00 80.00 90.00 100.00 120.00 140 00 I GO.00 180.00 F ORWA F 1.0'W LB/SEC 3/263 0 OO 3087 34 2885 37 27 12.88 2457.53 22 15.56 2005 14 1828 22 1679.09 1552.74 1443.54 1347.81 1262.61 124 I.39 1217.46 1191.78 1124.73 1060.97 1005.50 958 25 917.49'82.01 824 83 783.42 753.66 732.07 705.37 691.63 684,78 681.66 680.54 680.98 682.32 683 35 683 72 RO FLOW ENIIIALP Y'lu/I.B Bet~I 6 68-.44 1192.00 1194.24 1196.54 1199.08 1201.08 1202.51 1203.48 1204.12 1204.51 1204.72 1204.79 1204.78 1204.75 1204.72 1204.67 1204.50 1204.25 1203.96 1203.66 1203.35 1203.04 1202.47 1201.98 1201.59 1201.28 1200.88-1200.66 1200.54 1200.49 1200.47 1200.48 1200.50 1200.52 1200.53 PRESSURE PSIA 1106.08 1025.03 963.62 895.54 810.97 733.66 667.50 611.69 564.33 523.60 488.01 456.50 438.41 430.46 421.72 412.50 388.94 367.01 348.08 331.92 317.92 305.73 286.13 271.96 261.76 254.36 245.22 240.5 I 238.17 237.II 236.74 236.93 237.40 237.76 237.88 I I I Tl T I Tl rl Tl Tl TI Tl TI Tl Tl rl Tl Tl Tl Tl Tl Tl Tl Tl Tl'r I Tl Tl'r I Tl Tl Tl Tl T IME SEC.0.00 1.00 2.00 3.00 5.00 6.00 7.00 8.00 9.00 10,00 11.00 12.00 13.00'14.00 15.00 17.50 20.00 22.50 25.00 27.50 30.00 35.00 40.00 45.00 50.00 60.00 70.00 80.00 90.00 100.00 120.00 140.00 I GO.00 180.00 REVERSE FLO FLOW I.B/SEC C1'FZ S e-.ee 6174.67 5770.48 5435.19 4928.48.4445.GB 4029.26 3682.43 3392.85 3146.73 2934.87 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 W E N I I I A L P Y B IU/LB 1188.81 1192.00 1194.16 1196.47 I 199.02 120'I'.0 I 1202.43 1203.40 1204.04 1204.45 1204.68 1204.76 1204.74 1204.68 1204.62 1204.55 1204.44 1204.37 1204.33 1204.29 1204.25 I?04.23 1204.19 1204.15 1204.10 1204.04~1203.93.1203.80 1203.67 1203.55 1203 44 1203.24 1203.08 1202.95 1202,85 I.4 F T2 OE RUPTURE AT ZERO POWER-XXX FROM IG440I A TIME SEC.200.00 220.00 240 00 260.00 280.00 300.00 FORWARD F I.O'w FLOW ENTIIALPY IB/SEC BTU/LB 683.27 1200.52 679.85 1200.46 674.3 I 1200.36 667.83 1200.24 660.49 1200.IO 652.35 1199.95 PRESSURE PSIA 237.70 236.42 234.44 232.13 229.52 226.62 TIME SEC.T I+200.00 T I+220.00 T I+240.00 T I+260.00 T I+280.00 I I+300.00 REVERSE FLOW FLOW LB/SEC 0.00 0.00 0.00 0.00 0.00 0.00 ENIIIALPY BTU/LB 1202,78 1202.74 1202 72 1202.73 1202.75 1202.79 4r'FT2 OE RUPIURE Al CERO POWER DRY STEAM T Ihi SEC.0 00 I.00 2.00 3.00 4.00 5.00 6.00 7.00 8,00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 17.50 20.00 22.50 25 00 27.50 30.00 35.00 40.00 45.00 bo.oo 60.00 70.00 80.00 90.00 100*00 120.00 140.00 IGO 00 180.00 2JO.OG 231.31 231.23 225 72 217.77 209.00 200.63 192.82 185'59 178.85 172.52 166.50 Ilio.76 155.27 I 19.99 137.73 135~24 134.29 132.92 131 52 130.29 128.13 126.25 124.69 123.40 121.JG 119.74 I 18.39 117.22 116.19 114.48 113 05 111,87 110.89 I 188 1188.90 1189.18 1190.42 1191.95 1193.41 1194.74 1195.93 1196.98 1197.92 1198.77 1199 55 1200.25 1200.88 1201.46 1202.65 1202.68 1202.78 1202.90 1203.02 1203.12 1203.29 1203,43 1203.55 1203,64 1203.77 1203.88 1203.96 1204.03 1204.09 1204.19 1204.26 1204.32 1204.36 FOR'WARO F I.ON Fl OW ENIIIALPY le/SEC 8IU/le 380.T~JIFFY.dl bb~PRESSURE PSTA I 106.08 1103.44 1104.08 1097 17 1066.00 1026.57 986.78 949.25 914.25 881.64 851.00 821.94 794, 18 7G7.56 741.99 717.35 659.98 658.29 653.21 646.44 6J9.86 634.08 623.83 614.89 607.54 601.41 591.71 584.10 577.65 572.02 567.04 558.G I 551.74 546.10 54 I.40'I I II fl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl Tl I I T I Tl+Tl T I'+Tl Tl Tl T I ME SEC.0.00 I.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 17.50 20.00 22.50 25.00 27.50 3O.OO 35.00 40.00 45.oo 50.00 60.00 70.00 80.00 90.00 100.00 120.00 140.00 Ilio.00 180.00 REVERSE FLOW FLOW~LB/SEC 33o.'I e-.ee 230.4 I 232.34 232.96 228.07 220.66 212,38 204.5G 197.30 190.6 I 184.38 178.52 172.92 167.54 162~36 157.33 145.39 143.26 142.53 14 1.34 140.11 139.01 137.09 135.37 133.92 132.69 130.73 129.IS 127.88 126.72 125.67-123.84 122.24 120.87 119.73 EN I IIAL P Y elu/Le 1188.8 I 1188.79 I 188.64 1188.80 1189.95 1191.40 1192.80 1194.06 1195.18 1196.19 1197.09 1197.92 1198.67 1199.37 1200.02 1200.62 1201.91 1201.91 1201.99 1202.12 1202.24 1202.34 1202.52 1202.67 1202.80 1202.91 1203.07 1203.20 1203.30 1203.39 1203.47 1203.60 1203.7 I 1203.80 1203.88
.I FT2 OE RUPTURE AT 2ERO POWER" ORY STEAM T I ME SEC.200.00 220 00 240.00 2f'-)100 280.00 300.00 FORWARD FLOW FLOW ENTIIALPY LB/SEC BTU/LB 110.05'1204.40 109.28 1204:43 108.56 1204.46 107.86~1204.49 107.17 1204.52 106.48 1204.54 PRESSURE PSIA 537.31 533.60 530.12 526.74 523.39 519.99 T I ME SEC.T I+200,00 T I i 220 00 TI+240 00'll+260.00 T I+280.00 Tl t 300 00 REVERSE FLOW FLOW LB/SEC 118.73 117.83 116.99 116.18 115.38 114.58 EN[IIALPY BTU/LB 1203.94 1203.99 1204.04 1204.09 1204.13 1204.18 2ERO POWER IIME SEC.F I.OW LB/SEC.ENiIIALPY 8 IU/LB PRESSURE PSIA ISOLA1ION AI (SEC)$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$30 40 50 60 70 80 1.00 2.00 3.00 4.00 5.00.6.00 7.00 8,00 9.00 10.00 11.00 12.00 13.00 14.00 15.00 I G.OO 17.00 18.00 19.00 20 00 21.00 22:00 23 00 24.00 25.00 2GOO 27.00 28 00 29.00 30,00 31 00 32,00 33.00 34.00 35 00 242.07 240,63 239.24 237.89 236.62 235.42 234-26 233.15 232.II 231.10 230.12 229.17 228.22 227.29 226.35 225.42 224.,48 223 222.64 221.73 220,80.19.88 218 95 218.02 217.09 216.16 215.23 214,30 213.36 212.42 211 49 210.55 209 61 208,68 207 74 1186.81 1187.08 1187.35 1187.60 1187.83 1188.05 1188.27 1188.47 1188.66 1188.84 1189.02 1189.20 1189.37 1189.54 1189.71 1189.88 1190.05 1190.22 119039 1190.55 1190.72 1190.88 1191.05 1191.21 1191.38 1191.54 1191.70 1191,87 1192.03 1192.19 1192 35 1192.51 1192.67 1192.83 1192 99 1153.99 1147.60 1141.42 1135.50 1129.89 1124.56 1119.4'I 1114.54 1109.89 1105.38 I 100.99 1096 67 1092.39 1088.13 1083.88 1079.61 1075.33 107 I.IG IOGG.97 1062.76 1058.54 1054.30 1050.05 1045.78 1041.51 1037.23 1032.95 1028.G5 1024.'35 1020.04 1015.72 1011.40 1007.08 1002.76 998 45 1.000 I.000 1.000 1.000 I.000 1.000 I.000 I.000 I.000 I.000 1.000 1.000 1.000 I.000 I.000 I.000 1.000 1.000 I.000 I.000 I.000 1.000 I.000 1.000 1.000 I.000 1.000 I.000 I.000 I.000.985.970.956 ,912.929 I.000 1.000 1.000 I.000 I.000 I.000 I.000 I.000 1.000 1.000 I.000 1.000 1.000 I.000 1.000 I.000 1.000 I.000 1.000 1.000 I.000 1,000 1.000 I.000 1.000 1.000 I 000 I.000 1.000 1.000 1.000 1.000 1.000 I 000 1.000 I.000 I.000 1.000 1.000 1.000 1.000 1.000 I.000 I.000 I.000 1.000 1.000 I.000 I.000 1.000 1.000 I.000 1.000 I.000 I.000 1.000'I.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 1.000 I.000 I.000 I.000'I.000'I.000 I.000 I.000 I.000 I.000 I.000 1.000 I.000 I.000 I.000 I.000 1.000 1.000 I.000 1.000 1.000 1.000 I.000 I.000 1.000 1.000 I.000'I.000 I.000 1.000 I.000'I.000 I.000 1.000 1.000 I.000 I.000 I.000 1.000 I.000 I.000 1.000 1.000 1.000'I.000 I.000 1.000 I.000 1.000'I.000 1.000 I.000 I.000 I.000 1.000 1.000 I.000 I.000 1.000 I.000 1.000 1.000 I 000 I.000 1.000 I.000 1.000 1.000 I.000'I.000 I.000 1.000 1.000 I 000 I.000 I.000 I.000 1.000 1.000 1.000 1.000 I.000 1.000 I.000'I.000 1.000 1.000 I.000 I.000 1.000 1.000 1.000 I.000 I.000 1.000 1.000 1.000 I.000 1.000 1.000 1.000 I.000 I.000 I.000 I.000 I.000 1.000 1.000 1.000 1.000 ZERO POWER 1 INE SEC.FLOW LB/SEC ENTIIALPY BTU/LB PRESSURE PSIA ISOLATION AT (SEC)$$$$$$$$$$$$$$$$$$5$$$$$5$$$$5$$55$$$$5$$$$5$30 40 50 60 70 80 3G 00 37,00 38.00 39.00 40.00 41.00 42.00 43,00 44.00 45.00 46.00~47.00 48,00 49.00 50.00 51.00 52.00 53.00 54 00 55.00 56.00 57.00 58 00 59.00 60 00 G 1.00 62 00 G3 00 64.00 65.00 G6.00 67.00 68.00 69 00 70.00 206.81 205.87 204.94 204 01 203.09 202, 16 201.24 200.33 199 42 198.51 197.60 196.70 195.81 194.91 194.03 193.15 192.27 191.40 190.53 189.67 188.81 187.96 187 12 186.28 185.44 184.61 183.79 182 97 182.16 IBI 35 180.55 179..75 178.96 178 17 177 38 1193.15 1193.30 1193.46 I'193.61 1193.77 1193.92 1194.07 1194.22 1194.37 1194.52 1194.66 1194.81 1194.95 1195.09 1195.23 1195.37 1195.51 1195.64 1195.78 I'195.91 1196.04 1196.17 1196.30 1196.43 1196.55" 1196.68 1196.80 1196.92 1197.04 1197.16 1197.28 1197.39 1197.51 1197.62 I 197.73 994.13 989.83 985.53 981.24 976.96 972.70 9G8.44 964.20 959.97 955.77 951.57 947.40 943.25 93S.Il 934.99 930.90 926.83 922.77 918.75 914.74 910.75 906.79 902.85 898.94 895.05 891.18 887.33 883.51 879.7 I 875.94 872.19 868.46 864.74 86 1,02 857.32.916.905.893.883.872.862.853.844.835.827.819.811.804.797.790.783.776.770.764.758.752.746'741.736.730.725.720.715..710.706.701.697.692.688.684 I, 000 I.000'I.000 I, 000 1.000 ,984.969.955.941.928.916.904.893.882.872.862.853.844.836.828.820.812.805..798.791.784.778.772 g766.760.754.748.743.737.732 I.000 I.000 1.000 I.000 1.000 1.000 I.000 I.000 1.000 1.000 1.000 1.000 1.000 1.000 1.000.984.969.955.941.929.917.905.894.884.874.864.855.846.838.830.822.814.807.800.793 I.000 I.000 I.000 1.000 I.000 1.000 I.000 I.000 I.000 1.000 I.000 I.000 I.000 1.000 1.000 I.000 I.000 1.000 I.000 I.000 I.000 1.000 I.000'.000 I.000 ,984.969.955.912.930.918.906.896.885.876 1.000 1.000 1.000 1.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 1.000 1.000 1.000 I.000 1.000 I.000 1.000 I.000 I.000 I.000 I.000 I.000 I.000 I.000 1.000 I.000 1.000 1.000 1.000 I 000 I.000 I.000 1.000 I.000 1.000 I.000 I.000 I.000 1.000 1.000 1.000 I.000 I.000 I.000 I.000 I.000 I.000 1.000 1.000 I.000 I.000 I.000 1.000 1.000 1.000 I.000 I.000 1.000 1.000 I.000 1.000 1.000 I.000 I.000 I.000 I.000 1.000 ZERO POWER I I NE F LOW SEC.LB/SEC EN IIIAL P Y 8 IU/LB PRESSURE PSIA ISOLATION AI (SEC)$$$$$$$$$5$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$$30 40 50 60 70 80~71.00 72 00 73,00 74.00 75.00 76.00 77.00 78.00 79.00 80.00 8 I 00 82 00 83,00 84.00 85 00 86.00 87 00~.88.00 89 00 90.00 91.00 92.00 93.00 94.00 95.00 9G.OO 97.00 98.00 99,00 100.00 102.00 104 00 106.00 108.00 110.00 176.59 175.81 175,02 174.24 173.46 172.68 171.90 17 1.12 170.35 69.59 168 82 168.07 167, 32 166 57 IG5.83 Ie5.10 164.38 Iea, es 162.94 IG2.22 161.5'I 160.8 I 160.I I 159.42 158.73 158-05 157.37 156.70 156,.03 155.36 154.37 153 08 151 80 150.55 149.33 1197.84 1197.95 1198.06 1198.17 1198.28 1198.39 1198.50 1198.60 1198.71 1198.81 1198.91 I 199.0 I 1199.11 1199.21 1199 30 1199.40 1199.49 1199.58 1199.68 1199.77 1199.85 1199.94 1200.03'200.11 1200.20 1200.28 1200.36 1200.44 1200.52 1200.60 1200.75 1200.90 1201.05 1201.IB 1201.32 853.62 849.94 846.26 842.57 838.89 835.22 831.56 827.91 824.28 820.68 817.09 8 la,'54 810.00 806.50 803.02 799.57 796.14 792.73 789.35 785.98 782.64 779.3 I 776.01 772.74 769.48 766.25 763.04 759.85 756.68 753.53 747.31 741.19 735,.17 729.27 723.53.679.727.787.675.722.780.671.717.774.667.712.768.663.707.762.659 ,703.756;.655.698.75 1.652.694.745.648.689.740.644.G85.735.G41.GB I.729.G37.677.724.634.673.720.631.669.715.627.665.710.624.66 1.706.621.658.701.618.G54.697.615~.651.693.612.647.689.609.644.685.606.641.681.603.637.677.601.634.673.598.63 1.670.595.628.666.592.625.662.590.622.659.587.G 19.655.585.616.652.581.612.647.576.G06.64 1.571.GO I.635.567.596.629.5G2.591.624.BG6.984.857.969.848.955.840.942.832.930.824.9 18.817.907.809.896.802.886.796.87G.789.867.783.858.776.849.771.84'I.7G5 ,833.759.826.754.818.748.8 I I.743.804.738.798.733.791.728.785.724.779.7 19.773.715.768.710.762.706.757.702.752.698.74G.694.741 ,688.734.680.725.673.717.667.708.6GO.701 I.000 I.000 I.000 1.000 1.000 I.000 I.000 I.000 1.000 I.000.981.967.953.940.928.917.906.895.885.876.867.858.850.842.834.826.819.812.806.799.790.778.767.757.747 ZERO POWER T IME SEC.FLOW" L8/SEC ENTIIALPY eTU/I.e PRESSURE PSIA ISOLATION AT (SEC)$5$$$$$$$$$$$$$$$$$$$$$$$$$$'$$$$$$$$$$$$$$$$$30 40 50 60 70 80 112.00 114.00 116.00 118.00 120.00 122.00 124.00 126.00 128.00 130.00 132,00 I J4.00 136.00 138.00 140.00 142.00 144.00 146.00 148 00 150.00 160.00 i70.00 180.00 190.00 200.00 148.14 146.97 145.82 144 69 143.58 142.47 141.37 140.28 139.20 138.13 137.06 13G.01 I J4,97 133.93 132.91 131.89 130.89 129.92 129.06 128.31 125.18 122 50 120.I I 117.99 116.IO 1201.45 1201.57 1201.69 120'1.81 1201.92 1202.03 1202.14 1202.25 1202.35 1202.45 1202.55 1202.65 1202.74 1202.83 1202.92 1203.01 1203.09 1203~17 1203.23 1203.29 1203.52 1203~7 I 1203.86 1203.99 1204.10-717.89 712.37 706.94 701.58 69G.27 690.99 685.75 680.55 675.38 670.27 II65.19 660.IG 655.17 650.22 645.32 640.46 635.7 I 631.26 627.38 624.00 609.19 59G.46 585.16 575.02 566.00.558.586.618.654.554.58 1.6 13.648.550.577.608.642.546.572.602.636.542.568.597.630.538.563.592.624.534.559.588.6 19.530.555.583.6 14.526.551.578.608.522.547.574.603.5 18.543.569.598:5 15.539.565.594.5 11~535.561.589.508.53 1.557.584.505.528.553.580.502.525.550.577.500.523.548.574.498.52 1.545.572.496.519.543.569.494.517.541.567.487.508.532.557.480.502.524.548.474.495.518.541.469.490 ,511.534.464.484.506.528.693.738.686.729.679.721.672.713.666.705.659.697.653.690.647.683.641.676.635.669.630.663.624.657.619.651.614.645.609.640.606.635.602.632.599.628.597.625.594.622.582.608.573.598.565.589.558.469.552.457 APPENDIX B RESULTS OF CONTAINMENT PRESSURE AND TEMPERATURE ANALYSIS (356GAS/mf
)
h, MSLB<<COOLING TRAIN FAILURF.Percent Power 102 70 0 MSLB Break Size, ft.Full.6.645 Full.5.681 Full.4.7065 Full.1 DE DE Split DE DF, Split DF.DH Split DE DE~3 Split Peak Pressure, psig 31.7 26.3 27.3 33.5 27.0 28.3 30.9 27,2 30.5 29.6 17.3 25.3 Peak Temperature, 378 330 343 377 313 34'l 376 306 351 367 289 F 312 Time of Peak Pressure, sec.154 258 212 178 336 222 207" 480 250 240 1810 702 Time of End of Blowdown, scca 154 258 212 178 336 222 207 480 250 240 1810 702'
SUMMARY
OF CALCULATED CONTAINMENT PRESSURE AND TEMPERATURE B.MSLB-MAIN FEEINATER ISOLATION VALVF.FAIJ.UR'E Percent Power 102 30 MSLB Break Size, Full.6 2 DF.DF.ft 645 Full.5 681 Full.4.7065 Full.1 Split DE DE Split DE DE Split DE DE.3 Split Peak Pressure, psig 34.4 28.3 29.5 36.1 28.5 30.6 38.7 29.3 33.2 39.1 13.8 24.7 Peak Temperature,'78 319 F 343 377 313 349 378 307 351 366.291 311 Time of Peak Pressure, sec.190 3l4 256 2 1 7 402 274 249 563 301 289 2114 845 Time of End of Blowdovn, sec.190 314 256 217 402 274 249 563 301.289 2114 845
SUMMARY
OP CAI.GUTTED CONThINMENT PRESSURE AND TEMPERATURE DESLG DF.SLG C.MSLB-MAIN STEAM ISOLATION VALVE FAILURF.0.6x DESLG~MI~n.S I 3 ft.Pump Suction Split~MI n~SI DEHLG Min.SI DECLG Min.SI Percent Power 102 70 30 MSLB Break Size, ft Full.6.645 Full.5.681 Full.4 DE DE Split DE DE Split DF.DE.7065 Full.1.3 Split DE DH Split Peak Pressure, psig 31.3 26.2 27.4 33.3 27.3 28.5 35.8 27.3 30.9 35.4 13.3 23.1 Peek Temperature, F 332 343 379 314 350 379 305 350'68 291 310 Time of Peek Pressure,sec. 154 258 223 178 336 236 207 480 264 240 1810 737 Time to End of Bio+down,sec. 154 258 221 178 336 236 207 480 264 240 1810 737 o ao.OO eO.00 t ZO.OO Isa.OO tOO.00 ZqO.00 Z80 OO ZZO.OO QO.OO EOR OO.I.I c C)o EO C7 o zz'1 O Q~T CC Vl~-a O aA u)8 p H O 0)CI C)ci O a CV O D e4 a C)O O 40 O Cl Conf~)'n~en
~Press'ore bJ~P jqS48 (rlflv Poilu~-ng p,<<~f Il>FB)C7 O tO CI b.00$0, 00 80.00 I ZO.00 l 60.00 200.00 240.00 2SD.00 32G.00 360.00 408.00 T i~a (SE'C.)
O Q D ab.00 40.00.SQ.Ob I?0.DO 1&0.00 200.00 E40, 00 280, 00 320.00 360 00$$g 00: L I 3gg p (y g~iree.)O O O lO m 0 O Cc O CI O D CI O N O O L O Ch~O O WO K tv Ot cl O Q O 4J O O D Cl gV O O D C4 O 0 0 O lV O O O EO'fB O O cD O 0 O a o a , 00 NIDTE-7w.-eaurw~ieR TBSP.6: Ccyvlg/yP5P~u~
p y Cocc<~;ncicni'e~~e cprc-Warstkf5e-e, (Hs i~Alluw, 3o7o lo~cr Fgrll>~HQ I 55.00 lpga.00 t so.oa 200.oo t40.00 t80.oa 320.00 360~00 T l ME (SEC)O D O O D 0 4" I