ML20247M289
| ML20247M289 | |
| Person / Time | |
|---|---|
| Site: | Quad Cities  |
| Issue date: | 04/01/1987 |
| From: | NUS CORP. |
| To: | |
| Shared Package | |
| ML20247M280 | List: |
| References | |
| 546Y-M-02, 546Y-M-2, NUDOCS 8906050015 | |
| Download: ML20247M289 (177) | |
Text
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TABLE D-1 LOSS-OF-COOLANT ACCIDENT PARAMETERS TABULATED FOR POSTULATED ACCIDENT ANALYSES Design Basis Ass umption s I. Data and Assumptions Used to Estimate Radioactive Source from Postulated Accidents A. Power level, NWt B. Burnup 2,511 C. NA Fission products released from fuel (fuel 100% damaged ) D. Iodine fractions Organic Elemental 0.04 Particulate 0 91 0.05 II. Data and Assumptions Used to Estimate Activity Released A. Primary containment leak rate, t/ day B. 0.75 Free volume of primary containment, eu f t 2.75E+5 C. Secondary containment release rate, t/ day D. Leak rate through MSIV, scfh JO@( 11.5 E. Number of main steam lines 4 F. Leak rate from turbine condenser complex, t/ day 10 G. Volume and surface area (all four steam Ft 3 Ft 2 lines) Between inboard and outboard MSIV 170 470 Outboard and turbine stop valves 761 1,693 Turbine condenser complex 1.7x10 5 6.5x10 $ H. Deposition velocity for iodines, em/sec ' Particulate 0.012 j Elemental 0.012 Organic 0.0 I. Valve movement times ( See No te ) J. SGTS adsorption and filtration efficiencies, 4 Organic iodines 99 Elemental iodine 99 Particulate iodine 99 _ _ _ _ _ _ _ _ . _ _ _ - _ _ - _ _ _ _ _ _ _ - _ _ - _ _ - _ _ - Q
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9f9 ,r' Q g* J4(/ ]ei Fr t Tacle D (continued ) Design Basis As s umption s III. Dispersion Data, .sec/m A. Control room wake X/Q for time intervals SGTS of Bypass beak (Chimney) O to 2 hours 1.29E-3 7.0E-4* 2 to 8 hours 1.29E-3 6.45E-6 8 to 24 hours 7.61E-4 3.81E-6 1 to 4 days 4.84E-4 2.42E-6 4 to 30 days 2.13E-4 1.07E-6
'O to 2 hour fumigation conditions assumed according to Regulatory Guide 1.3 IV. Data for Control Room A. Volume of control room, f t 5.83E+4 B. Filtered intakei cfm 2,000 .l C. Efficiency _of charcoal adsorber, t . 99 D. Efficiency of BEPA, t 99.9 E. Unfiltered inleakage, cfm 10 F. Recirculation flowrate 0.0 G. Occupancy factors:
0 to 1 day 1.0 1 to 4 days 0.6 4 to 30 days 0.4 Note: The MSIV movement times are not applicable to the snalysis because the valves will close before any significant fuel failures occur. The control room HVAC intake valve movement times are not applicable because the calculated doses assume an unfiltered outside air intake of 2,000 cfm for the first 8 hours post-LOCA. I
64Wf-Yb'~0$ jd ID ~tyl g@ d/ Gg_2 f TABLE D-2 DBA-LOCA RADIOLOGICAL CONSEQUENCES CONTROL ROOM Doses -(Rem; Thyroid Skin Qole-Body
~
- 1. Bypass Leakage
- a. Activity inside control room 2.97 4.77E-1 1.52E-2
- b. Plume shine -- --
2.03E-3
- c. Direct shine -- --
5.70E-2
- 2. Stack Release a.' Activity inside control room 10.10 1.96 1.20E-1
- b. Plume shine -- -
1.66E-2 TOTAL CONTROL ROOM DOSES 13.07 2.46 2.11E-1 Note: The values provided above represent 30-day integrated doses. The doses are calculated assuming an unfiltered outside air intake of 2,000 cfm for the first 8 hours post-LOCA. At 8 hours, the con-trol room operators are assumed to remote manually activate the charcoal filtration unit. l l l
-_--_______-_-____ - ___ - - D
~
c [b Y- IA- Ci k O f 6 b '2L. The initial blowdown through the suppression pool is rtostly air with the trailing phases of blowndown essentially all steam. Most fission product release would accompany the ffcal steam release and would be scrubbed efficiently by the ste'am condensation. Airborne inorganic halogen and
)
solid fission products in the drywell would be rapidly removed by the containment spray and steam condensation and mixed with water in the suppression chamber. For the accident analysis, a partition factor of 100 ) for incrganic halogens is used. Inorganic halogens are assumed to be ! i re-evolved from the water as leakage from the containment reduces the inventory of airborne halogens. Combining the assumption of a high 1 f raction of organic halides with no ~ absorption in water and the I conversative water to air partition factor for inorganic halogens results in a very conservative high fraction of halogens remaining airborne for leakage from the containment. The inventory of airborne fission products in the drywell available for leakage into the reactor building is shown in Table 14.2.8. (3
%)
TABLE 14.2.8 LOSS OF COOLANT ACCIDENT PRIMARY CONTAINMENT AIRBORNE FISSION PRODUCT INVENTORY 4 Time After Noble Gases Halogens Accident (curies) (curies) { 1 minute 1.6x10 4.3X10' 30 minutes 5 5.2x10 2.7x10 1 hour 4.7x10 2.5x10' 2 hours 5 4.5x10 2.4x10' 12 hours 3.3x10 5 1.3x10 5 hcurs 5 4 3.2x10 1.2x10 i i 1 day 2.7x10 5 1.0x10 4 l 1 2 days 5 2.5x10 9.3x10 3
-0 10 davs 7.5x10' 2.4x10 25 days 1.2x10' 4.7x10 2 QUAD-CITIES SECTION 14 PAGE 41
_ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ - _ _ _ _ _ - _ _ _ _ _ _ _ _ _ _ _ _ _ - _ _ _ _ _ _ _ _ _ _ _ - - - 1
h. El{b]~ M '01 h ! 2.u.- f bb f( $ I, . I
'd rvwel l viu the liquid water. As noted in Figure 6.2.21, le ss than 47. of I f
l
). the assumed maximum number of damaged rods will experience cladding damage in the 200 seconds. It een therefore be concluded that the iodine activity will reach the suppression pool and that the mode of transport to the pool is unimpo rtant. As f ar as the nob'e gas activity is concerned, it is irrele- !
vant wSether or not the activity reaches the suppression pool as the decontamination ef fects of wa ter for the noble gases is negligible. It is therefore assumed that all of the released noble gases are airborne in the p r ima ry c ont a inme nt . These calculation are for 7x7 arrays. For 8x8 arrays l: the release will be 88% of the tables which are already conservative. Fission product Release from Drvvell to the Reactor Building The primary containment leakage ratus were calculated assuming that the primary containment leaks 0.5 percent of the contained free volume per 24 hours at 62 psig; the turbulent rough passage equation (0)* was used for interpola tion to lowe r pressures. The long term primary contairrnent pressure is shown in Section 5.2.3. The corresponding containment leakage for case d. .shown in Figure 5.2.13 represents a highly f aulted condition of one core spray, three containment cooling pumps, and three heat exchangers all inoperable. I M fission products leak frern the drywell, high pressure or reactor building high radiation signals isolate the af fected zone of the reactor i building and start the standby gas creatment system. The standby gas t r ea tme nt fan maintains the reactor building below atmospheric pressure and discharges a volume equivalent to 100 percent of the building volume i per day through high ef ficiency filters and charcoal absorbers to a 310 ft. elevated release point. All the noble gases and halogens released j into the reactor building are assumed to renain airborne. !
- This reference (3) will be included at the end of Section 14 O
.0UAD-CI TIES SECTION '4 PACE 43 }
_-_m_.m-ftEbYM Y {?'m ' Yl0 $ b} l Considering the leakage from the drywell to the reactor building. i radioactive decay, fallout and plateout, the air change rate of 100
.'c) 1 percent building volume per day, the airborne fission product inventory in the reactor building is shown in Table 14.2.9.
. - 1 TABLE 14.2.9 LOSS OF C00I. ANT ACCIDENT REACTOR BUILDING AIRBORIIE FISSION PRODUCT INVENTORY Time After Noble Gases Halogens Accident (curies) (curies) 0 1 Minute 8.8x10 2.4x10
~
30 Minutes 4.8x10 0-2.5x10 1 Hour 8.9x10 1 4.8 x10 0 2 0 2 Hours 1.6x10 8.6x10 1 Hours 6.0x10 2 2.4x10 1 O 12 Hours 6.6x10 2 2.6x10 I U 2 1 Day 7.4x10 2.8x10 1 3.1x10 I 2 2 Days 8.3x10 2 10 Days 2.0x10 6.5 x10 0 25 Days I 2.5x10 9.5x10"I Fission Product Release from Reactor Building to Atmosphere The halogeis which leak from the pressure suppression contaireent
~
into the reactor building are exhausted by the standby gas tree ment system threugh a demister, air heater, roughing filter, charcoal filter and a high efficiency filter. Because the high temperature and pressure steam atmosphere is contained within the pressure suppression system, the reactor building exhaust air is at low temperature and humidity and can be e References (9) through (14) and their abstracts are included at the end of Section 14. QUAD-CITIES SECTION 14 PAGE 44 1
u EYlff N-C'f. d6 cf _LN7 . treated to reduce the humidity so that the filters will be very ef fective for removal of organ!c halides. Tests on filter efficiencies have shown that inorganic halogens are removed by charcoal filters with ef ficiencies greater than 99.99 perc'ent 0,10)* and tests on filter ef ficienc ies have shown that organic halogens are removed by charcoal filters at c relative humidity belov 30' percent with filter ef ficiencies from 99.9 per':ent to (10, 11, 12, 13, 14)
.99.9999 percent. The charcoal f11ter on th-t EVESR at Vallecitos Atomic Power Laboratory has been retaining organic halogens produced at power operation with a filter efficiency from 99.8 pe.rcent to 99.9 percent at a relative humidity of 10 to 15 percent. The standby gas t rea tme nt system design is bcsed on the latest experimental results. The syst a is designed to provide the necessary residence time in filters.
Thus, with this design, the assumption of only a 99 percent filt er ef ficiency for the removal. of inorganic and organic halides in the standby gas treat:nent system is conservative by approximately four orders of magnitude. The compounding of pessimistic assumptions used in the loss af coolant anaysis results .in calculated doses fran ha;ogens that are 20 to 1000 times higher than would actually be expected. Discharge rates from the loss of cool at accident to the elevated release point are shown in Table 14.2.10.
- References (9) through (14) and their abstracts are included at the end of dection 14 l
Qt'AD-CITIES SECTION 14 PAGE 4 5 , - _- - _ _ _ _ _ _ - _ _ _ _ _ _ - _ _ _ _ _______-________- _ _--_- _______-__ _ ______ __-_______--_____- _ -- ________ _ -_____--_A
C b]- VA :0Y fgp& N r. ~ - 9 8,y [ G- t. ti .. r TABLE 14.2.10 LOSS OF COOLANT ACCIDENT
' FISSION PRODUCT RELEASE RATE FROM CHIhNEY-J ' Time 'a f ter Noble Gases Halogens Accident (curies /sec) (curies /sec) 1 minute -8 1.0x10 2.8x10
~
30 minute's- 5.6x10"' 2.9x10 1 hour 1.0x10 -3 5.5x10
~7 1.9x10 -3
~
2 hours 1.0x10 ' 12 hours 7.0x10 -3 2.8x10
~0 15 hours 7.7x10
-3 -6 3.0x10 1 day 8.6x10 -3 3.2x10
-6 2 days 9.7x10 ~3 -6 3.6x10 2.4x10 -3
~
10 days 7.5x10 25 days
~
~7 2.9x10 ' 1.1x10 O
/
O QUAD-CITIES SECTION 14 PAGE 46 _ _ _ _ _ _ _ - - _ - - _ _ - - - - - - - - -- - )
Mt M -OY um. o. studley I t US CORPORATION 83
- Ms '
f O b --,-. E.ias,'he1 M. Fallin THE ASSUAG MAAvLAND EOe781399 iIe 309 258-6000 May 29,1987 G-87-004 AIR No.12-82-6 M 12-2/3-82-1 AIR No. 4-82-2 M 4-1/2-82-2 NUS Project No. 6061 (546Y) - Ms. M. A. Jackson, SNCE i Commonwealth Edison Company P. O. Box 767, 35 FN West Chicago, IL 60690
Subject:
CECO - Control Room HVAC Upgrade, P. O. No. 259402 Meeting Minutes
Dear Ms. Jackson:
Enclosed please find the Meeting Minutes of the May 21, 1987 meeting held at Bechtel's office. Very truly yours, [a M. 3. Glarratano Project Manager
/gd Enclosure cc: 3. E. Hausman, SNPE N. Konstantinou
( 5) A Halliburton Company
. - ?ON NUCLE'AR l'
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E A-'- .. YGINEERING OlVISION , y, ; PROCEDURE 11 E - . .
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8 AGES ___ CALCULATION COVER SHEET
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[g[gtO [gbfed i REVIEW COMPLETED
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1 AN81 CASE - OC, 2000CFM SUPPLY, 10 CFM UNFILTERED INLEAMAGE, OHR PRES 5 2 52 1. 0 1. 0 3 2511 2.6E6 1.84E5 5.83E4 4 0. 0 0. 0 00 1. 0 1. 0 2 75ES 0. 0 5 7.2E3 2.88E4 8.64E4 3 456E5 2.592E6 6 8.e806E-8 8 6806E-8 8.6806E-8 8.6806E-8 8 6806E-B 7 1.157E-5 1.157E-5 1.157E-5 1.157E-5 1.157E-5 8 1. 0 1. 0 1. 0 1 0 1. 0 9 1.010E3 1.010E3 OE0 OE0 OEO 10 7.OE-4 6.45E-6 3.81E-6 1.45E-6 4.28E-7 11 7.00E-4 6.45E-6 3.81E-6 1.45E-6 4.28E-7 12 0. 0 00 00 0. 0 0. 0 13 0. 0 0. 0 0. 0 0. 0 00 14 0. 0 0. 0 00 00 0. 0 15 00 0. 0 00 0. 0 00 16 0. 0 0. 0 00 00 0. 0 17 0. 0 . 0. 0 00 0. 0 0. 0 18 0. 0 CO 1.812E-4 1.812E-4 1.812E-4 19 0. 0 0. O 1.812E-4 1.812E-4 1.812E-4 20 0. 0 0. 0 1.812E-4 1.812E-4 1.812E-4 21 0 01 0 01 0. 01 1.0000 1.0000 1.0000 22 0. 0 0. 0 0. 0 100 f,/Q 6 -7 7t* b de se 1 ANSI CASE - OC, 2000CFM SUPPLY. 2 32 1. 0 10 CFM UNFILTERED INLEAMAGE
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- 0. 0 0. 0 1. 0 1. 0 2.75ES 0. 0 4 0. 0 S 7,2E3 2.99E4 8.64E4 3.456ES 2.S92E6 6 S.690eE-9 8.690 @ 9 8.6906E-8 8.6806E-8 9.6806E-8 1.157E-S 7 1.137E-S 1.157E-5 1.157E-S 1.157E-S S 1. 0 1. 0 1. 0 1. 0 1. 0 1.26E3 OE0 OE0 OE0 9 1.26E3 10 7.OE-4 6.4SE-6 3.81E-6 1.4SE-6 4.2SE-7 11 7.00E-4 6.4SE-6 3.81E-6 1.4SE-6 4.2eE-7
- 0. 0 0. 0 0. 0 0. 0 C. 0 12 0. 0 13 0. 0 0. 0 0. 0 0. 0 14 00 0. 0 0. 0 0. 0 0. 0
- 0. 0 0. 0 0. 0 0. 0 0. 0 15 0. 0 16 0. 0 0. 0 . 0. 0 0. 0 i
- 0. 0 0. 0 0. 0 0. 0 0. 0 l 17 18 0. O O. 0 1.812E-4 1.312E-4 1.312E-4 19 0. 0 0, 0 1.812E-4 1.012E-4 1.812E-4 20 0. O O. 0 1.812E-4 1.012E-4 1.912E-4 0.01 0.01 1.0000 1.0000 1.0000 21 0.01 22 0. 0 0, 0 0. 0 9 4'120 1 ANSI C ASE - OC. ,2000CFM SUPPLY, 260 CFM UNFILTERED INLEAKAGE
& S2 1. 0 1. 0 -
3 2511 2.6E6 1. 84ES S.03E4
- 0. 0 0. 0 1. 0 1. 0 2.75ES 0. 0 4 10 S 7.2E3 2 90E4 8.64E4 3 4S6ES 2.592E6 6 8.6806E-8 8.6806E-B B.6806E-9 G.6806E-B B.6906E-9 1,157E-S 7 1.157E-S 1.137E-S 1.157E-S 1.157E-S B 1. 0 1. 0 1. 0 1. 0 1. 0 l
9 0. 0 0. 0 2.26E3 2.26E3 2.26E3 ' 10 7.OE-4 6.4SE-6 3.B1E-6 1.ASE-6 4.29E-7 l 11 7.00E-4 6.4SE-6 3.B1E-6 1.ASE-6 4.2BE-7 l l l 12 0. 0 0. 0 0. 0 0. 0 0. 0 13 00 0. 0 0. 0 0. 0 0. 0 14 0. 0 0. 0 0. 0 0. 0 0. 0 15 0. 0 0. 0 0. 0 0. 0 0. 0 16 0. 0 0. 0 0. 0 0. 0 0. 0 17 0. 0 0. 0 0. 0 00 0. 0 18 0. 0 0. 0 0. O O. 0 0. O l 19 0. 0 0. 0 0. 0 0. 0 0. 0 i 20 0. O O. 0 0. 0 0. 0 0. 0 l. 21 0.01 0.01 0.01 0.1239 0.1239 0.1239 22 00 0. 0 0. 0 NuS 166A MvistD 02e6
NUS CORPORA TION AND SUBSIDIARIES MDARD CAWMM SHEET-CUENT: FILE NO.: sy; W Opdaddlern, lkte '"{*? "' *Q.'; g. DY Nb 1 EST. CASE - OC, 2000CFM SUPPLY. 300 CFM UNFILTERED INLEAKAGE 2 52 1. 0 1. O w" 3 2S11 2.6E6 1.84ES S.83E4 4 0. 0 0. 0 0. 0 1. .O 1. 0 2.7SES 0. 0 S 7.2E3 2.SSE4 8.64E4 3.456ES 2.392E6 6 B.6806E-S 8.6806E-9 8.6806E-9 B.6806E-9 8.6806E-8 7 1.157E-S 1.157E-S 1.157E-S 1.157E-3 1.157E-S S 1. 0 1. 0 1. 0 1. 0 1. 0 9 1,300E3 1.300E3 OED DEO DEO 10 7.00E-4 6.4SE-6 3.31E-6 1.4SE-6 4.2AE-7 11 7.00E-4 6.4SE-6 3.81E-6 1.4SE-6 4.20E-7 12 0. 0 0. 0 0. 0 00 0. 0 13 0. 0 0. 0 0. 0 0. 0 0. 0 14 0. 0 0. 0 0. 0 0. O O. 0 15 O. 0 00 0. 0 0. O O0 16 0. 0 0. 0 0. 0 0. 0 0. 0 17 0. 0 0. 0 0. 0 00 0. 0 18 00 0. 0 1.812E-4 1.812E-4 1.912E-4 19 0. 0 0. 0 1.812E-4 1.812E-8 1.812E-4 20 0. 0 0. 0 1.812E-4 1.812E-4 1.812E-4 21 0.01 0.01 0.01 1.0000 1.0000 1.0000 22 0. 0 0. 0 0. 0 Th 2! f51. 32 EAST 1.0- OC. 2 010Cr4
- 1. 0 SU" L Y e ?31 CFM UNr1LTERE3 INLEAkact 3 2511 2. 6". 6 1.*4E5 '. . P 3 ~ 4 4 30 0. 0 91 10 i 7 2E! 1.C P.75r5 0. 0 2.8 tE 4 4.54E4 3 456Et 2 512E6 6
4 6A06 E-2 8.68D6C-8 8 6835E -B 8 6406E-R B.6 806E*4 7 8 1 15 T r. ! 1.15 ? E- 3 1 157 r-3 1.157E-5 1 157E-5 10 19 1.0 e 0.0 1. 0 1.0 1.3 P.303E3 2 300E3 2.300E3 11 1 30E-4 6.45E-6 3 41E-6 1 45E-6 11 7 07E-9 4 24E-7 6 49 E- 6 3 91 ~ - 6 1 45E-6 4.2dE-f 12 0.0 0. 0 0.3 0.0 0.0 13 0.0 0.0 01 00 0.0 14 0.0 0.3 15 00 00 0.3 0.J 0. 0 13 16 00 0.0 0.0 0.0 9.0 0.0 0.0 17 0.0 0. 0 Id 90 0.0 0.3 0.0 0. 0 30 19 C.0 0.0 00 0. 0 Dei 0.0 2J 00 0.0
- 3. 0 00 0.0 21 1.41 0.0 0.31 J. 01 0.1391 0 1391 22 00 0.0 S.1391 0.0 NU$ beA REVISED 0285
NUS CORPORA TION AND SUBS /D/ ARIES . TANDARD CALCU IOt CUENT: FILE NO gy b [~ N ~ h_a_g PAGE $ 0Fj g SUSJECT: CHECKED BY-UUb OWWW h&& ,me $ -$. . g , a a u s a g a e s ~ a ,< . r + : ,. g m c m . , ,
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- 0. 513 fws NUS 165A AfVl&ED 0286
NUS CORPORA TION AND SUBSIDIARIES TANDARD CALCUWlON SHEET CUENT: FILE NO.: - gy SVh Y~ M ~ h h Y&_4 9 AGE)forp}) c"'"" 2"Tixsa,+< % % a f s " i "*?; . , b V Y/ . sown (u4) fr 5: OtX.* by px 1r} C' # fir;c d & 7 ( trt b h __ OtB hr O< / 2. !4 Q,12 OMVW /. )7 Y'Gl G, Z'54 ZY4 94W /8eY .5 30 .>. fl L f6 + w k 99, y 5 31 ~ l8. 5:5 A= 12. s e L ehck os e = t.bz w 8 s ']zo e O. 59 5 pm e26sem - 2S. 59 2w. C bx<.Lt's 6 2x Cfn1 ebb e beg thel s+ue ao e., sftek M 44; da 2 e. /. B-r ZV Arv Di V98 0. /A / y,/f JY-7 M k /,pp OJ96 y,7 g, fie -7 lzo h v /,16 0,2Y7 47't
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7/w 22*GCM : 29 a.'f @n NUS 186A WVISED 0286
NUS CORPORA TION AND SUBSIDIARIES TANDARD CALCU HON gg FILE NO.! BY CUENT:drdo s,y y-in - 6 7 M4ae enae %,, hd w gc .
,9 b,4(!M) 89fo as Conc ' 2. 66 L (fn '* h 6 5.)
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t : : ; w - 100 M 9 00 h l h $fAhw hil(OHn} NU$ 156A fl[ VISED 0205
l NUS CORPORA TION AND SUBSIDIARIES TANDARD CALCMilON SHEET FILE NO.: CUENT; @ ow a-01 SY'MA d a "4cn a v ,
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h Q conshet d 6(fl.00w'. &puuawyk Sw hM $r /Z. h $t Jf g 13 , f f 5 N/ *f M " m no w e-o m u. 1 EST. CASE - OC. 2000CFM SUPPLY. 222 CFM UIFILTERED 116 EAKAGE 2 52 1. 0 1. 0 3 acts a.ese 1.ecco 3. sate 4 0. 0 0. 0 0. 0 1. 0 1. 0 2.75ES 0. 0 5 7.2E3 2.SSE4 8.64E4 3.456EU 2.592E6 6 S.6806E-3 8.6So&E-S 3.6806E-S 8.6806E-S 8.6806E-S 7 1.157E-5 1.157E-5 1.157E-5 1.157E-5 1.157E-5 8 1. 0 1. 0 1. 0 1. 0 1. 0 9 1.222E3 OE0 OE0 CEO OE0 to 7.00E-4 6. 4M-6 3.31E-6 1.4M-6 4.ESE-7 11 7.00E-4 6.4 K-6 3.31E-6 1.4K-6 4.2SE-7 12 0. 0 0. 0 0. 0 0. 0 0. 0 13 0. 0 0. 0 0. 0 0. 0 0. 0 14 0. 0 0. 0 C. 0 0. 0 0. 0 15 0. 0 C. 0 0. 0 0. 0 0. 0 16 0. 0 0. 0 0. O O. 0 0. 0 17 0. 0 0. 0 0. 0 0. 0 0. 0 10 0. 0 1.312E-4 1.312E-4 1. SIM-4 1.312E-4 19 0. 0 1.812E-4 1.312E-4 1.813E-4 1.01 5 -4 20 0. 0 1.312E-4 1.312E-4 1.013E-4 1.312E-4 21 0.01 0.01 0.01 1.0000 1.0000 1.0000 22 0. 0 C. 0 0. O NUS 166A RfVISE D 0286
NUS CORPORA TION AND SUBSIDIARIES STANDARD CALCULA TION SHEET CUENT: FILE NO.: sy Nh[- M. PAGE'gfop j
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/
CHECKED BY' I DATE-sWC m 1. ,p7 i Ob
) $ 5 $b0 h% L h f!bV l
1 EST. CASE - OC. 2000CFM SUPPLY, 222 CFM UNFILTERED INLEAKACE l ' 2 52. 1. 0 1. 0 3 2511 2.6E6 1.84E5 4 5.83E4
- 0. 0 0. 0 0. 0 1. 0 1. 0 5 7.2E3 2.SSE4 2.75ES 0. 0 8.64E4 3.456E5 2.592E6 6
7 8.1.157E-5 6806E-8 5. 6806E-3 8. 6806E-8 8. 6906E-8 8. 6806E-9 1.157E-5 1,157E-5 1.157E-5 1.157E-5 a 3. 0 1. 0 1. 0 9 1. o a. o
- 0. O 2.222E3 2.222E3 2.222E3 2.222E3 10 7.00E-4 6.45E-6 3.81E-6 1,45E-6 4.2SE-7 11 7.00E-4 6.45E-6 3.81E-6 12 1.45E-6 4.20E-7
- 0. 0 0. 0 0. 0 0. 0 0. 0 13 0. 0 0. 0 0. 0 0. 0 0. 0 14 0. 0 0. 0 0. 0 0. 0 0. 0 15 0. 0 0. 0 0. 0 16
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- 0. 0 0. 0 0. 0 0. 0 0. 0 20 0. 0 0. 0 0, 0 C. 0 21 0. 0 0.01 0,01 0.01 0.1099 0.10e9 22 0. 0 C. 0 0, 0 0.1099
$ M hs A YS &&W 1 ANSI EA SE - OC, 203 0CF4 SUSP L Y e 26 0 CFM UNFILTERED INLE AR AG E 2 52 1.0 1.0 1 2511 2.626 1 94E5 %.R3r4 4 00 0.3 3.3 10 10 2 75ES 0. 0 5 7 2E3 2.8 8E 4 8. 5 4 E 4 3.456ES 2.592[6 6 8.68 06 E-8 8 6A06E-8 8. 6 805 E -9 8.6806E-P 8 6806E-8 7 1 157E-5 1 157E-5 1 15f E -5 1 157E-5 1 15fE-5 8 1.0 1.0 1.0 1.0 10 ,
9 1 26E3 DE O 3E9 DEO DEO 10 7.0E-4 6.45E=6 3 81 E -6 1 45E-6 4 26E-7 11 7 00E-4 6.45E-6 3 81 E -6 1.45E-6 4.28E-T 12 0.J 0. 0 0 .0 00 0.0 13 0.0 0.0 0.0 0.0 00 14 0.0 0.0 1.0 0.0 0.0 15 0.0 0.0 0.0 0.0 0.0 16 00 00 J.0 0.0 0.0 17 0.0 3.0 3.0 0.0 0.0 19 0.0 1 812E-4 1 812 E -4 1.612E-4 1 812C-4 19 0.0 1 812E-4 1 812 E -4 1 812E-4 1 812E-4 21 0.0 1.812E-4 1. 812 E - 9 1.81 1.812E-4 21 J.01 0.31 3.01 1 0003 1.0000 22 0.0 0. 0 0.0 .
. 'N .
NuS 166A WSED 0286
NUS CORPORA TION AND SU2S/ DIARIES STANDARD CALCULA TION SHEET CUENT: FILE NO.- S SJECT b M-N g ,[l PAGE),[O$M
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so m zu ps;2.-m m . 1 AN51 C A SE = QC. 231"*F4 Suu L Y , P 'a ' Cvm UNFILilRED I NL E AK AG E 2 52 10 1.0
-3 2511 2 6E6 144 f 5 %.43E4 4 0.J 0. 0 J.) 1.0 1.0 2.75[5 0. C 5 f.2E3 2.4004 4.k4E4 3. 4 5 6E ' 2.592E6 6 8. 6 8 C 6 E- 6 8. 6 8 06 E-6 a. 6 801C -8 8 6 dC6E- 8 8.6 846C-8 7 1.157E-5 1.15 7 E- 5 1.15f E -% 1.157E-5 1 15FE-5 e 1.C 1. 0 1.0 10 10 9 0.C 2 26E3 2 24E3 2 26E3 2 26E3 10 7.0E-4 6.4 5E- 6 3.81~-6 1.45E-6 4.2dE-7 11 7.30E-4 6 45E*6 3.al .6 1 45E-6 4. 2 4F-7 12 0.0 0. 0 0.0 C.0 0.0 13 0.0 0. 0 1.0 0.0 0.C 14 0.J 0. 0 0.0 0.0 0.0 15 00 0.0 J .0 0.0 0.0 16 0.0 0.0 J.0 0.0 0.0 17 0.0 0.0 3.0 0.0 0.0 1s 0.0 00 00 0.0 00 19 0.0 0. 0 3.0 0.0 0.0 20 0.0 0. 0 0.0 9.8 0.0 21 0.01 3.01 1 01 0. 9 0 1239 0 1239 22 0.0 0.0 0.0 ,,
[ w eenn ; 2Hv %ss; 2 -r 12o ws i 21 EST. S2 CASE 1. 0
- OC. 2OOOCFM SUPPLY, 300 CFM UNFILTERED INLEAMAGE
- 1. 0 3 2S11 2.6E6 4
1.64ES S.53E4 O. O O. O O. O 1. O 1. O 2.7 DES 0. O S 7.PE3 2'90E4 5 64E4 3.456ES 6 2.592E6 7 8.6906E-9 1.157E-S B.6906E-B B.6806E-B B 6006E-6 8 6806E-B 1.IS7E-S 1.157E-S 1.157E-S 8 1 0 1.IS7E-S
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- 0. 0 0. 0 0. 0 0. 0 14 O. O
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- 0. 0 0. 0 00 00 20 00 0. 0 00 00 0. 0 0. 0 21 O 01 C. 01 0. 01 22 0. 0 0.1391 0.1391 0.1391
- 0. 0 00 NU$ 1MA RIVIMO O206
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- 0. 0 0. 0 0. 0 1 ANSI CASE - OC ,2000CFM SUPPLY. 260 CFM UNFILT. INLKO.. AUTD PRESS.
2 52 1. 0 1. 0 3 2511 2.6E6 1.84E5 5.03E4 4 0. 0 0. 0 0. 0 1. 0 1. 0 2.75E5 0. 0 5 7.2E3 2.88E4 8 64E4 3.456ES 2.592E6 6 7
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- 0. 0 0. 0 0. O NUS 1%$A REVISED 0286
NUS CORPORA TION AND SUBSIDIARIES STANDARD CALCULA TION SHEET
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gm(- w -o4 ('AL CU W g;f M t NUS CORPORATION INTERNAL CORRESPONDENCE i M-87-100 i TO: M. J. Giarratano
- l FROM: Dave Studley T d DATE: May 26, 1987
SUBJECT:
CECO, Control Room HVAC Upgrade,(546Y) Review of Bechtel's dose analysis inputs used in the original I:I D.3.4 habitability analysis A meeting in the Daseline was heldofattheBechtel's analysis office on S/21/87 to reconcile the di operator doses. ancies appear to be the cause of the variations in tM 1. The i.e. doX/Q's identified not include in the habitability the occupancy factors. studies are not the effective 2. The Gechtel model utilizes the volume of the c as well as the activity release rate. On the other hand, the NUS model containment activity and the activity release rate. utilizes The two different methods should result in identical doses provided the inputs are equivel . The of 1.6%Bechtel per perDresden da habitability study identifies a primary leak rate condenser complex.y of which 11.5 cfh per MSIV leaks thru the turbine NUS used a containment volume of 275,000 cf (as to a percent of activity released per second. identified in th However, the Bechtel calculation leakage useda rates containment volume of (the 158,000 158,000 cf for converting the cf assumes no mixir.g in the torus area). In addition, the Bechtel habitability studies identify a secondary containm leak rate leak containment of 100% per day; rate of 400% where per day. as their calculations utilized a exhaust rate of 4,000 cfm all of which is being ex smaller unmixed volume. The final dose analysis models will utilize Dresden and Quad Cities FSAR's.a secondary leak rate approach sim 3. For each leakage path, i.e. the stack or MSIV's, both Bechtel and NUS ran ) two separate and filtered models modes to ascertain the dose contribution from the unfiltered of operation. the 8 hour dose from a 30 day unfiltered mode.For the unfiltered mode, Bechtel This method is not ! conservative since it does not account for the dose contribution from l 1 placed in the isolation / pressurization mode.the residual acti
$1US 0,4 REWifED 0181 2
\ 6 Yhf W -667 l q ya cu h.( M-87-100 l May 26, 1987 Page 2 , 4. The Bechtel models used .a. control room volume of 58,000 cf and an intake rate in ofhabitability the 2,900 cfm, in lieu of the 132,000 cf and 2,000 cfm as identified studies. In their final analysis, Bechtel assumed that for the first 8 hours, the lower intake rate does not reduce the doses since the control room reaches equilibrium with the outdoors fairly rapidly and for the remaining 8 - 720 hours of the accidsnt. Bechtel manually corrected the doses using the Murphy /Campe methodology of calculating the iodine protection factor. (Note: This methodology shows 4 an increase in operator doses with the lower intake rate). 5. For the bypass leakage Bechtel's model included each of three volumes downstream of the primary containment where as the NUS model treated these volumes as one larger secondary volume. The Bechtel model utilizes a leak rate of 0.7667 cfm through the MSIV's and turbine stop valves l
.and a leak rate of 1.2 cfm from the condenser complex. Accounting for the multiple volumes will significantly reduce the doses due to the high hold-up times associated with these volumes (230 min. for one air change in the MSIV volume and 992 min. for one air change in the steam piping).
Taking credit for buildup of concentration in each volume significantly reduces the activity released during the fumigation conditions which coincides with the intake air being unfiltered. For the bypass leakage, the Bechtel factors, arethyroid doses at the control room intake, excluding occupancy as follows: 0 - 2 hrs 1.2 E-03 REM 2 - 8 hrs 1.2 E-01 REM 8 - 24 hrs 1.17 REM 24 - 96 hrs 30.7 REM 96 - 720 hrs 246 REM 6. At Dresden, Bechtel used a primary containment leak rate for the stack equal to the total integrated leak rate (1.6 %/ day) less the leakage thru the MSIV's (0.7%/ day), however for the Quad Cities analysis the MSIV leakage was not subtracted from the total integrated leak rate due to the lower leak rate (0.75%/ day). i DES /kc cc: K. Campbell R. Mychajliw h
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