ML20138L260

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Rev 2 to Fluid Analysis to Determine If Standby Gas Treatment Sys Purge & Vent Line Duct Work Overpressurized During DBA LOCA, Technical Rept
ML20138L260
Person / Time
Site: Pilgrim
Issue date: 10/31/1985
From:
TELEDYNE ENGINEERING SERVICES
To:
Shared Package
ML20138L251 List:
References
TR-6121-4, TR-6121-4-R02, TR-6121-4-R2, NUDOCS 8510310244
Download: ML20138L260 (73)
v • d • e


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TECHNICAL REPORT I

TR-6121-4 REVISION 2 PILGRIN NHCLEAR POWER STATION FLUID ANALYSIS TO DETERMINE IF THE STANOBY GAS TREATMENT SYSTEM PURGE AND VENT LINE DUCT WORK t

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OCTOBER 1985 0510310244 051023 PDR ADOCK 05000293 P

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25 BRAINTREE HILL PARK BRAINTREE, MASSACHUSETTS 02184 l

TECHNICAL REPORT TR-6121-4 REVISION 2 PILGRIM NUCLEAR POWER STATION FLUID ANALYSIS TO DETERMINE IF THE STANDBY GAS TREATMENT SYSTEM PURGE AND VENT LINE DUCT WORK IS OVERPRESSURIZED DURING DBA LOCA OCTOBER 1985 SPTELEDYNE ENGINEERING SERVICES 130 SECOND AVENUE WALTHAM, MASSACHUSETTS 02254 6174 0 3360

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TABLE OF DBA AND VALVE CLOSURE STARTING AT.0 SEC DIFFERENT gg B

~

DRYWELL DRYWELL VALVE CH0KED DUCT MACH VALVE F-5 TIME PRESSURE TEMP FLOW AREA FLOW VELOCITY PRESSUR NUMBER TIME E Qp SEC PSIG DEG R

% FULL LBM/SEC FT/SEC PSIG 0.0 0.006 580.093 100%

0.004 0.031 0.000 0.0000 0

o o

$$M 0.2 12.000 680.500 91%

6.914 52.744 0.164 0.0412 0.1999

  1. p 0.3 18.000 688.000 86%

9.805 74.794 0.329 0.0581 0.2999 5

~?

0.4 21.364 695.500 82%

10.972 83.699 0.412 0.0647 0.3999 3

0.5 23.414 703.000 77%

11.304 85.233 0.437 0.0663 0.4999

- T IT l

0.6 25.464 710.500 73%

11.519 87.870 0.454 0.0672 0.5999 NI I

N 0.7 27.514 718.000 68%

11.618 88.625 0.462 0.0674 0.6999 k

0.8 29.564 725.500 64%

11.603 88.512 0.461 0.0670 0.7999 3

0.9 31.614 733.004 59%

11.476 87.543 0.451 0.0659 0.8999 R

g 1

33.664 733.560 55%

11.292 86.138 0.436 0.0649 0.9999 f

m 1.5 39.185 736.340 43%

10.376 79.148 0.368 0.0595 1.4999 1

2 39.950 739.120 32%

7.767 59.250 0.206 0.0444 1.9999 2.5 40.715 741.900 25%

6.173 47.086 0.130 0.0353 2.4999 7

2.75 41.097 743.290 21%

5.353 40.837 0.093 0.0305 2.7499 P

h l

c ~z P 'm FLOW TABLE OF DBA AND VALVE CLOSURE STARTING AT.2 SEC DIFFERENT f

DRYWELL DRYWELL VALVE CHOKED DUCT MACH VALVE TIME PRESSURE TEMP FLOW AREA FLOW VELOCIT(

PRESSUR NUMBER TIME (p

g SEC PSIG DEG R

% FULL LBM/SEC FT/SEC PSIG 3_

m E

g<

0.0 0.006 580.093 100%

0.004 0.031 0.000 0.0000 0

,,y 0.2 12.000 680.500 100%

7.598 57.958 0.197 0.0453 0

0.3 18.000 688.000 95%

10.824 82.571 0.401 0.0642 0.1 g jg g 0.4 21.364 695.500 91%

12.176 92.880 0.507 0.0718 0.2

?- !'l g 0.5 23.414 703.000 86%

12.616 96.241 0.544 0.0740 0.3 5g 0.6 25.464 710.500 82%

12.938 98.697 0.573 0.0755 0.4 0.7 27.514 718.000 77%

13.144 100.263 0.591 0.0763 0.5 3 D 0.8 29.564 725.500 73%

13.234 100.952 0.599 0.0764 0.6 w

0.9 31.614 733.004 68%

13.211 100.778 0.597 0.0759 0.7 5

1 33.664 733.560 64%

13.139 100.225 0.591 0.0755 0.8 pS 1.5 39.185 736.340 48%

11.472 87.513 0.450 0.0658 1.3 2

39.950 739.120 37%

8.883 67.762 0.270 0.0508 1.8 N

2.5 40.715 741.900 28%

6.864 52.357 0.161 0.0392 2.3 p

2.75 41.097 743.290 24%

6.050 46.152 0.125 0.0345 2.55 F

TABLE OF DBA AND VALVE CLOSURE STARTING AT.4 SEC OIFFERENT o

e,.

DRYWELL DRYWELL VALVE CH0KED DUCT MACH VALVE E

D TIME PRESSURE TEMP FLOW AREA FLOW VELOCITY PRESSUR NUMBER TIME P o s

  • kp SEC.

PSIG DEG R

% FULL LBM/SEC FT/SEC PSIG 0.0 0.006 580.093 100%

0.004 0.031 0.000 0.0000 0

0.2 12.000 680.500 100%

7.598 57.958 0.197 0.0453 0

o o$$d 0.3 18.000 688.000 100%

11.334 86.462 0.439 0.0672 0

0.4 21.364 695.500 100%

13.380 102.066 0.612 0.0789 0

i 6

0.5 23.414 703.000 95%

13.929 106.255 0.664 0.0817 0.1 t

I. -

0.6 25.464 710.500 91%

14.358 109.530 0.705 0.0838 0.2 T

0.7 27.514 718.000 86%

14.670 111.906 0.736 0.0852 0.3 5

y 0.8 29.564 725.500 82%

14.866 113.398 0.756 0.0859 0.4 0.9 31.614 733.004 77%

14.947 114.018 0.764 0.0859 0.5

}

(

1 33.664 733.560 73%

14.986 114.319 0.768 0.0861 0.6 h

Z 1.5 39.185 736.340 53%

12.569 95.882 0.540 0.0721 1.1 m

2 39.950 739.120 41%

9.999 76.279 0.342 0.0572 1.6 3

2.5 40.715 741.900 31%

7.555 57.630 0.195 0.0431 2.1 2.75 41.097 743.290 27%

6.747 51.470 0.156 0.0585 2.35 f

N E

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TABLE OF DB' AND VALVE CLOSURE STARTING AT.6 SEC DIFFERENT DRYWELL DRYWELL VALVE CH0KED 00CT MACH VALVE k

TIME PRESSURE TEMP FLOW AREA FLOW VELOCITY PRESSUR NUMBER TIME kJ SEC PSIG DEG R

% FULL LBM/SEC FT/SEC PSIG pD

-J 0.0 0.006 580.093 100%

0.004 0.031 0.000 0.0000 0

i 0.2 12.000 680.500 100%

7.598 57.958 0.197 0.0453 0

0.3 18.000 688.000 100%

11.334 86.462 0.439 0.0672 0

g.

0.1 21.364 695.500 100%

13.380 102.066 0.612 0.0789 0

o5 m

-l 5 "l

(f) 0.5 23.414 703.000 100%

14.585 111.262 0.728 0.0856 0

0.6 25.464 710.500 100%

15.779 120.363 0.852 0.0921 0

o 0.7 27.514 718.000 95%

16.196 123.550 0.897 0.0940 0.1 O.8 29.564 725.500 91%

16.497 125.844 0.931 0.0953 0.2 Q

N 0.9 31.614 733.004 86%

16.683 127.259 0.952 0.0959 0.3 3

1 33.664.733.560 82%

16.834 128.413 0.969 0.0967 0.4 1.5 39.185 736.340 59%

14.191 108.254 0.689 0.0814 0.9 n%

2 39.950 739.120 46%

11.116 84.195 0.423 0.0636 1.4 2.5 40.715 741.900 34%

8.468 64.599 0.245 0.0484 1.9 y

2.75 41.097 743.290 30%

7.444 56.788 0.190 0.0425 2.15

.n TABLE OF DBA AND VALVE CLOSURE STARTING AT.7 SEC DIFFERENT 9"'A DRYWELL DRYWELL.

VALVE CH0KED DUCT MACH VALVE

=

TIME PRESSURE TEMP FLOW AREA FLOW VELOCITY PRESSUR NUMBER

~ TIME N

P'

- h\\

SEC PSIG DEG R

% FULL LBM/SEC FT/SEC PSIG p

P 0.0 0.006 580.093 100%

0.004 0.031 0.000 0.0000 0

0.2 12.000 680.500 100%

7.598 57.958 0.197 0.0453 0

a o 0.3 18.000 688.000 100%

11.334 86.462 0.439 0.0672 0

CD M 0.4 21.364 695.500 100%

13.380 102.066 0.612 0.0789 0

5 0.5 23.414 703.000 100%

14.585 111.262 0.728 0.0856 0

.h

.T 0.6 25.464 710.500 100%

15.779 120.363 0.852 0.0921 0

$' D 0.7 27.514 718.000 100%

1o.960 129.371 0.984 0.0985 0

0.8 29.564 725.500 95%

17.313 132.067 1.025 0.1000 0.1 0.9 31.614 733.004 91%

17.551 133.880 1.054 0.1008 0.2 3

1 33.664 733.560 86%

17.758 135.460 1.079 0.1020 0.3 6

1.5 39.185 736.340 64%

15.265 116.441 0.797 0.0875 0.8 D

m 2

39.950 739.120 48%

11.674 89.054 0.466 0.0668 1.3 1

2.5 40.715 741.900 37%

9.036 68.930 0.279 0.0516 1.8 N

2.75 41.097 743.290 31%

7.793 59.447 0.208 0.0445 2.05 h {

E

("

TABLE OF DBA AND VALVE CLOSURE STARTING AT.8 SEC DIFFERENT g

DRYWELL DRYWELL VALVE CH0KED DUCT MACH VALVE N

{

kJ TIME PRESSURE TEMP FLOW AREA FLOW VELOCITY PRESSUR NUMBER TIME SEC PSIG DEG R

% FULL LBM/SEC FT/SEC PSIG 0.0 0.006 580.093 100%

0.004 0.031 0.000 0.0000 0

0.2 12.000 680.500 100%

7.598 57.958 0.197 0.0453 0

0.3 18.000 688.000 100%

11.334 86.462 0.439 0.0672 0

0.4 21.364 695.500 100%

13.380 102.066 0.612 0.9789 0

g,3 o

m 0.5 23.414 703.000 100%

14.585 111.262 0.728 0.0856 0

f- !'l g 0.6 25.464 710.500 100%

15.779 120.363 0.852 0.0921 0

5g 0.7 27.514 718.000 100%

-16.960 129.371 0.984 0.0985 0

0.8 29.564 725.500 100%

16.129 138.290 1.124 0.1047 0

g Ng 0.9 31.614 733.004 95%

18.418 140.500 1.160 0.1058 0.1 H

1 33.664 733.560 91%

18.681 142.507 1.194 0.1073 0.2 1.5 39.185 736.340 68%

16.338 124.629 0.913 0.0937 0.7 o

n 2

39.950 739.120 50%

12.232 93.312 0.512 0.0700 1.2 2.5 40.715 741.900 39%

9.604 73.262 0.315 0.0548 1.7 N

2.75 41.097 743.290 33%

8.254 62.960 0.233 0.0471 1.95 N

P

TABLE OF DBA AND VALVE CLOSURE STARTING AT 1.0 SEC DIFFERENT gQ

{q DRYWELL DRYWELL VALVE CH0KED DUCT MACH VALVE TIME PRESSURE TEMP FLOW AREA FLOW VELOCITY PRESSUR NUMBER TIME j

I SEC PSIG DEG R

% FULL LBM/SEC FT/SEC PSIG

{

0.0 0.006 580.093 100%

0.004 0.031 0.000 0.0000 0

a o$$M 0.2 12.000 680.500 100%

7.598 57.958 0.197 0.0453 0

0.3 18.000 688.000 100%

11.334 86.462 0.439 0.0672 0

6 0.4 21.364 695.500 100%

13.380 102.066 0.612 0.0789 0

_b

?

0.5 23.414 703.000 100%

14.585 111.262 0.728 0.0856 0

6 ?

0.6 25.464 710.500 100%

15.779 120.363 0.852 0.0921 0

0.7 27.514 718.000 100%

16.960 129.371 0.984 0.0985 0

D 0.8 29.564 725.500 100%

18.129 138.290 1.124 0.1047 0

h 0.9 31.614 733.004 100%

19.286 147.121 1.272 0.1108 0

1 33.664 733.560 100%

20.529 156.601 1.442 0.1179 0

1 1.5 39.185 736.340 77%

18.484 141.003 1.169 0.1060 0.5 2

39.950 739.120 55%

13.349 101.828 0.610 0.0764 1

7 2.5 40.715 741.900 43%

10.740 81.925 0.395 0.0613 1.5 g

Q 2.75 41.097 743.290 38%

9.399 71.697 0.302 0.0536 1.75

{

p F

TABLE OF DBA AND VALVE CLOSURE STARTING AT 1.5 SEC DIFFERENT f

DRYWELL DRYWELL VALVE CH0KED DUCT MACH VALVE F

g TIME PRESSURE TEMP FLOW AREA FLOW VELOCITY PRESSUR NUMBER TIME SEC PSIG DEG R

% FULL LBM/SEC FT/SEC PSIG 0.0 0.006 580.093 100%

0.004 0.031 0.000 0.0000 0

(

0.2 12.000 680.500 100%

7.598 57.958 0.197 0.0453 0

0.3 18.000 688.000 100%

11.334 86.462 0.439 0.0672 0

0.4 21.364 695.500 100%

13.380 102.066 0.612 0.0789 0

g,5 o

m S Q 0.5 23.414 703.000 100%

14.585 111.262 0.728 0.0856 0

5 g (j) 0.6 25.464 710.500 100%

15.779 120.363 0.852 0.0921 0

0.7 27.514 718.000 100%

16.960 129.371 0.984 0.0985 0

D O.8 29.564 725.500 100%

18.129 138.290 1.124 0.1047 0

0.9 31.614 733.004 100%

19.286 147.121 1.272 0.1108 0

P 1

33.664 733.560 100%

20.529 156.601 1.442 0.1179 0

1.5 39.185 736.340 100%

23.851 181.940 1.946 0.1367 0

m 2

39.950 739.120 77%

18.810 143.486 1.210 0.1076 0.5 2.5 40.715 741.900 55%

13.579 103.584 0.631 0.0776 1

p 2.75 41.097 743.290 49%

12.262 93.538 0.514 0.0700 1.25 D'

e EE 5

N s

as P

C 6 h h E TABLE OF DBA AND VALVE CLOSURE STARTING AT 2.0 SEC DIFFERENT k.

DRYWELL DRYWELL VALVE CH0KED DUCT MACH VALVE N

g TIME PRESSURE TEMP FLOW AREA FLOW VELOCITY PRESSUR NUMBER TIME SEC PSIG DEG R

% FULL LBM/SEC FT/SEC PSIG 3

0.0 0.006 580.093 100%

0.004 0.031 0.000 0.0000 0

0.2 12.000 680.500 100%

7.598 57.958 0.197 0.0453 0

N

(\\,

0.3 18.000 688.000 100%

11.334 86.462 0.439 0.0672 0

g

'D O.4 21.364 695.500 100%

13.380 102.066 0.612 0.0789 0

f 0.5 23.414 703.000 1001 14.585 111.262 0.728 0.0856 0

p 0.6 25.464 710.500 100%

15.779 120.363 0.852 0.0921 0

0.7 27.514 718.000 100%

16.960 129.371 0.984 0.0985 0

p 0.8 29.564 725.500 100%

18.129 138.290 1.124 0.1047 0

r 0.9 31.614 733.004 100%

19.286 147.121 1.272 0.1108 0

P 1

33.664 733.560 100%

20.529 156.601 1.442 0.1179 0

t, 1.5 39.185 736.340 100%

23.851 181.940 1.946 0.1367 0

g 2

39.950 739.120 100%

24.271 185.143 2.015 0.1389 0

g 2.5 40.715 741.900 77%

19.134 145.959 1.252 0.1093 0.5 2.75 41.097 743.290 66%

16.495 125.826 0.931 0.0941 0.75 oE [T1 l3 U) 95

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Attechnent I - Ind:pIndint Varificatica Statement Calculatica # U 2>, Revisica # h:s bun independsntly verified by the follcwing method (s), as noted below: Design Review including verification that: Design inputs were correctly selected and included in the calculation. Assumptions are adequately described and are reasonable. Input or a'ssumptions requiring confirmation are identified, and if any exist, the s culation has been identified as " Preliminary" and a " Finalization Due Date" has bee specified. Design requirements from applicable codes, standards and regulatory documents are identified and reflected in the design. Applicable construction and operating experience was considered in the design. The calculation number has been properly obtained and entered. An appropriate design method or computer code was used. ~ "'~ A mathematical check has been performed.

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The output is reasonable compared to the input. Alternate Calculation O including verification of asterisked items noted above. The alternate calculation ( pages) is attached. .? Qualification Testing O for design fe'ature includ-ing verification of asterisked items noted above and the following: The test was performed in accordance with written test procedures. Most adverse design conditions were used in the test. Scaling laws were established and verified and error analyses were performed, if applicable. Test acceptance criteria were clearly related to the design calculation. Test results (documented in ) were reviewed by the calculation Preparer or other cognizant engineer. Independent Verifier Comments: e-rt2su1h oC h s a _ bd tetro_ Waved ~0

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