ML20151X862

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Rev 1 to PM-1013, Min Containment Pressure Available
ML20151X862
Person / Time
Site: Peach Bottom  Constellation icon.png
Issue date: 06/22/1998
From:
PECO ENERGY CO., (FORMERLY PHILADELPHIA ELECTRIC
To:
Shared Package
ML20151X850 List:
References
PM-1013, PM-1013-R01, PM-1013-R1, NUDOCS 9809170278
Download: ML20151X862 (52)


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ENCLOSURE 2 Minimum Containment Pressure Available Analysis 9809170278 900911 PDR ADOCK 05000277 P-PDR

$3(S\\30 M I

EM ~ /N E;hibit NE-C-420-1, Rev. 2

1. Cal.culat on No.

Effectivo Date:

CALCULATION COVER SHEET

3. tInst(s) MI PECO Nuclear p pg Doctype 061 b

fe e sted 4.h/ECR/Other No.

b~ OO M~L S. Last Page Ho-

8. System / Topic No.: /#, d _ /4 O _ 3 Z_ 70 *. //e, fet 7.

Description:

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Structure: 2a)a u.<,0) rou, un eron; usy(e.s >> ks Component: LG) c#Mtt Record of Revisions

11. Vendor Calc.
12. Assumptions
13. Signatures No.
10. Description of Revision Number Rrev.

YES NO Preparer Rev2 ewer i Approver (s) / Date

9. Rev.

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14. Related Calculation No(s).

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Provides Info. To:

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i Receives Info. Front m M-M M

17. Total Pages-

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16. Pmvides Info. To:

(DS Info. Only) tJFSAR/ Tech. Spec./etc. :

'Effect'ive Date: 9/4/94 Exhibit NE-C-420-3, Rev. 1 Page 1 of 1 PORC No RAS /kmm SQR NO l

CALC. # 7/r/ -/C/_7 REV. /

50 9 o

RESP MGR YES DCD #

DATE:

CALCULATION REVIEW CHECKLIST YES or N/A MANUAL COMPUTER CALC.

CALC, X

X CALCULATION IS THE APPROPRIATE BASIS FOR THE ACTIVITY V#f X

X CALCULATION ASSUMPTIONS, CONSIDERATIONS, AND Y#c METHODOLOGY CONFORM TO APPLICABLE DESIGN REQUIREMENTS X

X SOURCES OF DATA AND FORMULAS WERE REVIEWED AND hT VERIFIED TO BE CORRECT AND COMPLETE l

X X

INPUT DATE IS CORRECT AND USED PROPERLY V'#r X

THE ANALYTICAL METHOD'USED IN THE CALCULATION HAS

'Yt?

BEEN CONSIDERED AND IS PROPER FOR THE INTENDED USE X

MATHEMATICAL ACCURACY HAS BEEN CHECKED AND IS CORRECT v45 (INDICATE METHOD USED)

A)

COMPLETE CHECK OF EACH COMPUTATION var 5"

'N/#

B)

SPOT CHECK OF SELECTED COMPUTATIONS C)

PERFORMANCE OF ALTERNATE OR APPROXIMATION N/o CALCULATION (ATTECHED)

X X

CALCULATION RESULTS WERE CHECKED AGAINST APPLICABLE V#f DESIGN CRITERIA AND WERE FOUND TO BE IN COMPLIANCE X

X EXISTING CALCULATIONS REQUIRING REVISION AS A RESULT V4k-

' ~

OF THIS CALCULATION HAVE BEEN IDENTIFIED & DOCUMENTED X

THE ANALYTICAL METHODS DESCRIBED IN THE COMPUTER N/A CALCULATION

SUMMARY

IS PROPER FOR THE INTENDED USE

.,lmIfVM X

X ALL SYSTEM AND TOPIC NUMBERS ASSOCIATED WITH THE CALCULATION ARE LISTED X

COMPUTATIONAL ACCURACY HAS BEEN CHECKED AND IS AMt CORRECT (INDICATE METHOD USED)

'T'NI A)

CHECK SAMPLE CALCULATION USING DATA OTHER THAN THAT USED IN THE SAMPLE Nd B)

PERFORMANCE OF ALTERNATE OR APPROXIMATION CALCULATION (ATTACHED) h,M C)

DESCRIBE OTHER METHOD USED:

X PROGRAM USED IS APPROPRIATE, INPUT IS VALID, AND

///d OUTPUT IS REASONABLE CONSIDERING THE INPUT

.ASE CALCULATION HAS BEEN REVIEWED AGAINST CURRENT Vf(

B X

X DRAWING REVISIONS AND POSTED DCDS TO IDENTIFY SIGNIFICANT DIFFERENCES The criteria listed above are the minimum criteria to be considered and are not intended to limit the initiative of the reviewer to consider other criteria.

Attributes applicable to manual and computer calculations are noted by an "X" in the appropriate column.

I List the documents used to support this review.

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CALC. NO.

Plui.1og 3 CALCULATION SHEET PAGE 2

PECO ENERGY NUCLEAR GROUP l

1.

Purpose / Objective The purpose of this calculation is to determine the minimum containment pressure available (MCPA) following a design basis large break loss of coolant accident (DBA LG-LOCA). This MCPA it. intended to be used by other alculations to demonstrate that there is sufficient ECCS pump net positive suction head (NPSH) margin.

PBAPS Units 2 & 3 are not committed to NRC Safety Guide 1.1, and have a' ways taken credit for containment overpressure. During NRC review and approval of the PBAPS FSAR, the NRC questioned the use of containment l

overpressure for the DBA LOCA event (Reference Question 6.3 of the PBAPS FSAR). In response to the NRC question, PBAPS provided a curve of the MCPA which showed a margin between the MCPA and the containment i

overpressure required for the ECCS pumps to maintain adequate NPSH. Assumptions used in the analysis and described in the text of the question response were chosen to minimize the margin.

l This calculation will document the re-analysis of the MCPA expected following a DBA LG LOCA using the results of the PBAPS Power Rerate containment analysis. In addition, a calculation of the MCPA following a DBA LG-LOCA during containment purge operation is also performed.

l Data provided by General Electric for the Post DBA LG-LOCA for the suppression pool temperature ended at approximately 12 hours1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br /> following initiation of the event. Temperatures are sufficiently elevated that credit for containment overpressure will be required for some time beyond this interval. This calculation will extrapolate the suppression pool temperature data provided by General Electric, to assist in determining the point where credit for l

containment overpressure is no longer required.

I At the end of the calculation, an assessment of the MCPA is performed for other events which require credit for containment overpressure.

ACCEPTANCE CRITERIA This calculation will determine the MCPA following a DBA LG-LOCA for use in other calculations to determine that adequate NPSH margin exists for the ECCS pumps. As such, there are no specific ac.eptance criteria for this calculation. The results should be presented in a format which facilitates the use in other calculations.

IMPACTSTA TEMENT This calculation and its results makes no impact on the following:

TRUE FALSE Station administrative and implementing procedures, including 2

O Surveillance Test procedures Station operating procedures O'

O Issued Design Basis Documents (DBDs)

O S*

Licensing documents (i.e., SAR) CM 1 E

O Existing calculations O

S' l

Explanation of checkmarks are as follows:

' This calculation does not depend on any specific operating procedure and supports the use of the plant Transient Response Implementation Program (TRIP) procedures, including use of containment sprays.

2.

Changes required to DBDs and existing calculations are addressed in AR Al110856.

l i

l.96-21453 BN6 CALC. NO.

PM-1013 CALCULATION SHEET PAGE:

3 PECO ENERGY NUCLEAR GROUP 2.

Summary of Results j

i The MCPA available for any ECCS pump NPSH following the DBA LG-LOCA is shown in the following figures.

I The peak MCPA value of 22.10 psia (7.41 psig ) coincides, as expected, with the time of peak suppression pool temperature of 205.7 DegF and peak licensing basis drywell pressure (post blowdown) of 29.60 psia.

With the DBA LG-LOCA occurring concurrent with containment purge, sufficient nitrogen is lost from the containment (1091 lbm) to reduce the peak MCPA value to 21.21 psia (6.52 psig ) and coincides, as expected, with j

the time of peak suppression pool temperature of 205.7 DegF and peak licensing basis drywell pressure (post l

blowdown) of 29.60 psia. This reduction is expected since it lowers the partial pressure contribution of the mtrogen due to the reduced mass, while the partial pressure of the water vapor remains unaff-:ted (a function of containment temperature only).

I During the "Other Events", it was determined that Station Blackout and Inadvertent SRV Opening did not require j

containment overpressure credit. The MCPA during the ATWS event was calculated to be 4.86 psig, and the MCPA I

during the FSSD event was calculated to be 5.73 psig.

l The extrapolation of the suppression pool temperature shows that the temperature is expected to be below 170*F at j

approximately 50.4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> following the beginning of the event.

- - _. -... _ -. - ~. -. - - -... _ _ -. -

. i 196 21453 B/M i

l CALC. NO.

PM-1013 i

i CALCULATION SHEET PAGE:

4 PEc0 ENERGY REVISION -

1 4

NUCLEAR GROUP i

i i

i PBAPS Units 2 as 3 HPSWTg WF g

M laisamma Costalansent Pressure Analysis Spray Rate.10,000 gpm DBA Lor,. Br..k LOCA

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l Constant Mass Leakage f.

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n.. n....i Figure 1 - Minimum Containment Pressure Available Following a DBA LOCA-No Conteinment Purge

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L96 21453'8/96 CALC. NO.

PM.1013 CALCULATION SHEET PAGE:

5 PECO ENERGY REVISION -

1 NUCLEAft GROUP a

PBAPS Units 2 as 3 wswT n.so r Mlaimaan Centelamment Pressure Aaslysis Spray Rate.10.00f5,pm 1

DBA Large Break LOCa y

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Figure 2 - Minimum Containment Pressure Available Following a DBA LOCA-Containment Purge in Progress

2143) 8/96 CALC. NO.

PM-1013 CALCULATION SHEET PAGE:

6 PECO ENERGY REVISION :

1 NUCLEAR GROUP Torus Water Temperature Response PBAPS DBA LG4.OCA 20 240 230 lPEco Emwapotamon l 210 N 's iso lGE Lee.g Term Neopense Date l j orop. amo. An so.4 nour. l 14e Toru.b ter Temperature (F) 120 110 100 so 0

8 12 is 24 30 36 42 48 64 60 j

Tin = (heur=>

j Figure 1 - Suppression Pool Temperature Extrapolation l

l I

m........ -.

't96 21433'8/96 -

C ALC. NO..

PM4013 CALCULATION SHEET PAGE:

7 PECO ENERGY NUCLEAR GROUP 3.

Design Input / Criteria C onstants -

Reference Patm 14.69598677 psia 6.L 7.480519481 gal /cuft 6.L R (Nitrogen) 55.2 ft-Ibf/tm *R 6.M To 459.67 *R 6.L inputs l

RMM UFubpray Flow rate 70,000 gpm 6.B.5.J.xiv RHR Hx Ueff 215.52 BTU /hr.sqft *F 6.B, 5.J.ix RHR Hx Area 5851 sqft 6.B.5.J.ix RHR Hx MTD Correction Factor 0.977 (unitiess) 6.B, S.J.ix HPSW Flow rate 4500 gpm 6.T HPSW Ternperature 90 *F 6.B. 5.J.viii Dryw el Wetw ell Altspace Volume 175,800 127,700 cuft 6.A, 5.J.i Initial Temperature 145 95 'F 6.B, S.J.iii Initial Pressure 0.00 0.00 psig 0*.."

Initial Relative Humidity 100 %

100 %

5.J.iv Initial Containtnent Purge 0 lbm N2 Containtnent Leakage (v/o) 0.5% per day 6.V 5.J.x In addition, the containment temperature (T ) and pressure (Po) used to calculate the constant mass leakage rate is t

95 F and 15 psig, respectively.

4.

Computer Calculation NA. Although this calculation uses the results of a GE computer run, and process all input values using a spreadsheet developed by the Originator, this calculation is treated as a manual calculation.

l l.

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t%2115I896 CALC. NO.

PM-1093 CALCULATION SHEET PAGE:

8 PECO ENERGY NUCLEAR GROUP 5.

Assumptions and Identified Facts The following assumptions are made in performing this calculation, all of which are conservative and none of which require any verification. In addition, various facts are identified for clarification.

5.A.

He event analyzed is the DBA LG-LOCA, which assumes a complete guillotine break of a recirculation pump suction line, ne event is modeled because it results in the hottest torus water temperature, compared to an intermediate or small line break.

5.B.

Reactor blowdown mass and energy release is not re-evaluated. Instead, the temperature profile of the torus water is used as the driving force for the evaluation. His is acceptable because the Rerate analysis that generated the profile included various conservative assumptions that tend to predict maximum pool temperatures, which is also conservative in our consideration of ECCS pump NPSH.

5.C.

Deleted.

5.D.

Containment spray is assumed initiated immediately after initiation of the event (time = 0 seconds). Cooling water flow to the heat exchanger is not initiated until 10 minutes after initiation of the event (time = $94.45 seconds). This is consistent with the GE analysis that generated the pool temperature profile.

5.E.

Deleted 5.F.

The " system" is considered quasi-steady state. This is conservative because the time of peak torus water temperature occurs hours after initiation of the event. The dynamics of the blowdown and mass / energy / momentum conservation are of significance only early in the event when things are happening rapidly. At the time of concern (peak pool temperature), things are happening relatively slowly.

5.G.

Heat removal from the containment is independent of the point of return of torus cooling water, i.e., whether returned directly to the torus or via containment sprays. This is consistent with statements made in the UFSAR for PBAPS. Thus use of sprays does not alter the torus water temperature profile as developed by GE.

5.H.

Time assumed for inhiation of sprays is early in the event such that the containment atmosphere is at the same temperature as the spray water. This also assumes that the sprays are 100% efficient and sufficient for the containment size. This assumption is conservative in that, if undersized or less eflicient, the containment atmosphere would be at a higher temperature than the sprays and thus the containment pressure would also be higher.

5.1.

As a quasi-steady state system, with the temperature profile already computed using the GE SHEX code, evaluation of containment environment parameters can be performed for any point in time irrespective of any prior (or later) point in time. No differential or integral equations are necessary.

5.J.

Values for input parameters are used which will tend to result in hot torus water temperatures and minimum containment pressures, in that order of preference. Following this guidance, the following inputs are used:

5.J.i.

The containment air volume, taken from PBAPS UFSAR Table 5.2.1, is assumed at the maximum values. This assumption, although resulting in a greater initial mass of non-condensibles (NCs), results in a smaller increase in pressure as a result ofincreasing containment pressure. This was confirmed by changing the input to the smaller containment values and confirming that the margin increased.

5.J.ii.

Initial containment pressure is assumed at 0.0 psig instead of 0.75 used in the maximum containment pressure analyses. This assumptions is consistent with the original MCPA analysis and results in less mass of NCs and thus smaller containment pressures.

5.J.iii. Initial containment temperature is assumed at the Tech. Spec. maximum allowables of 145*F in

' 196-21453 8/96 CALC. NO. -

PM-1013 CALCULATION SHEET PAGE:

9 PECO ENERGY REVISION :

1 NUCLEAR GROUP the drywell and 95'F in the torus. This assumption again results in less mass of NCs. This assumption is consistent with the licensing analyses, which assumed these values because they result in higher peak (short-term) containment temperatures and thus higher peak (short-term) containment pressures.

5.J.iv.

Initial containment airspace relative humidity of 100% for both the drywell and the torus. This assumption again results in less mass of NCs. The licensing analyses used a relative humidity in the drywell of 20%, giving more mass of NCs and thus (slightly) higher peak pressures.

5.J.v.

Deleted.

5.J.vi.

No credit is taken for generation and release of non-condensibles from the reactor vessel.

5.J.vii. Deleted.

5.J.viii. Service water temperature is assumed at 90 F, consistent with the current licensing analyses.

Although a lower temperature would result in lower containment pressure, it would also y ield lower torus water temperatures. The following sensitivity study confirms use of higher service water temperatures is conservative:

The existing analysis uses a service water temperature of 90 F and yielded a maximum pool temperature of 206 F for the 102% of i 10% of original power and 10,000 gpm RHR flowrate (non-PERFORM).

GE has provided PECO with a letter stating that a change in service water temperature of 5'F (increase to 95'F) conservatively would increase the peak pool temperature by NO GREATER THAN 5'F. The negative of this is thus also true, that a decrease in service water temperature of 5'F (to 85'F) will drop the peak pool temperature NO GREATER THAN 5 F.

At a hot inlet temperature of 206 F and a service water temperature of 90 F, the hot exit will be NO LESS THAN 183.4*F. With a decrease in service water temperature of 85'F, GE states that the peak pool temperature will be NO LESS THAN 201'F, and the hot exit will be NO LESS THAN 179.7'F. This decrease in spray temperature (and thus containment temperature) from 183.4'0F to 179.7'F results in a decrease in available overpressure from 21.90 psia to 21.19 psia, or 0.71 pri. However, the decrease in peak pool temperature also results in a decrease in required overpressure due to the drop of saturation pressure from 13.03 psia to 11.77 psia, or 1.26 psi. This confirms that hot service water is conservative, with respect for minimum containment pressure analysis, for the DBA LOCA event.

5.J.ix.

The RHR heat exchanger effective surface area used in determining the spray temperature is the same as the value used in the GE analysis for pool temperature heatup. This value is conservatively low and assumes 5% tubes plugged. Low values for this parameter result in higher pool temperatures, which is conservative, but also results in higher containment pressures, which is non-conservative. However, for the same change in this parameter, the net impact is that low values of this parameter are conservative for safety system NPSH concerns, and thus conservative for this analysis.

5.J.x.

Containment leakage is assumed at the rate of 0,5% per day by volume. Results of the analysis have indicated that this has a minor impact on available overpressure. It is also conservatively assumed that only the nitrogen leaks.

5.J.xi.

It is assumed that the drywell and wetwell airspace are connected by a large opening such that they are one volume. This is conservative since the wetwell pressure cannot become greater than the drywell pressure by any appreciable amount due to the vacuum breakers. This assumption results allows as i

much return of NCs to the drywell as is required to balance pressures.

i 5.J.xii. Deleted.

5.J.xiii. Deleted 5.J.xiv. PECO Calculation 11187-M-08 indicates a maximum spray flow rate of 9,350 gpm, instead of the 10,000 assumed in this calculation. The design basis flow required for torus cooling remains 10,000 gpm.

s Use of 9,350 gpm has little impact on the margin calentated herein (approximately 0.02 psid).

l l

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  • 142145$ 8/96 '

CALC. NO.

PM-1013 CALCULATION SHEET PAGE:

10 l

PECO ENERGY NUCLEAR GROUP 5.J.xv. Deleted l

6.

References 6.A PBAPS UFSAR Table 5.2.1 6.B NE-163 3 " Peach Bottom Power Rerate Project Engineering Report" 6.C PECO Calculation 18247-M 30 "RHR Pumps NPSH Post LOCA" 6.D PECO Calculation 18247 M-29 " Core Spray [ Pump) NPSil Post LOCA" 6.E PECO Calculation 18247-M-31 "IIPCI System NPSil Following a LOCA" 6.F PECO Calculation i8247-M 32 "RCIC System NPSH Following a LOCA "

6.G PECO Calculation PM-1010 "RiiR Pump NPSH" 6.H PECO Calculation PM-101I " Core Spray Pump NPSH" 6.1 Pump Curves M 1 U-283 through 286,293 through 296,419 through 426,430 through 437, and M-1-JJ.

49 6.J Drawing S-51 " Containment Vessels - Requirements" 6.K EAS 10-0289 " Peach Bottom Suppression Pool Drawdown" 6.L ASME Steam Tables (fifth edition) 6.M Crane Technical Paper No. 410 (25th printing) 6.N Hydraulic Institute Standards (13th edition) 6.0 Standards of the Tubular Exchanger Manufacturers Association (TEMA)(7th edition) 6.P Attachment I to PECO NCR 95-05708 "PBAPS Safe S/D Analysis" 6.Q PECO Calculation 18247-M-001 " Maximum Torus Temp. For The ECCS Syst."

6.R PECO Calculation PM 760 " Power Rerate Evaluation - SBO Analysis" 6.S NEDC-24380-P "PBAPS 2 & 3 Suppression Pool Temperature Response" 6.T M 1-DD-9 " Process Diagram RHR System" 6.U PECO Calculation 1Il87 EC-017-0101 " Pressure Drops Across the RHR and Core Spray Strainers" 6.V PECO Calculation 18247 M-24 Rev.4 (Containment Purge N2 loss) i i

d I

., mm 1

CALC. NO. '

PM 1013 CALCULATION SHEET PAGE:

11 PECO ENERGY I

NUCLEAR GROUP 7.

Calculation A simplified model of the PBAPS containment is used. Initial conditions are assumed that tend to durease the margin between the MCPA and the required OP for the DBA LG-LOCA analysis.

CONVERSION FACTORS AND CONSTANTS USED P

Conversion factor - psig to psia 14.6959 G

Conversion factor - U.S. gallons per cubic foot 1728 /231 R.

Ideal gas constant for nitrogen (ft-lbf/lbm *R) 55.2 To Conversion factor 'F to *R 459.67 l

INPUTPARAMETERSAND VARIABLES USED Note: A subscript "i" denotes the initial condition valu. for the variable.

t Time from initiation of th 2 event (seconds)

T (t)

Torus water temperature at time t (*F) 7 V

Volume (airspace) of the drywell (cuft) 175,800 4

V.

Volume (airspace) of the wetwell (cuft) 127,700 j

V Total containment volume (cuft)

P Atmospheric Pressure in the drywell(psig) 4 P.

Atmospheric Pressure in the wetwell (psig)

T Atmospheric Temperature in the drywell(*F) 4 T.

Atmospheric Temperature in the wetwell('F)

RH Relative Humidity of the drywell atmosphere (%)

4 RH, Relative Humidity of the wetwell atmosphere (%)

P,,,(T)

Saturation pressure of water for a given temperature (psia) l Pv4 Partial pressure of water vapor in the drywell airspace (psia)

Pv, Partial pressure of water vapor in the wetwell airspace (psia)

Pa Partial pressure of nitrogen in the drywell airspace (psia) 4 Pa, Partial pressure of nitrogen in the drywell airspace (psia)

Ma4 Mass of nitrogen in the drywell airspace (Ibm)

Ma, Mass of nitrogen in the wetwell airspace (Ibm)

Total mass of nitrogen in containment (lbm)

Ma i

Mp Total mass of nitrogen purged from containment during blowdown (Ibm)

Lv Volumetric leakage rate of nitrogen (% per day by volume) 0.5%

Lm Mass leakage rate of nitrogen (Ibm /sec)

Po Conservatively high pressure for computing Lm (psig) 15 To Conservatively low temperature for computing Lm (*F) 95 I

L

  • > 196-21433 8/96 CALC. NO.

PM-1013 CALCULATION SHEET PAGE:

12 PECO ENERGY REVISION :

1 g

NUCLEAR GROUP U

RilP i. cat exchanger overall coefficient of heat transfer (BTU /hr sqft *F) 216.52 A

RllR heat exchanger effective tube surface area (sqft) 5851 LMTD RilR heat exchanger log-mean temperature difference (*F)

F RiiR heat exchanger mean temperature difference correction factor (unitiess) 0.977 Qa R11R containment cooling flow rate through the heat exchanger (gpm) 10,000 Qs HPSW flow rate through the RHR heat exchanger (gpm) 4500 Ts HPSW coeling water temperature (*F) 90 Ms llPSW mass flow rate through the RHR heat exchanger (Ibm /sec)

Cps (Ts)

Specific heat at constant pressure for the HPSW (BTU /lbm *F) hin(Tn)

RHR mass flow rate through the RHR heat exchanger (Ibm /sec)

Cpn(Ta)

Specific heat at :onstant pressure for the RHR (BTU /lbm F)

P.

Total containment pressure (psig) vfT)

Specific volume of water at the given temperature (cuft/lbm)

EQUA TIONS USED -MCPA Constants V = V + V, Equation 1 s

144 * (P + P,,,)

  • Lv
  • V t

,m=

Equation 2 24

  • 3600
  • R,
  • T + To t

Gs Al = 60

  • G *v (7;)

s 9"'

f Initial Conditions 144 * (Ps, + P,,, - RH,

  • P,,,(Ts, ))
  • V s

s Afas' =

Equation 4 R,. * (T, + To) s 144 * (P, + P,,, - RH,,

  • P,,(T,, ))
  • V, Ala"' =

Equation 5 R, * (T,, + T )

o Afaj = Afa, + Afa.,

Equation 6 s

w

14211538N6 CALC. NO.

PM-1013 CALCULATION SHEET PAGE:

13 PECO ENERGY NUCLEAR GROUP Once initial conditions are determined, conditions at any subsequent time can be determined, independent of conditions since the initiation of the event. This is founded in the conservative assumption that the containment sprays are sized such that they can completely control the containment environment and the containment environment will be at the temperature of the sprays.

Given a time = t, and a torus water temperature for that time of Tr(t) as provided in Reference 6.B:

Ga Af = 60

  • G
  • v (T )

n f r We know the temperature of the hot and cold water entering the RHR heat exchanger, Thi, and Tei, respectively.

We need to determine the temperature of the hot water exiting the heat exchanger. We can either guess at a LMTD or use the LMTD determined for the previous time step, and use this as an initial value for LMTD, then iterate until exit temperatures and LMTD are consistent.

O 4

Th.

Thi Tc, Tc, i

V V

HX = Af

  • Cpa * (Th, - Th,)

a

= AI,

  • Cp3 * (Tc, - Tc,)

Equation 8

= U

  • A
  • LAfTD
  • F o

Although F is dependent on the results, it does not change significantly and a conservative value can be chosen as a constant. Thus the iteration is simple, guess a value for LMTDo, calculate the heat transferred, HX, then calculate the exit temperature for the hot side, Th. A value for the exit temperature of the cold side can also be calculated, but is not important in our analysis.

U

  • A
  • F
  • LAITDo Th, = Th' -

Af

  • Cpa a

Equation 9 U

  • A
  • F
  • LAfTDo Tc* = Tc' +

Af

s

where,

s196-21453 8M6 l

CALC. NO..

PM-1093 CALCULATION SHEET PAGE:

14 PECO ENERGY NUCLEAR GROUP LAfTD, = GTD-LTD

,GTD' In\\LTDs GTD = Th - Tc, Equation 10 LTD = Th, - Tc, Assuming the conta' ament spray capacity is oversized for the containment, the containme.it temperature will be that of the spray water, Th.. The sprays also ensure the atmosphere in the containment is saturated. Since we know the initial mass of nitrogen and the (constant) mass leakage of nitrogen, we can determine the atmospheric conditions in the containment.

Afa = Afa, - Lm

  • I-Alp Equation i1 Pv = P,,,(Th,)

Equation 12 Afa

  • R, * (Th, + T )

o Pa =

Equation 13 144

  • V AICPA = Pv + Pa - P,,

Equation 14 The above equations provide us with a conservative profile for the minimum containment pressure available following an evaluated event, such as the DBA LG-LOCA. The " forcing function" for this evaluation is the temperature profile for the torus water. Other events can be evaluated in similar fashion provided a temperature profile for the torus water is avail ble.

Computation of all parameters is simple and straightforward, given input values and using the above equations. A

- spreadsheet is used for the computations. Inputs to the spreadsheet are provided in Section 3 above. Sample calculations are provided below and confirm the spreadsheet results. Printout from the spreadsheet is provided as.

EQUA TIONS USED - SUPPRESSION POOL TEAfPERA TURE EXTRA POLA TION Afc (dT/dt) = Qs (t) - C(T-90) p

where, C = Heat Removal Rate of RHRHx (GE Number) 90 = HPSW Temperature Q4 (t) = Decay Heat + Pump Work l

. Q4 (t) = Q,e* + P

  • * '196-21'4$3 BN6 CALC. NO..

PM-1013 CALCULATION SHEET PAGE:

IS PECO ENERGY NUCLEAR GROUP Assume Q,e'*' >> P for t small i.e. P is considered negligible Mc (dT/dt) = Q,e* - C(T-90) p (dT/dt) + (C/Mc) T = (Q/Mc )e* + (90C/Mc) p (dT/dt) + y T = pe* + 90y where; y = (C/Me )

p p = (QgMc )

p i

Homogeneous Solution:

T = Ae'"

3 i

Particular Solution:

Tp = Be* + D Total Solution:

T(t) = Ae'" + Be* + D (dT/dt) = -yAe'" + ABe*

From this diffential equation:

(dT/dt) + yT = pe* + 90y

(-yAe'" - ABe*) + y (Ae'" + Be* + D) = pe* + 90y

-ABe* + yBe* + yD = pe* + 90y i

e* terms:

(y - 1)B = p or B = p/(y - A)

Constants: yD = 90y or D = 90 T(t) = Ae'" + [p/(y - A)]e* + 90 Sample Calculations CONSTANTS Vd 175,800 cut 1

=

127,700 cuft Vw

=

303,500.00 cuft 175,800 + 127,700 V

=

=

0.5% per day Lv

=

4

196-21.l5[8M6 CALC. NO.

PM 1013 CALCULATION SHEET PAGE:

16 PEOO ENERGY GEAR GROUP Pt 15 psig

=

i To 95 *F

=

Lm I44, *(l5+14.69598677)* 0.5%*303.500.00 =

0.00245 lbm/sec

=

,~

24*3600*55.2*(95+459.67)

Qs 4500 gpm

=

90 *F T,

=

0.016098759 cutVibm vn

=

622.7835 lbm/sec Ms 4500

-=

=

60*7.480519481*0.016098759 0.9980 BTU /lbm *F Cp,

=

INITIAL CONDITIONS Pd 0.00 psig

=

Td 145

  • F

=

RHd 100 %

=

144*(0.00+14.69598677-100%*Psat(145))* 175.800 =

8,657.191bm

Mad,

=

55.2*(145+459.67) 0.00 psig Pw

=

95

  • F Tw 100 %

RHw

=

8,336.611bm 144*(0.00+14.69598677100%*Psat(95)* 127.700 Mawi

=

=

55.2*(95+459.67) 16,993.80 lbm 8,657.19 + 8,336.61 Ma,

=

.=

TIMESTEPSAMPLE CALCULATION 18,045.52 seconds t

=

201.2 *F T

7 0.016645 cuft/lbm vf(TT)

=

1.00530 BTU /lbm *F Cp,

=

10.000

-1,338.5 lbm/sec Ma

=

60* 7.480519481 *G.016645 Thi 201.20 F

=

90.00 *F Tcl

=

Guess an LMTD, 78.77 *F LMTD,

=

180.66 *F 201.20 - 216.52 *S851

  • 0.977*

78.77 no

=

=

1,338.56

  • 1.00530
  • 3600

(

0%-2t453 BM6 CALC. NO. :

PM-1013 CALCULATION SHEET PAGE:

17 PECO ENERGY NUCLEAR GROUP J

90.00 +

216.52 '5851*

0.977

  • 78.77 Tco 134.46 'F

=

=

622.7835

  • 0.9980
  • 3600 1

l GTD 180.66 - 90.00 90.74 'F

=

=

LTD 201.20 -134.74 66.74 F

=

=

LMTD 90.74 66.74 78.09 F

=

=

In(

90.74

/

66.74 )

Comparison of LMTD with LMTDy,, shows that our original guess was appropriate. Our containment environment temperature is then no less than the spray temperature of 181.07'F.

l With the previously calculated nitrogen mass loss due to initial containment purge operations, with the assumed constant nitrogen mass loss due to leakage, we can calculate our nitrogen mass in the containment as, 0 lbm Mp

=

16,993.80 - 0.00245 I 8,045.52 - 0=

16,949.53 lbm Ma

=

13.7170 psia 16.949.53

  • 55.2
  • f I81.07 + 459.67 )

Pa

=

=

144

  • 303,500.00 7.6918 psia P,(Temp)

=

6.7128 psig 7.6918 +

l 3.7170 -

14.69598677 MCPA

=

=

SUPPRESSION POOL TEMPER. t TURE EXTRAPOIA TION Coefficients for the earlier equations will be xletermined now.

From GE supplied suppression pool temperamre profile:

t = 39,047.27 seconds T = 205.4'F i

i t = 43,377.02 seconds T = 204.7'F 2

2 t, = 45,533.77 seconds T = 204.3'F 3

l Note: These points were chosen arbitrarily, late in the event because that is the timeframe that we are interested in. Since temperature is changing slowly, a wider time span is used to get a little more AT and thus increased accuracy.

(dT/dt),

dT T, - Ti

=

=

dt t

t-t 2 i i

l i

l

(9 %21453 8/96 l

l CALC. NO..

PM-1013 CALCULATION SHEET PAGE:

18 PECO ENERGY i

NUCLE ~ R GROUP j

From the differential equation:

i

= Qo " - c(T - 90)

Me dl e

i r

l dt t i l

(dT/dt)2 si.I T, - T,

=

=

dt t2 t, - t2

)

= Qo "- c(T - 90)

Me,dT c

2 dt t2 Q = [Mcp(dT/dt) + c(T - 90)]e+*" = mie'"'

i Q = [Mcp(dT/dt)2 + c(T - 90)]e**" = m2e' #

2 where; mi and m2 are known from the data points I = (mi m2 )e* 40 (mi m2) " e * ""

/

/

or A(t - t ) = in(mi m2) or A. = In(mi m2) / (t - t )

/

/

2 i 2 i Finally; Q,=mie"'

and; A = [T 90 - Be'*"]e"

i Other Analyzed Events Other analyzed events that may require credit for containment overpressure are Station Blackout, ATWS, Fire Safe Shutdown (FSSD), and inadvenent Open Relief Valve (IORV). Design Basis Document P-T 12, Table T2.1-12 1 provides a list of events which require containment cooling mode of RHR. The IORV event is chosen to bound all anticipated operational occurrences and abnormal operational transients.

This section will assess the MCPA, how much overpressure credit is required (CPR), and ensure adequate margin exists. For each of these events, a time-dependent temperature profile for the torus water is not available. Instead, the peak torus water temperature is provided. Comparison of the minimum margin calculated for the DBA LG-LOCA and the margin at the peak torus water temperature indicates that the e num margin is less than the margin at the peak temperature by less than 1 percent. Therefore, to estimae minimum margin for these events, the margin at peak temperature will be calculated and conservatively reduceo ey 2%. If the time of the peak pool l.

temperature is unknown (for evaluating total nitrogen leakage), a conservative time of 28800 seconds will be used.

l STATIONBLACKOUT i

Peak torus water temperature for the PBAPS SBO event is calculated in PM-760 (Reference 6.R) as 161'F at 15300 seconds. Calculation 18247-M-001 (Reference 6.Q) provides torus water temperatures for each ECCS/RCIC pump above which containment overpressure credit is required. The peak torus water temperature calcul.ted for the SBO event (161'F) is well below temperatures where containment overpressure credit is required.

1 4 21'45I 8/96 CALC. NO.

PM-1013 CALCULATION SHEET PAGE:

19 PECO ENERGY l

NUCLEAR GROUP l

l Therefore, an evaluation of available containment pressure is not required for the SBO event.

ATWS l

l Peak torus water temperature for the PBAPS ATWS event is calculated in Reference 6.B as 188 F at 3300 seconds.

I Calculation 18247-M-001 provides torus water temperatures for each ECCS/RCIC pump above which containment l

overpressure credit is required. Since the peak torus water temperature for the ATWS event (188'F)is greater than l

the temperatures of 18247-M-001 (Reference 6.Q), containment overpressure credit is required.

Therefore, an evaluation of available containment pressure is required for the ATWS event.

l The analytical method used for the ATWS event analysis is identical to that used for the DBA LG-LOCA analysis, with the exception that time-based pool temperatures are not provided for the ATWS event, only peak pool temperatures. As explained above, a conservative margin reduction of 2% is used to account for any difference between margin at peak pool temperature and minimum margin.

The analysis is detailed on the following spreadsheet printout. The MCPA determined was 4.86 psig.

FSSD Peak torus water temperature for the PBAPS FSSD event is calculated in Reference 6.P as 206*F at 28800 second;.

Calculation 18247 M-001 (Reference 6.Q) provides torus water temperatures for each ECCS/RCIC pump above which containment overpressure credit is required. Since the peak torus w ater temperature for the FSSD event (206'F)is greater than the temperatures of 18247-M-001 (Reference 6.Q), containment overpressure credit is required.

Therefore, an evaluation of available containment prenure is required for the FSSD event.

Initial containment parameters are identical to those u.d in the DBA LG-LOCA analysis. Service water temperature for pool and spray cooling is assumed at 40 F. Because torus water cooling is not initiated for the FSSD event until long after initiation of the event, use of colder water has only minor impact on the peak pool tempecture, but has a significant impact on the spray temperature and hence, the MCPA. Use of 40 F service water temperature is conservative.

The analytical method used for the FSSD event analysis is identical to that used for the DBA LG-LOCA and ATWS analyses, with the exception that time-based pool temperatures are not provided for the FSSD event, only peak pool temperatures.

The analysis is detailed on the following spreadsheet printout. The MCPA determined was 5.73 psig..

IORY Peak torus water temperature for the PBAPS IORV event is calculated in NEDC-24380-P (Reference 6.S) as 172*F at 3790 seconds. Calculation 18247 M-001 (Reference 6.Q) provides torus water temperatures for each ECCS/RCIC pump above which containment overpressure credit is required. The peak torus water temperature calculated for the IORV event (172'F) is well below temperatures where containment overpressure credit is required.

l Therefore, an evaluation of available containment pressure is not required for the IORV event.

l

.I96 2l'4$3' 8.96 CALC, NO.

PM-1013 CALCULATION SHEET PAGE:

20 l

PECO ENERGY REVISION.

1 NUCLEAR GROUP l

The results of these evaluations are as follows:

I inputs Veek rooi tiedw l

Temp.

Time Temp.

RHR Ficw Event

(*F)

(seconds)

(*F)

(gpm)

SB0 ist 15300-10.000 ATWS its 3300 90 10,000 FSSD 206 28800 40 10,000 SORV 172 3790 90 10,000 A I VV5 M80 TU,yWApp 60m 6UP F55 't dMa/dt 0.002453 lbm/:ec TSW 90 *F t

3300 sece LMTDo 69.43963 *F Ma(t) 18985.70f Ibm Tho 170.3198 'F Tco 128.4f 06 *F Or 10,000 gpm Os 4,500 gpm GTD 80.31983 *F TSP 188 *F TSW 90 *F LTD 59.58938 'F Psat(TSP) 8.9448678 psia Psat(TSP) 0.698f27 psia LMTD 69.4J963 *F Density 60.389019 lbm/cuft Densdy 62.11659 lbm/cuft T

170.3f 98 *F Cpf f.0036129 BTUAbm*F Cpf 0.99802 BTU /lbm*F Py 6.036849 psia Mr 1345.4729 lbm/see Ms

$22.7835 lbm/sec Pa f3.51559 psia MGPA 4.550 psig

~~

l tsuu uso is,yvapo som ide zon t j

dMaldt 0.002453 lbm/sec TSW 40 *F i

I t

28400 secs LMTDo f17.8559 *F Ma(t) 16923.140 lbm Tho 175.8499 *F Tco 104.4744 *F Or 10,000 gom Os 4,500 gpm GTD 135.8499 *F TSP 206 *F TSW 40 *F LTD 101.5258 *F Psat(TSP) 13.03f183 psia Psat(TSP) 0.12f 634 psia LMTD f f 7.8551 *F Density 59.962187 lbm/cuft Density 62.426f Ibm /cuft T

175.8499 *F Cpf f.0059784 BTUllbm*F Cpf f.004f26 BTUnbm*F PV 6.845799 psia Mr 1335.96Jf Ibm /sec Ms

$25.8867 lbm/sec Pa 13.58402 psia MUPA 5.7J4 psig l

l l

i t

l P

1

4 2ias3ioe OALC. NO..

PM-1013 CALCULATION SHEE PAGE:

21 PECO ENERGY REVISION :

1 NUCt. EAR GROUP 8.

Attachments 8.A Spreadsheet Printout for the MCPA following a DBA LOCA, without containment purge,14 pages, beginning on the next page.

l i

l.

i e

I

~~ _

m._

-m x. -

.-. - - - - - ~ -

~~--~m.-----mm-

-~m

-u-

_ _ ~.

_m m.

[T om e.

hO

$l

=O g !

ono.nM mmeenu,,-

Tune Tune SP Temp DW Pronoun Psat VI Mass flow Cp Tru

.To LMTD Ino Ta>

GTO LTD LMTD O

5 :

(seconds)

(hours)

(*F)

(pein)

(psi JAtwn)

C.=_)

(BTUAtwn T) (F)

(T)

(*F)

(T)

("F)

(*F)

(*F)

(*F)

{

Z AGO 0.0000 SEO fE45 0.4.

0.0f0ff4 f,302.87 490809 95.40 95.00 0.00 96.00 30.80 5.00 SD SAD C

t N

i 4 28 Ref37 f38.3 47.5f 2.825,6 0.016278 f,388.92 0.90033 f36.30 f36.30 0.00 f38.30 90.00 48.30 RSS

&OS N

f i

70.39 Ref98 139.0 47AB 2.81500 RefS208 f,307.88 0.90NS f39.00 f 39.00 0.00 139.00 30.00 4 00

&Of Om 88.08 0.0239 f3E4 47.25 1 84409 0.016290 f,3ST.70 E90960 f39.40 f3940 0.00 f39AS 90.00 49.40 SOS ROS C

18ESS S0297 f3&S MN 2.87435 0.016292 f,387.54 0.90082 f30.80 130.80 0.00 f 39.80 90.00 MSO E80 ASS f

j j

f3f.33 0.0905 f4R3 415*

19ff54 0.016295 f,3ST.34 R30055 f40.30 f40.30 ROS f40.30 90.00 50.30 8.80 R00 t

i 156.20 0.0434 f40.8 4E93 1Nef4 &Of6297 f,387.f3 E90058 140.80 140.80 0.00 f40.80 90.00 50m 0.80 ROO fif.33 RO5W f4f.2 4Ef9 2.9795f Ref8299 f,308.97 E90900 fdf.20 141.20

&OS f4f.20 S&OO Sf.20 RSS 0.00 205.70 S057f f4f.4 44 4 2.9N00 0.0f8300 f,306.89 0.900Sf f4fA0 f4fA0 0.00 f4fA0 90.00 SfA0 0.00 0.00 23R20 A8639 f4f.5 diep 3A0248 0.016300 f,388.85 R30082 141.50 f4f.50 RSS f4f.50 S&OS 5f.80 ROS 0.80 25545 0.07f0 14f.8 410f 3.0f0f5 Ref830f f,306.8f R.~0083 f4f.00 f4f.00 0.00 fdf 80 30.00 5f.80 ade ROO 20R70 a0780 f41.8 42.18 10f0f5 0.0f830f f,306.Sf 0.90083 f4f.80 141.00 0.00 f4f.00 90.00 5f.00 0.00 0.00 305.95 0.0050 f4f.7 of.54 10f785 RefS30f f,308.77 0.90083 f4f.70 f41.70 0.00 f41.70 90.00 5f.70 0.00 SAO 33f.08 SO920 14f.7 40.77 1 01785 0.01630f f,308.7T 0.90083 fdf.70 14f.70 0.00 f4f.70 90.00 6f.70 0.00 0.00 358.58 RSSSO f4f.7 40.f0 10f785 0.0fS30f f,308.77 0.90083 14f.70 f4f.70 0.00 f41.70 90.00 Sf.70 0.00 SE h

J9f.58 af080 94f.8 39.4f 1 92557 A0f8302 f,308.73 0.90984 fdf.80 14f.80 ROO f4f.80 30.00 5f.80 0.00 ROS 40E83 Eff30 f4f.8 36.7f 1 02557 Ref8302 f,308.73 0.99984 f4f 80 f41.80 0.00 fdf.80 90.00 5f.80 0.00 ROS 43f.83 Af200 141.8 36.14 1 02557 0.0f8302 f,388.73 0.00084 f4f.80 f4f.80 0.00 14f.80 30.00 Sf.80 0.00 0.00 45f 33 0.f254 f4f.9 3130 3.03330 0.0fS302 f,306.09 0.99984 f41.90 f4f 90 0.00 f41.90 90.00 5f.90 0.00 0 00 I

47189 0.f3f4 142.f 27.42 194083 RefS303 f,308.8f 0.90006 fd2.f0 14110 0.00 f42.10 90.00 52.f0 0.00 0.00 i

40E83 af377 f42.5 25.39 3.10308 OAFS 307 f,306.32

&99070 f42.80 f42.80 dop f42.80 90.00 52.80 0.00 ade i

52R83 0.f447 f419 24.43 Af9f58 0.014312 f,305.87 R90078 14190 f4190 0.00 f43.90 90.00 5190 AGO 0.00

{

54E08 0.f8f4 f4E2 2198 1298f8 0.0f63f8 f,385.33 0.90005 145.20 f45.20 0.00 f4E20 90.00 55.20 GM 0.00 500.78 af583 f48.5 2187 1 40780 0.0f6325 f,3Sd79 0.90003 f48.50 fM50 0.00 f4 Esp Stop 56.50 0.00 0 00 594AS 0.f851 147.8 21 4 182049 0.016331 f,384.26 f.8000f f47.80 90.00 40.99 f37A7 ff187 3113 47.47 40.99 i

808.28 Af85f f50.6 214f 1 7'800 0.0fS346 f,38100 f.00020 f50.80 90.00 42.97 f39.78 ff177 36.83 49.76 42.97

[

80E28 0.2237 1519 2140 4.09250 0.016383 f,30f.83 f.00043 15190 90.00 4E3f f4148 ff5.08 38.84 52AS 45.3f l

978.39 A27f2 f58.5 2150 4 35921 0.0f8378 f,300AD f.00062 fE50 30.00 47.f5 fMSS ffEOS 4042 5450 47.f5 f,f 55.f 4 0.3208 f58.9 2151 48f832 0.0f8389 f,35043 f.000Sf f58.00 90.00 48.85 f4E58 ff7.02 41.88 ESS 48.85 f,33&Of 0.37ff 181.0 2151 4 85000 0.0f840f f,358AS f.00097 fSt.00 30.00 50.34 f48.27 ff7.84 4116 58.27 50.34 f,520.39 OA223 783A 2153 5.09f08 0.0164f2 f,357.57 f.00ff4 f83.00 90.00 5f.75 f49.9f f f 8.83 ' 4437 59.9f 5f.75 f,70f.5f R4728 1848 2155 E3fff9 RefS422 f,358.75 f.00f29 f8480 90.00 5103 f5f.30 ff9.33 45A7 Sf.38 53E

?

f,808.f4 0.5245 108.5 2158 5.52838 0.Of643f f,355.98 f.00143 18E50 90.00 5423 f52.T7 f20.00 4 50 8177 5423 h

2,07489 A57M feto 218f 5.72232 Sof8440 f,35E28 f.00f56 18E00 90.00 55.29 f5400 f2&58 47.42 84.00 5E29

[

2,258.89 0.8289 100.4 2167 E9fedd 0.0f8448 f,354.80 f.00f89 180A0 90.00 56.28 155.f4 f2f.f3 48.27 Kf4 58.28 i

2,440.89 R$780 f70.7 2174 S.00978 0.0f8455 f,35199 f.00f81 170.70 90.00 57.20 f58.20 f2f.84 4 08 88 20 57.20 2,82128 R7284 f7f.9 2182 E29032 0.016482 f,35142 f.00f92 f7f.90 90.00 58.05 f57.f8 1211f 49.79 87.f8 58.05 f

2,005.78 A7802 f710 2188 E4f823 0.0f8488 f,352.80 f.00202 173.00 90.00 RS3 f58.08 f2154 SOAS 88.08 58.83 l

2,995.f4 RS320 f740 23.90 S.58583 0.0f8474 f,352.4f f.00212 f7400 90.00 50 54 f58.90 f22.93 5fA7 88.90 59.54

% T O h

[

f 3 f 77.38 E8828 175.0 2406 8.71508 0.0fS400 f,35f.93 f.00222 175.00 90.00 80.24 f59.7f f2132 5f.88 89.7f 80.24 i

3,55f.78 0.9006 176.8 2422 E99355 0.0f8af 1,35fA8 f.00240 fit.80 90.00 St.52 18f.ft 12403 52.77 79.18 Cf.52

~

I 3.385.28 0.9348 f75.9 2417 8.85352 RefodSS f,35f.50 f.0023f f7E90 90 00 80 88 180.45 f21e8 52.22 70A5 80.88 5 m O f

f 3,736.84 f.0300 177.8 2432 7.f2002 0A18498 f,350.87 f.00248 f77.00 90.00 82.08 18f.84 f24.34 5128 Tf.84 8108 3,92f.76 f.00N 178.4 244f 7.2404f 0.018500 f,350.28 f.00256 179 40 90.00 82.85 182A9 f2 DSS 51T4 T2AS S185 f

4 f06.5f f.f407 f79.1 2447 7.36234 40f8505 f,349.t3 f.00283 f 7910 90.00 83.15 f8108 f2493 54f7 7106 83.f5

<ma

,.,m fnA un 7.m77

  1. A,aa f.3a.=

,mm

,nm aa au fau fan ua ran au 447189 f.2427 f8R5 248f 1.5047f SOf85f3 f.340.24 f.00278 f80.50 90 00 84.f4 f8&20 f25.48 5102 7420 84f4 4 858.28 f.2934 18f.f 2400 7.00817 0.0185f7 f,3a.95 f.00284 181.f0 90.00 8458 18400 125.7f 55.39 TASS 84.58 d

Y l

483Ef4 f.3434 f8f.7 247s 7.79875

&#f8520 f,3ds.85 f.00291 18f.70 S&oo

$498 fSaf8 f25.95 5E75 7118 84.98 h

5.021a f.m2

,n2 x86 7n51f amn3

,.uta

,am fn=

um au

,8En snu na rem au g

i 0

h l

l

,[

.i

,~-

hT om 1-b b.

= O g,
c.,,.=

Twns Tame Temp Pv Ma Pa MCPA DWPressur Qy m)

<n=r=>

m o==>

ot=n>

o=.)

o-a) o=a) oZ 0.00 0.0000 K00 2.7908 f488180 1f.9054 0.0000 0.754d Q

49.28 0.0f37 138.30 2.8252 18,901 88 12.79f7 0.7209 318f4d 70.39 0.0f98 139.00 2.8157 ft90182 12.8497 0.9894 32.7840 h

KOS 0.0239 f39.49 2.8449 18,99158 f2.8582 f 007f 32.5540 10&89 0.0297 f39.80 1 8744 1899153 f2.8888 f.045f 32.2440 f

f 13f.33 0.0385 f40.30 19ff5 18,99147 12.8774 f.0930 3f.8340 f58.20 0.0434 f40.80 1 9491 f8,99141 f2.8881 f.f4f3 3f.2340 f8f.33 0.0504 f41.20 2.9795 18.99135 f2.8987 f.f802 3& 4940 205.70 0.057f f4f.40 2.9948 18,90129 f19009 f.ft97 29.7940 2$&20 0.0839 f4f.50 10025 fL99123 f2.9030 f.2005 28.9940 255.45 0.0Tf0 f4f.80 10f0f 18,991f7 fl906f f.2193 28.3140 200.70 0.0780 14f.00 10f0f ft991ff 12.906f f.2f92 27.484d 305.95 0.0050 14f.70 10f79 18,99105 119072 f.2290 - 21844d 33f.00 0.0920 f4f.70 10f79 18,992.98 f2.907f f.2290 28.074d p

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RHN Heat Exctange, Onginal Trne Tyne SP Ternp DW Pressure Prat Vf Mass Fkm Cp TN Tca LMTD Tho Tco GTO LTD LMID Qg

(=~ 48)

(hours)

(F)

(psia)

(psia)

(cufUtbm)

(Ibtn/sec) (BTIMtwn *F)

(F)

PF)

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OZ Qy 5,20L89 t.4461 182.8 24.94 7.98960 0.016527 1,348.10 1.00303 182.80 90.00 6L76 166.06 126.38 SL42 TLOS 6576 5,392.51 1.4979 18L3 2501 8.07793 0.016530 1,347.85 1.00306 183.30 90.00 66.12 166.49 126.57 56.13 78.49 66.12 I

5,571.01 1.5475 1818 2509 Lt0687 0.016533 1,347.60 1.00314 18180 90.00 66.47 166.89 12L77 57.03 76.89 66.47 5,751.84 1.5977 184.3 2116 8.25683 0.016536 1,347.35 1.00319 184.30 90.00 86.82 167.30 126.96 57.34 77.30 6682 b

5,931.78 f.6477 1848 2123 8.34722 0016539 1,347.10 1.00325 184 80 90.00 67.18 167.71 127.16 57.64 77.71 67.18 6,11L76 1.6985 1812 2L29 8.42028 0016542 1,346.89 1.00329 18120 90.00 67.46 168.04 127.32 57.88 78 04 67.46 0,297.76 1.7494 185.6 2L36 8.49388 0.016544 1,346.69 1.00334 185.60 90.00 67.74 168.36 12L47 58.13 78.36 67.14 6,47514 1.7906 1861 2L43 8.58663 0.016547 1,346.44 1.00339 186.10 90.00 68.10 168.77 127.67 58.43 TL77 6L t0 8,65214 1.8478 1865 2549 8.66145 G016550 1,346.24 1.00344 188.50 90.00 68.38 169.10 127.82 58.68 79.10 68.38 6,830.89 f.8975 166.8 2556 8.71791 0 016552 t,346.09 1.00347 186.80 90.00 88.59 16L34 127.94 58.86 7734 68.59 7,001.51 1.9449 187.2 2563 8.79368 0.016554 t,34588 1.00352 187.20 90.00 68.87 16t67 128.10 5K10 7767 68.87 7,177.89 f.9939 187.6 2169 8.87000 0.016557 1,34568 1.00357 187.60 90.00 69.16 16K99 128.25 59.35 11.99 6716 7,356.76 2.0435 187.9 25.75 L92780 0.016559 1,34L52 1.00360 187.90 90.00 69.37 170.24 128.37 5753 80.24 69.37 7,53676 20931 188.3 2581 A00409 0016561 1,34532 1.00365 188.30 90.00 6765 170.56 128.53 59.77 80.56 6785 f

7,713.51 2.1428

,88.3 2K87 9.06322 0016563 t,345.17 1.00368 188.60 90.00 69.86 170.81 128.65 59 95 80 $1 6tS6 7,89G51 2.1918 18L9 2193 9.12186

  1. 016565 t,34501 1.00372 188.90 90.00 70.06 171.05 128.76 60.14 81.05 70.08 8,069.14 2.2414 199.3 2598 9.20055 0.016567 t,34481 1.00377 189.30 90.00 70.36 171.38 128.92 60.38 81.38 70.36 3,241.14 2.2892b 1896 26.04 9.25994 0016569 1,34465 1.003a0 18760 90.00 70.57 171.62 12%04 60.56 81.62 70.51 8,41&39 2.3373 189.9 2609 9.31965 0016571 t,344.50 1.00384 18%90 90.00 70.78 111.87 129.15 60.75 81.87 7078 V

8,592.64 2.3808 190.2 26 18 9.37968 0.016573 1,344.35 1.00387 190.20 90.00 11.00 172.11 129.27 60.93 82.11 11.00 8,761.76 2.4338 190.4 26.23 K41968 0.016574 t,344.24 1.00390 190.40 90.00 71.14 172.28 129.35 61.05 3128 71.14 8,874 26 2.4651 190.6 26.27 9.46022 0.016576 1,34Ltd 1.00392 190.60 90.00 71.28 172.44 129.43 61.17 8244 71.28

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8,966.76 2.4963 190.C 26.30 K50071 A016577 1,34404 1.00395 190.80 90.00 71.42 172.60 12951 61.29 82.60 71.42 9,09t26 2.5276 191.0 26.34 9.54134 0.016578 1,34193 1.00397 191.00 90.00 71.56 172.77 12K58 61.42 8277 11.56 0,211.76 25588 191.2 26 2 9.58211 0.018580 1,34183 1.00400 191.20 90.00 71.70 172.93 12766 61.54 82.93 71.70 9,32426 2.5901 191.3 26.41 160256 0.016580 1,34178 1,00401 191.30 90.00 71.77 173.01 129.70 61.60 8101 71.77 9,436 78 28213 191.5 2645 9643:5 0.016581 t,343.67 1.00403 191.50 90.00 71.91 173.17 129.78 61.72 8117 11.91 h

9,54t26 2.6526 191.7 26.48 768469 0016583 t,34157 1.00406 191.70 90.00 72,06 173.34 12786 61.84 8134 72.33 9,661.78 26838 191.9 26.52 772596 0.016:34 t,343.47 1,00408 191.90 90.00 72.20 17150 12794 61.96 8150 72.20 9,774.26 17151 1910 26.56 9,74667 0.016585 1,34142 1.00409 192.00 90.00 72 27 173.58 129.98 6202 8158 72.27 9,886.78 17463 1922 2t59 9.78618 0.016586 1,3413i 1.06612 192.20 90.00 12.41 173.74 130.05 6215 8174 72.41 9,999.26 1 7776 192.4 26.83 K82964 c.016587 1,343.21 1.0M14 192.40 90.00 72,55 17191 130.13 62.27 819f T2.55 10,111.77 28068 192.6 2tCT 787164 A0165?9 1,343.10 1.00417 192.60 90.00 72.69 174.07 130.21 62.39 8 LOT 72.69 10,224 27 28401 1927 26.70

&89260 0.016589 1,343.05 1.00418 192.72 90.00 7276 17415 130.25 62.45 8415 72.76 10,342.89 2.8730 192.9 26.75 9.93462 0.016590 1,342.95 1.00420 192.90 90.00 72.90 17431 130.33 62.57 8431 72.90 10,45139 19043 1911 26.79 K97679 0.016592 1,342.84 1.00423 193.10 90.00 7105 174.48 130.41 6269 8448 7105 10,567.89 2.9355 1912 26.82 9.99794 0.016592 1,342.75 1.00424 193.20 90.00 7112 17456 130.44 62.76 8456 Tiff 10,800.39

19663, 1314 26.85 10.04033 0.016594 1,342.69 t.00427 19140 90.00 7126 174.72 130.52 6288 8472 73.26 ff 10,792.89 2.9960 193.6 2t89 10.00288 0.016595 1,342.58 1.00429 19160 90.00 7140 17L88 130.00 63.00 8488 73.40 10,90L39 1 0293 193.7 26.92 10.10421 0.016596 1,342 53 1.00430 193.70 90.00 13.47 17497 130.64 63.06 8497 7147 g g r-11,017.89 10605 1919 26.95 10.14699 0.016597 1,34143 f.00433 19190 90.00 7161 17113 130.72 6118 8113 7161 y m O 11,142.64 10952 194.1 27.01 10.18991 0.016598 1,34L32 1.00436 19410 90.00 73.75 175.29 130.80 6130 8529 73.75 g'

z 11,262.39 11284 19&2 27.04 10.21143 0.016599 1,34L27 1.00437 19& 20 90.00 7182 17L37 130.84 6136 BL37 73.82 z

Q 11,377.77 3.1605 1964 27.07 10.25458 0.016600 1,34L17 1.00439 19440 90.00 73.96 11L54 130.91 6149 8554 7196 11,490.14 11917 1945 27.11 10.27621 0.016601 1,34111 1.00441 19450 90.00 7404 17562 130.95 6155 8562 7403

(

11,609.77 12249 19&T 27.16 10.31959 0.016602 1,342.01 1.00443 19470 90.00 74.18 17L78 131.03 6MT 8578 14.18 11.76% 77 3.2674 1949 27.19 10.36312 0.016603 1,341.90 1.00446 19490 90.00 74.32 17594 131.11 63.79 8L94 74.32 a

11,88t14 3.3025 1951 27.22 1&40681 0.016605 t,341.80 1.00448 19510 90.00 7446 17611 131.19 6191 86.11 7446 h

g 12.042.02 13450 1953 27.27 10.45065 0.016606 1,341.69 1.00451 19130 90.00 TK60 176.27 131.27 6403 86.27 74 60 e

12,195.52 3.3876 1955 27.32 10.49464 0.016607 1,341.59 1.00453 19550 90.00 7tT4 176.43 131.34 6416 86.43 74.74 w

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PM.9013 CALCULATION SHEET PAGE:

36 PECO ENERGY REVISION :

1 NUCLEAR GROUP 8.D Spreadsheet Printout for the MCPA following a DBA LOCA, with containment purge,14 pages, beginning on

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I the next page.

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356.58 0A990 141.7 40.10 301785 0.016301 1,366.77 0.99963 141.70 141.70 QA0 141.70 90.00 61.70 0.00 0.00 381.58 0.1060 141.8 39.41 3.02557 OA16302 1,36L73 0.99964 141.80 141.80 0.00 141.80 90.00 51.80 0.00 000 406.83 0.1130 141.8 38.71 1 02557 0.016302 1,366.73 0.99964 141.80 141.80 0 00 141.80 90.00 51.80 ROO 0.00 431.83 0.1200 141.8 38.14 102557 0016302 1,36L73 0.99964 141.80 141.80 0 00 141.80 90.00 51.80 0 00 0.00 451.33 0.1254 141.9 32.30 103330 0.016302 1,368.69 0.99964 141.90 141.90 0.00 141.90 90.00 51.90 0.00 0.00 f

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7,53L76 2D935 188.3 2181 7004S9 0.018561 1,34532 1.00365 188.30 90.00 69.65 170.56 128.53 5t77 80.56 6765 f

7,71151 2.1426 188.6 2187 9D6322 OD16563 1,34517 1D0368 188.60 90.00 69 86 170.81 128.65 5795 8&B1 6tB6 7,890.51 2.1918 188.9 2L93

  1. 12186 OD16565 1,34501 1.00372 188.90 90.00 70.08 171.05 128.76 60.14 81D5 70.06 8.06t14 12414 1873 2196 9.20055 0.016567 1,34& 81 1.00377 18t30 90.00 70.36 171.38 128.92 60.38 81.38 70.36 8,24t.14 2.2892 1876 26.04 K25994 6016549 1,34465 1.00380 18760 90 00 10.57 17tA2 12704 60.56 81A2 70.57 8,414.39 13373 1879 26.09 731965 6016571 1,14 & 50 tD0384 18790 90.00 70 78 171.87 12L15 60.75 8127 70.78 C

1 8,592.64 2.3868 190.2 26.18 737968 0.016573 1,34435 1.00387 19020 90.00 11.00 172.11 12727 6&93 82.11 71.00 8.76116 2.4338 190 4 26.23 9.41988 6016574 1,344.24 1.00390 190.40 90.00 71.14 172.28 129.35 61 05 82.28 71.14 8,87426 2.465t g 190.6 26.27 746022 0 01C576 1,34414 1.00392 190.60 90.00 71.28 172.44 12%43 61.17 8244 71.28

~~~

8.96L76 24963 190.8 26.30

  1. 50011 0016577 1,34& 04 1.00395 190.80 90D0 11.42 17160 12tSt 6119 8160 71.42 9.09t26 2.5276 191.0 26.34 754134 0216578 1,34193 1.00397 191.00 90.00 71.56 17177 12tS8 61.42 82.77 71.56 9,21126 15588 191.2 2L37 9.58211 0.016580 1,34183 1.00400 191.20 90.00 11.70 172.93 12te6 61.54 82.93 71.70 9,32& 26 2.5901 191.3 26.41 9 60256 0.016580 1.34178 1.00401 191.30 90D0 71.77 17101 12910 6tA0 8101 71.77 9.436.76 2.6213 191.5 26.45 9.64355 0.016581 1,34167 1.00403 191.50 90.00 71.91 173.17 129.78 61.72 8117 71.91 9.54926 18526 1911 26.48

%68469 6016583 1,34157 1.00406 19110 90D0 72 06 17134 12186 61.84 8134 7106 9.56116 16838 191.9 26.52 9.72598 0 016584 1,343.47 1.00408 191.90 90.00 72.20 17150 129.94 61.96 81M 12.20 9.77A26 27151 192D 26.56 9.74667 6016585 1,34142 1.00409 192.00 90.00 72.27 173.58 129.97 6203 8158 72.27 9.88L76 2.1463 1912 26.59 918818 0.015586 1,34131 1.00412 19L20 90.00 72.41 173.14 130D5 62.15 8174 72.41

\\

9,99t26 17776 192.4 26.63 9.82964 0D16587 1,34121 1D0414 19140 90.00 72.55 17191 130.13 62.27 83.91 72.55 10,111.77 2.8068 192.6 26A7 781164 OD19589 1,34110 1D0417 19260 90D0 72.69 17407 13& 21 62.39 84 07 7769 10,22427 2.8401 192.7 26.70 9.89260 0016589 1,34105 1.00418 19210 90.00 72.76 17&ts 130.25 62.45 8415 72.76 10,34289 2.8730 192.9 2L75 9.93462 6016590 1,34295 1.00420 19290 90.00 72.90 174.31 130.33 62.57 8431 7190 10,45139 2.9043 193.1 26.79 9.97679 0016592 t,342.84 1.00423 19110 90.00 73.05 17t48 130.41 62.69 8448 73.05 10,567.89 19355 193.2 26 82 799794 0016592 1,34219 1.00424 19120 90.00 7112 17tS6 130.44 62.76 8456 7112 10,600.39 2.9668 1914 26.85 10.04033 0.016594 1,342 69 1.00427 19140 90.00 73.26 17412 130.52 62.88 8472 7126 10,792.89 1 9980 1916 2L89 10.06288 0.016595 1,342.58 1.00429 193.60 90.00 7140 17488 130.60 63D0 8488 7140

% N O f

f 10,90139 10293 1917 26.92 1010421 0.016596 1,342.53 1.00430 193.70 90 00 73.47 174.97 130.64 6196 8497 7147 11.017.89 3.0005 193.9 2L95 10.14699 0.016597 1,342.43 1.00433 19190 90 00 73.61 17L13 130.72 63.18 8513 73.61 g m O 11,141 64 3.0952 1941 27.01 10.18991 0.016598 1,342.32 1.00436 194.10 90.00 7175 17129 130.80 6130 8529 7175 11,262.39 11284 194.2 27.04 16 21143 0.016599 1,342.27

-1.00437 194.20 90.00 7182 17537 130.84 6136 8137 7182 11,377J7 3.1605 1944 27.07 10.25458 6016600 1,342.17 1.00439 19440 30.00 73.96 17154 130.91 6149 8154 73 96 11,490.14 11917 1945 27.11 1&27621 0.016601 1,342.11 1.00441 19450 90 00 7404 17562 130.95 6155 8562 7404 11,603.77 1 2249 19&T 27.16 10.31959 Okt0602 1,342 01 1.00443 19470 90.00 7418 17518 131.03 63.67 8578 74.18 11,762.77 12674 1949 27.*9 10.36312 0.016603 1,341.90 1.00446 19490 90.J0 7432 17594 131.11 63.79 8594 74.32 11.88t14 13025 1911 27.22 10.40681 0.016605 1,341.80 1.00448 19L10 90.00 74.4%

176.11 131.19 6191 86.11 74.46 12,042.02 1 3450 1953 27.27 10.43065 0.016606 1.34t.69 1.00451 19530 9000 7460 176.27 131.27 6LO3 86.27 1460 12,19552 13876 1915 27.32 10.49464 0016607 1,341.59 1.00453 19550 90.00 7414 17L43 131.34 6416 8643 7474 u

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RHR Heat Exctia, Ongmal Qg Time lime SP Temp DW Pressure Psat Vf Mass Flow Cp The To LMTD Tho Tco GTD LTD LMTD

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@g 12.350.89 1 4308 1917 27.35 1&S3878 0.016609 1,341.48 1.00456 19170 90.00 74.88 176.00 131.42 04.28 86.80 7488 12,50114 3.4737 1959 27.40 10.58308 0.016610 1,341.38 1.00459 19190 90.00 7102 176.76 13f.50 6440 S&T6 7102 I

12,600.39 1 5108 196.1 27.44 10.62754 0.016611 1.341.27 1.00461 196.10 90.00 7117 176.92 131.58 6&S2 86.92 Titi 12,813.39 1 5593 196.2 27.49 10.64963 0.016612 1,341.22 1.00462 196.20 90.00 7124 177.00 131.62 6458 87.00 7124 0

12,970.77 1 9030 196.4 27.53 10.69452 0.018613 1,341.11 1.00465 196.40 90.00 75.38 177.17 131.70 6470 87.17 75.38 4

13,117.27 16437 1K6 27.56 10.73936 0.016614 1,341.01 1.00468 1K60 90.00 7152 177.33 131.77 64.83 87.33 75.52 c

13,27139 1 6876 196.8 27.61 10.78436 0.018616 1,340.90 1.00470 1K90 90.00 7106 177.49 131.85 6495 87.49 7166 13,438.02 3.7329 197.0 27.65 10.82952 0.016617 t,340.80 1.00473 197.00 90 00 7180 177.65 131.93 6107 87.65 7180 13.591 52 1 7700 197.2 27.69 10.87484 0.018618 1,340.09 1.00476 197.20 90.00 7194 177.82 132.01 6119 87.82 7E94 13,748.14 18199 197.3 27.72 10.89756 0.016619 1,340.64 1.00477 197.30 90.00 76.01 177.90 13105 6125 37.90 76.01 13,907.64 1 8632 197.5 27.77 10.94311 0 016620 1,340.53 1.00479 197.50 90.00 76.16 178.06 132.13 65.37 88.06 76.16 14 071.14 19087 197.7 27.80 10.96882

  1. 018622 1,340.43 1.00482 197.70 90.00 76.30 178.22 132.20 6150 38.22 78.30 h

14222.27 3.9506 197.9 27.84 11.03469 0016623 1,340.32 1.00485 197.90 90.00 76.44 178.39 132.28 6562 88.39 TK44 1A38164 1 9955 198.0 27.90 11.05769 E016624 1,340.27 1.00486 1 %.00 90.00 76.5f 178.47 132.32 6168 88.47 76.51 p

1AsetB9 4 0416 198.2 27.93 11.10380 0.016625 t,340.16 1.00489 1K20 90.00 76.65 178.63 132.40 0100 88.63 76.65 1A706.39 4 0651 198.4 27.96 11.15007 0.016626 t,340.06 1.00491 198.40 90.00 76.79 178.79 132.48 65.92 88.79 76.79 14,866.02 41294 1K5 27.99 11.17326 0.016627 1,340.00 1.00493 196.50 90.00 70.86 178.88 132.52 6198 88.88 76.86 15,027.7' 41744 198.7 28.05 11.21977 0.010628 1.33t90 1.00495 1K70 90.00 77.00 17704 132.59 Ktt SLO 4 77.00 15,188.14 42189 198.8 28.08 11.24309 0.016629 133tB4 1.00497 1K80 90.00 77.07 179.12 132.63 66.17 8712 77.07 C

1534102 L2619 199.0 28.11 11.28964 0.010630 1,339.74 1.00499 199.00 90.00 77.22 17& 28 132.71 66.29 89.28 77.22 15,49127 43042 1911 28.14 f t.31328 0.016631 1,33tS8 1.00501 199.10 90.00 77.29 179.36 132.75 66.35 St36 77.29 15,600.27 4.3501 19t3 28.17 11.36027 0.018632 1,33tS8 1.00504 19t30 90.00 77.43 17753 132.83 66.47 Bt53 77.43

~

15,81t 64 L3943 1974 28.20 11.38383 0.016633 1,33752 1.00505 199.40 90.00 77.50 17tti 132.87 66.53 89.61 77.50 15.97t02 4.4386 1996 28.23 11.43107 0.013634 1,33742 1.00508 199.60 90.00 77.64 f 79.77 132.95 6& 65 8777 77.04 16,13139 44812 19t1 28.27 11.45475 0.016635 1.339.36 1.00509 199.70 90.00 77.71 179.85 132.99 66.71 89.85 77.71 f

16,296.27 4.5267 199,9 2630 11.50223 0.016636 1,33t26 1.00512 199.90 90.00 77.85 180.02 133.06 8K84 90 02 77.85 1% 447.77 45688 200,0 28.32 11.52604 0.016637 1,33t20 1.00513 200.00 90.00 77.92 180.10 13110 68.90 90.10 77.92 18,604.02 46122 200,1 28.35 11.54988 0.046637 1,33tts 1.00514 200.10 90.00 77.99 180.18 13114 66.96 90 18 77.99 16,766.14 4 6573 200.2 28.38 11.57376 0.016638 1,339.10 1.00516 200.20 90.00 78.06 160.26 133.18 67.02 90.26 78.06 16,922.27 A7006 200,4 28 41 11.62166 0.016639 1,338.99 1.00518 200.40 90.00 78.21 180.42 13126 67.14 90.42 78.21 17,0 SLO 2 4.7461 200.5 28.43 11.64567 0016640 1,338.94 1.00520 200.50 90.00 78.28 180.53 13130 67.20 90.50 78.28 17,248.02 47911 200.6 28.49 11.66972 0.016641 1,338.88 1.00521 200 60 90.00 78.35 180.59 133.34 67.26 90.59 78.35 h

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I 19,766.14 14908 202.3 28.82 12.08492 0.018652 1,337.97 1.00545 202.30 90.00 79.55 181.97 134.00 88.30 91.97 7755 19,920.39 15334 202.4 28.84 12.10973 0016653 1,337.92 1.00546 202.40 90.00 79.62 182.05 13& O4 68.36 92.05 79 62 e

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(seconds)

(hotrs)

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f4,222.27 3.9508 f78.39 7.2483 f5,887.91 12.7878 5.3382 f1f4n f4,38184 1 9955 178.47 7.2595 f5,887.5f f2.7892 A3527 f120N p

f4,549.89 404f8 f78.83 7.2859 f5,887.f0 f2.792f 5.3820 f123n f4,708.39 4.085i fTL79 7.3124 15,8K72 f2.7950 5.4f f 5 f128M f4,888.02 4.f294 f7E88 7.3257 f5,8K33 f2.7984 5.420f 13.29 4

{

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f 7,4f402 48372 180.75 7.8388 fR800.08 12.82t8 5.7895 13.82M l

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33,832.82 9.3424 20E7 29.88 f195224 Ref0075 f,330Lf3 f.00003 206.70 90.00 Sf.96 f8474 fR33 70.37 M74

  1. f.98 33,777.39 9.3828 208.7 29.57 f2.902N 0.0f0075 f,33E f 3 f.00003 208.70 90.00
  1. f.95 18474 fM33 7R37 94.74
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% 7 O I

h h

l 33,93f.82 1 4284 205.T 2957 f195224 0.0f0075 f,3Mf3 f.00093 205.70 90.00

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34,235.f4 9.8000 205.7 29.57 fits 224 0.0f9875 f 338.f3 f.00003 205.70 9800 Sf.96 18474 f35.33 70.37 M 74 81.95 h

34,300.02 9.8528 20ET 2157 f195224 Ref0875 f 3Mf3 f.00003 205.70 90.00 Sf.95 f8474 fR33 FR37 M 74 Sf.95 i

34,SdESd 9.8963 20E7 29.88 f198224 0.0f8878 f,33Ef3 f.00003 20E70 90.00 8f.96 184.74 fM33 70.37 M74 8f.98 34,708.84 9.8407 205.7 2150 f198224 Ref8878 f,338.13 f.00W3 205.70 90.00 Sf.95 f8474 fM33 70.37 M 74 81.96 j

34,800.89 9.8838 205.7 29.88 f195224 0.0f0878 f,33Ef3 f.00003 20E70 90.00 St.95 f8474 f3E33 7R37 94.74 Sf.95 3E0fR89 9.7278 20E7 29.98 f1982N 0.0f0875 f,33Ef3 f.80003 205.70 90.00 Sf.98 18474 fM33 70.37 9474 8f.98 Mf7E89 9.TTf4 20E7 29.50 f195224 0.0f8875 f,3Xf3 f.00003 205.70 30.00 Sf.96 18474 fR33 78.37 9474 Sf.95 N

I M332.89 9.8147 20E7 29.50 f195224 RefG878 f,3Xf3 f.00093 205.70 90.00 Sf.95 f8474 f35.33 70.37 M T4 Sf.95 I

M487.Sd 19577 20ET 29.88 f195224 Ref8878 f,338.f3 f.80003 20E70 Stoo St.98 f84.74 f35.33 70.37 M74 81.95 i

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Trne Time Temp

.Pv Ma Pa MCPA DW Pressur (seconds)

(hours)

(T)

(psis)

(Ibm)

(peas)

(peig)

(peig) 3 OZ C

27,959.02 7.7864 18433 12821 15,834 21 12.8795

. 8.4468 f4794d 28,f f 2.f4 7.8889 f84.33 1262f f5,83184 12.8792 E4453 f4.8040 E

28,272.84 7.8835 18433 8.282f 15,831 44 f18789 E4450 f48M 28,4f127 7.893f 1844f 8.2788 1183109 12.8003 8.48f0 f48f40 C

28,587.52 7.9384 1844f 8.2708 fE83172 f18800 E4007 f4.8 fed f

28,7f7.84 7.877f 18441 8.2788 f5,832.35 ft.8797 8.4004 148340 28,875.39 8.8200 fM4f 8.2788 15,83f.96 f2.8793 S.400f 14 8340 29,021 27 8.8834 184.49 8.2915 f5,831.59 f18807 E4782 ftS44d 29,f8E N 8.f07f 184 49 8.2915 f5,83f.20 12.8003 S.4758 f4844d 29.344 84 8.f5t3 184.49 8.2915 15,830 8f f18800 8.4755 148440 l

29,497.89 8.f939 184.49 8.2915 fE830.44 f18797 E4752 f4.8440 29,85E39

, E2379 f8457 8.3082 15,83E05 12.8810 E49f3 14.844d 29,80152 8.2785 18457 8.3082 f5,82E89 f2.8007 E.4910 f48440 29,953.77 8.3205 f84.57 8.3082 f5,82E32 f28804 8.4907 14.844d 30, fos.39 8.3829 f8tS7 8.3082 f5,828.N f1880f 8.4904 ftSHd 30,288.77 8.4000 184.57 8.3082 15,828.55 f2.8798 8.4900 f4.8He 30,42E39 8.450f f84.57 8.3082 f5,828.17 f18795 E4897 f48740 30,578.27 14940 184N 8.3210 fE827.79 f2.8008 8.5058 f48748 3E731f4 -

8.5370 fM68 8.3210 f5,827.4f f2.8005 E5055 f48740 30,89184 8.5818 f8488 8.3210 fE827.0f f2.8002 8.5052 148740 3f,047.77 8.8244 f8408 8.3210 fE828.H f28799

'8.5049 f4.8740 3f,20139 8.s878 18488 13210 #ES28.25 12.8798 S.5048 f48740 3f,358.89 8.7f08

- f 8488 8.32f6 15,82E87 f18793 E5043 f48740 O

31.512.84 8.7535 184.08 13210 f5,825.49 '

f2.8790 8.5040 14904' 3f,087.02 8.7984

- f8474 8.33S8 fE82Ef2 f2.8803 E5201 14.9048 31.8f8.89 8.8308 18474 8.3358 15,82474 12.8000 8.5197 14904d

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31,988.52 8.8798 f8tT4 8.3358 fE82438 f18797 E5f95 149040 y

t 32 f f152 8.9204 184.74 8.3358 f5,82t02 f2.8794 8.5f92 f49040 32,287.f4 8.9831 18474 8.3368 f5,821H 12.8791 8.5f89 ft9HE

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32,42f.39 9.8059 18474 8.3358 15,82127 f18788 S.5185 f4904d i

j 32,571f4 9.0481

- 184.74 8.3388 15,822.89 f2.8785 5.5f82 14.9040 32,72f.77 0.0094 18tT4 8.3358 f5,822.53 12.8782

' S.5f79 148940 a

32,872.52 9.f313 18474 8.3358 fES22.f 8 118779 E5f78 f48940 3102402 9.f733 184.74 8.3358 15,82f.79 118778 E5f73 f4.8940 33,f7f.27 9.2f42 f84.74 8.3368 fES2f.43 12.8773 8.5170 14.8940 33,32E39 9.2573 18474 8.3358 15,821.86 118770 S.5f87 14.8940 33,48f.02 9.3003 18474 8.3358 f5,820.87 12.8787 E5fM f4.8840

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33,832.52 9.3414 18474 8.3358 15,820.29 f2.8783 E5f8f ftSHE i

33,777.39 9.3828 18474 8.3358 fE8f9.M f2.87sf 8.5188 f4.8740 T T O f

khh 33,93f.52 9.4254 18474 8.3358 15,81158 f2.8758 8.5f55 ftS74d 34,08102 9.4881 18474 8.3358 f5,819.18 12.8754 5.5f52 ft8He 5 m 9 34,23114 9.5098 184.74 E3358 f5,8f8.82 f2.875f

8. Side ftS748 h

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r 34,390 02 9.5528 184.74 13358 f5,818.44 f2.8748 E5f48 148740 34,548.H 9.5988 f8474 E33SS f5,8fE05 f2.8745 S.5f43 14.8840

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34,700.84 9.0407 184.74 8.3358 f5,811.08 f18742 8.5140 f48840

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34.800.89 18830 18474 8.3358 f5,817.28 12.8739 E.5f37 ftSNd 35,0f8.89 17275 18474 8.3358 f5,8fS.89 118738 8.5f34 ftSNd 35,f78.89 9.77f4 18474 8.3358 f5,818.51 12.8733 8.5830 f48840 N

35,332.89 9.8147 18474 8.3358 fE818.f2 f2.8730 E5f27 f48848 i

f 35.487.84 9.8877 184.74 8.3358 fE815.74 12.8728 8.Sf24 f48840 l

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Qg Time Time SP Temp DW Pressure Psat Vf Mass Flow Cp Ttu Ta (MTD The Too GTD LTD LMTD as (seconds)

(houm)

(O (pois)

(pain)

(aafumm)

(tmhec) (BTubm *F1 FO PO PF)

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35,84& 84 190f8 20E7 2185 f2.95224 0.0f8875 f,3M f 3 f.80893 20E70 90.00 81.96 f8414 fM33 70.37 M 74 St.88 35,7M 84 9.9438 208.7 29.54 fl95224 0.0f8875 f,3Mf3 f.00803 20E70 90.00 St.98 f8474 135.33 70.37 M 74 Sfm E

M962.52 9.9005 20E7 29.54 f195224 R0f8875 f,338.f3 f.00833 208.70 90.00 Sfm 184.74 fM33 70.37 M 74 Sf.95 Mf01f4 10.0284 20ET 29.53 f2.96224 Ref887S f,33Ef3 f.00003 205.70 SROS St.95 18474 fM33 70.37 M 74 Sf.95 C

i M2SE39 10.0709 20E7 29.53 f2.95224 0.0f8875 f,338.f3 f anent 20E70 50.00 31.95 fM74 f38.33 FR37 M74 Sf.96 4

l M400.39 10.f f 34 205.7 29.33 12.9822d 0.0f8875 f,33tf3 f.00SO3 206.70 Stop Sfm 18474 f35.33 FR37 M74 8f.98 38,500.39 fRfSS7 2017 29.52 12.95224 0.0f8875 f,33tf3 f.00503 20E70 90.00 Sf.95 f84.74 f35.33 70.37 M 74 St.95 t

M7f2.52 fRf979 208.7 28.53 f2.95224 0.0f8875 f,3Mf3 f.00003 205.70 30.00 81.95 fM74 fM33 70.37 94.74 81.96 M887.02 f0.2400 20EF 2152 fi95224 Ref0875 f,338.f3 f.00093

'206.70 90.00

  1. f.95 fM74 f35.33 FR37 M74 Sf.98 37,027.52 f0.20S4 20E8 29.5f f19200f Ref8874 f,3Xf8 f.00002 20E00 90.00 Sf.88 f8&S$ fM29 70.31 M88 31.88 37,f77.27 10.3270 20ES 29.5f f2.9200f

&#19874 f,33tf 8 f.00832 105.00 90.00

  1. f.88 18488 fM29 70.3f 94 08
  1. f.88

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37,331.39 10.3e98 205.8 29.50 f19200f 0.0f8874 f,3M f 8 f.00592 205.80 90.00 St.88 fM98 f3129 70.31 94.88 8f.88 I

37,48189 10.4f38 20E6 29.49 f2.9280f 0.Of8874 f,t38.f8 f.00002 205.00 SROS St.88 18488 f35.29 7R3f 94 88 Sf.8B 37,84139 10.458S 20E6 29.49 f2.9200f Ref8874 f,338.f8 f.00552 205.80 90.00 Sf.88 f8488 f35.28 70.31 M88 Sf.88 p

37,798.f4 10.4995 20E8 29.48 f 2 9200f 0.0f8874 f,338.f 8 f.00002 205.00 90.00 St.88 f84.88 f35.29 FR3f Mas Sf.88 h

l 37.99& 52 f0.Sd35 205.8 2147 f2.9200f 0.0f8874 f,338.f 8 f.00892 20E00 90.00 Sf.88 f84.00 f35.29 70.3f M88 Sf.88 38,108.89 10.5858 20ES 29.47 1189983 0.0f8874 f,338.24 f.0059f 208.80 90.00 8f.8f fMST f35.25 70.25 94.57 Sf.Sf 38,27f.52 fRS3fo 208.5 2145 12.89083 0.018874 f,338.24 f.00891 205.50 M00 81.8f 18457 13E25 70.25 MST Sf.*f 38,42f.f4 f0.8725 20E5 29.45 f189983 R0f8874 f,3M24 f.00Sef 205.50 90.00

  1. f.8f 18457 f3125 70.25 MST Sf.*f I

38,577.84 10.7f80 205.5 29.44 f2.89983 0.0f8874 f,3M24 f.00Sef 205.30 30.00

  1. f.8f fM57 f35.25 7R25 M57
  1. f.8f 30,731f4 f0.7589 208.5 29.45 f189083 R0f8874 f,3M24 f.0059f 205.50 90.00 St.8f f84.57 f3125 FR2S 94.57 St.Sf l

38,888.84 10.8024 205.5 29.44 f189983 0.0f0874 f,338.24 f.0059f 20ESO 90.00

  1. f.8f fM57 f35.25 70.25 M ST Sf 8f 39,0d7.27 10.8485 20Ed 29.43 f187309 0.0f8873 f,33129 f.00SSO 205.40 90.00 Sf.74 f84.49 f3121 FRf9 94.49
  1. f.74 O

39,20t f4 10.8900 20E4 29.42 f187309 RefS873 f,338.29 f.00089 20E40 90.00

  1. f.74 f8449 f35.2f 70.f9 MdB Sf.74 39,38189 10.9344 20E4 29.42 f187309 0.0fS$73 f,338.29 f.00000 208.40 50.00 Sf.74 f8&49 f38.2f 70.f9 MdB 8f.74

[

39,520.77 f0.9783 20E4 2140 f2.87309 E0f0STS f,338.29 f.00089 20E40 30.00 31.74 f8449 f35.21 7&fs M4B Sf.74 39,877.02 f f.02f4 206.4 29.40 f2.87309 0.018873 f,3X29 f.00 SOS 208.40 30.00 Sf.74 18449 f35.21 7&f9 M40 Sf.74 39,837.39 f f.0859 208.3 29.38 f2.84789 0.0f8872 f,3M3d f.00588 205.30 90.00 3f.87 f844f f3iff 70.f 3 944f 8f.87 l

39,989.8d f f.1082 2013 29.37 f2.84759 0.0f8872 f,338.3d f.00508 205.30 90.00 St.87 f84.4f f 35.f 7 FRf3 Sd.4f

  1. f.ST 40,fS2.52 f f.f S38 20E3 29.37 f184759 0.0f0872 f,3M3d f.00 SOS 205.30 90.00 Sf.87 1844f f35.f7 7Ef3 M4f 81.87 40,299.02 f f.1942 205.3 29.38 f184759 &#19872 f,33134 f.00608 205.30 50.00 Sf.87 fM4f f 35.f 7 7&f3 M4f 81.87 p

40,450.27 1f.2382 2012 29.35 f182f54 Ref0872 f,3M40 f.00008 20E20 90.00 St.80 18433 135.f4 FROS M33

  1. f.00 40,007.84 f f.2790 2012 2135 f182f54 Ref8872 f,3M40 f.00008 20E20 90.00 Sf.80 f84.33 f35.f4 70.08 M33 8f.00 h

40,781f4 f f.3231 205.2 29.34 f2.82fS4 Refe872 f,3M40 f.00000 20E20 90.00 8f.80 f8433 f3Ef4 75.08 M33 Sf.80 40,91152 f f.3854 205.2 2133 f2.82fS4 0.0f8872 f,3M40 f.00508 20E20 90.00 St.80 18433 131f4 70.08 M33 Sf.00 l

41,078.f4 f f.4100 205.f 2132 f179554 E0f887f f,33145 f.00606 208.f0 30.00 St.53 18428 f3Ef0 70.00 94.28 81.83 t

4f,232.f4 f f.4834 205.f 29.3f f2.79554 0.0f887f f,338.45 f.00605 20Ef0 90.00 Sf.53 f8425 f3Ef0 70.00 M25 Sf.S$

1 4?,3Sf.27 f f.4948 20Ef 29.31 f179554 0.01887f f,338.45 f.00605 208.f 0 90.00 St.53 18425 f31f0 70.00 M25 Sf.53 4f,53484 ff.5374 208.f 29.33 f179554 0.0f8871 f,338.45 f.00585 20Ef0 S0.00 Sf.53 18425 f31f6 70.00 94.25

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% 7 O

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4f,sSS.02 f f.5000 208.0 2132 f178957 0.0f8870 f,338.Sf f.00SS3 206.00 90.00 St.48 184f7 f3108 80.94 Mf7

  1. f.48 41,8Mf4 f f.8217 20E0 29.30 12.79957 R0fe870 f,33E5f f.00SS3 20E00 90.00 31.48 f84f7 f3108 GR94 Mf7 Sf.48 5 m O 41,992.f4 f f.0848 20E0 29.30 f2.70957 0.0f8870 f,3M5f f.00883 20E00 90.00 81.48 184.17 f3108 89.94 Mf7 81.48 l

42.f53.02 f f.7092 205.0 29.29 f2.78957 0.0f8870 f,3315f f.00083 205.00 SR00 81.48 f8df7 135.0f 89.94 Mf7 Sf.48 42,307.52 f f.752f 204.9 29.29 f174385 R018870 f,33E58 f.00632 204.90 90.00 81.38 f8408 f35.02 88.88 MOS Sf.38 42,458.84 f f.794f 204.9 2127 f2.74385 0.014870 f,3XS$

f.00882 20t90 90.00 Sf.38 f8409 135.02 88.88 MOS Sf.38 42,8f2.52 f f.5308 204.9 2128 11 74385 0.018870 f,338.58 f.00SS2 20t90 30.00 Sf.38 f8409 f35.02 89.88 MOS

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f.00SS2 204.90 90.00 St.38 18409 f38.02 SESS MOS Sf.38 i

42,9f8.89 f f.92f4 204.8 29.2S f2.7f778 0.0f8809 f,33&S2 f.00S00 20480 SR00 St.3f f8480 f3498 09.82 M60 8f.31 D

l 43,087.89 f f.9833 20&S 29.2d f1Tf778 Ref8889 f,338.82 f.00000 29t80 90.00 Sf.3f f84.00 13498 89.82 MOS

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43,22f.84 f10000 204.8 29.23 f2.7f 778 0.0f8809 f,33tS2 f.00000 204.80 SR00 St.3f f84.80 f3138 SES2 MOO Sf.31 g

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f 1

amo 27 h

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one=

Tane Time Temp Pv Me~

Pa MCPA DW Preneur O

(seconds)

(hours)

(*F)

(pois)

(8sm)

(pain)

(psig)

(peig)

[

C 35,848.84 9.90f8 188.14 13388 fE8fS.35 12.8723

&Sf2f f4854d M79&ed.

9.N35 18414 8.3358. f 5,8f489 f2.8720 8.5ff8 f484dd N

- M952.52 9.9888 18474 8.3358 fE8f480 f187f7

.$.5ff5 f4.848d h

38,102.f4 fRS294 18474 8.3358 fE8ft34 f257f4 8.5ff2 148340 38,255.39 10.0709 18474 8.3358 f5,8f188 1187ff 8.5f88 ft3Nd f

M488.39 10.ff34 18474 8.3358 fE8f3.#

f2.8708 E5f88 ft3341 M589.39 10.f557 18474 8.3358 15,8f11f f18785 8.5f83 ftS24d 38,7f2.52 fRf979 f8474 8.3358 f5,8f174 12.8702 8.5f00 14 8340 38,857.02 fE2488 f8474 a nna 15 8f2.38 12.8899 8.5097 f482dd 37,027.62 ft2854 18488 8.3210 fEttf.97 f2.8879 8.4929 ftSf4d 37,f71.27 10.3278 f8488 8.3210 fE8f f.00 11N78 8.4928 148 fed 37,331.39 10.3898 f8488 8.3210 f 5,8f f.22 f2.8873 8.4923 faaedd h

37,488.89 70.4f38 18488 8.3210 f5,810.84 f1N70 8.4920 f47941 37,843.39 10.4505 18488 8.3210 f5,8f848 f2.8867 8.49f7 f47941 p

37,79Ef4 - f04995 f8488 8.32f0 f5,8f0.08 12.8884 8.4914 14 7840 37,958.52 fR5438 f84.88 8.3210 15,809.00 f2.888f 8.49ff f4774d 30,108.89 f0.5868 f8401 8.3082 fE809.3f 12.8842 8.4744 f47741 M27f.52 10.8310 18457 8.3082 f5,80ES2 f2.8838 E474f f475W 38,421.f4 10.8725 f44f7 8.3082 15,888.55 12.8835 8.4738 14784d I

38,577.N

- 10.7f 89 f8457 8.3082 f5,888.f8 f2.8832 8.4735

.f4744d 38,772.f4 fR7589 f8457 8.3882 fE807.79 f2.8829 E4732 f47540 38,888.84 10.8024 f8457 E3082 15,807.40 f2.8828 E4728 f4744d

=

39,047.27 f0.8485 18&46 8.29ff f?,807.Of f2.8807 L4582 f47340 O

39,204f4

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39,38189 10.9344

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39,520.77 149780 f8449 8.2915 15,805.85 f18597 14552 f47040 39,877.02 ff.02f4 18448 8.29f5 1E805.47 12.8594 E4549 f47840 39,837.39 f f.0859 f844f 8.2768 f5,805.07 f18575 8.4362 14.8ME 39,989.84 f f.f082 18441 8.2788 f 5,80470 12.3572 8.4379 14 8740 40,f52.52 f f.f 535 18441 12768 19.80430 f18588 8.4378 f48748 40,290.02 f f.f 942 f844f 8.2758 i M194 f18585 8.4373 f4888d 40,450.27 ff.2382 18433 8362f f 5.M157 f2.8548 8.4207 f48541 h

40,007.84 ff.2799 f8433 8.2821 fE803 f8 12.8543 8.4204 f48540 40 781f4 - f f.323f 18433 8.2821 fisc133 12.8540 8.420f ft eded 40,915.52 f f.3854 18433 8.2821 f5,802.43 12.8537 8.4f98 f4834d 4f,078.f4 ff.4f00 18425 8.2474 f5,802.04 f2.85f7 8.4032 f4.CNd 49,232.f4 f f.4534 18435 8.2474 fE801.85 f2.85f4 8.4028 148f40 of,38f.27 ff.4948 f84.25 8.2474 15,80f.29 12.85f f 8.4025 fd8f40 W D O b

4f,53484 ff.5374 f8L25 8.2474 f5,800.9f f2.3508 L4022 f4.834d h

4f,888.02 f f.5000 184f7 8.2327 15,800.53 118489 E3857 f483#

4f,838.f4 f f.12f 7 18df7 8.2327 fE800.f 7 f2.8488 EJ854 f4.90dd 5m O 4f,992.f4 f f.8845 f84f7 8.2327 fE799.79 118483 8.385f 148040 42.f5102 f f.7092 184f7 8.2327 fE799.39 f2.8480 E3847 148840 h

42,307.52 f f.752f f8409 8.21Sf f 5,799.0f f2.8480 8.3882 f45988 l

42,458.84 ff.79df 18409 8.2181 f 5,798.84 12.8457 8.3879 f4.5748 42,812.52 ff.8380 18409 8.2f8f f5,798.27 f18554 E3878 145640 42,78f.02 f f.878f 18489 8.2f8f fE797.90 f2.845f 4.3873 f4.5540 42,918.89 ff.9214 18400 8.2035 fE797.52 f2.8432 E3597 ftS5dd N

T F

43.Nr.N ff.uS3 fuS9 nm35 fE797.,5 flun 8.35u f<MW 43,22f.84 f2.0000 f8400 n035 f5,79sTr fruts 6.350f f<8340 g

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RHR Heat Exchanger aO s-Trne Trne SP Temp DW Pr >ssurt Psat Vf Mass Fm Cp Tru To LMTD Tho Tco GTD LTD LMTO O

o (seconds)

(hours)

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