ML20210C906
| ML20210C906 | |
| Person / Time | |
|---|---|
| Site: | Mcguire, McGuire  |
| Issue date: | 11/12/1986 |
| From: | Dungan K, Mowrer M PROFESSIONAL LOSS CONTROL, INC. |
| To: | |
| Shared Package | |
| ML20210C807 | List: |
| References | |
| TAC-60320, TAC-60321, NUDOCS 8702090476 | |
| Download: ML20210C906 (36) | |
Text
.- .
awbe-IBROFESSIONAL LOSS CONTROL, INC.
EVALUATION OF THE NEED FOR FIRE PROTECTION OF STEEL PENETRATING FIRE BARRIER WALLS MCGUIRE NUCLEAR STATION DUKE POWER COMPANY November 12, 1986 Prepared By: Professional Loss Control, Inc.
Rev. 0 .
/ ,c---
penaethW.Dungan,P.E.
- President Reviewed By: I \ - h Michael E. Mawrer, P.E.
Vice President 8702090476 DR 870130 ADOCK 05000369 PDR P. O. Box 446 e Oak Ridge, Tennessec 37831 e (615) 482-3541
= ._ t Table of Contents Section Subject Page 1.0 St at ement of P robl em. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1 2.0 M e t h o d o l o gy . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1 3.0 Re s u l t s . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 10 4.0 C o n c l u s i o n s . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 12 Attachment 1 Configuration Factors Attachment 2 Computer Calculations Attachment 3 References i
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. 9 EVALUATION OF THE NEED FOR FIRE PROTECTION OF STEEL PENETRATING FIRE BARRIER WALLS MCGUIRE NUCLEAR STATION DUKE POWER COMPANY 1.0 STATEENT OF PROBLEM Gypsum board on metal stud fi re barrier walls are constructed on elevations 716, 733, and 750 to provide partial barrier separation and act as a radiant energy shield such that a fire will not affect redundant pumps and/or motors required to achieve cold shutdown under an Appendix R fire scenario. These walls run floor to ceiling and provide an effective barrier to the spread of flame and hot gases between pumps.
Since these barriers were installed subsequent to initial plant design, they had to be built around some seismic support steel and some structural steel. The concern raised by the NRC was that the expansion or failure of this steel, when heated, might cause a breaching of the fire barrier, allowing the radiant transfer of heat to adjacent pumps.
This analysis was performed to determine the size opening in these barriers required to cause damage to adjacent pumps or motors.
2.0 NETH000 LOGY The methodology applied to conduct this analysis consisted of two basic parts,1) define the damageability of pumps and mators and 2) determine the conditions capable of causing damage.
t 2.1 Damageability The radiant heat flux thresholds published for equipment damage vary widely. As a piece of equipment is exposed to a radiant heat flux, the surfaces begin to heat. At the same time, the surfaces are cooled by conduction and convection. The damage level is usually related to a component temperature which is a I
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'o 9 function of radiant heat flux, time, convective cooling, conduc-tion and radiation losses. For this evaluation, conservative values of threshold radiant heat fluxes were used as follows:
- 1) Motors: for motors, a heat flux of 20 kW/m2 was used.
- This was the minimum flux at which cable insulation degradation occurred in small scale tests sponsored by EPRI (1). Since the insulation on motor windings is shielded from direct radiation by motor housings, this is a conservative threshold.
- 2) Pumps: for pumps, a heat flux of 30 kW/m2 was used.
Bryan (2) suggested a value of 37.5 kW/m2 for the onset of equipment damage. Values for some cable materials degrade at higher fluxes (teflon, 43 kW/m2 ).
2.2 Radiant Heat Transfer Figure 1 shows a layout, elevation view, of a pump or motor exposed to radiant heat from a wall opening a height above the floor of H, an opening height of b and at a distance from the pump / motor of r. For a worst case, r can be taken as d, the per-pendicular distance from the equipment surface to the wall. Fig-ure 2 shows the resulting plan view with an opening width of w
= a1 + a2-The radiant ' heat transfer from this opening to the equipment is given. by the equation (3): ?
q'= EF : o (Tf 4-Te) 4 where q = radiant flux in kW/m2 or Btu /ft 2-sec E = etnissivity of the flame F = view factor or configuration factor o = Stefan-Boltzman Constant 5.669 x 10-5 kW/m2g4 ,
or 0.1714 x 10-8 Btu /hr ft2 R4 Tr = flame temperature K or R Te = equipment temperature K or R r = transmissivity 2
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s 1 For a conservative simplification, the emissivity was taken at its maximum value of 1.0 The transmissivity of the atmosphere was also taken at its maximum value of 1.0 This yields the sim-plified conservative equation: '
q=F a(Tf 4-Te) 4 To quantify F, the view factor, the parallel plane geometry was assumed. This approach is similar to that developed by the Amer-ican Iron and Steel Institute for evaluating heat transfer to external steel members outside a window exposed to a fire inside the building. Figure 3 on page 6 shows the geometry for this view factor and defines X and Y.
The generalized form of F for this geometry for an opening of width and height is given below:
F= 1 X tan- Y + Y tan ' X 2
2w (1 + X )1 f2 2 (1 + X )1 f2 (1 + Y2)1/2 (1 + y2)1f Attachment 1, extracted from the AISI methodology (4) shows the values for F(4) in graphic form.
Three flame temperatures were used in calculating the radiant heat flux from openings; 1100 K (1520 F), 1200 K (1700 F) and 1300 K (1880 F). Typical flame temperature from burning cable c' insulation is around 1100 K (5). The flame temperature from other burning solids such as polystyrene or polypropylene is reported as 1200 K (6) and from burning solvents such as hexane j is 1300 K (6). These temperatures are very conservative for these plant areas. These temperatures can be related to the tem-perature of the ASTM E-119 furnace exposure (standard time and l temperature) at 30 minutes, I hour and 2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br /> respectively.
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O t The equipment temperature was assumed to be 300'K. Attachment 2 provides the calculation of radiant flux in W/m 2 -for these flame temperatures and various values of X and Y.
To calculate the total radiant flux received by the target, .the fluxes received from each portion of the opening (as shown in Figure 3) must be summed 9
- 91 + 42 + 43 + 44 For worst case, maximum flux for minimum total opening area, the target must be in line with the center of the opening. This means that a1 = a2 and bi=b2 and that 41 " 42 " 43 = q4 or q = 441 The values for qi as calculated and shown in Attachment 2, are one-fourth of the total worst case flux. In order to determine the minimum area of an opening to create a threshhold flux, val-ues of X and Y which yield a flux of q critical were tabulated.
4 The area of the opening would be given by the following equation:
A = 4 X Yd2 The minimum area is given by the minimum product of XY. Tables 1 through 6 show the values of X and Y to provide critical fluxes and show the minimum product of XY. Based on these tables the following six equations for minimum area were developed as a v function of d, distance from the wall (in inches):
Tr( K) Flux (kW/m2 ) Area 1100 20 A = 1.12d2 1100 30 A = 1.92d2 1200 20 A = 0.72d2 1200 30 A = 1.20d2 1300 20 A = 0.48d2 1300 30 A = 0.80d2 7
TABLE 1 Flame Temperature 1100*K Flux 4 x 5.0 = 20 kW/m2 X Y Minimum XY
>1.2 0.3 0.7 0.4 0.28 0.6 0.5 0.5 0.6 0.4 0.7-1.1 0.3 >1.2 TABLE 2 Flame Temperature 1100*K Flux 4 x 7.5 = 30 kW/m2 X Y Minimum XY
>1.1 0.5 0.8 0.6 0.48 0.7 0.7 0.6 0.8-1.0 0.5 >1.1 TABLE 3 Flame Temperature 1200 K
, Flux - 4 x 5.0 = 20 kW/m2 X 'eY Minimun XY
>1.3 0.2 0.6 0.3 O.L 0.4 0.18 0.4 0.5 0.3 0.6-1.2 0.2 >1.3 8
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TABLE 4 Flame Temperature 1200*K Flux 4 x 7.5 = 30 kW/m2 X Y Minimum XY
>1.4 0.3 0.8 0.4 0.30 0.6 0.5 0.5 0.6 0.4 0.8 TABLE 5 Flame Temperature 1300 K Flux 4 x 5.0 = 20 kW/m2 X Y Minimum XY
>0.7 0.2 0.4 0.3 0.12 0.3 0.4 0.2 >0.7 l
TABLE 6 Flame Temperature 1300 K Flux 4 x 7.5 =-30 kW/m2 X Y Minimum XY
>1.9 0.2 0.20 ,,
0.7 0.3 '
0.5 0.4 .
0.4 0.5 0.3 0.7 9
3.0 RESULTS Case 1 Floor elevation 716'-0" West of Column line 56 -
d = 1'3" (15")
Equipment: Motor Critical Flux: 20 kW/m2 Flame Temperature Area in sq. inch (sq. ft.)
1100 K 252 (1.75).
1200 K 162 (1.125) 1300 K 108 (0.75)
Case 2 Floor elevation 716'-0" East of Column line 56 d = 7 ft (84")
Equipment: Pump Critical Flux: 30 kW/m2 Flame Temperature Area in sq. inch (sq. ft.)
1100 K 13548 (94) 1200 K 8467 (58.8) 1300 K 5645 (39.2)
Case 3 Floor elevation 733'-0" West of Column line 56
, ; dc = 7 ft (34")
Equipment: Motor and Pump Critical Flux: 20 kW/m2 i-Flame Temperature Area in sq. inch (sq. ft.)
l 1100 K 7903 (54.9) 1200 K 5080 (35.3) i 1300 K 3387 (23.5) 10
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Case 4 Floor elevation 733'-0" East of- Column line 56 d = 8.5-ft (102")
l Equiprent: Motor and Pump Critical Flux: 20 kW/m2 9
Flame Temperature Area in sq. inch (sq. ft.)
1100 K 11652 (80.9) 1200 K 7491 (52) 1300 K 4994 (34.7)
_ Case 5 Floor elevation 750'-0" West of Column line 56 d = 6 ft (72")
Equipment: Motor and Pump Critical Flux: 20 kW/m2 Flame Temperature Area in sq. inch (sq. ft.)
1100*K 5806 (40.3) 1200 K 3732 (25.9) 1300 K 2488 (17.3)
Case 6 Floor elevation 750'-0" West of Column line 56 d = 6 ft (72") -
Equipment: f.iotor and Pump -i e,,
Critical Flux 20: kW/m2 Flame Temperature Area in sq. inch (sq. ft.)
1100 K 5806 (40.3)
, 1200'K 3732 (25.9) 1300 K 2488 (17.3) 11
4.0 CONCLUSION
S Based on the results in section 3.0 only one case, Case 1, elevation 716*-0" west of Column line 56, need be considered in the realm of credibility. For all other cases, the equipment is located far enough -
from the wall to require unreasonably large openings, almost equiva-lent to wall collapse. Since the steel penetrating these walls does not support the walls, wall collapse from expansion or failure of penetrating steel is not credible.
1 1
l File Ref: DP-01-01-101 12 1
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O e ATTACHMENT 1 Extracted from Fire-Safe Structural Steel A Design Guide American Iron and Steel Institute 1979 CONFIGURATION FACTORS From curve for value ofx and its intercept with the value ofy, read 6, configuration factor,from scale on left. '
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.7000001 1.2 10105.09 .1904141 1100 .0000001 1.2 10956.73 .1537271 1100 .9000001 1.2 11677.04 .14145 4 1100 1 1.2 12284.04 .14C0107
. 1100 1.1 1.2 12794.69 .1599917 1100 1.2 1.2 13223.27 .1cO1834-1100 1.3 1.2 135G3.5 .164547 1100 1.4 1.2 13G96.79 .1602211
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.1797029 1100 1.3 1.? 15271.02 .134999 1100 1.4 1.9 15644.35 .1595117 1100 1.5 1.9 15962.5 .1933657 1100 1.6 1.9 16234.93 .1956S59 1100 1.7 t.9 16468.91 .1995002 1100 1.0 1.9 16670.99 .3019422 1100 1.9 1.9 16344.73 .3040523 1100 2 1.9 1499S.33 .0050532 1100- .1 2 1969.97 2.DU637EE-O?
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1300 2 1.4 30050.9 .19105?1 ' 1300 .1 1.5 3692.139 2.EOS567E-02 1300 .2 1.5 7270.OGG 9.502354E-02 1300 .3 1.5 10635.54 .0650657. 1300 .4 1.5 13717.69 0.495342E-02 1300 .5 1.5 16476.03 .1020407 1300 .6 1.5 13901.6 .1170573 1300 .7000001 1.5 21002.36 .1300673 1300 .0000001 1.5 22303.54 .1412219 1300 .9000001 . 1.5 24336.06 .1507170 1300 1 1.5 25636.4 .15G7653 3 1300 1.1 1.5 26735.27 .1655711
- 1300 1.2 1.5 27663.9 . .1713221 r 1300 1.3 1.5 20449.15 ' .1761351 ..
1300 1.4 1.5 29114.22 .1803037 1300 1.5 1.5 39670.79 .1009002 1300 1.6 1.5 39157.35 .1867763 1300 1.7 1.5 30567.68 .1n93173 1300 1.0 1.5 30921.19 .1?14944 1300 1.9 1.5 31233.35 .1933657 1300 2 1.5 31434.01 .1947799 1300 .1 1.6 3736.569 2.314051E-02 1300 .2 1.6 7?53.331 4.537003E-03 1300 .3 1.6 10766.64 .0666776 1300 .4 1.6 13G70.2 3.60217GT-02 1300 .5 1.6 166GS.93 .1033543 1300 .6 1.6 19151.10 .11060? 1300 .7000001 1.6 21207.11 .1310307 1300 .G000001 1.6 23121.01 .1431031 1300 .9000001 1.6 24634.53 .1823712 1300 1 1.6 26v11.08 .1610911 ! 1300 1.1 1.6 27136.1 .1600534 1300 1.2 1.6 POOO7.77 .1737471 1300 1.3 1.6 20G73.69 .17t17394 1300 1.4 1.6 29577.31 .1931749 1300 1.5 1.6 3015?.35 .1067763 1300 1.6 1.6 9065S.10 .189047 17 i m - - -1 pg, q ei-=1 ~ --- - - y.- g y-. g - -
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1300 1.5 1.7 30569.68 .1993175 1300 1.6 1.7 31079.22 .1924731 1300 .1.7 1.7 31515.65 .1951759 1300 1.8 1.7 31890.64 .1974902 1300 1.9 1.7 32213.91 .1995002 1300 2 1.7 22493.56 .2012321 1300 .1 1.0 3804.700 2.2562??E-02' 1300 .2 1.2 7494.071 4.641066E-02 1300 .3 1.8 10963.53 6.792791C-02 1300 .4 1.8 14156.27 8.7669542-02 1300 .5- 1.0 17016.63 .105334 1300 .6 1.8 19537.7 .1209?67 1300 .7000001 1.3 21727.16 .1045633 1300 .G000001 1.3 23615.13 .1462431 1300 .9000001 1.0 25227.21 .2562317 1300 1 1.0 26599.43 .164729G 1200 1.1 1.3 27765.03 .1719403 1300 1.2 1.8 2G754.66 .1700771 1300 1.2 1.0 29595.46 .1832842 1000 1.4 1.3 30310.95 .1377153 1300 1.5 1.0 30921.19 .1914044 1300 1.6 1.3 31443.04 .1947262 1300 1.7 1.8 31890.64 .1774952 1300 1.8 1.8 32275.76 .1992832 1300 1.9 1.e 32602.22 .2019422 1300 2 1.3 32096.13 .2037255 r 1300 .1 1.9 3031.064 2.372571E-02 1300 .2 1.9 7544.336 4.673664E-02 1000 3 1.9 11646,.42 .0604103 1300 4 1.9 14250.07 3.03'M10E-03 1300 .5 1.9 17143.53 .1061696 1300 .6 1.9 1C6G7.6 .121925 1300 .7000001 1.9 21960.96 .1556323 1300 .0000001 1.9 23307.64 .1474402 1300 .9000001 1.7 25439.15 .!573943 1300 1 1.9 24039.51 .1661547 1300 1.1 1.9 23011.97 .1734777 - 1300 1.2 1.0 29017.18 .1797029 1300 1.3 1.9 27372.35 .104999 1300 1.4 1.9 20601.04 .1395117 1300 1.5 1.9 31223.35 .19336S7 1300 1.6 1.9 317G 6.i?4 .1766.t51 1300 1.7 1.9 32013.91 .199500.' 1300 1.0 1.9 22600.22 . nO t 94H'd 1300 1.9 1.9 32949.03 .D040120 1300 2 1.9 33244.6 .FAGOO32 1300 .1 D 3G57.347 U.30607.FC-02 1366 .2 P 7P.90.767 .0470009 18
a o o . 1300 .3 2 11112.54 6.OS1970E-02 1300 .4 2 19346.4 8.824701E-02 1300 .5 2 17251.4 .1068376 1300 .6 2 19215.3 .1227152 1300 .7000001 2 D2047.42 .1365293 1300 .8000001 2 23971.97 143458 1300 .9000001 2 25620.33 .1596663 1300 1 2 27026.5 .1673747 1300 1.1 2 CG223.71 .174729 1300 1.2 2 2?242.64 .1010492 1300 1.3 2 30110.49 .1e54,3e 1300 1.4 2 30850.9 .1910591 1300 1.5 2 314G4.01 .1949799 1300 1.6 2 32036.G .1923615 1300 1.7 2 32493.56 .2012321 1300 1.0 2 32896.19 .2037255 1300 1.9 2 33244.6 .305G833 1300 2 2 33547.11 .2077567 19
O 44 C) 0 ATTACHMENT 3
5 . e. ATTACHMENT 3 REFERENCES
- 1) " Categorization of Cable Flammability." EPRI NP 1200 Part 1 Electric Power Research Institute, Palo Alto, California, 1979.
- 2) John L. Bryan, " Defining Damageability " Symposium on Quantitative Fire Hazards Analysis Techniques, SFPE, College Park, Maryland, March 4, 1985.
l 3) C.0. Bennett and J.E. Myers, Momentum, Heat and Mass Transfer, McGraw-Hill, New York, 1962.
- 4) " Fire Safe Structural Steel: A Design Guide," American Iron and Steel Institute Washington, DC. 1979. .
- 5) W.H., Schmidt and F.R. Krause, " Burn Mode Analysis of Horizontal Cable Tray Fire," SAND 81-0079, NUREG/CR-2431, Sandia National Laboratories, February 1982.
- 6) V. Babrauskas, Chapter 21, Sect. 6, NFPA Fire Protection Handbook, 16th Edition, NFPA, Quincy, Massachusetts, 1986.
l
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